## March 4,2013
Carey Willoughby Monitoring and Analysis Division Source Test Engineering South Coast Air Quality Management District 21865 Copley Drive Diamond Bar, CA 91765-4182 Subject: 

## Initial Source Test Report for Unit 2 CPV Sentinel, LLC (CEC Docket No. 07-AFC-3) SCAQMD Title V (A/N 

## 472137, Facility ID No. 152707) Dear Mr. Willoughby: 

# . sierra research 1801 

### J Street Sacramento CA 95811 Tel: (916) 444-6666 Fax: (916) 444-8373 Ann Arbor MI Tel: (734) 761-6666 Fax: (734) 761-6755



## On behalf of CPV Sentinel, LLC, I am submitting the enclosed initial source test report for Unit 2 at the CPV Sentinel Energy Project. Testing was conducted in accordance with Condition of Certification AQ-7 and Section H, Condition D29.3 of facilities Title V Permit. Should you have any questions or require additional information related to this submittal, please contact me at (916) 444-6666. Sincerely,

Tom Andrews Senior Engineer CC: Roy Olivares, SCAQMD Craig Hoffman, California Energy Commission EPA Region 9 (r9.aeo@epa.gov) Charles Aldred, EPA Region 9 Mark McDaniels, CPV Sentinel, LLC

# SOURCE TEST REPORT FOR INITIAL COMPLIANCE TESTING AT CPV SENTINEL ENERGY PROJECT UNIT 2
PREPARED FOR : GEMMA POWER SYSTEMS CALIFORNIA, INC. 

## 2461 MAIN STREET GLASTONBURY, CONNECTICUT 06033 FOR SUBMITTAL TO: SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 

## 21865 COPLEY DRIVE DIAMOND BAR, CALIFORNIA 91765-4178
PREPARED BY : DELTA AIR QUALITY SERVICES, INC. 

## 1845 N. CASE ST. ORANGE, CALIFORNIA 92865 714-279-6777 ARLENE BELL / ROBERT 

## A. FINKEN FEBRUARY 28,2013 REPORT NUMBER: R0410673 

# Della f).

Air Quality Services, Incorporated

## CONFIDENTIALITY STATEMENT

This information contained in this communication is intended exclusively for the individual or entity 

## to which it is addressed. This communication may contain information that is proprietary, privileged or confidential or otherwise legally exempt from disclosure. If you are not the named addressee, you are not authorized 

## to read, print, retain, copy, or disseminate this message or any part of it.

R0410673 

### ii

## REPORT 

## REVIEW AND CERTIFICATION

I certify that all work performed in the preparation and production of this report was performed by me or under my supervision and that 

## all data presented is authentic

.

# _-------I.a.LL!l'<L\,'---'-"'~=--=---E--J,v_A_9_ Date : 

## I Arlene Bell Vice President , Analytical Services

I certify that I have also reviewed this report , both in form and content , and that all data , calculations, and presentations are authentic , accurate , and complete

.

R0410673 

## Robert 

## A. Finken President

iii

## CON T ENTS SECT I ON PAGE 1
. 0 I NTRODUCTION AND SUMMARy

.... . ............ .. ... . . • .. . . . . . . . ...... 1 2
. 0 UN IT DESCRIPTION AND TEST CONDI T IONS

. . ... . .... . ...... . .......... . . . ......... . ......... 3 2
. 1 UN I T DESCRIPTION

................................. . ... . ...... . ........... . ... . 3 2
. 2 TEST CONDITIONS

... . .. ........ . .. . . . . .... . .. ............. . ....... . .. . .. . .... . ..... 5 2.3 SAMPLE LOCATION

.. . .......... . ..... . .. . . ............... . ... . ...... . . ..... ..... . . .... ........ . . .. .. . .. 6 3
. 0 TEST DESCRIPTION

.. . . .. .. . . . . .. . . .. . . . .. .. . . ... . . . . .. .. . .. . . .. . . . .. . . ... ..... . . . ......... . ... .. . . ..... . ..... . . . . 9 3.1 O 2 , 

## CO 2 , 

## NO x AND CO

....... . . . .... . .......... . . ... . .. . . .. . . . ...... . ..... . ..... . .. . . . .. . ... . ....... 10 3
. 2 NH3 BY SCAQMD METHOD 207.1
.. .. ... . . . . .. .. . .... .. ..... . . . .. .. . . .. . .. 11 3
. 3 SOx BY SCAQMD METHOD 307
. 91
................................ . . . . .. 11 3.4 ROG BY MODIFIED SCAQMD METHOD 25
. 3
. . . . . ..... . .... . .... ... .... .... 11 3
. 5 PM BY SCAQMD METHOD 5
. 1
... . ..... . . . .. .. .... . ... .. ... . . . . . . . .. 14 4
. 0 RESULTS

.... . .... .. .. .. ... .. . . .. . .... .. . . . .. . ........ . ......... . ...... . ... . . . . 16 5.0 DISCUSSION AND TEST CRITIQUE

.. . .... . ...... . ....... . . ........... 24 APPENDICES A QUALITY ASSURANCE

.... . ..... . . . ..... ........... . ... .. ...... . .... . ... . .... . ...... . ... A-1 A.1 Quality Assurance Program Summary

... . ......... . .......... . . . .... . .... . ..... .. .......... A-2 A.2 SCAQMD and CARB Certifications

............ . ........ . .. . ...... . ............. . . .. .. . ......A-7 A.3 Equipment Calibration and Calibration Gas Certificates

. .... . .. . . .. . . . .... A-8 A.4 Delta CEM System Description and SCAQMD Method 100.1 Calibration and Test Sequence

. . .. ............ . . . .... . . . .... A-9 B PROCESS DATA

. . .. . . .. . .. . .... . .......... .. . . .. . .. .. .. . .... ... . .. . ........... B-1 B

. 1 Process and CEMS Data.

. . .. . ... . . . . . . ... . . . ........... . . . .. . B-2 B.1.1 Sentinel Unit 2 Stratification Test

........ . ... . . .. . .. ............. . . B-3 B.1.2 Sentinel Unit 2 Ammonia , ROG , and 

## NO x /CO Testing

..... B-4 B

. 1
. 3 Sentinel Unit 2 PM Testing

.... . . . . . .. . .. ... ... ..... . . ... . ........ .. .. .. . . . . .. B-5 B

. 2 Fuel Analysis Data

.. . .. . . .... .. .. . . . . . . . .. .. . ... . ..... . . . .... . .... .... .. . . .... . . . . . .. . . . ... . . . .. ... . . B-6 C TEST DATA.

. .. . . . . .. . .. ... .. . ....... . . . ..... . . . . . .. . . . ... . ................. . ..... . . . .. . .... .. . . . ... . .... . . . C-1 C

. 1 Stratification and Preliminary Flow Rate Tests

.. . . . .... . ...... . . .... .. .... . . . .. .. . . .. . ..... C-2 C

. 2 CEM Data

... . . .... . ..... .. ... . .. ......... . . ................ . ......... . ... .. .. . . . ... . .... . ..... .. C-3 C.2

. 1 CEM Quality Assurance Measurements

. .......... .. .......... . .. .. . .. .... . . . C-4 C

. 2
. 2 NOx and CO Compliance

..... . ... . . . .... . ... ... .. . .. . ... . ............ . .. C-5 C

. 2.3 One Minute Data Logger Data.

.. ...... . .. ... .. . . . .. . . . . ... C
- 6 C

. 3 Ammonia Data by SCAQMD Method 207
. 1.
. ...... . ....... . . . . . . . . ... . ... . . .. ..... C-7 C.4 SOx by SCAQMD Method 307.91
........ . ... ... ... . .. . . .. . ... . ..... C-8 C

. 5 ROG by Modified SCAQMD Method 25
. 3
...... . . .. C-9 C

. 6 PM by SCAQMD Method 5
. 1
. . .............. . ....... ... . ... .. ... .. .. ........... . . .... C-10

R04106 73 

### iv

# o E F G 

## H GENERAL EMISSIONS CALCULATIONS

........... . ...... . ... .. .......... . ........ ............ 

## 0-1 CHAIN OF CUSTODY

............................... . .. . .. . . .......... . ...... . .................................. E-1 

## INSTRUMENT STRIP CHARTS

...................................... .. . .......... .. ........ . .......... 

## F-1 FACILITY PERMIT TO OPERATE CONDITION D29

. 1
....... . ..... . 

## . . ..... . ......... . . . . . G-1 CORRESPONDENCE AND TEST PLAN

. . .. . .. . . . . . . . . .. . . .. . ..... . ... . .. . ........ . ...... . .. . H-1

R0410673 v

## 1.0 INTRODUCTION AND SUMMARY Delta Air Quality Services , Inc. has been contracted by Gemma Power Systems California , Inc. (GEMMA) to perform the initial Permit to Operate Compliance Testing at the CPV Sentinel Energy Project Units 1 , 2 , 3 , 4 , 5 , 6 , 7 , and 8. Condition D29

. 1 of the Permit to Operate requires source tests within 180 days of initial startup
. This document is the test report for the initial compliance for CPV Sentinel Unit 2
. Tests were performed at three load conditions to determine oxides of nitrogen (NO x ) , carbon monoxide (CO), oxides of sulfur (SOx) , reactive organic gases (ROG) , particulate matter (PM) , and ammonia (NH 3 ) emissions. Bob Finken was the Senior Program Manager for Delta and can be reached at (714) 279-6777
. No conflict of interest , as defined in SCAQMD Rule 304 , exists between Gemma or CPV Sentinel Energy Project and Delta. Testing was conducted on January 30-31 and February 1 , 2013. The Delta test crew consisted of Ali Aleshaiker , Shannon Scrugham , and Justin Miller. Table 1-1 contains a summary of the test results and applicable limits

. This table also compares the results at three load conditions , 50% , 75% , and 100%, that were tested

. All test results showed the unit to meet the permit limits. Section 2
. 0 of this document provides a description of the facility and sample locations

. A description of the sampling strategy and test methods is provided in Section 3
. 0
. Section 4
. 0 contains detailed test results

. Section 5 contains a discussion and test critique. The appendices contain all test and laboratory data , calculations , and quality assurance data.

R0410673 1

## TABLE 1·1 CPV SENTINEL ENERGY PROJECT UNIT 2 STACK TEST RESULTS SUMMARY Parameter Units 100% 75% 50% Limit Rule ppm@ 15%0, 2.37 2.22 202 2.5 1703(a)(2) NO, ppm @ 15% 0, 2
. 37 2
. 22 2.02 15 40 CFR 60 Ib/MMscf 9.38 9
. 01 8.48 12.26 11 ) 

### 2012 CO ppm @ 15% 0, 1.89 0
. 52 0.25 4 1703(a)(2) NH, ppm@ 15% 0, 1.51 0.98 0.73 5 1303(a)(1 ) gr/dscf @ 3% 0, 0.0005 0
. 0004 0
. 0005 0
. 01 475 Particulate gr/dscl @ 12% CO, 0.0007 0
. 0005 0
. 0005 0.1 409 Ib/hr 0.75 0.49 0.42 11 

### 475 PM ,0

### /PM'5 Ib/MMscf 0.89 0.71 0.78 5.71 1 ') 

# so ,l') Ib/MM8tu 0.0003 0.06 40 CFR 60 gr 

### H,S/1 00 sci 0.013 0.25 14) 

### SCAQMD Permit Condition 861
. 1 ROGs ppm @ 15% 0, 0.75 0.55 0
.68 2.0 1303(a)(1) (1) The 12.261b/MMscl is a RECLAIM emission factor, not a limit. (2) This is stated in the permit as an emission factor. 

### (3) SO, results calculated based on 100% load condition

. (4) 0
. 25 gr H,S/1 00 sci sulfur content limit is based on annual average of monthly sample results

.

R0410673 

### 2 

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### ............. .........

## 2.0 UNIT D E SCR I PT I ON AND TEST CONDITIONS
2.1 UNIT DESCRIPTION 

## CPV Sentinel Energy Project is located at 62575 Powerline Road , Desert Hot Springs , California 92240. The facility consists of eight (8) identical generating units. The CPV Sentinel Energy Project consists of eight (8) LMS100PA combustion turbines in simple cycle operation

. The units are natural gas fired with a rated heat input of 891
. 7 MMBtu per hour at 72 degrees Fahrenheit. Each LMS100PA employs water injection and is equipped with a CO catalyst and Selective Catalytic Reduction (SCR) system for NO, control. The LMS100PA is a General Electric (GE) combustion turbine with an intercooler located between the low pressure compressor (LPC) and high pressure compressor (HPC)

. Off engine combustion air to closed loop water intercooling is used for increased gas turbine thermal efficiency. Heat removed from the off-engine intercooler is circulated through a closed loop cooling system. Heat is rejected from the closed loop cooling system to an open loop cooling system via a shell and tube heat exchanger

. The open loop system rejects heat via a mechanical draft counterflow cooling tower
. The cooling tower is provided with drift elimination to comply with air emissions limits

. Figure 2- 1 presents a block diagram of the units

. Figure 2-2 shows a general arrangement of the major components
.

R0410673 

### 3

## FIGURE 2-1 SIMPLIFIED PROCESS BLOCK DIAGRAM CPV SENTINEL ENERGY PROJECT COMBUSTION TURBINES

Simplified Process Flow Diagram


### A i r Water

Air Cooling Tower

Closed Loop Cooling

LMS100PA

Natura l Gas Fuel Water Demineralized

R0410673 Air Water Heat

Exhaust to Atm.

Exhaust CO Catalyst SCR I--



### Ammonia 19% Aqueous



## 4

## FIGURE 2-2 GENERAL ARRANGEMENT OF MAJOR COMPONENTS

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## 2.2 TEST CONDITIONS The permit requires that the tests will be performed at three operating conditions; 1) maximum, 2) average, and 3) minimum load. Full load is nominally 100 megawatts and minimum load is approximately 50 megawatts. Since these will be the initial tests for the units and no long term average will have been established , average conditions will be approximated at 75% of capacity or approximately 75 megawatts.

R041 0673 

# Della b.

..

# -

...... 

## 5

## Unit operating data was collected during the tests by the facility from the CEMS DAS

. Table 2-1 below presents the average operating condition for each parameter
. TABLE 2-1 AVERAGE OPERATING CONDITIONS Parameter 50% Load 75% Load 100% Load Fuel Flow Rate , hscfh 5,373 6,923 8,319 Turbine Generating Output (MW) 55 80 101 Ammonia Flow , Ib/hr 106.4 110 .0 109
. 9 Exhaust Temperature , o f 

## 796 785 781 Exhaust Flow Rates , kscfh 15 ,627 18 , 349 20 , 378 Notes : Data from facility DAS except exhaust gas temperature where PM test data was used

. Data collected during PM test i ntervals at each condition

.



## Process data obtained during testing is contained in Appendix 

## B

. 2,3 SAMPLE LOCATION There are four 4 " test ports located at 90 degrees apart around the circumference of the 13'6 " diameter stacks

. The ports are located 323" downstream (2.0 diameters) of the nearest flow disturbance (duct breeching) 

## 84' upstream (0.5 diameters) of the nearest flow disturbance (silencers)

. The sampling location meets the minimum requirements of SCAQMD Method 2
. 1 ; at least 2 diameters downstream and at least 0
. 5 diameters upstream of the nearest flow disturbances

. Figure 2-3 presents the details of the sample location.

R0410673 6Stack Exit 1080.0 in. Silencer Bottom 925.9 in.
Ports 841.6 i n . Platform 789
.6 in.

Base of Stack 518.5 in

.

Grade 0.0 in

. 

## FIGURE 2-3 SAMPLE LOCATION DETAILS

Inside D i ameter, i n.

-- 162

-- 

# T 84 Distance A, inches, 0.5 Diameters 

# ! Sample ports 

# T

323 Distance B, inches, 2.0 Diameters

.._--=E;:;:xh.:;:aust Flow

Elevation View 90 ft

66 ft

.



## o ft



## Prior to performing the tests, gaseous stratification was investigated with a 12 point traverse as described in 40 CFR 75, and the presence of cyclonic flow was checked using the techniques described in SCAQMD Method 2. The results of the yaw angle and stratification checks indicate that the angle criteria was met. The average angle was 2.8 0 

## which meets the SCAQMD criteria of 10 degrees or less. The stratification criteria was not met. Results of the stratification checks are presented in Table 2-2. 12-point traverses were used for ammonia, NOx , 

## and CO compliance tests.

R0410673 7 

# Delta tJ.
"' '''''''' ''''''''''"' -

## TABLE 2-2 12-POINT STRATIFICATION CHECK RESULTS GEMMA POWER SYSTEMS CPV SENTINEL UNIT 2 0, CO, NO, CO Port Point % % 

## ppm ppm East 3 13.52 4.24 1.59 0
. 09 East 2 13.53 4
. 24 1.58 0
. 17 East 1 13.56 4.23 1.64 0.20 South 3 13.48 4.29 1.78 0.16 South 2 13.48 4.29 1
. 81 0.23 South 1 13.43 4.32 1.87 2.40 West 3 13.07 4.54 2.27 1.94 West 2 1308 4.53 2.35 1.91 West 1 13.08 4
. 54 2.27 1.69 North 3 1308 4.54 2.34 1
. 12 North 2 13.08 4
. 55 2.40 0.60 North 1 1307 4.55 2.53 0
. 57 Average 13.3 4.4 2.0 0.9 Maximum 

### 13.6 4.6 2.5 2.4 

### Minimum 13.1 4.2 1.6 0.1 Maximum Difference from Average 

### 0.3 0.2 0.5 1.5 Max Difference (% of average) 2.0% 3.9% 24.2% 159.6%
Criteria:



### If < 

### 10%, use single point. Action Taken:

12-point traverse used for RATA runs Runs in conjunction with NH3 test, use 12-point traverse 

## Table 

## 2-3 illustrates the location of sample traverse pOints for each type of test. TABLE 2-3 SAMPLE POINT LAYOUT

PM (24 pts.) Cyclonic Flow Check (16 pts .) StraUNH3 , NO" and CO Compliance (12 Pts.) Sample 

### % of i n. 

### % 

### of in. % 

### of in .

Point Diameter from Wall Diameter 

### from Wall Diameter from Wall 2.1 3,4 3.2 5.2 4.4 7
. 1 2 6.7 10.9 10.5 17.0 14.6 23.7 3 11
. 8 19.1 19,4 31,4 29
.6 48.0 4 17.7 28 .7 32
. 3 52.3 70,4 114.0 5 25 40
. 5 67
. 7 109
. 7 85,4 138.3 6 35.6 57.7 80
. 6 13Q.6 7 64,4 104.3 89.5 145.0 8 75 121.5 9 82.3 133.3 10 86,4 140.0 11 93.3 151.1 12 97
. 9



### R0410673 

## 8 

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### .........

# -
....

## 3.0 TEST DESCRIPTION Table 3-1 summarizes the test methods and techniques that were used as the reference methods

. The test matrix has been developed to meet the requirements of Section 29
. 1 of the facility Permit (Application Number 472137) dated April 15 , 2011
. The test matrix indicates the number of runs that were performed for each parameter and each condition

. The permitted emission limits are summarized in Table 3-2
. The following sections describe each method in further detail. Flue gas oxygen and carbon dioxide concentration were measured in conjunction with all tests using SCAQMD Method 100.1. The flue gas flow rate was measured in conjunction with each ammonia and particulate test. This measured flue gas flow rate was used for all emission rate calculations of NOx , CO , NH 3 , 

## ROGs and SOx

.

Parameter NOx 0 2 /

C0 2 

## CO NH 3 S02 PM ROG Method SCAQMD 100
. 1 SCAQMD 100
. 1 SCAQMD 100
. 1 SCAQMD 207
. 1 

## TABLE 3-1 T EST MATR IX SENT I NEL UNIT 2 50% Load 75% Load

2 runs' 2 runs'" 

## With each run 2 runs' 2 runs'" 

## 2 runs 2 runs 100 % Load 2 runs '

2 runs ' 2 runs SCAQMD 30 7. 91 Fuel Sample , 2 Samples

SCAQMD 5
. 1 3 runs · 

## 1 run run Modified SCAQMD 25
. 3 1 pair 1 pair 1 pair Test Durat ion 60 m i nutes

60 m i nutes 60 m i nutes N/A 240 minutes

- 60 m i nutes (1 ) 1 ) 

## ROG tests were nominally 60 minutes. Flow controllers will be setup for 60 minutes. The test was performed until the canister vacuum reaches approx i mate ly 10 "H g . Actual tes t time may be less than o r mo re than 6 0 m i nutes per sample . 

### • Addit i onal runs performed compared to test plan

.



## R0410673 9

## TABLE 3-2 CPV SENTINEL ENERGY PROJECT PERMITTED EMISSION LIMITS Parameter Units ppm@ 15%02 

### NO, ppm@ 15% O 2 Ib/MMscf CO ppm @ 15% O 2 

## NH3 ppm@ 15 % O 2 

### gr

/ dscf @ 3% O 2 Particulate grldscf @ 12% CO 2 Ib/hr PM lO

### / PM 2 5 Ib/ MMscf SO, Ib/MM8tu gr H2 S/1 00 scf ROGs ppm @ 15% O 2 (1) The 12
. 261b/MMscf is a RECLAIM emission faclor , not a limit. (2) This is staled in the permit as an emission faclor. 

### Limit 2
. 5 15 12.26(1) 4 5 0.01 0
. 1 11 5
. 71 (2)

0
. 06 0.25 (3)

2.0 Rule 1703(a)(2) 40 CFR 60 2012 1703(a)(2) 1303(a)(1 ) 475 409 475

40 CFR 60 SCAQMD Permit Condition 861.1 1303(a)(1 )
(3) 0
. 25 gr H 2S/100 

### scf sulfur can lent limit is based on annual average of monthly sample results

.


## 3 . 1 

## O 2 • 

## CO 2 • 

## NO x AND CO 

## O 2 , 

## CO 2 , 

## NO, and CO concentrations were measured using SCAQMD Method 100
. 1
. These measurements were made with one of Delta ' s mobile emission measurement laboratories. The system consists of a stainless steel or glass probe, heated Teflon line , moisture removal system, sample pump, sample filter, unheated Teflon line, and individual component analyzers. The measured concentrations are averaged over each sampling period, then corrected for system bias and analyzer drift. All quality assurance procedures required by SCAQMD Method 100.1 were performed including pre- and post-test Calibration Error , Sample System Bias and Analyzer Drift. The sampling was performed using a 12-point traverse at each test condition

. At the 75% load condition , the compliance test was performed concurrently with the Relative Accuracy Test Audit (RATA). In this case , data from the RATA was used to demonstrate compliance with the NO , and CO emission limits

.

R0410673 10 

# Della i'!. 

# "'_.....w._....

### NO , concentrations were measured on a 0-5 ppm range . CO concentrations were measured on a 0-10 ppm range . CO 2 

### concentrations were measured on a 0-10% range . O 2 

### concentrations were measured on a 0-20% range . The measured concentrations are averaged 

## over each sampling period , then corrected for system bias and analyzer drift

. The drift and bias corrected result were then used to calculate emissions in units required by the permit including ppm , ppm corrected to 15% O 2 , 

### pounds per hour, and pounds per million standard cubic feet of natural gas . 

## 3.2 NH3 

## BY SCAQMD METHOD 

## 207.1 Duplicate flue gas samples were collected non-isokinetically at each test condition using SCAQMO Method 207
. 1
. A 12-point traverse was performed during each NH 3 slip test
. The sample gas is drawn through a glass probe, Teflon sample line , two impingers each containing approximately 100 ml of 0
. 1 N H 2 

### S0 4 , 

### an empty impinger , an impinger containing silica gel , and a dry gas meter
. The optional nozzle and filter were not used since the units are natural gas fired

. The contents of the probe , sample line and the first three impingers are recovered and analyzed by SCAQMO Method 207
. 1 for ammonia concentration using the Ion Selective Electrode technique

. One reagent blank sample, one 01 water sample , and one field blank sample was analyzed

. Ammonia slip is reported in units of ppm , corrected to 15% O 2 . 

### The tests were performed 

## over a period of at least 60 minutes

. 

## 3
. 3 SOx 

## BY SCAQMD METHOD 

## 307.91 Oxides of sulfur were measured using SCAQMO Method 307-91
. Two fuel samples were collected in Tedlar bags and sent to Saybolt Laboratory for sulfur analysis as total reduced sulfur as H 2 

### S

. 

## 3.4 ROG 

## BY MODIFIED SCAQMD METHOD 

## 25.3 Sampling and analyses are performed using Modified SCAQMO Method 25
. 3 procedures. The sample apparatus and analyses are provided by Atmospheric Analysis and Consulting (MC) in Ventura California

. At each test condition , two (one paired sample , consist of 2 canisters) flue gas samples are extracted simultaneously from four points (one per port) in the stack through pre-cleaned (high temperature conditioned) stainless steel probes connected to an outof-stack flow controller, into stainless steel Summa polished canisters

. The flow controller is set to fill the evacuated canister to a pressure of -400 mm Hg 

## over a period of a period of one hour

.

R0410673 11

## Modifications to the Method 25
. 3 sampling procedures suggested or accepted by SCAQMD are :
• Elimination of the in-stack filter • Elimination of the water vial portion of the 25
. 3 equipment • The final pressure in the Summa Canisters is maintained at between 400 and 500 mm HG (10 -14 in

. Hg) absolute

. Figure 3 - 1 presents a schematic drawing of the sample apparatus
. 

## FIGURE 3-1 MODIFIED SCAQMD METHOD 25.3 SAMPLING APPARATUS

Fil te r Pro be F lex Lin e
Flow Controlle r



## R0410673 12 

# Della /').

. '"_
.........

# , -

## The samples are analyzed for NMNEOC (Non-Methane Non-Ethane Organic Compounds , i

. e. Reactive Organic Compounds ROG) using modified SCAQMD Method 25
. 3 TCA procedures

. Analysis consists of a fore-flush and back-flush of a gas chromatography (GC) column , followed by an oxidizer , a methanizer , and a flame ionization detector (FlO). The GC separates the NMNEOC from other constituents of the sample (methane , ethane , CO 2 , 

## H 2 

## 0, O 2 , 

## N 2 , 

## etc.)

. The oxidizer converts the NMNEOC to carbon dioxide. The methanizer converts the resulting CO 2 

## to methane

. The methane content is detected by the FlO as ppm carbon. Modifications suggested by SCAQMD to the Method 25.3 analytical procedures approved for MC under the lAP are: • Pressurization of the canisters to 900 mm Hg with Ultra High Purity (UHP) helium analyzed/certified to contain less than 0
. 05 ppmv of total hydrocarbons as carbon • Analyzing only the Summa canister fraction of the normal 25
. 3 sample

. No water vial used in sampling , no water vial analysis

. • Utilization of a larger 

## (-2 ml) sampling loop • Development of a custom low level (0

. 1 - 5.0 ppmV propane) calibration curve • Performance of a Minimum Detection Limit (MOL) study • Determination of a Practical Quantitation Limit (PQl) from the MOL study Results are reported in parts per million by volume as carbon to 2 significant digits , corrected to 15% O 2 

## using the O 2 

## from the CEM measurements
. The average of the results for the duplicate samples is compared to the Emission Standard for determination of the compliance status
. Detailed procedures from SCAQMD concerning the application of the modified SCAQMD Method 25
. 3 to perm i t condition 029.1 are located in the test plan in Appendix H

.



## R0410673 

## 13

## 3.5 PM BY SCAQMD METHOD 5.1 Particulate matter was measured using SCAQMD Method 5.1. SCAOMD Method 5
. 1 is cited as the table in Condition D29.1 lists District Method 5. District Method 5
. 1 measures total particulate. This total particulate measurement could include material >10 microns

. Use of the cyclone as in 201A prevents overstating of PM 10 

## emissions if all of the PM emissions from these units are not PM 1O . 

## It was assumed for reporting purposes that the SCAOMD Method 5
. 1 total PM results will be used to determine PM 10 

## compliance. A single test was required to be performed at each of the three conditions ; 100% , 75%, and 50% load conditions. Triplicate tests were performed at the 100% load condition to ensure sufficient data were collected. All results are included in the average result. Flue gas is drawn through a stainless steel nozzle, glass or stainless steel probe, unheated Teflon line followed by four impingers. Impingers #1 and #2 contain approximately 100 ml of deionized water , impinger #3 is empty , and impinger 

## #4 contains silica gel. A backup filter is placed between impingers #3 and 

## #4
. The sample was collected isokinetically (90 - 110%) using a 24-point traverse at the exhaust stack location

. Each point was sampled for 10 minutes resulting in a 240 minute sample time pertest. Figure 3-3 presents a diagram of the sampling system
.

R041 0673 14

## FIGURE 

## 3-3 SCAQMD METHOD 5.1 SAMPLE SYSTEM

Temperature

Sensor Probe

# ~

PijotTube Connecting Tef lon Tubing 

### Filter Temperature 

### " Sensor 

# : - ------- - impCngers**~** 

# --- , Nozzle

# "..~~~~ / S· T ype Pitot Tube
Manometer



### Orifice

R0410673 Temperature Water 

### Sensors



## Dry Gas

Meter



## 15 Empty Silica Gel 

### Vacuum Line



# Della /'-,. """""''"''''-, -

## 4 .0 RESULTS The test results are presented in the following tables: Table 4-1 Table 4-2 Table 4-3 Table 4-4 Table 4-5 Table 4-6 Table 4-7 NO" CO, Ammonia (NH 3 ), 

## and ROG
- 100% load PM results - 100% load NO" CO, NH 3 , 

## and ROG
- 75% load PM results - 75% load NO" CO, NH 3 , 

## and ROG
- 50% load PM results - 50% load 

## SO, results Additional test runs were performed for some parameters to ensure that sufficient valid data were collected. Table 3-1 contains a test matrix with this information. Additional data is presented in the Appendices, including all field data, laboratory data, and calculations.

R0410673 16

### TABLE 4-1 COMPLIANCE TEST RESULTS CPV SENTINEL ENERGY PROJECT SENTINEL UNIT 2 NO

.. CO, NH 3, AND ROG 100% LOAD JANUARY 30, 2013 Test Number Run 1 Run 2 Average Limit Condition 103 MW 103 MW Test Date 1/30/2013 1/30/2013 Star! Time 11 :01 13: 11 Stop Time 12:17 15 : 05 Fuel Flow , hscfh 8,438 8,434 Stack Flow Rate , dscfm 339,745 344 , 040 Stack 

## 0, (%) 12
. 98 12
. 97 12
. 98 Stack NO. (ppm) 

## @ 15% 

## 0, 2.49 2.25 2.37 2.5 Stack NO. (lb/MMscf) 9.78 8
. 98 9.38 12.26(') Stack CO (ppm) 

## @ 15% 

## 0, 2.21 1
. 58 1.89 4 Moisture Fraction (%) 0.104 0.103 PPM NH3 (flue gas) 1.87 2.19 2.03 PPM NH 3 

## @ 15% 

## 0, 1.39 1.63 1.51 5 Ib/hr NH, 1.70 202 1.86 Ib/MMscf fuel NH, 2.02 240 2.21 Stack ROG(1), ppm 

## @ 15% 

## 0, 0
. 75 0.75 2.0 1) Collected as a simultaneous pair. 

### 2) The 12
. 26 Ib/MMscf is a RECLAIM emission factor, not a limit. 3) Higher ROG result shown of pair. RDP was 23.9%. Lower ROG result was 0.46 ppm @ 

### 15% 0,
.

R041 0673 

### 17

### TABLE 4-2 COMPLIANCE TEST RESULTS CPV SENTINEL ENERGY PROJECT SENTINEL UNIT 2 PM -100% LOAD JANUARY 30-31, 2013 Test Number S-2/STK-PM-100-1 S-2/STK-PM-100-2 S-2/STK-PM-100-3 Average Lim it Condition 103 MW 100 MW 100 MW Test Date 1/30/2013 1/30/2013 1/31/2013 

### Start Time 9:26 13:45 8 : 33 Stop Time 13:34 17:51 1239 Fuel Flow, hscfh 8,459 8,239 8,260 Stack Flow Rate , dscfm 366,608 352,398 368,538 Stack 0" % 13.07 13.24 13.08 Stack CO" % 4.42 4
. 34 4.42 Moisture Fraction , % 0
. 103 0.096 0.103 Particulate Emissions Grain Loading, gr/dscf 0.0003 0.0002 0
. 0002 0
. 0002 Grain Loading 

### @ 3% 

## 0, 0.0007 0
. 0004 0.0005 0.0005 0.01 Grain Loading 

### @ 15% 

## 0, 0
. 0002 0.0001 0.0002 0
. 0002 Grain Loading 

### @ 12% 

### CO, 0.0009 0.0005 0
. 0006 0.0007 0.1 Mass Emissions, Ib/hr 1.02 0.54 0.67 0.75 11 (1) 

### Emission Rate, Ib/MMscf 1.21 0.66 0.82 0.89 5
. 71(') (1 ) 11 

### Ib/hr PM limit from SCAQMD Rule 475. 

### (2) This is stated in the permit as an emiss ion factor.

R0410673 18 

# Oelta t-..

.. 0..0.>-"
. , ... ..,......

### TABLE 4-3 COMPLIANCE TEST RESULTS CPVSENTINELENERGYPROJECT SENTINEL UNIT 2 NO" CO, NH 3 , 

### AND ROG 75% LOAD FEBRUARY 1, 2013 Test Number Run 1 Run 2 Average Limit Condition 80MW 80MW Test Date 

### 2/1/2013 2/1/2013 Start Time 9:10 11 :05 Stop Time 10:34 12 : 15 Fuel Flow, hscfh 6 , 912 6,936 Stack Flow Rate, dscfm 306,797 301 , 392 Stack 

## 0, (%) 13.47 13.32 13
. 39 

### Stack NO x 

### (ppm) 

## @ 15% 

## 0, 2.27 2.16 2.22 2.5 Stack NO x 

### (lbIMMscf) 9.23 8.78 9.01 

## 12,26 1 ') 

### Stack CO (ppm) 

## @ 15% 

## 0, 0.38 0.67 0.52 4 Moisture Fraction (%) 0.093 0.101 PPM NH3 (flue gas) 1.20 1
. 29 1
. 25 

### PPM NH 3 

### @ 

### 15% 

## 0, 0.95 1.00 0.98 5 

### Ib/hr NH3 099 1
. 05 1
. 02 Ib/MMscf fuel NH3 1.43 1.51 1.47 

### Stack ROG I1 ), 

### ppm 

## @ 15% 

## 0, 0.55 0.55 2.0 1) Collected as a simultaneous pair. 2) The 12.26 Ib/MMscf is a RECLAIM emission factor, not a limit.

R0410673 19

### Test Number Condition Test Date Start Time Stop Time Fuel Flow, hscfh Stack Flow Rate, dscfm Stack 

## 0" % Stack CO" % Moisture Fraction, % Particulate Emissions Grain Loading, gr/dscf 

### Grain Loading 

## @ 3% 

## 0, Grain Loading 

## @ 15% 

## 0, TABLE 4-4 COMPLIANCE TEST RESULTS CPV SENTINEL ENERGY PROJECT SENTINEL UNIT 2

PM -75% LOAD FEBRUARY 1, 2013 S-2/STK-PM-75-1 80MW 2/1/2013

8:11 13:22 6,923 314,715

13.35 4
. 26 0.090

0.0002 

### 0.0004 0
. 0001 Average

0.0002 

### 0.0004 0.0001 

### Grain Loading @ 

### 12% 

## CO, 0.0005 0.0005 Mass Emissions, Ib/hr 0.49 0.49 Emission Rate, Ib/MMscf 0.71 0.71 (1) 11 Ib/hr PM limit from SCAQMD Rule 475. (2) 

### This is stated in the permit as an emission factor.

R041 0673 20 Limit



### 0.01

0.1 11 (1) 

### 5.71(2)

### TABLE 4-5 COMPLIANCE TEST RESULTS CPV SENTINEL ENERGY PROJECT SENTINEL UNIT 2 NO., CO, NH 3 , 

### AND ROG 50% LOAD FEBRUARY 1, 2013 Test Number Run 1 Run 2 Average Limit Condition 55MW 56MW Test Date 2/1/2013 2/1/2013 

### Start Time 14:20 15 : 53 Stop T i me 15:35 17:09 Fuel Flow , hscfh 5 , 361 5 , 391 Stack Flow Rate , dscfm 282 ,277 278 , 356 Stack 

## 0, (% ) 14
. 38 14.36 14.37 Stack NO, (ppm) 

## @ 15% 

## 0, 1.99 2.05 2.02 2
. 5 Stack NO, (lb/MMSCF) 8
.44 8.52 8.48 12.26 1 ') 

### Stack CO (ppm) 

## @ 15% 

## 0, 0.23 0.27 0.25 4 Moisture Fraction (%) 0.092 0.095 PPM 

### NH3 (flue gas) 0.72 0
. 89 0
. 81 PPM NH, 

## @ 15% 

## 0, 0.65 0.81 0.73 5 Ib/hr NH3 0.55 0.67 0
. 61 Ib/ MMscf fuel NH3 1
. 02 1.24 1.13 Stack ROG I1 ), 

### ppm 

## @ 15% 

## 0, 0.68 0
. 68 2.0 1) Collected as a s i multaneous pa i r . 

### 2) 

### The 1 2.26 

### Ib/ MMscf is a RECLAIM emission factor , not a limit.

R0410673 21 

# Delta l1



# .. """"'

........ , 

### ...

# _ .....

### TABLE 4-6 COMPLIANCE TEST RESULTS CPV SENTINEL ENERGY PROJECT SENTINEL UNIT 2

PM -50% LOAD FEBRUARY 1, 2013 Test Number S-2/STK-PM-50-1 Average Limit Condition 55MW Test Date 

### 2/1/2013 Start Time 14:14 Stop Time 18:25 Fuel Flow, hscfh 5 , 373 Stack Flow Rate, dscfm 292,783 Stack 

## 0" % 14.29 Stack CO" % 3.80 Moisture Fraction , % 0
. 075 Particulate Emiss ions Grain Loading , gr/dscf 0
. 0002 0.0002 

### Grain Loading 

## @ 3% 

## 0, 0.0005 0.0005 0.01 Grain Loading 

## @ 15% 

## 0, 0.0001 0.0001 

### Grain Loading 

## @ 12% 

## CO, 0.0005 0.0005 0.1 Mass Emissions, Ib/hr 0.42 0.42 11 (1) 

### Emission Rate, Ib/MMscf 0.78 0.78 

## 5.71 1 ') 

### (1) 11 Ib/hr PM limit from SCAQMD Rule 475
. (2) This is stated in the permit as an emission factor.



### R0410673 22

### R041 0673 

### Test Number Condition Test Date SO,, Ib/MMBtu gr H,S/100 scI 

## TABLE 4-7 COMPLIANCE TEST RESULTS CPV SENTINEL ENERGY PROJECT SENTINEL UNIT 2 SOx FROM FUEL ANALYSIS FEBRUARY 1, 2013 Average 101 MW 

### 2/1/2013 0.00003

0.013 

### Limit

0.06
(1) 0.25 gr 

### H,S/100 scf sulfur content limit is based on annual average of monthly sample results.



## 23

## 5.0 DISCUSSION AND TEST CRIT I QUE Testing was conducted according to the test plan and reference methods

. All tests demonstrated compliance with the permit limits. The 

## following should be noted:
• Two runs were conducted for NOx 

## and CO at each condition to ensure that sufficient valid data were collected. • The 

## ROG test at 100% l oad did not meet the relative percent difference (RDP) criteria specified i n SCAQMD Method 25.3 for duplicate canisters

. The RDP for this test was 23
. 9% with the criteria being less than 20%
. • One run was not detected and reported at the PQL 

## level. It is not stated if the SCAQMD 25.3 criteria for RDP apply to the procedures accepted for modified Method 25.3 approved in the test plan

. Each canister separately met the permit limit of 2.0 ppm @ 15% O 2 . 

## The higher ROG result was 0
. 75 ppm 

## @ 15% O 2 . 

## The lower ROG result was 0.46 ppm 

## @ 15% O 2 . 

## The higher of the two results is presented in Tables 1-1 and Table 4-1.

R0410673 24 

# Della /}. 

# "'_

... , 

# ..

# _ ....

## APPEND I X A QUALITY ASSURANCE

R041 0673 

## A-1 

# Oe/ta i"J. """"""<" ' "'-

## Appendix A . 1 Quality Assurance Program Summary

R0410673 A-2 

# Del/a t...
..

# _ ......... ............

## QUALITY ASSURANCE PROGRAM SUMMARY 

## Delta Air Quality Services , Inc. is committed to providing emission related data which is complete , precise , accurate , representative , and comparable

. Delta's quality assurance program and procedures are designed to ensure that the data meet or exceed the requirements of each test method for each of these items

. The quality assurance program consists of the following items :
• Assignment of an Internal QA 

## Officer • Development and use of an internal QA Manual • Personnel training • Equipment maintenance and calibration • Knowledge of current test methods • Chain-of-custody • QA reviews of test programs Assignment of an Internal QA Officer : Delta has assigned an internal QA Officer who is responsible for administering all aspects of the QA program. Internal Quality Assurance Manual : Delta has prepared a QA Manual according to the guidelines issued by EPA. The manual documents and formalizes all of Delta's QA efforts. The manual is a " liv i ng" document which is revised as Delta adds capabilities and procedures. The QA manual provides details on the items provided in this summary. Personnel Training: Personnel training is essential to the production of high quality test results

. Delta ' s training programs include : • A requirement for all technical personnel to read and understand the test methods performed • A requirement for all technical personnel to read and understand the Delta QA manual • In-house training • Quality Assurance meetings • Attendance at EPA sponsored training courses • Maintenance of training records

. Equipment Maintenance and Calibration: All laboratory and field equipment used as a part of Delta's emission measurement programs is maintained according to manufacturer's recommendations

. A summary of the major equipment maintenance schedules is summarized in Table A-i. In addition to routine maintenance , calibrations are performed on all sampling equipment according to the procedures outlined in the applicable test method

. The calibration intervals and techniques for major equipment components is summarized in Table A-2

. Knowledge of Current Test Methods : Delta maintains current copies of EPA , ARB , and SCAQMD Source Test Manuals and Rules and Regulations

. Delta personnel coordinate , attend , and present papers at emission testing related conferences

. Delta personnel maintain memberships in the Air and Waste Management Association and Source

R0410673 A-3

## Evaluation Society. Delta personnel continually work with industry and regulatory agencies in monitoring and developing new methods and rules. Chain-of-Custody: Delta maintains chain - of-custody documentation on all 

## data sheets and samples

. Samples are stored in a locked area accessible only to Delta source test personnel. Data sheets are kept in the custody of the originator , program manager , or in locked storage until return to Delta ' s office. Upon return to the office , copies are made and stored in a locking file. The original data sheets are used for report preparation and any additions are initialed and dated. QA Reviews : Every Delta report is reviewed by someone separate from the report author

. The reviewer is selected based on knowledge of the test methods used and the source tested

. Periodic field, laboratory , and report reviews are performed by the QA Officer. Test plans are reviewed to ensure proper test methods are selected and reports are reviewed to ensure that the methods were followed and any deviations from the methods are justified and documented

.

R0410673 A-4

## TABLE A-1 EQUIPMENT MAINTENANCE SCHEDULE Equipment Acceptance Limits Frequency of Service Methods of Service Pumps 1. Absence of leaks Every 500 hours of 1
. Visual inspection 2
. Ability to draw operation or 6 months, 2. Clean manufacturers whichever is less 3. Replace parts required vacuum 4. Leak check and flow Flow Meters 1. Free mechanical Every 500 hours of 1. Visual inspection movement operation or 6 months, 2. Clean whichever is less 3
. Calibrate Sampling Instruments 1. Absence of As recommended by As recommended by malfunction manufacturer manufacturer 2. Proper response to zero , span gas Integrated sampling 1
. Absence of leaks Depends on nature of 1. Steam clean tanks use 2. Leak check Mobile van sampling 1
. Absence of leaks Depends on nature of 1. Change filters system use 2. Change gas dryer 3. Leak check 4. Check for system contamination Sampling lines 1
. Sample After each test series 1. Blow dry, inert gas degradation less through line until than 2% dry.

R0410673 A-5 

# Oelta l1

.. 

# - ..

## TABLE A-2 MAJOR SAMPLING EQUIPMENT CALIBRATION REQUIREMENTS Sampling Equipment Cal i bration Frequency Calibration Procedure 

### Acceptable C al i bration 

### Criteria Continuous Analyzers Before and after each 

### 3-point calibration error < 

### 2 % 

### of analyzer range 

### test day test 

### Continuous Analyzers Before and after each 2-point sample system < 

### 5% 

### of analyzer range 

### test run bias check Continuous Analyzers After each test run 2-point analyzer drift < 

### 3% of 

### analyzer range 

### determination CEMS System Beginning of each day leak check < 

### 1 in

. Hg decrease in 5 min

. at > 20 in

. Hg Continuous Analyzers 

### Daily 3-point linearity < 

### 1

### % of analyzer range NO , Analyzer Da i ly 

### N0 2 -> 

### NO converter > 

### 90 % 

### effic iency S-type pitot tube Sem i-annually 

### Dimensional calibration Meet dimensional cr iter i a of Method 2 S-type pitot tube Annually Wind tunnel calibration Defined in Method 2
S
- type pitot tube Prior to each project 

### Visual inspection Meet dimensional crite r ia of Method 2 Differential Pressure 

### Semi
- annually Correction factor based +/- 

### 5 % 

### Gauges ( except for 

### on 5-point comparison to manometers) 

### standard Different ial Pressure 

### Bi - month l y 

### 3-po int comparison to +/- 5 % 

### Gauges (except for 

### standard , no correction manometers) 

### factor 

### Man o meter Semi-annually Clean and replace flu i d Barometer 

### Semi-annually Adjusted to mercury - in- +/- 0
. 1 i nches Hg glass or National Weather Service Station Dry gas meter Semi
- annually Calibration check at 4 +/- 2% 

### flow rates using a N 1ST

traceable standard Dry gas meter Bi-monthly Calibration check at 2 +/- 

### 2 % 

### of semi-annual flow rates using a N 1ST factor

traceable standard Dry gas meter orifice Annually 4-point calibration for IIH@ Temperature sensors 

### Sem i- annually 

### 3- point calibration vs . +/- 1
. 5 % NIST traceable standard



### R041 0673 A-6

## Appendix A.2 SCAQMD and CARB Certifications

R0410673 A-7 

# Delta /1 "'0.-, ......... __

# South Coast Air Quality Management District 21865 Copley Drive, Diamond Bar, CA 91765-4178 (909) 396-2000 • www.aqmd.gov



## Mr. 

## Robert A. 

## Finken Delta Air Quality Services, Inc. 1845 N
. Case 

## Street Orange, CA 92865 Subject: LAP Approval Notice Reference # 96LAI220 Dear Mr. 

## Finken: January 11, 2012

We completed our review of the renewal application you submitted for approval under the South Coast Air 

## Quality Management District's Laboratory Approval Program (AQMD 

## LAP). We are pleased to inform you that your firm 

## is approved for the period beginning January 31, 2012, and ending January 31, 2013 for the following methods : SCAQMD Methods 1-4 SCAQMD Method 100.1 SCAQMD Methods 25.1 and 25.3 (Sampling) SCAQMD Methods 5.1, 5
.2, 5.3, and 6.1 SCAQMD Rule 1420

- (Lead) Ambient Sampling USEPA CTM-030 and ASTM D6522-00 Thank you for participating in the SCAQMD LAP. Your cooperation helps us to achieve the goal ofthe LAP: to maintain high standards of quality in the sampling and analysis of source emissions. You may direct any questions or information to 

## LAP Coordinator, Glenn Kasai. He may be reached by telephone at (909) 396-2271, by facsimilie at (909) 396-2099, or via e-mail at gkasai@aqrnd.gov
.

RE:GKlgk 

## cc: Mike 

## Garibay Glenn Kasai 120111 LapRenewaJ
.doc . 't' '' ,. ,

# ~nr/,y**~** ___ _ ;/ Ru Eden, Senior Manager Laboratory Services & 

## Source Test Engineering

# South Coast Air Quality Management District 21865 Copley Drive , Diamond Bar, CA 91765-4178 (909) 396-2000 • www.aqmd.gov


## December 19,2012
Mr. Robert A. Finken Delta Air Quality Services, Inc. 1845 N. Case Street Orange, CA 92865 Subject: LAP Approval Notice Reference # 96LA 1220
Dear Mr. Finken: We completed our review of the renewal application you submitted for approval under the South Coast Air Quality Management District's Laboratory Approval Program (AQMD LAP). We are pleased to inform you that your firm is approved for the period beginning January 31, 2013 , and ending January 31, 2014 for the following methods, subject to the requirements in the LAP Conditions For Approval Agreement and conditions listed in the attachment to this letter: SCAQMD Methods 1-4 SCAQMD Method 100.1 SCAQMD Methods 25.1 and 25.3 (Sampling) SCAQMD Methods 5.1 , 5.2 , 5.3 , and 6.1 SCAQMD Rule 1420

- (Lead) Ambient Sampling US EPA CTM-030 and ASTM D6522-00 Thank you for participating in the SCAQMD LAP
. Your cooperation helps us to achieve the goal of the LAP : to maintain high standards of quality in the sampling and analysis of source emissions. You may direct any questions or information to LAP Coordinator, Glenn Kasai. He may be reached by telephone at (909) 396-2271, by facsimilie at (909) 396-2099, or via e-mail at gkasai@aqmd.gov.

RE : GKlg k


### cc : Mike Garibay Glenn Kasai 121218 LapRenewal.doc

# ~ R,dy po"

# s,,~ Laboratory Services & 

## Source Test Engineering

# State of California 

# Air Resources Board Approved Independent Contractor Delta Air Quality**Servic~~** 

# Incorporated

, . , 

# This is to certify thitt the company'Jisted above has been approved by the AirHesources Board 

# to**conduCt:pom~pl\ance** 

# testing pursuant to titleH7, Catifomla**Coqe 6fR~gu1ations.**  

# section 91207 until June 30, 2013, for**thO~e** 

# test metnoUs 

# Ii$ted below:**~:** il



## . ARB 

# sliurce Test

# M~th"ods:**1~ 2,**  

## 3, 4,"5, 6, 'S, 17, 20,sqt 100 '(CQ. CO2, NO
.. O,.l. S02)

.**~** ,


## Alberto**Aya~,** 

## PhD., M

. S.E. Chief, Monitoring and Laboratory Division

# State of California 

# Air Resources Board
Delta**A)W1f~JifY ~e!v.i.~~** **}' IR~~tPora**  

# This is to f'ArHhlftH":::If

. 

# by the**pursuan~** 

# to**~i~~IT ~i** **sa~**



# until

# JU!1~**2q> J'il** **2tY1 :~** 



# u.s. n approved testing section 91207

# 1;l~**I, ~~~~~<f** **r~j~d** below:**~** •. " 7/./0, 

# I, "T! I. I

### .L\I~**:~1}" l**  

## version)

Alberto Ayala, 9fl.D., M.S.E. Chief, Monitoring and Laboratory Division

## Appendix A.3 Equipment Ca l ibration and Calibration Gas Certificates



## R0410673 A-8 

# Delta j'j,

......... _,"" --"Ofifice Method· T riplicate RunsIFour Calibration Po i nts Engtish Meter Bo)( Units , English K' Factor SEMI · ANNUAL DRY GAS M ETER/O RIFICE CALIBRATION

Filename ' F '\compdat!l\Oe1ta P1.Iblic\CatibraMns\MelefS\19-wcs12012\[Semi · Annual Meier Calibration 19 wcs 1()'2S·12

. )(\sjWCS MO<IeI #
. 10 , Dale '**~5000** 19·wcs 1012512012 File Modified From

. APEX 522 Series Meter box**Cal bra~on**  Revised : 418/2005

Volume Volume dH Time Initial Fina l (in H2O) (m in) {cu ttl (cu tt) 0
. 13 26.00 351.800 357,170 0
. 13 26,00 357.170 362
. 550 0
. 1 3 26
.00 362
. 550 367
. 942 066 12,00 367
. 942 373 .42 5 066 12 ,00 373. 425 378
.895 066 12
.00 378
. 895 384,378 1
. 90 7
. 00 384
. 378 389
.855 1
. 90 7
. 00 389.855 395340 190 7
. 00 395
. 340 4 00
.829 3
. 70 5
. 00 "00

.829 4 06
. 200 3
.70 5
.00 "06.200 411.586 3
. 70 500 ""

. 586 416995

METER ORIFICE VOLUME VOLUME VOLUM E CORRECTED CORRECTED CORRECTED

Vm(std) Vm(std) Vcr (sld)



# w" l iters (cu ttl 5,406 153
. 1 5
. 265 5,400 152
. 9 5 , 265 5 , 397 152.8 5
. 265

5.479 155
. 2 5.422 5459 154
. 6 5.419 5
.469 154
. 9 5.4 17

5
.472 155
. 0 5
. 369 5
.470 1 54
. 9 5
. 369 5
.466 154
. 6 5.367

5
. 367 152
.0 5
. 338 5372 152
. 1 5.336 5387 152
.6 5338

SIGNED S ig na ture on File Bar

. Pressure : 29
.65 Performed By : G
. Bridge Meter Senal # ; DRY GAS METER READINGS CRITICAL ORIFICE READINGS Volume Initial Temps

. Final Temps. Orifice K' Orifice Actual Total Inlet Outlet Inle l Outlet Seri al# Coefficien l Vacuum ('" ') (deg F) (deg F) (deg F) (deg F) (number) (see above) (in Hg) 5,370 63
. 0 62
.0 65
. 0 63
. 0 33 0
. 1553 26
. 0 5.380 65
. 0 63
.0 67
. 0 64
. 0 33 0
. 1553 26
. 0 5
. 392 67,0 64
.0 68
. 0 66
. 0 33 01553 26.0 5.483 68
. 0 66.0 70.0 67.0 

# " 0
. 3465 22,5 5470 70,0 67
. 0 70.0 67
. 0 

### I 

# " 0
. 3465 22,5 5483 70
. 0 67
.0 70
. 0 68
. 0 

# " 0
. 3465 22 , 5 5477 70.0 68
.0 72.0 68.0 

# " 0
. 5888 19
. 5 5485 72.0 68
. 0 73
. 0 69
. 0 

# " 0
. 5888 19
. 5 5489 73
.0 69
. 0 7 "

. 0 69.0 63 0
. 5888 195 5371 7" 69
. 0 750 69
. 0 73 0
. 8202 17
.0 5386 750 69.0 77
. 0 70
.0 73 0
. 8202 17
.0 5.4()9 77.0 70
. 0 77
. 0 70
.0 

### I 73 08202 17
. 0

DRY GAS METER ORIFICE CALIBRATION FACTOR CALIBRATION FACTOR Individual VOLUME VOLUME Roo CORRECTED NOMINAL Y dH@

Vcr(std) Vee Value Value 0
.95 < Y

liters 

# '" 

# " (number) in H2O < 1
. 05? 1491 52 4 0 1
. 798 Pass 149
. 1 5,2 4 0 1
. 794 Pus 149
. 1 5 , 24 0 1 .789 Pass Average 1.794 1536 5396 0990 1.819 P 1535 5398 0 ,993 1,619 Pass 1 534 5
. 401 0
.990 1 ,619 P ass Average 0.991 1 .8 1 9 152
. 1 53" 0981 1
.812 P 1521 53" 0982 1
.610 Pass 1520 5
. 356 0
.982 1
.610 Pass Average 0 .9 82 1
. 811 1512 5332 0
. 995 1
. 819 P 1512 5332 0
. 994 1
. 817 Pass 1512 5332 0991 1
. 815 Pass**'---'AO ~'"';;;;ge**  Vd: 0.985 dH@:1.810 Q@dH=I : 0
. 557 Date 1012512012 (In. Hg)

Initial (deg F) 64
. 0 6 4 ,0 64.0 64
. 0 64.0 65.0 65
. 0 65.0 65
. 0 66
. 0 66
. 0 66
.0

Individual

OrifICe Ym ax ·Ymin

< 0.010?

Pas s

Pass

Pass Ambient Temperature Fin al Average (d'9 ') (d'9 ') 64
. 0 64
. 0 64.0 64
. 0 64
. 0 64
. 0 64 .0 640 65 .0 64
. 5 65
.0 65
.0 65.0 650 65.0 650 66
. 0 655 66
.0 660 66.0 660 66
. 0 660

Orifice Ofifice Average Average 0.98 < YrYd dH@ · dH@av

< I.on < 0
. 155?

Pass Pass

Pass Pass

Pass Pas s**Sem~Anooa l**  MeIer Calibfalloo 19 we i 10 · 25 · 12 WCS 211912013 157 PMOrifice Method - Triplicate RunsIFour Calibration Points English Meter Box Units , English K' Factor SEMI · ANNUAL DRY GAS METER/ORIF I CE CALIBRATION

Model # : 10# : Filel"lilme : F \compdata\Oelta Public\CalibratiooslMeters\9-P&M\2012I{Semi-Annual Meter Calibration -9-pm 9-21-12.xlsIWCS Dale : 9P&M 912112012 File Modified From ' APEX 522 Series Meter box Calibr ation Revised : 41812005

Volume Volume dH Time Initial Final in H2O} (min) {cu ttl (cu 11) 0. 14 2600 383 ,4 00 388
. 805 0
. 14 26
. 00 38 8,805 394
. 205 0
. 14 26
. 00 394 ,205 399
.6 15 0
. 64 12
. 00 350,820 356
. 2 70 0
. 64 12
. 00 356 ,270 361
. 730 0
. 64 1200 361,730 367 .175 1
. 90 700 367
. 175 372
. 585 190 700 372
. 585 377.990 190 7
.00 377 990 383.400 3
.70 5
.00 334.700 340
. 065 3
. 70 500 340.065 345.430 370 500 345
. 4 30 350 810

DRY GAS M ETER VOLUME VOLUME VOLUM E CORRECTED CORRECTED CORRECTED

Vm(sld) Vm(std) Vcr(std) (cu tt) li ters) (eu 11) 5
. 269 1492 5.176 5.254 148 ,8 5
. 171 5.254 148.6 5 .1 67
5,354 1516 5
. 343 5.359 151
. 8 5.340 5334 1511 5
. 335

5
. 311 150.4 5
. 286 53<12 lSO

. 1 5
. 284 53<12 1SO 1 5.28 1

5
. 330 1510 5277 5320 lSO

. 7 5
. 274 5
.330 1510 5274

SIGNED : Signature on File Bar

. Pressure

. Performed By: 29
. 72 {in. H9} M

. Edmondson

DRY GAS METER READINGS CRITICAL ORIFICE READINGS Volume I nllial Temps Final Temps Orifice K' Orifice Actual Total Inlet Outlel Inlel Outlet Serial # Coefficient Vacuum Initial 

## "''' Idea Fl dea F) (dea F) (de<! F) {number (see above) i n Ha) (dea F) 5.405 78
. 0 770 79
. 0 78 ,0 33 0,1553 23.0 770 5.400 79,0 78
. 0 80
. 0 79,0 33 0,1553 23.0 78,0 5
. 410 80,0 790 8 1 .0 80,0 33 0
. 1553 23
.0 79,0 5.450 75 ,0 74
. 0 75.0 74,0 

# " 0.3465 20.0 75,0 5.460 

### I 750 74
. 0 76
. 0 75,0 

### I 

# " 0,3465 20
. 0 75 ,0 5
.445 76
.0 750 770 76,0 48 0,3465 200 76.0 5 .41 0 770 76
. 0 77.0 760 

### I 63 05888 17
.0 77.0 5.405 77
. 0 76
. 0 78.0 77
.0 63 0
. 5888 17
.0 77.0 5410 78
. 0 770 78
. 0 77.0 63 0
. 5888 170 78
.0 5
. 365 720 720 73
.0 730 73 0
.8202 150 73.0 5
. 365 730 730 740 740 73 0
. 8202 15
. 0 740 5380 74
. 0 740 740 74
. 0 73 08202 15
. 0 74.0
ORIFICE DRY GAS METER ORIFICE CALlBRATlON FACTOR CALlBRATION FACTOR Individual Individu al VOLUME VOLUME Roo Orifice CORRECTED NOMINA L Y dH@

VCf(std) Vcr Value Value 0,95 < Y Yma )( - Ymin

liters) i'" ") (number) (in H2O ) , < 1
. 05? < O,OI 0? 146
.6 5.307 0,982 1.939 Pass 1465 5,3 1 2 0
. 984 1.939 Pass 146
. 3 5
. 3 1 7 0.983 1.939 Pass Average 0
. 983 1
.939 P a ss 151
. 3 5452 0.998 1784 Pass 151
. 2 5455 0997 1,784 Pass 151 1 5.460 1.000 1,784 Pass Average 0.998 1 .18 4 Pass 1497 541 4 0
. 995 1.834 Pa ss 1496 5417 0997 1.834 Pass 1496 5 41 9 0996 1
. 834 Pass Averag4i! 0.996 1
. 834 Pass 1494 5
. 370 0990 1
.840 Pa ss 14g 4 5372 0
. 991 1.839 Pass 149
. 4 5
. 372 0990 1.837 P ass Average 0
. 990 1
.839 Pa ss Average Yd : 0.992 dH @: 1
. 849 Q@dH:l : 0
. 552 Date : 9121120 1 2 Ambient Temper ature Final Average (dea F) 

# "eo Fl 78 ,0 77.5 79.0 78.5 80
. 0 79
. 5 75
. 0 750 76.0 75,5 770 76,5 77.0 770 78
. 0 77.5 78
. 0 78,0 74.0 735 74.0 74
. 0 74.0 74
. 0

Orifice Onfice Average Average 0.98 < Yf'(d dH@-dH@av

< 1.02? < 0
. 1557

Pass Pas s

Pass Pas s

Pass Pass

Pass Pass**~mi·Armu.'** Me1e' C.l i b,,,ion**9·~m** 9· 21

- 12 WCS 2/19120 1 3 158 PMOrifice Method - Triplicate RunslFol1f Calibration PO i nts English Meier Box Units

. English K' Factor SEMI·ANNUAl DRY GAS METER/ORIFICE CALIBRATION

Mode l #
. lOti

. C5000 17WCS Filename

. F : lcompdata\Oelta Public\Calibrations\Meters\17-wcs\2012\jSeml-AAnual Metei' Calibration 9-19-12 WCSJds]WCS Date 911912012 file Mod ified From : APEX 522 Senes Meter box Calibration Bar. Pressure 29.79 (in. Hg) Revised : 4/812005 PerlOfl'ned By

. :;ARY BRIDGE

DRY GAS METER READINGS CRITICAL ORifiCE READINGS Volume Volume Volume Inilial Temps

. Final Temps Orifice K' Orifice Actual dH Time Initial Fina l Total Inlet Oullet Inlet**Ou~et** Serial# Coefficient Vacuum Initial (in H2O) (min) {eu ttl (eu ttl (eu ttl 

# "eo F) 

# "eo F) 

# "eo F) (deo F) (number) (see above) (in Hg) (deg F)

0 .1 1 26
. 00 368
. 900 374,275 

### I 5 ,375 74,0 73,0 

### I 74
. 0 73
. 0 33 0
. 1553 23,5 730 0
. 11 26,00 374
. 275 379
.658 5.383 74 ,0 73,0 77.0 75
. 0 33 0
. 1553 23 ,5 73,0 0
. 11 26,00 380
. 200 385 .5 81 5.381 77.0 75,0 77.0 75.0 33 0
. 1 553 23
. 5 73,0 0
. 55 12 ,00 389.200 394.650 5.450 73,0 730 74.0 73
.0 48 0
. 3465 200 74.0 0
. 55 1200 394.650 400
. 128 5478 74,0 73,0 75
. 0 7 4
. 0 

# " 0
. 3465 20 ,0 74.0 0
. 55 12
. 00 400
. 128 405 .593 5
. 465 75 ,0 74
.0 76
. 0 74
. 0 

# " 0
. 3465 20
.0 74
. 0 1
. 70 7
. 00 405 .593 411.028 5435 76.0 "0 77.0 75.0 

# " 0
. 5888 \65 74.0 1
. 70 7
. 00 411 .028 416.485 5457 77
.0 750 78.0 75.0 

# " 0
. 5888 16
. 5 74
.0 1.70 7
. 00 416
.485 421.937 5
. 452 760 75
. 0 79.0 76
.0 

# " 0
. 5888 '65 74
.0 3
. 30 500 421
. 937 427
. 253 5
. 316 790 760 81
. 0 76
.0 73 08202 13
.0 74.0 3
. 30 5
. 00 4 27
. 253 432.550 5.297 8" 760 82
.0 76.0 73 0
. 8202 13
.0 74.0 3
. 30 5
.00 432.550 437 .886 5336 820 76
. 0 83.0 77
.0 73 0
. 8202 13.0 74
.0

DRY GAS METER ORIFICE DRY GAS METER ORifiCE CALIBRATION FACTOR CALIBRATION fACTOR Individual Individual VOLUME VOLUME VOLUME VOLUME VOLUME Roo Orifice CORRECTED CORRECTED CORRECTED CORRECTED NOMINAL Y dH@

Vm(sld) Vm(s l d) Ver(std) Ver(std) V" Value Value 0
. 95" Y Ymax - Ymin (eu tt)

. ( l iters) (eu tt) ( l iters leu ttl number) (in H2O) < 1
.05? < O.O'O? 5
. 296 150
. 0 5,210 147,6 5285 0
. 984 1,520 Pass 5
. 291 149
. 8 5.2 1 0 147
. 6 5
. 285 0
. 985 1.517 Pass 5
. 277 149.4 5.208 14 7.5 5287 0.987 1,5 1 5 Pass Average 0.985 1 .517 Pass 5378 152
. 3 5.360 151
. 8 5447 0,997 1 529 Pass 5
. 398 152 ,9 5,360 151 8 5447 0993 1,528 Pass 5
. 378 1523 5.360 151 

### e 5447 0997 1,526 Pa ss Average 0.995 1.528 Pass 5
. 356 151 7 5
. 313 1505 5399 0
. 992 1632 PlISS 5
. 370 1521 5
. 313 1505 5.399 0.989 1631 Pass 5
.358 151
. 7 5
. 313 '505 5
. 399 0992 1629 Pass Averag4 0.991 1 .63 1 Pass 5
. 235 148
. 2 5 .287 1497 5
. 372 1 .010 1628 Pa ss 5209 147
. 5 5.28 7 1497 5 372 1
. 015 1
. 628 Pass 5
. 240 1484 52'" 1497 5375 '
. 006 1628 Pa ss Average 1
. 011 1
. 628 Pass 

## 1 ---- Average Yd: 0.996 dH @: 1 .5 76 Q@dH"l : 0.597 SIGNED Date

. Ambient Temperature Final Average (deg f) 

# "eo F) 73
. 0 73
. 0 73
. 0 730 74
. 0 73
. 5 74 .0 "0 74 .0 74
.0 74
. 0 74
. 0 74
. 0 7" 7 4
. 0 74
. 0 7 4
. 0 74
. 0 74.0 "0 74.0 7" 75
. 0 7 "

Orifice OrifICe Ave ra ge Averag e 0.98" YfYd dH@ -dH@ av

" 1

. 02?

Pass

P ass

Pass

P a ss .. 0, 155?

Pass

Pas s
i i
, Pas s ,

,
Pa ss**Sem~AMual** Mete r Ci l lbrilion 9·1 9-12 WCI WCS 211MQ13 t S6 PMStandard Pitot Tube Dimensional Calibration Record

A 

# -
, --- -- - 

### @ A M Stclion AA


# • 

# T

Tip ccep,al}l I Y

Criteria Yo; Y., 

# 0'. 

# ",. 0" ro. -0.101 M1 >6 01 M2 >8 01 Hemispherical, 90 · Bend with PitotlO Date Calibrated B Elliptical, or curved or mitered 01 02 

# ., .2 Ratio 02/01 601 801 Status Conical Tip unction 8 y Y 0.31 0.029 2
. 110 2.550 0.094 1.860 2.5 

### Pass

### 5 Type Pitot Tube Dimensional Calibration Record

Side View 

# ,L

# W f

# ~ M,

# ~ 1

= __ 

# --c 

# A B3t r

,
End View
Acceptability "3/16" < Dt <

Criteria z < 1/8" w < 1132" y" 3/8" nla nla nla nla nla

Side View , Side View ,

Impact Impact Pitot ID Date Calibrated By openings openings Pa: Pb Tub i ng Mt M2 M3 M4 M. Properly P roperl y Diameter, dt aligned, Z < aligned , w 1/8" < 1132 "
026 Y Y Y 0 .3 74 0.882 0.870 0
. 882 0.876 0 .437 --_. -

Reference "A Type -S Pilot Tube Calibration Study, Robert F

. Vollaro , October 15, 1975 If tube is not visibly deformed it is assumed that Pa = Pb = . 5 x avg . of M1 M2, and that average face opening plane angles represent individual angles to tube axis M
.

nla

M.

0.457 

# -+/ M, 

# r- 

# ;. §( P :b 

# t

- ,- M : M, Pa 

# • 1 

# -+1**~** Too View

1.0SDt<P<1

. S 10 degrees 5 degrees Dt Average Face Average Face Opening Plane Angle, offset Opening Plane from Frontal Angle Ratio of Pl Ot Status perpendic ular from parallel to to transverse Longitudinal axis Axis
0.9 0
.4 1
. 2 

### Pass

-OIL WATER PTC-10 PTC-10 36 1 212 TEMPERATURE SYSTEM CALIBRATION STANDARD

361 212 361 212 

### #8

361 212 360 212 360 212 360 212 360 212 0
. 1% Pess 

### o 0
. 0% Pass**F- -"~** 

## ____**~~~**

## __**~~**

## __**~~**

## ____**~;-** 

## ____**~~+-~~**

# __**~**

# ____**~~**

# __**~~-f**

## __**~**

## ____**~~ ,pass**  OIL PTC-11 362 362 362 362 360 360 360 360 Pass WATER PTC-11 213 213 213 213 212 2 1 2 212 212

WATER

OIL WATER

OIL WATER PTC-22 PTC-23 PTC-23 PTC-24 PTC-24 360 214 361 213

Calibrated By: DMW. RM

. RMO, DA, ME 360 214 361 213 360 214 361 213 360 214 361 213 360 212 360 212 212 360 212 360 212 360 212 360 212 360 212 360 212 

### o 2

January 2 , 2013Reference Thermometer I D.: TIC Readout t.o. I D
. 

# '" Readina 1 OIL PTC·25 362 WATER PTC·25 213

ICE PTC·25 32 OIL PTC·26 362 WATER PTC·26 212

ICE PTC·26 31 OIL PTC·27 363 WATER PTC·27 213

ICE PTC·27 30 OIL PTC·2S 362 WATER PTC-28 212

ICE PTC-28 30 OIL PTC·29 361 WATER PTC-29 211

I CE PTC-29 31 OIL PTC-30 361 WATER PTC-30 212

I CE PTC-30 31 OIL TRO-l 361 WATER TRO·l 212

ICE TRO·l 33 OIL TRO-4 362 WATER TRO-4 211

ICE TRO-4 32 OIL TRO-5 362 WATER TRO-5 214

ICE TRO-5 32 OIL TRO..e 36 2 WATER TRO..e 212

ICE TRO..e 31 OIL TRO-8 362 WATER TRO ·S 213

ICE TRO·S 35 OIL TRO-9 361 WATER TRO·9 212

ICE TRO-9 32 OIL TRO·ll 360 WATER TRO-l1 214

ICE TRO-ll 31 OIL TRO·12 360 WATER TRO-12 213

ICE TRO-12 32 OIL TRO-13 361 WATER TRO-13 212

ICE TRO-13 31 OIL TRO-1S 364 WATER TRO·1S 213

ICE TRO·1S 31 OIL TRO·16 364 WATER TRO-16 212

ICE TRO-16 32 OIL TRO·1S 362 WATER TRO-IS 213

ICE TRO - IS 32 OIL TRO-19 363 WATER TRO-19 213

ICE TRO-19 31 OIL TRO-20 364 WATER TRO·20 212

ICE TRO·20 33 OIL TRO·22 363 WATER TRO-22 213

ICE TRO-22 31 OIL TRO·23 362 WATER TRO-23 212

I CE TRO-23 31 OIL TRO-24 362 WATER TRO-24 213

I CE TRO-24 32 T1 TEMPERATURE SYSTEM CALIBRATION STYPE 

### #26**F9~195** T2 F95·195 T3**F9~195** TIC . Readout Reference Thermometer ·F 

# ., Readina 2 Readina 3 Averaae Readina 1 Readina 2 Readina 3 Averaoe

362 362 362 360 360 360 360 213 213 213 212 212 212 212 32 32 32 32 32 32 32 362 362 362 360 360 360 360 212 212 212 212 212 212 212 31 31 31 32 32 32 32 363 363 363 360 360 360 360 213 213 213 212 212 212 212 30 30 30 32 32 32 32 362 362 362 360 360 360 360 212 212 212 212 212 212 212 30 30 30 32 32 32 32 361 361 361 360 360 360 360 211 211 211 212 212 212 212 31 31 31 32 32 32 32 361 361 361 360 360 360 360 212 212 212 212 212 212 212 31 31 31 32 32 32 32 361 361 361 360 360 360 360 212 212 212 212 212 212 212 33 33 33 32 32 32 32 362 362 362 360 360 360 360 211 211 211 212 212 212 212 32 32 32 32 32 32 32 362 362 362 360 360 360 360 214 214 21 4 212 212 212 212 32 32 32 32 32 32 32 362 36 2 362 360 360 360 360 212 212 212 212 212 212 212 31 31 31 32 32 32 32 362 362 362 360 360 360 360 213 213 213 21 2 212 212 212 35 35 35 32 32 32 32 361 361 36 1 360 360 360 360 212 212 212 212 212 212 212 32 32 32 32 32 32 32 360 360 360 360 360 360 360 21 4 214 21 4 212 212 212 212 31 31 31 32 32 32 32 360 360 360 360 360 360 360 213 213 213 212 212 212 212 32 32 32 32 32 32 32 361 361 361 360 360 360 360 212 212 212 212 212 212 212 31 31 31 32 32 32 32 364 364 364 360 360 360 360 213 213 213 212 212 212 212 31 31 31 32 32 32 32 364 364 364 360 360 360 360 212 212 212 212 212 212 212 32 32 32 32 32 32 32 362 362 362 360 360 360 360 213 213 213 212 212 212 212 32 32 32 32 32 32 32 363 363 363 360 360 360 360 213 213 213 212 212 212 212 31 31 31 32 32 32 32 364 364 364 360 360 360 360 212 212 212 212 212 212 212 33 33 33 32 32 32 32 363 363 363 360 360 360 360 213 213 213 212 212 212 212 31 31 31 32 32 32 32 362 362 362 360 360 360 360 212 212 212 212 212 212 212 31 31 31 32 32 32 32 362 362 362 360 360 360 360 213 213 213 212 212 212 212 32 32 32 32 32 32 32

Cal ibrated By: DMW, RM, RMO , CA, ME Differeoce ·F 2 1 0 2 0 1 3 1 2 2 0 2 1 1 1 1 0 1 1 0 1 2 1 0 2 2 0 2 0 1 2 1 3 1 0 0 0 2 1 0 1 0 1 0 1 4 1 1 4 0 0 2 1 0 3 1 1 4 0 1 3 1 1 2 0 1 2 1 0 %.("R) 0.2% 0.1% 0.0% 0 . 2% 0 . 0% 0.2% 0.4% 0 . 1% 0.4% 0.2% 0.0% 0.4% 0 . 1% 0.1% 0.2% 0 . 1% 00% 02% 0 . 1% 0 . 0% 02% 0 .2°'" 0 . 1% 0 . 0% 0 . 2% 0 .3% 0 . 0% 0.2% 0 . 0% 0 . 2% 0 . 2% 0.1% 0.6% 0 . 1% 0 . 0% 0 . 0% 0 . 0% 0 .3% 0 . 2% 0.0% 0 . 1% 00% 01% 0 . 0% 0 . 2% 0.5% 0.1% 0.2% 0.5% 0.0% 0.0% 0.2% 0.1% 0.0% 0. 4% 0 . 1% 0,2% 0,5"'" 0,0% 0,2% 04% 0.1% 0.2% 0 . 2% 0 . 0% 0 . 2% 0 . 2% 0.1% 0.0% P .n 

# ."

. "

. n

. n

. n

. n 

# ." '" .n P P P P P P P P P P

# .n P P P 

## '"

'" '" '" '" 

# '" .n P P P P P .n

.n P P 

## '"

.n P P 

# '"

.n P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P P .n



# ." ."

. " '" '" .n 

# '"

. n 

# '"

. n 

### .n 

# '" 

# '" '" ." .n .n 

# '" '" 

# ." ." '" 'n 

## '" .n .n .n .n .n .n .n .n



# . " .n .n .n .n .n .n .n 

# ." .n .n .n

Ja nuary 2 , 2013

# 06118 11.

Air Qualify Services , Incorporated 

## NOZZLE CALIBRATION DATA
Nozzle I.D. 

# ,-)1.,.L.,/
.. vl 1lJ· 

## .J..3 'I 

## 5z ;f1iL Date ,. C).tf. 

### , 3 

## Material 

## 55 Bv**.I::!** 

## ,f? v ..**~-1..** 

## Confiauration IL or Hook) 

## I.J,., ,JlC

Maximum Difference Di - Dj 

## = OC'U:l... 

## (must be 0
. 004 " ) Average Dn 

## = 

# C · J 3 

# vi

Note: Measure three diameters with micrometer

DS934098 Date of last revision 

### 9/28/2012 Master Document StoragelFormslDatasheetslCalibration Forms

## Appendix A.4

R041 0673 

## Delta CEM System Description and SCAQMD Method 100.1 Calibration and Test Sequence

A-9

## SCAQMD METHOD 100.1 CALIBRATION SEQUENCE AND CALCULATIONS DEFINITIONS : 

## 1) Analyzer Calibration :

2) Calibration Error :

3) Analyzer Linearity:

4) Sample System Bias :

R0410673 Zero and span gas(es) are introduced directly to the analyzer. Adjustments are made to the analyzer zero and upscale readings , as necessary to match the certified concentrations of the calibration gas . Zero , mid (40-60% of full 

## scale) , and high (80-100% of full 

## scale) calibration gases are introduced directly to the analyzer and the analyzer response to each gas is recorded (without adjustment to the analyzer). The Calibration Error (difference between the analyzer response to the calibration gas and the certified concentration of the calibration gas) must not exceed ± 2% of the analyzer full 

## scale for any of the three gases . Analyzer linearity is defined as the difference between an analyzer response to the mid range gas and the predicted analyzer response to the mid range gas based on the analyzer response to the zero and high range gas . The Analyzer Linearity test is required on a semi-annual basis and must not exceed ± 1

## % of the analyzer range . It 

## should be noted that this linearity requirement is more stringent than the best available calibration standards (+1-2%) 

## for the low CO and NO x 

## concentrations expected during this test program . For this reason , an analyzer linearity of less than 2% will be considered as acceptable for this program . The sample system bias test involves introducing zero and one upscale (mid or high) calibration gas to the entire sampling system and recording the analyzer response . The analyzer response to the calibration gas after it has passed through the entire sample system is compared to the analyzer response to same the calibration gas injected directly to the analyzer. The test is used to determine the effect which the sample system has on the species of interest and correct the measured values for any effect which the system has. The sample system bias is required to be less than ± 5% of the analyzer range for both the zero and upscale gas .

A-10 

# . !!t!la. 4.

## PROCEDURES AND CALCULATIONS : Figure 1 presents a flow chart for the SCAQMD Method 100
. 1 calibration sequence . All calibrations are documented as one-m i nute averages from the reference method Data Acquis it i on System

. Following assembly of the system , analyzer warm up time , and a successful leak check of the sample system , the calibration/test sequence presented in Figure 1 can begin

. An Analyzer Calibration is performed as necessary by adjusting the zero and span settings of the analyzer

. These calibrations are not necessarily recorded on the chart recorder. Calibration Error is then determined at three levels for each range ( which i s ex pected to be used ) of each analyzer. This check is performed , at a minimum , once at the beginning and once at the end of each test day

. The calibration error must not exceed ± 2 % of the full range of the analyzer as determined by the following equation : Calibration Error Analyzer Response- Cal. Gas Value )/ 

# = • 100 '10 Analyzer Range The data from the Calibrat i on Error test can be used to determine Analyzer Linearity

. The analyzer response to the mid gas is predicted using linear regression and the analyzer response to the zero and high calibration gas and the zero and high calibration gas values

. The analyzer linearity must be demonstrated on a semi-annual basis using the following equation : Analyzer Response - Predicted Response Analyzer Linearity 

## = • 

## 100 % Analyzer Range where : Res p onse to Hig h Gas . Res p onse to Z ero Gas Predicted Res pons e ;: * 

### M id G as Va lue + 

### Response to Zero Ga s H igh Gas Value 

## The Sample System Bias test is performed before and after each test run and must not exceed ± 5% of the analyzer range for both the zero and upscale span gas . The system bias is calculated using the following equation : Response to System Bias - Response to Analyzer Cal Sample System Bias 

# = • 100 % Analyzer Range

R041 0673 A - 11

## where: Response to Analyzer Cal 

## = The analyzer response to the last time the same calibration gas was introduced directly to the analyzer (this may be the pre-test calibration error value or a more recent analyzer calibration adjustment) Zero and Calibration Drift are calculated for each test run based on the analyzer response during the pre- and post-test sample system bias test. Zero and upscale drift must not exceed ± 3% of the analyzer range. I D ' ft Pos t - T e st Syst em B ios R esonse - Pre - Te s t S yst em B i os Re sponse A na yzer n 

## = ' 100% A n a lyzer Range The pre- and post-test analyzer response during the sample system bias test are used to correct the raw test average for any sample system bias and analyzer drift

. The drift/bias corrected data are the actual reported concentrations and are used for subsequent calculations (mass emission rates , Ib/MMBtu , corrections to 3% or 15% O 2 , etc
. )

. The drift/bias corrections is performed using the following equation:

where: C c 

## = Drift/bias corrected concentration 

## C = Raw Test Average C m 

## = Average of pre- and post-test response to sample system bias span Co 

## = Average of pre- and post-test to sample system bias zero C ma 

## = Span gas value ADDITIONAL QUALITY ASSURANCE CHECKS: SCAQMD Method 100
. 1 specifies the allowed analyzer interferences for each analyzer type. No interference checks are required for O 2 or NO, analyzers

. Interference tolerances are given for CO, CO 2, and S0 2 analyzers

. The analyzers used by Delta are certified by the manufacturers to have interference responses which meet the requirements of Method 100
. 1
. SCAQMD has published a draft method for determining the efficiency of a N0 2 to NO converter
. This test will be performed once on the day of the test. The converter efficiency must be 90% or greater
.

R041 0673 A-12 

# Del/a l:!.. "' '''''"''' 

### .........

# _.

## Analyzer Cal
Cal No Error < 

## 2% No Yes IYes

System 1\1" 

## System Bias < 

## 5% Problem? Yes Don't Know Stratified No Location? Yes Multi-Point Single Point Test Test 

# 1 System No Bias < 

## 5% Yes Cal No Drift < 

## 3% 

# 1

Yes Note: AQMD policy allows multiple 

## Another 1 No Analyzer Cal test runs 10 be validated by one set 

# I of pre- and post-test sample system 

## Test? (if necessary) bias tests as long as the bias 

# 1 checks are performed within 2 hours 

## Yes of the previous bias check. 

## No No Analyzer 

# [ Cal 

# lCal? Error < 

## 2% Yes 

# 1 Yes No Yes System 

# [ Finish 

# 1 Bias < 

## 5% I--


## FIGURE 1: SCAQMD METHOD 100.1 CALIBRATION AND TEST SEQUENCE

R0410673 A-13

## APPENDIX B PROCESS DATA

R0410673 B-1

## Appendix B.1 Process and CEMS Data

R0410673 8-2

## Appendix B.1.1 Sentinel Unit 2 Stratification Test



## R0410673 8-3 

# Del/a t..

........ , 

### ...... 

# "'--

# Data Summary Repo r t Company : 

### CPV Sentinel, LLC 62575 Powerline Road Source: Data Group : Report Nam e : 

### Desert Hot Springs, CA 9 2 240 Turbine 2 2>1-Min Cales

# ~('h~\ 

# Ur'ld 1 s}t<+ 

# T RACE
Environmen tal Sys tems, Inc.

Start of Report : 

### 2> I-Min Summary - RATA 01/30/2013 08,30 End of Report, 01/30/201 3 09,03 

### validation : 

### All Available Data Group#-Channel# Long Descrip. Short Descrip. 

### Units Range 01/30/2013 08:30 01/30/2013 08:31 01/30/2013 08:32 01/30/2013 08:33 01/30/2013 08:34 01/30/2013 08;35 01/30/2013 08:36 01/30/2013 08 : 37 01/30/2013 08;38 01/30/2013 08:39 01/30/2013 08:40 01/30/2013 08 : 41 01/30/2013 08:42 01/30/2013 08;43 01/30/2013 08:44 01/30/2013 08;45 01/30/2013 08:46 01/30/2013 08: 4 7 01/30/2013 08: 4 8 01/30/2013 08:49 01/30/ 2 013 08:50 01/30/2013 08:51 01/30/2013 08 ; 52 0 1 /30/2013 08;53 01/30/2013 08;54 01/30/2013 08:55 01/30/2013 08:56 01/30/ 2 013 08:57 01/30/2013 08:58 01/30/2013 08:59


### Date/Time Printed: G12-C4 GIZ-CII G12-C20 G12 -C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass 2>StkFlow

loS loS 1.6 1.6 1.6 1.6 1.6 1.6 1.6 1.7 1.7 1.7 1.7 loB 1.9 1.9 2.0 2.1 2.1 2.1 2.1 2.1 2.2 2.3 2.2 2.3 2
. 3 2.3 2.3 2.3 Stk 02 t 0-25 13 .45 13
. 43 13
. 42 13
. 43 13.43 13
. 44 13.42 13. 4 3 13.43 13. 4 4 13.43 13
. 43 13.41 13 .22 13.03 13.03 13
. 04 13.0 4 13.04 13.05 13
. 04 13
. 05 13.05 13
. 05 13.05 13.04 13
. 04 13.05 13
. 05 13
. 03
01/30/2013 10,19 

### NOx Mass Ib/hr 0-100 3
. 57 3
. 58 4
. 47 4.46 4 .46 4
. 45 4
. 46 4.45 4.46 4.45 4.45 4.46 4 .48 4.48 4.47 4.47 5.36 5.36 5.36 5
. 35 5
. 36 5.35 5.3 4 5
. 35 5.34 5.3 4 5.33 5.33 5.34 5.34 StkFlow 

### kscfh 0-300000

21789 21784 21755 217 4 6 21736 21712 21718 21696 21729 21702 21707 21713 21759 21226 20690 20693 20699 20675 20675 20681 20675 20664 20646 2065 9 20639 20621 20586 2 0614 2062 4 20605 G12-C) GI2-Cl3 GI2-ClO G12-C6 G12-C7 G12-Ca G12 -C18 G12-C 2>Stk CO 2>CO M ass 2>NOx Rate 2>Stk NOXc 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo Stk 

### co ppm 0-1000

0.1 0.1 0.2 0.2 0.2 0.2 0
. 2 0.2 0.2 0.2 0.2 0.2 1.6 2.3 0.3 0.3 1.S 1.B 1.7 1.6 1.S 1.6 1.6 1.6 1.6 1.' 1.3 1.2 0.7 

### O.B CO Mass 

### Ib/hr 0-100 0.00 0
. 00 0.00 0.00 0.00 0
. 00 0.00 0.00 0.00 0.00 0.00 0.00 2.69 3
. 58 0.89 0.89 2
. 68 2.68 2.68 2
. 68 2
. 68 2.67 2
. 67 2.67 2
. 67 1. 78 1. 78 1. 78 0
. 89 0
. 89 NO x Rate 

### Ib/mmBtu 0-1 0
. 00 4 0.004 0.005 0.005 0.005 0.005 0.005 0.005 0.005 0
. 005 0
. 005 0
. 005 0.005 0
. 005 0.005 0.005 0.006 0.006 0
. 006 0
. 006 0.006 0.006 0
. 006 0
. 006 0.006 0.006 0.006 0
. 006 0
. 006 0.006 Stk NO X c 

### ppm 0-300 1.19 1.18 1.26 1.26 1. 26 1. 2 7 1. 26 1. 26 1. 26 1. 34 1. 34 1. 34 1. 34 1. 38 1. 42 1. 42 1. 50 1. 58 1. 58 1. 58 1. 58 1.58 1. 65 1. 73 1. 65 1. 73 1. 73 1. 73 1. 73 1. 72 Stk COe Gas 

### ppm 0-1000 

### hscfh hscfh 0-10000 0.08 0.08 0.16 0.16 0
. 16 0.16 0
. 16 0
. 16 0.16 0.16 0.16 0
. 16 1. 26 1. 77 0.22 0.22 1.13 1. 35 1.28 1. 20 1.13 1.20 1.20 1.20 1.20 1. 05 0.98 0.90 0.53 0
. 60 8 4 92.4 8513.4 8513.4 8498.4 8494
. 8 8473.8 849 9 .0 8479.2 8 4 91.8 8470.2 8483.4 8485.8 8526.6 8528
. 4 8518.8 8520.0 8511
. 6 8502
. 0 8502.0 8493
. 6 8502.0 8486
. 4 8479
. 2 84 8 4
. 6 8476.2 8 4 79
. 8 8 4 65.4 8466
. 0 8470.2 8 4 84.0 NlBlnj 

### lb/hr 0-1000 110.0 110.0 110.0 llO
. O 110.0 110.0 110
. 0 110.0 110
. 0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110
. 0 110
. 0 110.0 110.0 110.0 110
. 0 110.0 110
. 0 110.0 110.0 110.0 110
. 0 110
. 0 110.0 MW Lo
0

- 1 102 103 103
. . 102. 103. : 102. ; 103.1 103
.. 102
.. 102. : 102. : 102. : 103. ; 103 103. ! 103 . ; 103. ( 102.**~** 102
. . 102. 103. ( 102. ! 103
. ( 102
.. 102. : 102
.. 102
. 102. ! 103. ( 10 2 

### PagE

### Group#-Channel# G12-C2 G12-C 4 G12-C11 G12-C20 G12-C3 G12-C13 G12-C10 G12-C6 G12-C7 G12-C8 G12-C18 G12-C 

### Long Descrip. 2>Stk NOx 2>Stk 02 2>NOx Mass 2>StkFlow 2>Stk CO 2>CO Mass 2>NO x Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NIB Inj 2>MW Lo 

### Short Descrip . Stk NOx Stk 02 NOx Mass StkFlow Stk CO CO Mass NOx Rat e Stk NO X c Stk COe Gas hsefh NH3Inj MW Lo 

### Units ppm % 

### lb/hr ksefh 

### ppm Ib/hr Ib/mmBtu 

### ppm ppm hsefh 

### lb/hr Range 0-150 0-25 0-100 0-300000 0-1000 0-100 0-1 0-300 0-1000 0-10000 0-1000 0-1 01/30/2013 09;00 2.3 13
. 04 5.33 20572 1.1 1. 78 0.006 1. 73 0.83 8459.4 110.0 102
. . 01/30/2013 09;01 2.4 13.03 6.22 20546 0.8 0.89 0.007 1. 80 0.60 8459.4 110.0 103.1 01/30/2013 09:02 2.4 13
. 04 6.23 20602 0.7 0.89 0.007 1. 80 0.53 8472
. 0 110.0 102. : 01/30/2013 09;03 2.4 13.0 4 6.24 20630 0.6 0.89 0.007 1. 80 0.45 8483.4 110.0 102. : 

### Period Average 2.0 13.20 4.96 21076 0.' 1. 29 0.006 1. 50 0.66 8490.2 110.0 102
. 8 

### Period Max Value 2.4 13 .45 6.24 21789 2.3 3.58 0
. 007 1. 80 1. 77 8528.4 110.0 103. 

### Period Min Value 1.5 13.03 3.57 20546 0.1 0.00 0.004 1.18 0.08 8459.4 110.0 102
. 

### Period Totals 

## = 6.6800E+1 4.4864E + 2 1. 6849E+2 7.1656E+5 2.9800E+1 4.3700E+1 1.8900E-1 5.0980E+1 2.2590E+1 2.8866E+5 3.7400E+3 3.4963E+ 

### Period 

### % Recovery 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.



### Date/Time Printed: 01/30/2013 10,19 

### 2> I-Min Summary

- RATA

- Continued PagE

## Appendix B.1.2 Sentinel Unit 2 Ammonia, ROG and 

## NOxlCO Testing

R0410673 

### 8-4

# Data Summary Report Company : 

### CPV Sentinel, LLC 62575 Powerline Road Desert Hot Springs, CA 92240 

### Source : Turbine 2 Data Group: Report Name :

# ~AL \

# \jA~t 

# 2 (CMol'r;fitld. 

# 7**-11,;-r~** 

# - tJ }\.,- 

# so- ! 

# TRACE
Environmental S./fs/ems, Inc
.

Start of Report: 2>1-Min Cales 2>Summary

- I-Min RATA 02/01/2013 14,20 End of Report, 02/01/2013 15,35 

### validation: All Available Data Group#-Channel# Long Descrip. 

### short Descrip . units Range 02/01/2013 14:20 02/01/2013 14:21 02/01/2013 14:22 02/01/2013 14:23 02/01/2013 14:24 02/01/2013 14:25 02/01/2013 14:26 02/01/2013 14:27 02/01/2013 14:28 02/01/2013 14:29 02/01/2013 14:30 02/01/2013 14 : 31 02/01/2013 14:32 02/01/2013 14:33 02/01/2013 14:34 02/01/2013 14:35 02/01/2013 14:36 02/01/2013 14:37 02/01/2013 14:38 02/01/2013 14;39 02/01/2013 14:40 02/01/2013 14:41 02/01/2013 14:42 02/01/2013 14:43 02/01/2013 14:44 02/01/2013 14:45 02/01/2013 14:46 02/01/2013 14:47 02/01/2013 14:48 02/01/2013 14:49


### Date/Time Printed: G12-C4 Gl2 -ell G12-C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass

2
. 0 1.9 1.8 1.9 1.9 1.9 1.8 1.9 1.9 1.9 1.8 

### 2.2 1.9 2.1 2.2 2.2 2.1 2.0 2.1 2.1 

### 2.0 2.0 

### 2.0 2.0 1.9 2.0 2.1 2.0 2.2 2.2 Stk 02 

# • 0-25 14.3 4 14.36 14
. 36 14.36 14
. 35 14.35 14
. 36 14.36 14 .37 14.36 14.36 14.34 14.37 14.34 14
. 34 14
. 33 14 .35 14.34 14.34 14.34 14.35 14.35 14.35 14.35 14.36 14 .35 14.34 14
. 34 14.32 14.32


### 02/01/2013 16,13 

### NOx Mass Ib/hr 0-100 3.93 3.35 3.36 3.35 3.36 3.35 3.35 3.35 3.36 3.36 3.35 3.91 3
. 35 3.91 3.90 3.91 3.91 3.91 3.92 3.93 3.92 3.92 3.92 3.92 3.35 3.92 3.93 3.92 3.93 3.93 G12-C20 2>StkF!ow



### StkFlow

kscfh 0-300000

15572 15558 15588 15561 15553 15532 15542 15560 15601 15586 15535 15509 15541 15510 15477 15489 15517 15514 15558 15570 15576 15546 15564 15571 15556 15571 15570 15554 15540 15536 G12 -C3 2>Stk CO

Stk CO ppm 0-1000

0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.3 

### 0.3 0.3 

### 0.3 0.3 

### 0.3 0.3 

### 0.3 G12-CD G12 -ClO G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass



### Ib/hr 0-100 0.56 0.56 0.56 0.56 0.56 0
. 56 0.56 0.56 0
. 56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0
. 56 0.56 0.56 0.56 0.56 0
. 00 0
. 56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 NOx Rate 

### Ib/mmBtu 0-1 0.007 0.006 0.006 0.006 0.006 0.006 0.006 0.006 0.006 0.006 0.006 0.007 0.006 0
. 007 0.007 0.007 0.007 0.007 0
. 007 0
. 007 0.007 0.007 0.007 0.007 0.006 0.007 0
. 007 0.007 0.007 0.007 Stk NQXc ppm 0-300 1. 80 1. 71 1. 62 1. 71 1. 71 1. 71 1. 62 1. 71 1. 72 1. 71 1. 62 1. 98 1.72 1. 89 1. 98 1. 98 1. 89 1. 80 1. 89 1. 89 1. 80 1. 80 1. 80 1. 80 1. 71 1. 80 1. 89 1. 80 1. 97 1. 97 G12-C7 G12-C8 2>Stk COc 2>Gas Flow



### Stk COc Gas hscfh ppm hscfh 0-1000 0-10000 0.27 0.27 0.27 0.27 0
. 27 0.27 0.27 0.27 0.27 0 .2 7 0
. 27 0.27 0.27 0 .2 7 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.18 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 5344.2 5323.2 5333.4 5324.4 5329.8 5322.6 5317.8 5323.8 5329.8 5332.8 5315.4 5322.6 5309.4 5323 .2 5311.8 5323.8 5317.2 5324.4 5339.4 5343.6 5337.6 5327.4 5333 .4 5335.8 5322.6 5335.8 5343 .6 5338.2 5349.6 5348.4 G12-C18 2>NH3 Inj NH3Inj



### Ib/hr 0-1000 106.8 107.0 106.7 107
. 0 107
. 2 107.7 107 .2 106.5 106.3 107.3 105.7 104.7 106.5 105.2 104.0 104.5 106.0 107.0 105
. 7 106.3 105.8 106
. 3 106
. 7 106.8 107.7 107.0 106.2 107.0 107.0 106.8 G12-C 2>MW Lo

MW Lo
0-1 54. : 5 4
.. 54
. . 54
.. 54
.. 54
. . 54 54. 54. : 

### 54 54
. . 5. 54
.. 54. : 54. c 54. : 5 •. 5 •. 54
.. 54. 54
.. 54. 55. c 55. c 5 4
.. 55. c 54. : 54 55. c 55. c 

### PagE

### Gr o up# -Channel # Long Descr i p . S hort Descrip. units Range 02/01/2013 14:50 02/01/2013 14:51 02/01/2013 14:52 02/01/2013 14:53 02/01/2013 14:54 02/01/2013 14:55 02/01/2013 14:56 02/01/2013 14:57 02/01/2013 14:58 02/01/2013 14:59 02/01/2013 15:00 02/01/2013 15:01 02/01/2013 15:02 02/01/2013 15:03 02/01/2013 15:04 02/01/2013 15:05 02/01/2013 15:06 02/01/2013 15:07 02/01/2013 15:08 02/01/2013 15:09 02/01/2013 15:10 02/01/2013 15:11 02/01/2013 15:12 02/01/2013 15:13 02/01/2013 15:14 02/01/2013 15:15 02/01/2013 15:16 02/01/2013 15:17 02/01/2013 15:18 02/01/2013 15:19 02/01/2013 15:20 02/01/2013 15:21 02/01/2013 15:22 02/01/2013 15;23 02/01/2013 15;24 02/01/2013 15:25 02/01/2013 15:26 02/01/2013 15;27 02/01/2013 15:28 02/01/2013 15:29 

### Date/Time Printed: G12-C4 G12

- C11 G12

- C2 2::>Stk NOx

Stk NOx 

### ppm 0-150 2::>Stk 02 2::>NOx Mass

2.1 2.1 2.2 2.1 1.9 2
. 1 2.1 2.1 2.2 2.1 2.2 2.1 2.1 2.1 2.0 2.0 2.0 2.0 2
. 2 2.2 2.1 2.1 2.1 2.2 2.0 2.1 2.2 2.0 2.1 2.1 2.2 2.2 2.2 2.2 2.1 2.0 2.1 2.1 2.1 2.2 Stk 02 t 0-25 14.33 14.33 14.33 14.34 14.35 14.33 14.32 14.3 2 14.32 14.33 14.32 14.32 14 .31 14 .33 14.33 14.3 4 14.34 14.34 14.32 14.33 14 .33 14.34 14
. 33 14.30 14.31 14.32 14 .32 14.34 14.31 14.32 14.31 14
. 31 14.31 14.31 14 .32 14.32 14.30 14.31 14.31 14.31
02/01/2013 16,13 NOx Mass 

### lb/hr 0

- 100 3.94 3.94 3.94 3.94 3.38 3.95 3.94 3.95 3.94 3.94 3.94 3.94 3.95 3.94 3.94 3.94 3.93 3.92 3.94 3.94 3.93 3.93 3.94 3.95 3.96 3.95 3.97 3.96 3.98 3.98 3.99 3.98 3.98 3.98 3.98 3.97 3.98 3.98 3.98 3.99 G12-C20 2::>StkFlow

StkFlow

kscfh 0-300000

15586 15586 15579 15605 15637 15625 15582 15620 15585 15600 15568 15577 15596 15583 15595 15605 15596 15554 15580 15590 15569 15584 15586 15564 15617 15601 15688 15689 15697 15711 15725 15703 15711 15722 15723 15707 15689 15694 15722 15736 G12-C3 2::>Stk CO

Stk CO 

### ppm 0-1000

0.3 0.3 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.3 0.3 0.3 0.3 0 .3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.2 0.3 0.2 0.2 0.2 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 G12

- Cl3 G12-CI0 G12-C6 2::>CO Mass 2::>NOx Rate 2::>Stk NOXe

CO Mass 

### lb/hr 0

- 100 0.56 0.56 0.00 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.00 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.57 0.56 0.00 0.00 0.57 0.00 0.00 0.00 0.00 0.57 0.57 0.57 0.57 0.57 0.57 0.57 NOx Rate lb/mmBtu 0-1 0.007 0.007 0.007 0.007 0.006 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXe 

### ppm 0

- 300 1. 89 1. 89 1. 98 1. 89 1. 71 1. 89 1. 88 1. 88 1. 97 1. 89 1. 97 1. 88 1. 88 1. 89 1. 80 1. 80 1. 80 1. 80 1. 97 1. 98 1. 89 1. 89 1. 89 1. 97 1. 79 1. 88 1. 97 1. 80 1. 88 1. 88 1. 97 1. 97 1. 97 1. 97 1. 88 1. 79 1. 88 1. 88 1. 88 1. 97 G12-C7 G12-C8 2::>Stk COe 2>Gas Flow

Stk COe Gas hsefh ppm hscfh 0-1000 0

- 10000 0.27 0.27 0.18 0.27 0.27 0.27 0.27 0
. 27 0.27 0.27 0.27 0.27 0
. 27 0.27 0.18 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.18 0.18 0.27 0.18 0
. 18 0.18 0.18 0.27 0.27 0.27 0.27 0.27 0.27 0.27 5357.4 5357.4 5355.0 5355.6 5358.6 5370.6 5364.0 5377.2 5365.2 5362.2 5359.2 5362.2 5377.2 5356.2 5360.4 5355.6 5352.6 5338.2 5363.4 5358.6 5351.4 5348.4 5357.4 5374.2 5384.4 5370.6 5400.6 5384.4 5412.0 5408.4 5421.6 5413.8 5416.8 5420.4 5412.6 5407.2 5417.4 5410.8 5420.4 5425.2 G12-C18 2::>NH3 Inj NH3Inj



### 1b/hr 0-1000 105.2 105.8 105.7 107.3 107.3 106.0 106.5 106.3 106.7 106.7 106.8 106.8 107.2 107.5 107.5 106.8 107.2 106.2 105.7 105.8 107.2 104.3 106.0 107.0 106.7 107.2 107.3 109.0 108.8 107.8 107.5 108.2 107.8 108.8 108.3 108.3 108.7 107.8 106.8 107.8 

### 2>Summary

- l-Min RATA

- Continued G12-C 2 >

MW 

### Lo MW Lo

0-1 55. ! S5.1 54. : 55.1 54 55.1 55 55
. . 55. 55. 1 54. 55
.. 55.: 54. : 55
.. 54 55.1 54. : 55
. . 55.1 54. : 55.1 55.: 55
. . 55 ' 55
. . 55. 55. 56.1 55
.. 56. : 56.1 S5. < 56. 1 56.1 55
. . 55. : 56.1 56
.. 55. 

### PagE

### Group#-Channel# Long Descrip. Short Descrip
. Units Range 02/01/2013 15:30 02/01/2013 15:31 02/01/2013 15:32 02/01/2013 15:33 02/01/2013 15:34 02/01/2013 15:35 

### Period Average Period Max Value Period Min Value Period Totals 

# = Period 

### % Recovery

Date/Time Printed: G12-C4 G12-C11 G12-C20 G12

- C2 2>Stk NOx

Stk NOx 

### ppm 0

- 150 2>Stk 02 2>NOx Mass 2>StkFlow

2.1 2.0 2.1 2.1 2.0 2.0 2.1 2.2 1.8 1
. 5660E+2 100.0 Stk 02 

# • 0-25 14.3 2 14.32 14.32 14 .33 14
. 32 14.32 14
. 33 14.37 1 4 .30 1.0892E+3 100.0

02/01/2013 16,13 NOx Mass 

### 1b/hr 0

- 100 3.98 3.97 3.98 3.96 3.97 3.97 3.84 3.99 3.35 StkFlow kscfh 0-300000

157 26 15681 15733 15658 15678 15674 15604 15736 15477 2.9221E+2 1.1858E+6 100.0 100.0 G12-C3 G12

- Cl3 G12-C10 G12

- C6 G12-C7 G12-C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flo w 2>NH3 Inj 2>MW Lo

Stk 

### co ppm 0

- 1000

0.2 0.3 0.2 0.3 0.3 0.3 0.3 0 .3 0.2 2.1700E+l 100.0 CO Mass Ib/hr 0-100 0.00 0.57 0.00 0.57 0.57 0.57 0.48 0.57 0.00 3.6530E+1 100.0 NOx Rate Ib/mmBtu 0-1 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.006 S.1900E-1 100.0 stk NOXc 

### ppm 0

- 300 1. 88 1. 79 1. 88 1. 89 1. 79 1. 79 1. 85 1. 98 1. 62 1.4066E+2 100.0 Stk COc Gas hscfh 

### ppm 0-1000 0.18 0 .2 7 0.18 0.27 0.27 0.27 0.26 0 .2 7 0.18 1.9530E+1 100.0 hscfh 0

- 10000 5413 .8 5398.2 5416.2 5382.0 5397.0 5395.8 5361.2 5425.2 5309.4 4.0745E+S 100.0 NH3Inj Ib/hr 0-1000 109.3 108.5 108.5 107.3 108.5 108.0 106
. 9 10 9. 3 104.0 MW Lo
0-1 55. 55.: 55.: 55.· 55. · 55.· 55
. 1

56. 54. 8.1250E+3 4.1874E+ 100.0 100.



### 2>Summary

- I-Min RATA

- Continued PagE

# Data Summary Report Company : 

### CPV Sentinel, LLC 62575 Powerline Road Desert Hot Springs, CA 92240 Source : 

### Turbine 2 Data Group : 

### 2>1-Min Cales Report Name :

# ~~\ 

# 0...: 

# r- Z (j,NlVrttcllc.(. 

# TRACE**~-l** \71"lL-

# ~~-S7-2- EnIJi ro n men/al Systems, [nc.

Start of Report: 2>Summary

- I-Min RATA 02/01/2013 15,53 End of Report, 02/01/2013 17,09 

### validation: All Available Data Group#-Channel# Long Descrip . 

### Short Descr i p. Units 

### Range 02/01/2013 15:53 02/01/2013 15 : 54 02/01/2013 15:55 02/01/2013 15:56 02/01/2013 15:57 02/01/2013 15:58 02/01/2013 15:59 02/01/2013 16:00 02/01/2013 16:01 02/01/2013 16:02 02/01/2013 16:03 02/01/2013 16:04 02/01/2013 16:05 02/01/2013 16:06 02/01/2013 16:07 02/01/2013 16:08 02/01/2013 16:09 0 2 /01/2013 16:10 02/01/2013 16:11 02/01/2013 16:12 02/01/2013 16:13 02/01/2013 16:14 02/01/2013 1 6 :15 02/01/2013 16:16 02/01/2013 16:17 02/01/2013 16:18 02/01/2013 16:19 02/01/2013 16:20 02/01/2013 16:21 02/01/2013 16:22


### Date/Time Printed: G12-C 4 GI2-CII G12-C2 2>Stk NO x

Stk NOx ppm 0-150 2>Stk 02 2>NO x Mass

2.3 2
. 0 2.2 2.1 2.0 2.1 2.1 

### 2.1 2.2 2.2 2.3 

### 2.3 2.1 2.1 

### 2.1 2
. 2 2.2 

### 2.3 2.2 2
. 1 2.2 2.1 

### 2.2 2.2 2.2 

### 2.2 2.2 2.0 2.1 

### 2.1 Stk 02 

# • 0-25 14
. 31 14.31 14.31 1 4. 34 14.34 14.34 14.35 14.34 14.33 14.32 14.3 2 14.32 14.34 14.34 14.34 14.30 14.32 14.33 14
. 32 14
. 32 14.31 14
. 31 14
. 29 14
. 29 1 4. 30 1 4 .28 14
. 29 14.31 14
. 30 14
. 31


### 02/01/2013 17,53 NOx Mass Ib/hr 0-100 4.52 3.95 3
. 96 3.93 3.92 3.92 3.92 3.93 3
. 93 3.94 4.51 4.51 3.93 3.93 3.93 3.94 3.94 4.51 3.96 3.96 3.96 3.97 3.98 3.99 3
. 98 3.99 3.98 3.99 4.00 3.99 G12-C20 2>StkFlow

StkFlow

kscfh 0-300000

15612 15603 15647 15586 15559 155 4 9 15560 15561 15564 15580 15584 15587 15586 15586 15586 15529 15566 15621 15650 15655 15635 15678 15648 15718 15682 15671 15660 15739 15747 15741 G12-C3 2>Stk CO

Stk CO ppm 0 -1 000

0.3 0.3 0.3 0.3 0.2 0.2 0.3 0
. 3 0.3 0
. 3 0.3 0.3 

### 0.3 0.3 0.3 0.3 0.2 0.3 0.2 

### 0.2 0.2 0.3 0. 2 0.3 0.3 0
. 3 0.3 

### 0.3 0.3 0.3 GI2

- C13 G12 -Cla G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

co Mass Ib/hr 0

- 100 0.57 0.56 0.57 0.56 0.00 0.00 0
. 56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.00 0.56 0
. 00 0
. 00 0
. 00 0.57 0
. 00 0.57 0.57 0.57 0
. 57 0
. 57 0.57 0.57 NOx Rate Ib/mmBtu 

### 0

- 1 0.008 0.007 0.007 0.007 0.007 0.007 0
. 007 0
. 007 0.007 0
. 007 0.008 0.008 0.007 0.007 0.007 0
. 007 0.007 0.008 0
. 007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0
. 007 0
. 007 0.007 0.007 Stk NOXc ppm 0-300 2.06 1. 79 1. 9 7 1. 89 1. 80 1. 89 1. 89 1. 89 1. 98 1. 97 2.06 2.06 1. 89 1. 89 1. 89 1. 97 1. 97 2.07 1. 97 1. 88 1. 97 1. 88 1. 96 1. 96 1. 97 1.96 1.96 1. 79 1. 88 1. 88 G12-C7 G12-C8 GI2-CIa 2 >Stk COe 2 >Gas Flow 2 >NH3 Inj

Stk COe Gas hscfh NH3 Inj ppm 0-1000 0.27 0. 2 7 0.27 0.27 0
. 18 0.18 0.27 0.27 0.27 0.27 0
. 27 0.27 0.27 0.27 0.27 0.27 0
. 18 0.27 0.18 0
. 18 0.18 0.27 0.18 0
. 27 0.27 0.27 0.27 0.27 0.27 0.27 hscfh 0-10000 5382.6 5379.6 5394.6 5349.0 5340.0 5336.4 5332.2 5340.6 534 9 .6 5363.4 5364.6 5365
. 8 5349.0 5349.0 5349.0 5362.2 5358
. 6 5369.4 5387.4 5389
. 2 5390.4 5405.4 5411.4 5435
. 4 5415.0 5427.6 5415.6 5426.4 5 4 37.2 5427.0 Ib/hr 0-1000 106.7 106.3 105.8 106.3 106.8 105.7 106.0 105.3 105.3 105.3 106.2 105.5 106.3 106.3 106.3 105.3 106
. 5 106.3 108.3 108.7 108.7 108.3 108.0 108.7 109
. 7 108.8 108.7 108
. 5 107.5 107.8 G12-C 2>MW La

MW La
0 - 1 55
. . 55
.. 55.! 54. : 54
. . 54. : 54. 54 54 55. < 55 55
.. 55.: 55.: 55.: 55. : 54 55
.. 55. 55.! 56.1 55. : 55. ! 56. : 55. : 56. : 56
. : 56. : 56.: 56. : 

### PagE

### Group#-Channel# Long Descrip
. Short Descrip. Units Range 02/01/2013 16:23 02/01/2013 16:24 02/01/2013 16:25 02/01/2013 16:26 02/01/2013 16:27 02/01/2013 16:28 02/01/2013 16:29 02/01/2013 16:30 02/01/2013 16:31 02/01/2013 16:32 02/01/2013 16:33 02/01/2013 16:34 02/01/2013 16:35 02/01/2013 16:36 02/01/2013 16:37 02/01/2013 16:38 02/01/2013 16:39 02/01/2013 16:40 02/01/2013 16:41 02/01/2013 16:42 02/01/2013 16;43 02/01/2013 16:44 02/01/2013 16:45 02/01/2013 16;46 02/01/2013 16;47 02/01/2013 16:48 02/01/2013 16:49 02/01/2013 16:50 02/01/2013 16:51 02/01/2013 16;52 02/01/20 13 16:53 02/01/2013 16:54 02/01/2013 16:55 02/01/2013 16;56 02/01/2013 16:57 02/01/2013 16:58 02/01/2013 16:59 02/01/2013 17;00 02/01/2013 17;01 02/01/2013 17:02 

### Date/Time Printed: G1 2 -C4 G12-ell G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass

2.0 2.1 2.1 2.1 2.1 2.1 2.0 2.1 2.2 2.1 2.2 2.2 2.1 2.0 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.2 2.1 2.2 2.2 2.2 2.1 2.0 2.0 2.0 2.1 2.0 2.0 2.1 2.1 2.2 2.2 2.1 2.1 2.2 Stk 02 

# , 0-25 14.32 14.31 14.32 14.30 14.30 14.32 14.32 14.30 14.29 14.31 14.31 14.30 14.32 14.33 14.33 14.32 14.33 14.31 14.32 14.31 14.30 14.31 14.31 14 .30 14.29 14.30 14 .32 14 .32 14.34 14.33 14.32 14.33 14.32 14.34 14.34 14.32 14
. 33 1 4.34 1 4. 33 14.33 

### 02/01/2013 17,53 NOx Mass 

### lb/br 0-100 3.98 3.99 3.98 3.98 3.99 3.97 3.96 3.98 3.99 3.98 3.99 3.99 3.97 3.96 3.95 3.97 3.95 3.98 3.97 3.98 3.98 3.99 3.99 4.00 4.01 4.00 3.98 3.97 3.95 3.95 3.95 3.94 3.94 3.92 3.93 3.94 3 .93 3.94 3.95 3.95 G12-C20 2>StkFlow

StkFlow

kscfh 0-300000

15737 15748 15735 15694 15703 15704 15657 15684 15691 15704 15727 15731 15674 15674 15647 15693 15625 15696 15704 15708 15698 15746 15730 15748 15761 1 5774 15747 15700 15661 15633 15610 15592 1 5564 15535 15572 15585 15560 15628 15616 15633 G12 -C3 2>Stk CO

Stk CO 

### ppm 0-1000

0.3 0.2 0.2 0.2 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0 .3 0.3 0.3 0.3 0.3 0 .3 0.3 0.3 0.3 0.3 0.2 0.2 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 G12-Cl3 G12-CIO G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass 

### lb/br 0-100 0.57 0.00 0.00 0.00 0.00 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.56 0.57 0.56 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.00 0.00 0.00 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 NOx Rate 

### Ib/mmBtu 0-1 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXc 

### ppm 0-300 1. 79 1. 88 1. 88 1. 88 1. 88 1. 88 1. 79 1. 88 1.96 1. 88 1. 97 1. 97 1. 88 1. 80 1.89 1. 88 1. 89 1. 88 1. 88 1. 88 1. 88 1. 97 1. 88 1. 97 1.96 1. 97 1. 88 1. 79 1. 80 1. 80 1. 88 1. 80 1. 79 1. 89 1. 89 1. 97 1. 98 1. 89 1. 89 1. 98 G12-C7 G12-CS 2>Stk CDc 2>Gas Flow

Stk COc Gas hscfh 

### ppm hscfh 0-1000 0-10000 0.27 0.18 0.18 0.18 0
. 18 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 

## o 27 0.27 0.27 0.27 0.27 0.27 0.18 0.18 0.18 0.27 0.27 0.27 0 .27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 5417.4 5429.4 5416.8 5419.2 5422.2 5406.0 5389.8 5415.6 5426.4 5414.4 5422.2 5431.8 5395.8 5387.4 5378.4 5402.4 5370.6 5411.4 5406.0 5415.6 5420.4 5428.8 5423.4 5437.8 5450.4 5446.8 5421.0 5404.8 5374.8 5373.6 5373.6 5359.2 5358.0 5331.6 5344.2 5365.2 5348.4 5363.4 5367.6 5373.6 GI2 -CIS 2>NH3 Inj NH3Inj



### lb/br 0-1000 108.3 108.3 108.7 109.2 108.7 108.7 107.5 108.3 109.3 108.3 106.0 109.2 108.7 107.2 108.0 106.0 107.2 107.8 107.8 107.0 107.8 106.7 107.5 107.3 107.0 108.8 109.7 108.2 106.8 105.5 107.2 107.5 1 07.2 105.0 104.8 105.3 104.8 103.8 105.0 105.2 

### 2>Summary

- 1-Min RATA

- Continued G12-C 2>MW La

MW La
0-1 56.1 56. : 56. : 56.1 56. ! 56
. ! 55. ! 56
.. 56.1 56.1 56. : 56.! 55
.. 55
.. 55
.. 55. 55
.. 56.1 55. 56. : 56.1 56. : 56. : 56
.. 56.: 56.: 56.1 56.1 55. : 55
.. 55
. . 55. 55
.. 54. ; 55.1 55
.. 55.1 55. ! 55. : 55. !**Pag~**

### Group#-Channel# Long Descrip . Short Descrip. Units Range 02/01/2013 17 : 03 02/01/2013 17:04 02/01/2013 17:05 02/01/2013 17:06 02/01/2013 17:07 02/01/2013 17 : 08 02/01/2013 17:09 

### Period Average = 

### Period Max Value Period Min Value Period Totals 

## = Period 

### % Recovery



### Date/Time Printed: G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2.1 2.1 2.1 2.1 2.1 2.1 2
. 1 2.1 2
. 3 2.0 1. 6360E+2 100.0 G12 -C4 G12-C11 2>Stk 02 2>NOx Mass

Stk 02 

# , 0 -2 5 NOx Mass lb/hr 0-100 14.31 3
. 97 14.32 3.97 14
. 32 3.96 14
. 31 3.9S 14
. 32 3.95 14.32 3.96 14.33 3.96 14.32 3.99 14.35 4.52 14.28 3.92 1
. 1024E+3 3.0731E+2 100.0 100.0

02/01/2013 17,53 G12-C20 2>StkFlow

StkFlow

kscfh 0-300000

15668 15695 15636 15605 15617 15639 15681 15653 15774 15529 1.2052E+6 100.0 G12

- C3 2>Stk CO

Stk CO 

### ppm 0-1000

0.2 0.2 0.3 0.2 0.3 0.3 0.3 0.3 0.3 0 .2 2.1400E+1 100.0 G12

- C13 G12

- C10 G12-C6 2>CO Ma ss 2>NOx Rate 2>Stk NOXc

CO Mass 

### 1b/hr 0-100 0.00 0
. 00 0
. 57 0.00 0
. 56 0.57 0.57 0.44 0.57 0.00 3.3920E+1 100.0 NOx Rate lb/mmBtu 0-1 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 5.4300E-1 100
. 0 Stk NOXc 

### ppm 0-300 1. 88 1. 88 1. 88 1. 88 1. 88 1. 88 1. 89 1. 90 2.07 1. 79 1.4664E+2 100.0 G12-C7 G12-C8 2>Stk COe 2>Gas Flow

Stk COe Gas hsefh ppm hscfh 0-1000 0-10000 0.18 0.18 0.27 0.18 0.27 0.27 0.27 0.25 0.27 0.18 1.9260E+1 100.0 5401.8 5403.0 5382.6 5380.2 5376.0 5383.8 5389.8 5390.5 5450.4 5331.6 4.1506E+5 100.0 G12-C18 2>NH3 Inj NH3Inj



### 1b/hr 0-1000 106 .2 106.8 106.8 106
. 8 105 .7 106.5 105.2 107.1 109.7 103.8 8.24S2E+3 100.0



### 2>Summary

- I

- Min RATA

- Continued G12-C 2>MW Lo

MW Lo
0-1 56.1 56.1 5S. : 55. ! 55. : S5. ! S5. : 55.6

56. 54. 4.2831E+ 100.



### PagE

# Data Summary Report Company: CPV Sentinel, LLC 62575 Powerline Road Desert Hot Springs, CA Source : Data Group: Report Name: Start of Report: Turbine 2 2>1-Min Cales 2>Summary

- I-Min RATA 02/01/2013 09,10 G12-C4

# ~11'\l\ 

# VII;} l

92240 

# :J-dS'TIL-

- N\-\';-**t~** 

# - (

End of Report, 02/01/2013 10,3 4 G12-ell Gl2 -Cl3 

# tONlt \

'If#-t 

# TRACE
Ellviro llm ell ial Syslems, Illc
.

Validation: All Available Data G12 -ClO G12-C6 G12-C7 G12-CB G12 -C1S 

### Group#-Channel# Long Descrip. Short Descrip. units G12-C2 2>Stk NOx

Stk NOx 2 >Stk 02 2 >NOx Mass G12-C20 2>StkFlow

StkFlow

kscfh 0-300000 G12-C3 2>Stk CD

Stk CO ppm 0-1000 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk CDc 2>Gas Flow 2>NH3 Inj G12-C 2>MW La

MW La 

### Range 02/01/2013 09:10 02/01/2013 09:11 02/01/2013 09 : 12 02/01/2013 09:13 02/01/2013 09:14 02/01/2013 09 : 15 02/01/2013 09:16 02/01/2013 09:17 02/01/2013 09:18 02/01/2013 09:19 02/01/2013 09:20 02/01/2013 09:21 02/01/2013 09:22 02/01/2013 09:23 02/01/2013 09:24 02/01/2013 09:25 02/01/2013 09:26 02/01/2013 09:27 02/01/2013 09:28 02/01/2013 09:29 02/01/2013 09:30 02/01/2013 09:31 02/01/2013 09:32 0 2 /01/2013 09:33 02/01/2013 09:34 02/01/2013 09:35 02/01/2013 09:36 02/01/2013 09:37 02/01/2013 09:38 02/01/2013 09:39


### Date/Time Printed: ppm 0-150 2
. 6 2.5 2 .6 2.4 2.4 2.4 2.5 2.5 2.5 2.5 2.5 2.6 2.5 2.5 2.5 2.6 2.5 2.6 2.6 2
. 5 2.4 2.4 2.4 2.4 2 .4 2.5 2.5 2.5 2.5 2.5 Stk 02 

# • 0-25 13 .41 13 .4 1 13 .4 0 13.41 13.41 13.41 13.41 13 .42 13 .42 13 .40 13 .41 13
. 40 13 .40 13.40 13.40 13.41 13 .41 13 .40 13 .41 13 .41 13 .40 13 .42 13 .41 13 .41 13 .4 1 13. 4 1 13.40 13 .4 1 13.41 13 .41
02/01/2013 16,12 NOx Mass Ib/hr 0-100 5.81 5.08 5.82 5.09 5
. 09 5.08 5.07 5.07 5.07 5.08 5
. 06 5.80 5.08 5.08 5.08 5.79 5.06 5.82 5.81 5
. 06 5.08 5.06 5.07 5
. 06 5.06 5.07 5.09 5.09 5.09 5.08 17661 17651 17655 17671 17674 17636 17592 17634 17638 17605 17581 17602 17626 17625 17609 17589 17579 17654 17647 17582 17628 17584 17593 17556 17572 17592 17655 17664 17664 17627 0
. 7 0
. 7 0.7 0.7 0.7 0.7 0.7 0.8 0.7 0.7 0.8 0.7 0
. 7 0
. 7 0.6 0.6 0.6 0.6 0.6 0.6 0.7 0
. 7 0.7 0.7 0.7 0.7 0.6 0.6 0.6 0.6 CO Mass 

### 1b/hr 0-100 0
. 73 0
. 73 0.73 0.73 0.73 0.73 0
. 72 0
. 72 0.72 0.73 0.72 0.73 0.73 0 .7 3 0.73 0.72 0
. 72 0.73 0.73 0.72 0.73 0.72 0.72 0.72 0
. 7 2 0.72 0.73 0.73 0.73 0
. 73 NDx Rate Ib/mmBtu 0-1 0.008 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.008 0.007 0.008 0
. 008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0
. 007 0.007 Stk NDXc ppm 0-300 2.05 1. 97 2.05 1. 89 1. 89 1. 89 1. 97 1. 97 1. 97 1. 97 1. 97 2.05 1. 97 1. 97 1. 97 2.05 1. 97 2
. 05 2.05 1. 97 1. 89 1. 89 1. 89 1. 89 1. 89 1. 97 1. 97 1. 97 1. 97 1. 97 Stk CDc Gas hscfh NH3Inj ppm 0-1000 0
. 55 0
. 55 0.55 0.55 0.55 0.55 0.55 0.63 0.55 0.55 0.63 0.55 0.55 0.55 0.47 0.47 0.47 0.47 0.47 0.47 0
. 55 0
. 55 0.55 0.55 0
. 55 0.55 0.47 0 .4 7 0.47 0.47 hscfh 0-10000 6920.4 6916.8 6927.6 6924.6 6925.8 6910.8 6893.4 6900.6 6902.4 6907.8 6889.2 6906.6 6916.2 6915.6 6909.6 6892.2 6888.6 6927.0 6915.0 6889.8 6916.8 6881.4 6894.0 6879.6 6885
. 6 6893.4 6927.6 6921.6 6921.6 6907.2 

### Ib/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 1 10.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 0-1 80
.**~** 80. : 80. : 80. : 80
. . 80
. . 79. ' 80.1 80. : 80. ( 79. 79. ' 79. 80. : 79
.**~** 80
. 1 79. ' 79. : 80.1 79
.**~** 80,1 79. ' 79. 79 79. ' 79. 80
. . 79. : 79. : 79. : 

### Pag(

### Group#-Channel# Long Descrip
. Short Descrip
. Units Range 02/01/2013 09:40 02/01/2013 09:41 02/01/2013 09:42 02/01/2013 09:43 02/01/2013 09:44 02/01/2013 09:45 02/01/2013 09:46 02/01/2013 09:47 02/01/2013 09:48 02/01/2013 09:49 02/01/2013 09:50 02/01/2013 09:51 02/01/2013 09:52 02/01/2013 09:53 02/0 1 / 2013 09:54 02/01/2013 09:55 02/01/2013 09:56 02/01/2013 09:57 02/01/2013 09:58 02/01/2013 09:59 02/01/2013 10:00 02/01/2013 10:01 02/01/2013 10:02 02/01/2013 10:03 02/01/2013 10:04 02/01/2013 10:05 02/01/2013 10:06 02/01/2013 10:07 02/01/2013 10:08 02/01/2013 10:09 02/01/2013 10:1 0 02/01/2013 10:11 02/01/2013 10:12 02/01/2013 10:13 02/01/2013 10:14 02/01/2013 10:15 02/01/2013 10:16 02/01/2013 10:17 02/01/2013 10:18 02/01/2013 10:19 

### Date/Time Printed: G12 -C4 G12-Cl1 G12-C20 G12 -C2 2>Stk NOx

Stk NOx 

### ppm 0

- 150 2>Stk 02 2>NOx Mass 2>StkFlow

2.S 2.4 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.S 2.S 2.6 2.6 2.6 2. 4 2.S 2.S 2.6 2.6 2.4 2.4 2.S 2.S 2.S 2.4 2.4 2.S 2.S 2.4 2.4 2.4 2.4 2.4 2.S 2.6 2.4 2.4 2.S 2.4 2.4 Stk 02 

# • 0

- 25 13.40 13.41 13 .41 13 .41 13 .40 13 .40 13 .4 0 13.39 13.39 13.40 13. 4 0 13.39 13.39 13 .40 13.42 13 .41 13.40 13.39 13 .39 13 .39 13 .40 13 .41 13 .40 13 .41 13 .42 13.42 13.41 13.40 13.40 13.41 13.41 13 .42 13.41 13 .4 1 13.40 13 .41 13 .41 13 .40 13 .4 1 13. 43 

### 02/01/2013 16,12 NOx Mass 

### 1b/hr 0-100 5.08 5.06 5.80 5.80 5.80 5.81 5.82 5.80 5.81 5.08 5.08 5.81 5.82 5.84 5.09 5.10 5.11 5.84 5.85 5.10 5.09 5.10 5.09 5.09 5.09 5.10 5.11 5.11 5.11 5.10 5.10 5.08 5.08 5.07 5.80 5.08 5.09 5.10 5.09 5.08 StkFlow ksefh 0

- 300000

17616 17561 17621 17621 17602 17614 17646 17578 17598 17600 17611 17615 17641 17712 17683 17722 17727 17704 17728 17650 17651 17693 17664 17668 17692 17716 17726 17730 17710 17716 17696 17650 17625 17598 17603 17622 17667 17674 17657 17682 G12-C3 G12 -C13 G12 -CIa G12-C6 G12 -C7 G12 -CS G12 -CIS G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk co ppm 0-1000

0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.6 0
. 6 0.6 0.6 0.6 0.6 0.6 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.6 O .S 0.6 0.7 0.6 0.6 0.7 0.7 0.7 0.6 0.6 0.8 0.7 0.6 0.7 0.7 0.7 0.6 CO Mass 

### Ib/hr 0-100 0.73 0 .72 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0
. 73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.72 0.73 0.73 0.73 0.73 0
. 73 0.73 NOx Rate 

### Ib/mmBtu 0-1 0.007 0.007 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.007 0.008 0.008 0.008 0.007 0.007 0.007 0.008 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0 .00 7 0.007 0.008 0.007 0.007 0.007 0.007 0.007 Stk NOXe 

### ppm 0-300 1. 97 1. 89 2.05 2.05 2.05 2.05 2.05 2.12 2.04 1. 97 1. 97 2.04 2.04 2.05 1. 89 1. 97 1. 97 2.04 2.04 1. 89 1. 89 1. 97 1. 97 1. 97 1. 89 1. 89 1. 97 1. 97 1. 89 1. 89 1. 89 1. 89 1. 89 1. 97 2.05 1. 89 1. 89 1. 97 1. 89 1. 90 Stk COe Gas 

### ppm hsefh hsefh 0-1000 0.55 0.55 0.55 0.55 0.55 0.55 0
. 55 0 .47 0.47 0.47 0.47 0.47 0.47 0.47 0.55 0.55 0.55 0.55 0.55 0.55 0.55 0.55 0.47 0.39 0.47 0.55 0.47 0 .47 0.55 0.55 0.55 0.47 0.47 0.63 0.55 0.47 0.55 0.55 0
. 55 0.47 0-10000 6912.0 6881.4 6904.8 6904.8 6906.6 6911.4 6924. a 6906.6 6914.4 6906.0 6910
. 2 6921.0 6931.2 6949.8 6919.8 6944.4 6955.8 6955.8 6965.4 6934.8 6925.8 6933.0 6931. 2 6923.4 6923.4 6933. 

## a 6946.2 6957.0 6949.2 6942.0 6934.2 6907.2 6906.6 6895.8 6907.2 6905.4 6922.8 6934.8 6919.2 6910.2 NH3Inj 

### 1b/hr 0-1000 110.0 110.0 110.0 110. a 110. 

## a 110.0 110 .0 1 10.0 110. 

## a 110.0 110. 

## a 110.0 110.0 110.0 110.0 110. 

## a 110.0 llO.O 110.0 110.0 110.0 llO. 

## a 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110. 

## a 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued MW Lo
0-1 80.1 79
. 79. : 79. : 79.: 79. ! 79. : 80 .1 79. 79
.. 80 80.1 80 .: 80.: 80 .1 80. : 80. : 80. 80. 80. ! 80

. 1 80. 79
. 80
. 1 80 .: 80 .: 80 80. 80 80
.. 80.: 80.1 80 .1 79
.. 80 79. 79. : 79. 79. 79
.. 

### PagE

### Group#-Channel# Long Descrip . Short Descrip . units Range 02/01/2013 10:20 02/01/2013 10:21 02/01/2013 10:22 02/01/2013 10:23 02/01/2013 10:24 02/01/2013 10:25 02/01/2013 10:26 02/01/2013 10:27 02/01/2013 10:28 02/01/2013 10:29 02/01/2013 10:30 02/01/2013 10:31 02/01/2013 10:32 02/01/2013 10 : 33 02/01/2013 10:34 

### Period Average = 

### Period Max Value Period Min Value Period Totals 

## = Period 

### % Recovery



### Date/Time Printed: G12-C2 2>Stk NDx

Stk ND x 

### ppm 0-150 2.5 2.5 2.4 2.4 2.4 2.4 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2
. 5 G1 2 -C4 G12-Cll G12-C20 2>Stk 02 2>NO x Mass 2>StkFlow

Stk 02 

# • 0-25 13.42 13 .39 13 .41 13 .41 13 .42 13
. 41 13 .4 3 13 .43 13
. 4 3 13.43 13
. 42 13 .4 1 13.42 13.42 13
. 42 N Ox Mass lb/hr 0-100 5.09 5.09 5.07 5.07 5
. 05 5.06 5
. 04 5
. 05 5.05 5
. 06 5
. 06 5.06 5.07 5
. 06 5.07 StkFlow kscfh 0-300000

17698 17613 17612 17596 17571 17569 17559 17573 17574 17599 17606 17579 17621 17600 17635 G12-C3 G12-C13 G12-C10 G1 2 -C6 G12-C7 G12-C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk CDc 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk 

### co ppm 0-1000

0.7 0.6 0.6 0.6 0.6 0.7 0
. 6 0.6 0.6 0.6 0.5 0.5 0.6 0.6 0
. 6 CD Mass 

### 1b/hr 0-100 0.73 0.73 0
. 72 0
. 72 0 .72 0.72 0.72 0.72 0.72 0.72 0
. 72 0.72 0.72 0
. 72 0
. 72 NOx Rate lb/mmBtu 0

- 1 0.007 0
. 007 0.007 0
. 007 0
. 007 0
. 007 0
. 007 0
. 007 0.007 0
. 007 0
. 007 0.007 0.007 0.007 0
. 007 Stk NO X c 

### ppm 0-300 1. 97 1. 96 1. 89 1. 89 1. 89 1. 89 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 Stk CDc Gas hscfh hscfh 0-10000 

### ppm 0-1000 0.55 0.47 0.47 0.47 0.47 0.55 0.47 0.47 0.47 0.47 0.39 0.39 0. 4 7 0.47 0.47 6925.8 6920.4 6901.2 6895
. 2 6876.0 6884
. 4 6862.2 6867.6 6868.2 6877
. 8 6889. 8 6888
. 6 6 895. 8 6887.4 6901.2 NH3Inj 

### 1b/hr 0-1000 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 MW Lo
0-1 79
.. 80.1 79
.. 79. : 78. : 79. ! 79 78. : 79 79
.. 79. 79
. . 79.! 79
.. 79
. ! 2.5 13. 4 1 5.24 17635 0.7 0.73 0.007 1.96 0.51 6912.0 110.0 79.8 2
. 7 13.43 5.85 17730 0.8 0
. 73 0
. 008 2
. 12 0.63 6965.4 110.0 80. 2.4 13.39 5.04 17556 0.5 0.72 0
. 007 1.89 0.39 6862.2 110
. 0 78. 2.1180E+2 1. 1396E + 3 4.4566E+2 1. 4 989E+6 5.5600E+1 6.1780E+1 6 .1400E-1 1.6683E+ 2 4.3630E+1 5.8751E+5 9.3500E+3 6
. 7887E+ 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100
. 0 100.

02/01/2013 16 , 12 

### 2>Summary

- I-Min RATA

- Continued**pag~**

# Data Summary Report Company:

S o ur c e : Data Group: Report Name: 

### CPV Sentinel , LLC 62575 Powerline Road Desert Hot Springs, CA Turbine 2 92240

# S~B~\**~Id"** 

# 2-**5-11~\L-** 

# tJ\-\;-1-7-2. 

# .. v.,p1- 

# TRACE
Environmental Systems, 

## [nco

S tart of Report : 

### 2>1-Min Cales 2>Summary

- l-Min RATA 02/01/2013 11,05 End of Report, 02/01/2013 12,15 

### validation: All Available Data G

roup#-Channel# Long De scrip . sho rt De s crip . units Range 02/01/2013 11 : 05 0 2 /0 1 /2013 11 : 06 02/01/2013 11:07 02/01/2013 11:08 02/01/2013 11:09 02/01/2013 11:10 02/01/2013 11:11 02/01/2013 11:12 02/01/2013 11:13 0 2 /01/2013 11:14 02/01/2013 11:15 02/01/2013 11:16 02/01/2013 11:17 02/01/2013 11:18 02/01/2013 11:19 02/01/2013 11:20 02/01/2013 11:21 02/01/2013 11:22 02/01/2013 11:23 02/01/2013 11:24 02/01/2013 11:25 02/01/2013 11:26 02/01/2013 11:27 02/01/2013 11;28 02/01/2013 11:29 02/01/2013 11:30 02/01/2013 11:31 02/01/2013 11;32 02/01/2013 11:33 02/01/2013 11:34


### Date/Time Printed: G12-C4 G12-C11 G12-C2 2>Stk NOx

Stk NOx 2>Stk 02 2>NOx Mass
ppm 0-150 2.4 2.5 2.5 2.4 2.4 2.5 2.5 2.4 2.6 2.5 2
. 5 2
. 3 2.4 2.5 2.5 2.5 2
. 5 2
. 4 

### 2.6 2.4 

### 2.5 2.5 2.6 

### 2.5 2.5 2.4 2.6 

### 2
. 4 2.4 

### 2.4 Stk 02 

# • 0-25 13 .4 1 13
. 40 13.40 13 .42 13 .40 13 .40 13 .40 13 .41 13.39 13 .40 13
. 39 13.39 13.41 13
. 40 13 .40 13 .40 13
. 40 13
. 41 13
. 40 13.40 13
. 40 13.39 13
. 38 13.40 13
. 40 13 .41 13 .41 13 .41 13
. 40 13 .42


### 02/01/2013 16,12 NOx Mass 

### 1b/hr 0-100 5.13 5.14 5.12 5.10 5.13 5.13 5.13 5
. 12 5.85 5.13 5.16 5.15 5.12 5
. 11 5.11 5.10 5.11 5.10 5.84 5.11 5.11 5
. 11 5.84 5.10 5
. 10 5
. 09 5
. 82 5.08 5
. 09 5.08 G12-C20 2>StkFlo w

StkFlow

kscfh 0-300000

17797 17827 17758 17738 17778 17788 17772 17774 17734 17799 17870 17835 17769 17716 17721 17695 17715 17697 17707 17704 17723 17691 17677 17684 17681 17657 17679 17648 17646 17672 G12-C3 2>Stk CO

Stk CO ppm 0-1000

1.8 1.6 1.3 1.1 1.6 1.4 1.7 1.5 1.5 1.4 1.6 1.7 1.6 1.5 1.5 1.8 1.6 1.7 1.6 1.7 1.9 

### 2.0 1.2 1.1 1.3 1.3 1.2 1.0 1.0 1.1 G12 -C13 G12-C10 G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass

Ib/hr 0-100 2.20 2.20 1. 46 1. 46 2
. 20 1. 4 7 2.20 2.19 2.19 1.47 2.21 2.21 2
. 19 2.19 2.19 2.19 2.19 2.18 2.19 2.19 2.19 2
. 92 1. 4 6 1. 46 1.46 1. 45 1. 45 1. 45 1.45 1.45 NOx Rate Ib/mmBtu 

### 0-1 0.007 0.007 0.007 0
. 007 0.00 7 0.007 0.007 0
. 007 0
. 008 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.008 0.007 0.007 0.007 Stk NOXc ppm 0-300 1. 89 1. 97 1. 97 1. 89 1. 89 1. 97 1. 97 1. 89 2.04 1. 97 1.96 1. 81 1. 89 1. 97 1. 97 1. 97 1. 97 1. 89 2.05 1. 89 1. 97 1.96 2
. 04 1. 97 1. 97 1. 89 2.05 1. 89 1. 89 1. 89 G12-C7 G12-C8 2>Stk CDc 2>Gas Flow

Stk COc Gas hscfh ppm 0-1000

1.42 1. 26 1. 02 0.87 1. 26 1.10 1. 34 1.18 1.18 1.10 1.26 1.34 1.26 1.18 1.18 1.42 1. 26 1. 34 1. 26 1. 34 1. 49 1. 57 0.9 4 0.87 1. 02 1. 02 0.95 0.79 0.79 0.87 hscfh 0-10000 6973.8 6994.8 6967.8 6 9 41.4 6975.6 6979.8 6973.2 696 4 .8 6967.8 6984.0 7021. 2 7007
. 4 6963.0 6951.6 6953.4 6943.2 6951.0 6934.8 6948.0 6946.8 6954.0 6 9 51.0 695 4 .6 6 9 39.0 6 9 37.8 6919.2 6927.6 6915.6 6924.0 6915.6 G12-C18 2>NH3 Inj NH3Inj

lb/hr 0-1000 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110
. 0 110
. 0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110
. 0 110.0 G12-C 2>MW Lo

MW Lo



### 0-1 80
. 1 80
.. 80
. 80.1 80.1 80. : 80. : 80.1 80. : 81.: 80. 80.: 80.1 79
.. 80.1 79
.. 79. ! 79. ! 79. : 79
.. 79
. . 79
.. 79
. ! 79
.. 79
. 79
. . 79
.. 79
. : 79. : 79
.. pagEGroup#-Channel# Long Descrip
. Short Descrip. Un its Range 02/01/2013 11:35 02/01/2013 11:36 02/01/2013 11:37 02/01/2013 11:38 02/01/20 13 11:39 02/01/2013 11:40 02/01/2013 11:41 02/01/2013 11:42 02/01/2013 11:43 02/01/2013 11:44 02/01/2013 11:45 02/01/ 2013 11:46 02/01/2013 11;47 02/01/2013 11:48 02/01/2013 11:49 02/01/ 2 013 11:50 02/01/2013 11:51 02/01/2013 11:52 02/01/2013 11:53 02/01/2013 11:54 02/01/2013 11:55 0 2/01/2013 11:56 02/01/2013 1 1 :57 02/01/2013 11:58 02/01/2013 11:59 02/01/2013 12:00 02/01/2013 12:01 02/01/2013 12:02 02/01/2013 12:03 02/01/2013 12:04 02/01/2013 12:05 02/01/2013 12:06 02/01/2013 12:07 02/01/2013 12:08 02/01/2013 12:09 02/01/2013 12:10 02/01/2013 12:11 02/01/2013 12;12 02/01/2013 12;13 02/01/2013 12:14 

### Date/Time Printed:**G12~C4** G12-C11 G12-C20 G12 -C 2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass 2>StkFlow

2.4 2.5 2.6 2.5 2
. 4 2.6 2.5 2.5 2.5 2.4 2.5 2.5 2.6 2.5 2.6 2.6 2.5 2.5 2.5 2.6 2.6 2.5 2.5 2.5 2.5 2.4 2.4 2.5 2.5 2.5 2.6 2.5 2.3 2. 4 2.4 2.5 2.3 2.3 2.4 2.4 Stk 02 \ 0-25 13 .42 13 .41 13 .39 13 .39 13 .40 13.39 13 .40 13 .40 13.39 13.40 13.41 13.41 13.41 13.40 13 .4 0 13.39 13.39 13.40 13.40 13. 40 13 .40 13 .40 13 .39 13 .40 13.39 13.39 13.40 13.38 13.38 13 .39 13.38 13 .38 13 .40 13.39 13.39 13.37 13.39 1 3.40 1 3.39 13 .38
02/01/2013 16012 NOx Mass 

### Ib/hr 0-100 5.09 5.09 5.83 5.10 5.09 5.84 5.08 5.08 5.10 5.07 5.08 5.09 5.80 5.07 5.80 5.80 5.08 5.06 5.07 5.79 5.80 5.07 5.09 5.07 5.07 5.08 5.07 5.09 5.08 5.09 5.82 5.11 5.11 5.11 5.10 5.12 5.11 5.10 5.10 5.09 StkFlow kscfh 0-300000

17695 17665 17672 17659 17645 17697 17626 17629 17646 17586 17622 17656 17633 17571 17593 17566 17577 17559 17576 17580 17591 17585 17642 17 596 17571 17586 17568 17589 17566 17629 17618 17683 17703 17708 17655 17689 17696 1769 4 17646 17616 G12-C) G12-C13 G12 -CI0 G12-C6 G12-C7 G12

- C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO 

### ppm 0-1000

1.3 1.1 1.3 1 4 1.1 1.0 0 .8 0. 9 0.8 0.8 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.5 0.4 0.4 0.4 0.3 0.3 0.2 0
. 1 0.2 0.2 0.2 0.2 0.1 0.2 0.1 0.2 0.2 0.2 0.1 0 .2 0. 2 0.2 0.2 CO Mass 

### Ib/hr 0-100 1.45 1.45 l.46 l. 46 l. 45 1.46 0.73 1. 45 0 .7 3 0.72 0.73 0
. 73 0.73 0.72 0.72 0.72 0.73 0.72 0.72 0.72 0.72 0. 72 0.73 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0
. 00 0.00 0.00 0.00 NOx Rate 

### Ib/mmBtu 0-1 0.007 0.007 0.008 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.008 0.008 0.007 0.007 0.007 0.008 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXc 

### ppm 0-300 l. 89 1. 97 2.04 l. 96 l. 89 2.04 l. 97 1. 97 1. 96 1. 89 l. 97 1. 97 2.05 1. 97 2.05 2.04 1. 96 l. 97 1. 97 2.05 2.05 1. 97 1.96 l. 97 1. 96 1. 89 1. 89 l. 96 l. 96 l. 96 2.04 1. 96 l. 81 l. 89 1. 89 1. 96 l. 81 l. B1 1. B9 l. BB Stk COe Gas 

### ppm hscfh hscfh 0-1000 l. 03 0.87 l. 02 l.10 0.87 0.79 0.63 0.71 0.63 0.63 0
. 55 

### o 47 0 .4 7 0.47 0.47 0.47 0.47 0.39 0.31 0.31 0.31 0.24 0.24 0.16 0.08 0.16 0.16 0
. 16 0.16 0.08 0.16 0.08 0.16 0.16 0.16 0.08 0.16 0.16 0.16 0
. 16 0-10000 6924.6 6922.2 6943.2 6938.4 6923.4 6953.4 6916.2 6917.4 6933.0 6900.6 6905.4 6918.6 6909.6 6894.6 6903.0 6901.8 6906.0 6889.8 6896.4 6B98.2 6902.4 6900.0 6931. 8 6904 .2 6903.6 6909.6 6893.4 6919.8 6910.8 6926.4 6931.2 6957.0 6946.2 6957.6 6936.6 6968.4 6952.8 6942.6 6933.0 6930.6 NH3Inj 

### lb/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 llO.O 110.0 110.0 110 .0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 l10.0 llO.O 110.0 l10.0 110.0 110.0 

### 2>Summary

- 1-Min RATA

- Continued MW La
0

- 1 79.: 79
. . 80.1 79. : 79. ' 80.1 79
.. 79 79. ! 79.: 79. : 79.! 79
.. 79
.. 79
.. 79. : 79.: 79. ! 79. : 79
. : 79. : 79
. . 79
.. 80
. 1 79. : 79
.. 79. 80.1 79
. 79
. . 80. ( 80
. . 80. ( 80. 79. : 80
.. 80
. ! 80. : 79. : 80. : 

### pag EGroup#-Channel# G12

- C2 G12-C 4 G12 -C11 G12-C20 G12-C3 G12 -C13 G12

- C10 G12-C6 G1 2- C7 G12

- C8 G12

- C18 G12

- C Long Descrip. 2>Stk NOx 2;:.Stk 02 2;:.NO x Mass 2;:.StkFlow 2;:.Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXe 2>Stk COe 2;:.Gas Flow 2;:.NH3 Inj 2>MW Lo Short Descrip
. Stk NOx Stk 02 NOx Mass StkFlow Stk CO CO Mass NOx Rate Stk NOXe Stk COe Gas hsefh NH3Inj MW Lo Units ppm 

# • Ib/hr ksefh ppm Ib/hr Ib /mmBtu ppm ppm hsefh Ib/hr Range 0-150 0-25 0-100 0-300000 0 -1 000 0-100 0-1 0-300 0-1000 0-10000 0-1000 0-1 02/01/2013 12:15 2.4 13.38 5.09 17619 0.2 0.00 0.007 1. 88 0.16 6931.8 110.0 80. : Period Average 2.S 13.40 5.22 17671 0
. 9 1.12 0.007 1. 95 0.72 6936.2 110.0 79.8 Period Max Value 2.6 13.42 5.85 17870 2.0 2.92 0.008 2.05 1. 57 7021.2 110.0 8l. Period Min Value 2.3 13.3 7 5.06 17559 0.1 0.00 0.007 1. 81 0
. 08 6889.8 110.0 79. Period Totals 

## = 1.7580E+2 9.5122E+2 3
. 7069E+2 1.2546E+6 6.4600E+1 7
. 9480E+1 5.0900E-1 1.3831E+2 5.0890E+1 4.9246E+5 7.8100E+3 5.6660E + Period 

### % Recovery 100.0 100
. 0 100.0 100.0 100.0 100.0 100.0 100.0 100
. 0 100.0 100.0 100.



### Date/Time Printed: 02/01/2013 16,12 2>Summary - I

- Min RATA

- Continued**pag~**

# Data Summary Report Company: CPV Sentinel, LLC 62575 Powerline Road Desert Hot Springs, CA Source: 

### Data Group: Report Name : 

### Turbine 2 2>1-Min Cales 92240

# ~+1l\Ll 

# G

.. if 1- [2km (2....t\ 

# ICoWl{'fiWiL(.. /0(1 /0 

# TRACE
Environmental Systems, Inc.

Start of Report: 2> I-Min Summary

- RATA 01/30/2013 11,01 End of Report, 01/30/2013 12,17 

### Validation: All Available Data Group#-Channel# 

### Long Descrip. Short Descrip. Units Range 01/30/2013 11:01 01/30/2013 11:02 01/30/2013 11:03 01/30/2013 11:04 01/30/2013 11:05 01/30/2013 11:06 01/30/2013 11:07 01/30/2013 11;08 01/30/2013 11;09 01/30/2013 11;10 01/30/2013 11:11 01/30/2013 11:12 01/30/2013 11:13 01/30/2013 11:14 01/30/2013 11:15 01/30/2013 11:16 01/30/2013 11:17 01/30/2013 11:18 01/30/2013 11:19 01/30/2013 11:20 01/30/2013 11:21 01/30/2013 11:22 01/30/2013 11:23 01/30/2013 11:24 01/30/2013 11:25 01/30/2013 11:26 01/30/2013 11:27 01/30/2013 11:28 01/30/2013 11:29 01/30/2013 11:30


### Date/Time Printed: G12-C4 Gl2-ell G12-C2 2>Stk NOx

Stk NOx 2 >Stk 02 2 >NOx Mass 

### ppm 0-150 3.0 2.9 3.0 3.0 3.0 3.0 3.0 3.0 2.8 3.0 2.9 2.8 2.8 3.0 2.8 3.0 2.8 3.1 2.8 2.9 2.8 2.9 2.9 2.9 2.8 2.9 3.0 2.9 2.9 2.9 Stk 02 

# • 0-25 13.02 13.02 13.02 13.03 13.01 13.02 13.03 13.03 13.04 13.03 13.04 13.05 13.05 13.04 13.05 13.04 13.05 13.02 13.04 13.05 13.06 13.06 13.05 13.04 13.03 13.03 13.02 13.03 13.02 13.03
01/30/2013 13 ,14 NDx Mass 

### Ib/hr 0-100 7.11 7.10 7.10 7.11 7.12 7.10 7.10 7.09 7.09 7.10 7.08 7.07 7.06 7.06 7.05 7.06 7.07 7.96 7.05 7.08 7.07 7.08 7.08 7.08 7.09 7.09 7.10 7.08 7.08 7.06 G12-C20 2>StkFlow

StkFlow

kscfh 0-300000

20528 20492 20506 20544 20546 20511 20525 20505 20532 20540 20496 20493 20478 20427 20434 20430 20483 20425 20419 20515 20512 20541 20516 20494 20486 20499 20487 20476 20435 20409 G12-C3 2>Stk CO

Stk CO 

### ppm 0-1000

3.2 3.3 3.2 3.3 3.2 3.2 3.2 3.0 3.1 3.1 3.2 3.3 3.6 3.4 3.1 3.2 2.9 3.4 2.4 3.S 3.7 3.7 3.S 3.0 3.0 2.9 2.9 2.8 2.8 3.0 G12

- CD GIZ-ClD G12-C6 2>CO Mass 2>NOx Rate 2>Stk NDXc



### co Mass 1b/hr 0-100 4.44 5.32 4.44 5.33 4.4 5 4.44 4.44 4.43 4.43 4.44 4.43 5.30 5.30 5.29 4.41 4.41 4.42 5.30 3.53 5.31 5.30 5.31 5.31 4.42 4.43 4.43 4.43 4.43 4.42 4.41 NDx Rate 

### Ib/mmBtu 0-1 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.009 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 

### Stk NOXc ppm 0-300 2.25 2.17 2.25 2.25 2.24 2.25 2.25 2.25 2.10 2.25 2.18 2.10 2.10 2.25 2.10 2.25 2.10 2.32 2.10 2.18 2.11 2.18 2.18 2.18 2.10 2.17 2.25 2.17 2.17 2.17 G12-C7 G12

- CB 2>Stk CDc 2>Gas Flow



### Stk CDc Gas hscfh ppm hscfh 0-1000 0-10000 2.40 2.47 2.40 2.47 2.39 2.40 2.40 2.25 2.33 2.32 2.40 2.48 2.71 2.55 2.33 2.40 2.18 2.55 1. 80 2.63 2.78 2.78 2.63 2.25 2.25 2.17 2.17 2.10 2.10 2.25 8463.0 8448.0 8454.0 8458.8 8481.0 8455.8 8451.0 8442.6 8443.2 8457.0 8428.2 8416.2 8410.2 8400.0 8392.2 8401.2 8412.0 8420.4 8396.4 8425.2 8413.2 8425.2 8425.8 8427.6 8434.8 8440.2 8446.2 8430.6 8424.6 8403.0 GI2

- C1S 2>NH3 Inj NH3Inj



### 1b/hr 0-1000 110.0 110.0 110.0 110 .0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 G12-C 2>MW La

MW La

0-1 102. ' 10 2.: 103.: 102. ' 103.: 102. : 103.1 102. ' 103.1 102. : 102.: 102. 102 102
.. 101.: 102
. ! 102.: 10 2. : 102.1 102. : 102.1 102.1 102. ' 102. : 102. : 102. : 102
.. 102
. : 102.: 102.1 

### PagE

### Group#-Channel# Long De scrip. Short vescrip. Units Range 01/30/2013 11;31 01/30/2013 11;32 01/30/2013 11:33 01/30/2013 11:34 01/30/2013 11;35 01/30/2013 11:36 01/30/2013 11:37 01/30/2013 11:38 01/30/2013 11:39 01/30/2013 11:40 01/30/2013 11:41 01/30/2013 11:42 01/30/2013 11:43 01/30/2013 11:44 01/30/2013 11:45 01/30/2013 11:46 01/30/2013 11:47 01/30/2013 11:48 01/30/2013 11:49 01/30/2013 11:50 01/30/2013 11:51 01/30/2013 11:52 01/30/2013 11:53 01/30/2013 11:54 01/30/2013 11:55 01/30/2013 11:56 01/30/2013 11:57 01/30/2013 11:58 01/30/2013 11:59 01/30/2013 12:00 01/30/2013 12:01 01/30/2013 12;02 01/30/2013 12:03 01/30/2013 12;04 01/30/2013 12:05 01/30/2013 12:06 01/30/2013 12:07 01/30/2013 12:08 01/30/2013 12;09 01/30/2013 12:10 

### Date/Time Printed: G12

- C4 G12

- Cl1 G 1 2

- C20 G12-C2 2>Stk NOx

Stk NOx 2>Stk 02 2>NOx Mass 2>StkFlow
ppm 0-150 3.0 2.9 2.9 2.8 3.0 3.0 2.9 3.0 3.0 3.1 3.0 2.9 2.9 2.9 2.9 3.0 3.0 2.9 2.9 2.9 2.9 2.9 2.9 3.0 3.0 3.0 3.0 2.9 3.0 2.9 3.0 3.0 2.9 2.9 2.9 2.9 3.0 2.9 2.9 3.0 stk 02 

# • 0-25 13.03 13.03 13.02 13.02 13.02 13.02 13.02 13.01 13.02 13.00 13.00 13.01 13.01 13. 01 13.02 13.01 13.02 13. 02 13.02 13.02 13.02 13.02 13.01 13.00 13.00 13.00 13.01 13.02 13.00 13.01 13.00 12.99 13. 01 13.00 13.00 12.99 13.00 12.99 12.99 12.98
01/30/2013 13,14 NOx Mass I b/hr 0-100 7.08 7.07 7.09 7.09 7.09 7.09 7.09 7
. 08 7.08 7.99 7.10 7
. 08 7.09 7.08 7.08 7.07 7.08 7.08 7.06 7.07 7.07 7.06 7.06 7.08 7.09 7.0B 7.09 7.07 7.10 7.09 7.10 7.11 7.10 7
. 09 7.09 7.09 7.09 7.11 7.10 7.12 StkFlow kscfh 0-300000

20463 20448 20479 20476 20485 20476 20469 20432 20457 20465 20439 20415 20437 20421 20451 20389 20441 20434 20393 20407 20428 20384 20371 20380 20409 20401 20448 20422 20456 20459 20441 20462 20469 20430 20431 20407 20421 20440 20430 20442 G12-C3 G12

- C13 G12-C10 G12

- C6 G12

- C7 G12

- C8 G12

- C18 G12

- C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO ppm 0-1000

2.9 2.8 2.8 2.8 2.7 2.8 2.8 2.8 2.8 2.7 2.8 2.8 2.7 2.7 2.9 2.8 2.7 2.7 2.8 2
. 7 2.8 2.8 2.8 2.7 2.7 2.7 2.7 2.8 2.6 2.8 2.6 2.6 2.7 2.6 2.7 2.6 2.7 2.5 2.7 2.4 CO Mass Ib/hr 0

- 100 4.42 4.42 4.43 4.43 4.43 4.43 4.43 4.43 4.43 4.44 4.44 4.42 4.43 4.43 4.43 4.42 4.42 4.42 4.41 4.42 4.42 4.41 4.41 4.42 4.43 4.43 4.43 4.42 3.55 4.43 3.55 3.56 4.44 3.55 4.43 3.55 4.43 3.55 4.44 3.56 NOx Rate Ib/mmBtu 0-1 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.009 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0
. 008 0.008 0.008 Stk NOXe ppm 0

- 300 2.25 2.17 2.17 2.10 2.25 2.25 2.17 2.24 2.25 2.32 2.24 2.17 2.17 2.17 2.17 2.24 2.25 2.17 2.17 2.17 2.17 2.17 2.17 2.24 2.24 2.24 2.24 2.17 2.24 2.17 2.24 2.24 2.17 2.17 2.17 2.16 2.24 2.16 2.16 2.23 Stk COe Gas hsefh ppm hscfh 0-1000 0-10000 2.17 8425.2 2.10 8419.2 2.10 8442.6 2.10 8441.4 2.02 8445.0 2.10 8441.4 2.10 8438
. 4 2.09 8434.2 2.10 8433.6 2.02 8458.2 2.09 8447.4 2.09 8427
. 0 2.02 8436.0 2.02 8429.4 2.17 8431.2 2.09 8416.2 2.02 8427.0 2.02 8424.0 2.10 8407.2 2.02 8413.2 2.10 8421.6 2.10 8403.6 2.09 8409.0 2.02 8423.4 2.02 8435.4 2.02 2.02 2.10 1. 94 2.09 1. 94 1. 94 2.02 1. 94 2.02 1. 94 2.02 1. 86 2.01 1. 79 8431.8 8440.8 8419.2 8454.6 8445.0 8448.6 8467.8 8449.2 8443.8 8444.4 8445.0 8440.2 8458 . 8 8454.6 8470.2 NH3Inj Ib/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2> I-Min Summary

- RATA

- Continued MW Lo
0

- 1 1 02.! 102
. : 102
.. 102. ! 102
. . 102. : 102
.. 102. : 102 .: 102. l 103. 1 102.! 102. : 102.l 103.: 102.: 102 .: 102
. . 102. 102. : 102
.. 102.: 102. ! 102. : 102.l 102. 102. 102
. : 103. : 102
. . 102 103. : 102.: 102. : 102. ! 102. : 102.: 103. t 103
.. 103
. . 

### Pagt

### Group#-Channel# Long Descrip. Short De s cr i p. Units Range 01/30/2013 12:11 01/30/2013 12:12 01/30/2013 12:13 01/30/2013 12:14 01/30/2013 12:15 01/30/2013 12:16 01/30/2013 12:17 

### Peri od Average Peri od Max Value Period Min Value Period Totals "" P e riod 

### % Recovery

Date/Time Printed: G12-C4 G12-C11 G12

- C20 G12-C3 GI2

- Cl3 GI2

- CIO G12

- C6 G12-C7 GI2-CB GI2-CIS G 1 2

- C G12-C2 2:>Stk NOx Stk NOx 2:>Stk 02 2 :>NOx Mass 2:>StkFlow 2:>Stk CO 2:>CO Mass 2:>NOx Rate 2:>Stk NOXe 2:>Stk COe 2:>Gas Flow 2:>NH3 Inj 2:>MW Lo
ppm 0-150 2.9 3.0 3.0 2.9 Stk 02 

# • 0-25 13.00 12.98 12.97 12.98 NOx Mass Ib/hr 0-100 7.10 7.13 7.14 7.12 StkFlo w kscfh 0-300000

20460 20477 20494 20456 Stk CO ppm 0

- 1000

2
. 6 2.5 2.5 2.6 CO Mass Ib/hr 0-100 3.55 3.56 3.57 3.56 NOx Rate Ib/mmBtu 0-1 O.OOB 0.008 0.008 0.008 Stk NOXe ppm 0

- 300 2.17 2.23 2.23 2.16 3.1 12.98 8.00 20429 2.4 3.56 0.009 2.31 3.1 12.97 7.14 20490 2.6 3.57 0.008 2.31 3.1 12.97 7.13 20447 2.3 3.56 0.008 2.31 2.9 13.02 7.12 20459 2.9 4.37 0
. 008 2.20 3.1 13.06 8.00 20546 3.7 5.33 0.009 2.32 2.8 12.97 7.05 20371 2
. 3 3
. 53 0.008 2.10 2.2640E+2 1. 0022E+3 5.4846E+2 1. 5753E+6 2.2160E+2 3. 3662E+2 6.1900E-1 1. 6942E+2 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 Stk COe Gas hscfh ppm hscfh 0-1000 0-10000

1. 94 1. 86 1. 86 1. 94 1. 79 1. 93 1. 71 2.15 2.78 1. 71 1.6589E+2 100.0 8456.4 8484.6 8502.6 8476.2 8464.8 8500.8 8482.8 8438.2 B502.6 8392.2 6.4974E+5 100.0 NH3Inj Ib/hr 0

- 1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 8.4700E+3 100.0

01/30/2013 13,14 2:> l-Min Summary

- RATA

- Continued 

### MW Lo
0

- 1 102. : 103. : 104.1 103
. . 103. : 103. ! 103. : 102.6

104. 101. 7.9037E+ 100.



### Pagt

# Data Summary Report Com pany : CPV Sentinel, LLC 62575 Powerline Road 

### Desert Hot Springs, CA Source : Turbine 2 Data Group : 2>1-Min Cales 

### Report Name : 2>Summary

- I-Min RATA S t art of Report : 

### 01/30/2013 13,11 G12-C4 

### 92240 

# 7 CU1 

# foll.\**~** 

# t L 

# (lfM-**~**

# ... '2

# ~'**\~ ~Q1~4** **n't** End of Report, 

### 01/30/2013 15 , 05 GI2

- CII G12-C20 G12-C3 G12-C13 GI2-CIO 

# TRACE

/CO 

# I/o Ellv ir o nme ll ta l Syste ms , ItI C.

Validation: 

### Valid Data Onl y G12-C6 G12-C7 G12

- Ca GI2 -C lS G12-C 

### Group#-Channel# Long Descrip
. Short Descrip
. 

### Units G12-C2 2>stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass 2>StkFlow 2>Stk 

### co 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk CDc 2 >Gas Flow 2>NH3 Inj 2>MW La


### Range 01/30/2013 13:11 01/30/2013 13:12 01/30/2013 13:13 01/30/2013 13:14 01/30/2013 13:15 01/30/2013 13:16 01/30/2013 13:17 01/30/2013 13:18 01/30/2013 13:19 01/30/2013 13:20 01/30/2013 13:21 01/30/2013 13:22 01/30/ 2 013 1 3:23 01/30/ 2 013 13:24 01/30/2013 13:25 01/30/2013 13:26 01/30/2013 13:27 01/30/2013 13;28 01/30/2013 13:29 01/30/2013 13:30 01/30/2013 13:31 01/30/ 2 013 13:32 01/30/2013 13:33 01/30/2013 13:34 01/30/2013 13:35 01/30/2013 13:36 01/30/2013 13:37 01/30/2013 13:38 01/30/2013 13:39 01/30/2013 13:40


### Date/Time Printed: 2.8 2.8 2.9 2.8 2.8 2.7 2.8 2.8 2.8 2.8 2.8 2.8 2.7 2.8 2.7 2.8 2.7 2.9 2.9 2.8 2.9 2.9 2.9 2.9 2.8 2.8 2.8 2.7 2.7 2.8 Stk 02 

# • 0- 2 5 12.96 12.95 12.94 12.96 12
. 95 12 .96 12.95 12.94 12
. 94 12.95 12.96 12.96 12.96 12. 9 6 12.96 12.96 12.97 12.94 12.91 12.93 12.9 3 12.93 12
. 92 12.92 12.93 12.93 12.94 12.96 12.95 12.95


### 01/31/2013 12,20 NOx Mass Ib/hr 0 -1 00 7.10 7.12 7.13 7.11 7.11 6.22 7.10 7.11 7.09 7.10 7
. 09 7.08 6.20 7.08 6.20 7.08 6.19 7.12 7.16 7.15 7.14 7.15 7.14 7.14 7.15 7.13 7.12 6.21 6.21 7.10 StkFlow kscfh 0-300000

20356 20375 20384 20366 20359 20360 20309 20325 20274 20327 20310 20304 20302 20 2 88 20317 20285 20308 20368 20395 20400 20391 20 4 1 4 20370 20363 20403 20361 20355 20337 20320 20333 Stk 

## co ppm 0-1000

2 .5 2.6 2.5 2.6 2.6 2.8 2.6 2.9 2.7 2.7 2.7 2.8 2.8 2.7 3.0 2.7 2.9 2.9 2.6 2.8 2.6 2.6 2.8 2.5 

### 2.5 2.8 2.6 2 .5 2.9 2.7 CO Mass Ib/hr 0

- 100 3.55 ).56 3.57 3.55 3.56 4.44 3.55 4.44 3.55 3.55 3.54 4.43 4.43 3.54 4.43 3.54 4.42 4.4 5 3.58 4.47 3.57 3.58 4.47 3.57 3.57 4.46 3.56 3.55 4.44 3.55 NOx Rate Ib/mmBtu 0-1 0.008 0.008 0.008 0.008 0.008 0
. 007 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.007 0.008 0.007 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.007 0.008 Stk NOXc ppm 0

- 300 2.08 2.08 2.15 2.08 2.08 2.01 2.08 2.08 2.08 2.08 2.08 2.08 2.01 2.08 2. 01 2.08 2.01 2.15 2.14 2.07 2.15 2.15 2.14 2.14 2.07 2.07 2.08 2.01 2.00 2.08 Stk COe Gas hsefh p pm hsefh 0-1000 0-10000

1.86 8455.8 1.93 8474.4 1.85 8488.8 1.93 8460.0 1.93 8467.8 2
. 08 8457.6 1.93 8446.8 2.15 8464.2 2.00 8443.2 2.00 8454.6 2.01 8436.6 2.08 8434.2 2. 08 8433.6 2 .01 8427.6 2.23 8439.6 2.01 8426.4 2.16 8425.2 2.15 8482.2 1.92 8525.4 2.07 8506.2 1.92 8502.6 1. 92 2
. 07 1. 85 1. 85 2.07 1. 93 1. 86 2.15 2.00 8512.2 8504. 4 8501.4 8507.4 8490.0 8476.8 8448.0 8451.6 8457.0 NH3Inj Ib/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0

63.2 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110 .0 110.0 110.0 110.0 MW Lo
0-1 103.: 103. : 103. 103. ( 103
.. 102.1 102.: 103.: 102
.. 102
.. 103.! 102
.. 102
. . 10 2
.. 102
.. 102. ! 102.'**103.~** 104.' 103. 103. ' 103.' 103,! 103.' 103. 1 03,! 103 102,' 103.: 102.' Pagt

### Group#-Channel# Long Descrip . Short Des c r i p. Units Range 01/30/2013 13:41 01/30/2013 13:42 01/30/2013 13:43 01/30/2013 13:44 01/30/2013 13:45 01/30/2013 13:46 01/30/2013 13:47 01/30/2013 13:48 01/30/2013 13:49 01/30/2013 13:50 01/30/2013 13:51 01/30/2013 13:52 01/30/2013 13:53 01/30/2013 13:54 01/30/2013 13:55 01/30/2013 13:56 01/30/2013 13:57 01/30/2013 13;58 01/30/2013 13:59 01/30/2013 14:00 01/30/2013 14:01 01/30/2013 14:02 01/30/2013 14:03 01/30/2013 14:04 01/30/2013 14;05 01/30/2013 14:06 01/30/2013 14:07 01/30/2013 14:0B 01/30/2013 14:09 01/30/2013 14:10 01/30/2013 14:11 01/30/2013 14:12 01/30/2013 14:13 01/30/2013 14:14 01/30/2013 14:15 01/30/2013 14:16 01/30/2013 14:17 01/30/2013 14:1B 01/30/2013 14:19 01/30/2013 14:20 

### Date/Time Printed: G12

- C2 G12-C4 2>Stk NOx 2>Stk 02

Stk NOx Stk 02 ppm 

# • 0-150 0-25 2.8 12.95 2.7 12.96 2.7 12.95 2.7 12.95 2.8 12.95



### 01/31/2013 12,20 G12-C11 2>NOx Mass

NOx Mass Ib/hr 0-100 7.09 6.20 6.20 6.20 7.10 G12-C20 G12-C3 G12-Cl3 2>StkFlow 2>Stk CO 2>CO Mass

StkFlow Stk CO cb Mass

kscfh ppm Ib/hr 0-300000 0 -1000 0-100

20306 2.7 3.55 20301 2.7 3.54 20293 2
. ' 4.43 20270 2.8 4.43 20332 3.0 4.44 G12-CI0 G12-C6 G12-C7 G12

- C8 G12-C18 G12-C 2>NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW La

NOx Rate Stk NOXe Stk COe Gas hsefh NH3Inj MW La Ib/mmBtu ppm ppm hscfh Ib/hr 0-1 0 -3 00 0-1000 0-10000 0-1000 0-1 0.008 2.08 2.00 8445.6 110.0 103
.. 0.007 2.01 2.0 1 8433.0 110.0 103.4 0.007 2.00 2.15 B440.2 110.0 102. 0.007 2.00 2.08 8430.6 110.0 103.4 O.OOB 2.0B 2.23 B456.4 110.0 102. '



### 2>Summary

- l-Min RATA

- Continued PagE

### Group# - Channel# Long Descrip . S hort Descr i p . Units Range 01/30/2013 14:21 01/30/2013 14:22 01/30/2013 14:23 01/30/2013 14:28 01/30/2013 14 :29 01/30/2013 14 :30 01/30/2013 14:31 01/30/2013 14:32 01/30/2013 14:33 01/30/2013 14:34 01/30/2013 14:35 01/30/2013 14:36 01/30/2013 14:37 01/30/2013 14:38 01/30/2013 14:39 01/30/2013 14:40 01/30/2013 14:41 01/30/2013 14:42 01/30/2013 14:43 01/30/2013 14:44 01/30/2013 14:45 01/30/2013 14:46 01/30/2013 14:47 01/30/2013 14:48 01/30/2013 14:49 01/30/2013 14:50 01/30/2013 14:51 01/30/2013 14:52 01/30/2013 14:53 01/30/2013 14:54 01/30/2013 14:55 01/30/2013 14:56 01/30/2013 14:57 01/30/2013 14:58 01/30/2013 14:59 01/30/2013 15:00 01/30/2013 15:01 01/30/2013 15:02 01/30/2013 15:03 01/30/2013 15:04 

### Date/Time Printed: G12-C4 G12-Cl1 G12-C20 G12 -C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass 2>StkFlow

2.5 2.6 2.5 2.6 2.6 2.6 2.7 2.5 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.6 2.7 2.7 2.6 2.7 2.7 2.7 2.6 2.7 2.7 2.7 2.6 2.7 2.6 2.7 2.6 2.7 Stk 02 

# • 0-25

12.95 12.95 12.95 12.95 12.94 12.96 12.95 12.97 12.96 12.96 12.96 12.97 12.96 12.96 12.95 12.95 12.96 12.95 12.94 12.94 12.95 12.95 12.94 12.95 12.95 12.95 12.95 12
. 96 12.94 12.95 12.95 12.96 12.96 12.95 12
. 95 12.95 12.95 

### 01/31/2013 12,20 NOx Mass Ib/hr 0-100

6.20 6.19 6.19 6.19 6.18 6.18 6.16 6.17 6.17 6.17 6.17 6.17 6.17 6.18 6.18 6.18 6.18 6.18 6.19 6.19 6.18 6 .18 6.19 6.17 6.19 6.19 6.18 6.18 6
. 18 6.18 6.18 6.16 6.17 6.17 6.17 6.17 6.18 StkFlow ksefh 0-300000

20288 20238 20261 20234 20205 20232 20167 20225 20210 20206 20207 20224 20197 20249 20228 20231 20237 20231 20210 20212 20218 20215 20218 2 0197 20261 20254 20215 20243 20201 20222 20203 20167 20197 20180 20186 20189 20225 G12-C3 G12

- Cl3 G12-C10 G12-C6 G12-C7 G12
- C8 G12-C18 G12-C
. 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO ppm 0-1000

2.0 1.9 1.9 2.0 1.9 1.9 1.8 1.8 1.6 1.6 1.7 1.7 1.5 1.6 1.5 1.6 1.4 1.5 1.5 1.5 1.6 1.7 1.7 1.5 1.7 1.5 1.4 1.6 1.5 1.6 1.6 1.5 1.5 1.6 1.4 1.5 1.4 CO Mass 1b/hr 0-100

2.66 2.65 2.65 2.65 2.65 2.65 2.64 2.64 2.64 2.64 2.64 2.64 1. 76 2.65 1. 77 2.65 1. 77 1. 77 1. 77 1. 77 2.65 2.65 2.65 1. 76 2.65 1. 77 1. 77 2.65 1. 77 2.65 2.65 1. 76 1. 76 2.64 1. 76 1. 76 1. 77 NOx Rate Ib/mmBtu 0-1

0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXe ppm 0-300

1. 86 1. 93 1. 86 1. 93 1. 93 1. 93 2.00 1. 86 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 2.00 1. 93 1. 93 2.00 2.00 1. 93 2.00 2.00 2.00 1. 93 2.00 2.00 2.00 1. 93 2.01 1. 93 2.00 1. 93 2.00 Stk COe Gas hsefh ppm hscfh 0-1000 0-10000

1. 48 1.41 1.41 1.48 1.41 1.41 1. 34 1. 34 1.19 1.19 1.26 1. 26 1.11 1.19 1.11 1.19 1. 04 1.11 1.11 1.11 1.19 1.26 1.26 1.11 1.26 1.11 1. 04 1.19 1.11 1.19 1.19 1.11 1.11 1.19 1. 04 1.11 1. 04 8438.4 8417.4 8427.0 8415.6 8414.4 8404.2 8388.0 8391.0 8395.2 8393.4 8394.0 8390.4 8389
. 8 8411.4 8413.2 8414.4 8406 .6 8414.4 8416.2 8417.4 8409.0 8407.8 8419.8 8400.6 8427.0 8424.0 8407.8 8409.0 8412.6 8410.8 8403.0 8377.2 8389.8 8393.4 8395.8 8397.0 8412.0 NH3Inj 1b/hr 0-1000

110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110 .0 110.0 110 .0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 11 0.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued MW Lo
0-1

103
.. 1 02. ! 102. ' 102
. . 102 102
. . 101. 102.: 1 02.1 1 02. : 101.: 101
.. 102.1 102
. . 102. : 102
. . 102. ' 102. ! 102. : 102
. . 102
. . 102. 102.1 102.1 102. ! 102
.. 102. ! 102. 102
.. 102. 102. 102
.. 102. : 102
.. 102. f 102.1 102. 

### Pag(Group#-Channel# G12-C2 G12-C4 G12-Cl1 G12-C20 G12-C3 G12-C13 G12-ClO Gl2-C6 G12 -C7 G12 -CB G12-CIB GI2-C Long Descrip. 2>Stk NOx 2>St:k 02 2>NOx Mass 2>StkFlow 2>St:k CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 2>NH3 Inj 2>MW Lo Short Descrip
. Stk NOx Stk 02 NOx Mass StkFlow Stk CO CO Mass NOx Rate Stk NOXc Stk CDc Gas hscfh NH3Inj MW Lo Units 

### ppm 

# • 1b/hr kscfh 

### ppm lb/hr lb/mmBtu 

### ppm ppm hscfh 1b/hr Range 0 -1 50 0-25 0-100 0-300000 0-1000 0-100 0-1 0-300 0-1000 0-10000 0-1000 0-1 01/30/2013 15:05 2.7 12. 9 5 6.18 20205 1.4 1. 76 0.007 2.00 1. 04 8403.6 110.0 102.: Period Average 2.7 12.95 6.52 20276 2.1 3.06 0.007 2.01 1. 59 B433.7 109.4 102.6 Period Max Value 2.9 12.97 7.16 20414 3.0 4.47 0.008 2.15 2 .23 8525.4 110.0 104. Period Min Value 2.' 12.9 1 6.16 20167 1.4 1. 76 0.007 1. 86 1. 04 8377.2 63.2 101. Period Totals = 1.9770E+2 9.4S32E+2 4.7561E+2 1.4801E+6 1.S660E+2 2.2335E+2 5.3700E-l 1. 4669E+2 1.1617E+2 6.1S66E+5 7.9832E+3 7.49S1E+ Period 

### % Recovery 64.0 64.0 64.0 64.0 64. a 64.0 64.0 64.0 64.0 64.0 64.0 64.



### Date/Time Printed: 01/31/2013 12,20 

### 2>Summary

- I-Min RATA

- Continued PagE

# Data Summary Report Company: CPV Sentinel, LLC 62575 Powerline Road 

### Desert H ot Springs, CA 92240 

# 'JC?i,\.t\

# V~"\- 1,

# 9-A~**~2** Source: Data Group: Report Name: 

### Start of Report : Turb ine 2 

### 2>1-Min Cales 2>Summary

- I-Min RATA 01/30/2013 13,11 G12-C4 

# t\¥o,**\~b- ~p~,**  eAtt
End of Report: 01/30/2013 15:05 Gl2-ell G12-C20 Gl2-C) G12 -C13 G12-CIO 

# TRACE
Environmental Systems, [" c.

validation: All Available Data G12-C6 G12-C7 G12-C8 G12-C18 G12

- C 

### Group#-Channel# Long Descrip. Short Descrip
. units G12-C2 2>Stk NOx

Stk NOx 

### ppm 0

- 150 2>Stk 02 2>NOx Mass 2>StkFlow 2>Stk CO 2>CD Mass 2>NOx Rate 2>Stk NOXc 2 >Stk CDc 2>Gas Flow 2>NH3 Inj 2>MW La


### Range 01/30/2013 13:11 01/30/2013 13:12 01/30/2013 13:13 01/30/2013 13:14 0 1 /30/ 2 013 13:15 01/30/2013 13:16 01/30/2013 13:17 01/30/2013 13:18 01/30/2013 13:19 01/30/2013 13:20 01/30/2013 13:21 01/30/2013 13:22 01/30/2013 13:23 01/30/2013 13:24 01/30/2013 13:25 01/30/2013 13:26 01/30/2013 13:27 01/30/2013 13:28 01/30/2013 13:29 01/30/2013 13:30 01/30/2013 13;3 1 01/30/ 2 013 13:32 01/30/2013 13:33 01/30/2013 13;34 01/30/2013 13 :35 01/30/2013 13:36 01/30/2013 13:37 01/30/2013 13:38 01/30/2013 13 :39 01/30/2013 13:40


### Date/Time Printed: 2.8 2.8 2.' 2.8 2.8 2.7 2.8 2
. .8 2.8 2.8 2.8 2.8 2.7 2.8 2.7 2.8 2.7 2.' 

### 2.' 2.8 2.' 2.' 2.' 2.' 2.8 2.8 2
. 8 2.7 2.7 2.8 Stk 02 

# • 0-25 12.96 12.95 12.94 12.96 12.95 12.96 12.95 12.94 12
. 94 12.95 12.96 12.96 12.96 12 .96 12.96 12.96 12.97 12.94 12.91 12.93 12.93 12.93 12.92 12.92 12.93 12.93 12.94 12.96 12.95 12
. 95
01/31/2013 12 , 21 NOx Mass 

### Ib/hr 0

- 100 7.10 7.12 7.13 7.11 7.11 6.22 7.10 7.11 7.09 7.10 7. 09 7.08 6.20 7.08 6.20 7.08 6.19 7.12 7.16 7.15 7.14 7.15 7.14 7.14 7.15 7.13 7.12 6.21 6.21 7.10 

### StkFlow kscfh 0-300000

20356 20375 20384 20366 20359 20360 20309 20325 20274 20327 2031 0 20304 2 0302 20288 20317 20285 20308 20368 20395 20400 20391 20414 20370 20363 20403 20361 20355 20337 20320 20333 

### Stk CO 

### ppm 0-1000

2.5 2.6 2.5 2.6 2.6 2.8 2.6 2.' 2.7 2.7 2.7 2.8 2.8 2.7 3.0 2.7 2.' 2.' 2.6 2.8 2.6 2.6 2.8 2
. 5 2.5 2.8 2.6 2.5 2.' 2 .7 CO Mas s 

### Ib/hr 0

- 100 3.55 3.56 3.57 3.55 3.56 4 .44 3.55 4.44 3.55 3.55 3.54 4.43 4.4 3 3.54 4.43 3.54 4.4 2 4.45 3.58 4.47 3.57 3.58 4.47 3.57 3.57 4.46 3.56 3.55 4 .44 3.55 NOx Rate Ib/mmBtu 0-1 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.008 0.008 0
. 008 0.008 0.008 0.007 0.008 0.007 0.008 0.007 0.008 0
. 008 0.008 0
. 008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.007 0.008 

### stk NOXc 

### ppm 0-300 2.08 2.08 2.15 2.08 2.08 2.01 2.08 2.08 2.08 2.08 2.08 2.08 2.01 2.08 2.01 2.08 2.01 2.15 2.14 2.07 2.15 2.15 2.14 2.14 2.07 2.07 2.08 2.01 2.00 2.08 

### Stk CDc 

### Gas hscfh ppm 

### hscfh 0-1000 0-10000

1.86 8455.8 1.93 8474.4 1.85 8488.8 1.93 8460.0 1.93 8467.8 2.08 8457.6 1.93 8446.8 2.15 8464 .2 2.00 8443.2 2.00 8454.6 2.01 8436.6 2 .08 84 34.2 2.08 8433.6 2.0 1 8 4 27.6 2.23 8439.6 2.01 8426.4 2.16 8425.2 2.15 8482.2 1.92 8525.4 2.07 8506.2 1.92 8502.6 1 .92 8512.2 2
. 07 8504.4 1. 85 8501. 4 1.85 8507.4 2.07 8490.0 1. 93 1. 86 2.15 2.00 8476.8 8448.0 8451.6 8457.0 NH 3Inj 

### Ib/hr 0-1000 110. 0 110 .0 110. 0 110.0 110.0 110.0 110 .0 110.0

63.2 110 .0 110. 0 110.0 110.0 110.0 110.0 11.0.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110 .0 110.0 110.0 110.0 1 10.0 MW Lo
0-1 103
.. 103.: 103
.. 103.1 103. : 102. 102
. . 103. : 102
.. 102 103. 1 102
.. 102
.. 102
. . 102
.. 102.! 102
. . 103. 104 103 ' 103.' 103.' 103. 103.' 103. 103.! 103." 102.: 103.: 102.' 

### Pag(

### Group#

- Channel# Long Descri p . Short De s cri p. U

n i ts Range 01/30/2013 13:41 01/30/2013 13:42 01/30/2013 13:43 01/30/2013 13:44 01/30/2013 13:45 01/30/2013 13:46 01/30/2013 13:47 01/30/2013 13:48 01/30/2013 13:49 01/30/2013 13:50 01/30/2013 13:51 01/30/2013 13:52 01/30/2013 13:53 01/30/2013 13:54 01/30/2013 13:55 01/30/2013 13:56 01/30/2013 13:57 01/30/2013 13:58 01/30/2013 13:59 01/30/2013 14:00 01/30/2013 14:01 01/30/2013 14:02 01/30/2013 14:03 01/30/2013 14:04 01/30/2013 14:05 01/30/2013 14:06 01/30/2013 14:07 01/30/2013 14:08 01/30/2013 14:09 01/30/2013 14:10 01/30/2013 14:11 01/30/2013 14:12 01/30/2013 14:13 01/30/2013 14:14 01/30/2013 14:15 01/30/2013 14:16 01/30/2013 14:17 01/30/2013 14:18 01/30/2013 14:19 01/30/2013 14:20 

### Date/Time Printed: G12 -C4 G12 -C11 G12-C20 G12-C2 2>Stk NOx

Stk NOx 2 >Stk 02 2 :>NOx Mass 2 >S tkFlow
ppm 0-150 2.B 2.7 2.7 2.7 2 .B 44.4 B 61. 

### a B 60.1 B 21.1 B

1.3 B 6.9 B 16.1 B 51.3 B 57.0 B 54.5 B 56.1 B 56.8 B 57 .0 B 57.1 B 57.3 B 57.1 B 57.2 B 57.6 B 57.48 57.78 57.48 42.78

3.88 2 .9 8 L18 2.88 3.28 2.48 2.3 B 2.2 B 2.2 B 2.1 B 2.38 2.2 B 2.28 stk 02 

# • 0-25 12.95 12.96 12.95 12.95 12.95 13.278 13.348 13.38 B 14.11 B 15.878 15.618 14.54 B 13.85 B 13.80 B 13.838 13.808 13.808 13.80 B 13.79 B 13 .78 B 13.78 B 13.77B 13.768 13.76 B 13.75 B 13.77 B 14.078 15.138 15.64 B 15.23 B 14. 07 8 13.38 B 13 .30 B 13.318 13.328 13.31 B 13.328 13.298 13.23 B 12.96 B
01/31/2013 12,21 NOx Mass Ib/hr 0-100 7.09 6.20 6.20 6.20 7.10 100.008 100.00B 100.00B

34.41B

1. 65 8 10.59 B 33. 04 B 100.00B 100.00B 100 .00B 100.00B 100. 00 B 100.00 B 100.00B 100.008 100. 00 8 100.008 100
. 00B 100.00B 100.00B 100
. 00 B

87.358

5.09 B 3.858 1.66 B 5.908 7.85 B 6.19 B 6 .19 B 5.31 B 5.31 B 5.31 B 6.21 B 5.318 5.318 StkFlow kscfh 0-300000

20306 20301 20293 20270 20332 193398 200908 19248 B 135688

9923 B 13012 B 171948 1983 58 20470 B 200468 204838 20483 B 205648 20459 B 204848 204248 204928 20434 B 204028 204228 203658 171198 11462 B 111098 133258 174708 21125 B 211888 211998 21235 B 212428 212618 21234 B 209868 202888 G12-C3 G12 -C13 G12-C10 G12-C6 G12

- C7 G12 -C8 G12 -C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2 >St k NOXc 2>Stk COc 2>Gas Flow 2 > NH3 Inj 2>MW Lo Stk CO ppm 0-1000

2.7 2.7 2.9 2
. B 3.0 1. 58 0.08 0.08 0.08 0.08 0.0 B 0.0 B 

### o. a 8 0.0 B 0.08 0.08 0.08 0.0 B 0.0 B 0.08 0.08 0.0 B 0.08 0.0 B 0.08 0.08 0.0 B O. 

### a 8 0.08 0.08 0.4 B 2.6 B 4.38 3.9 B 3.2 B 2.8 B 3.08 2.68 2
. 48 2.6 B CO Mass Ib/hr 0-100 3.55 3.54 4.43 4.43 4.44 2.438 0.008 O. 00 8 0.00 B 0.00 B 0.00 B O. 00 8 0.008 O. 00 B 0.00 B 0.008 0.008 0.00 B 0.008 0.00 B 0.00 B 0.008 0.00 B 0.008 0.00 B 0.008 0.008 0.00 B 0.00 B 0.00 B 0.66 B 4.36 B 6.19 B 6.19 B 5.318 4.438 4.438 4.44 B 3.54 B 3.54 B NOx 

### Rate Ib/mmBt.u 0-1 

### O.OOB 0.007 0.007 0.007 0 .008 0.126 B 0.175 B 0.174 B 0.068 B 0.0068 0.0288 0.055B 0.1588 0.174 B 0.168 B 0.1728 0.1748 0.174 B 0.1758 0.1758 0.1748 0.1748 0.1758 0.175 B 0.1758 0.175 B 0.1368 0.014 8 0.0128 0.004 B 0.009 B 0.009 B 0.007 B 0.007 B 0.006 B 0.0068 0.0068 0.007 B 0.006 B O. 006 8 stk NOXe ppm 0 -300 2. 08 2.01 2.00 2.00 2.08 34.338 47.61B 47.15 B 18.33B

1. 52 B 7.70 B 14.94 B 42.93 B 47.37B 45.488 46.628 47.208 47.37 B 47.388 47.488 47.328 47.338 47.60 B 47
. 438 47.618 47.508 36.898

3.898 3.258 1 .1 48 2.428 2.51 B 1.868 1.79 B 1. 71 8 1.71 B 1. 63 B 1.78 B 1. 69 8 1. 63 B Stk COe Gas hscfh ppm hsefh 0-1000 0-10000 2.00 8445.6 2.01 8433.0 2.15 8440.2 2.08 8430.6 2.23 8456.4 1.168 7719.68 O
. OOB 7945.8B 0.008 O
. 00 B 0.00 B 0.00 B 0.00 B O. 00 8 0.00 B 0.008 0.008 0.00 B 0.008 0
. 00 B 0.008 0.008 0.008 0.00 B 0.00 B 0.008 0.008 0.00 B 0.00 B 0.008 0.00 B 0.35 B 2.04 B 3.34 B 3.03 B 2.498 2.18 B 2.34 B 2.028 1.858 1.93 B 7572.6B 4819.88 2611.28 3601.2B 5721.0B 7315.88 7603.88 7414.88 7608.6 B 7608.68 7638.6B 7610.48 7630.2B 7608.08 7644.08 7633.28 7621.28 7639.28 7596.6B 6117.0B 3460.2B 3057.08 3952.88 6242.4B 8311.2 B 8424.68 8418.08 8421.08 8434.8B 8431.28 8454.08 8421.0B 8427.6 B NH3Inj Ib/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 B 110.08 110.08 110.08 110.0 B 110.08 110.0 B 110.0 B 11 0.0 B 110.0 B 110.0 B 110. 08 110 .0 B 110.08 110.08 110.0 B 110.08 110.08 110.0 B 110.08 110.08 110 .0 B 110.08 110 .0 B 110.0 B 110.0 B 110. 

## a 8 110.0 B 110.08 110.08 110.08 110.0 B 110.0 B 110.08 110.0 B 

### 2>Summary

- I-Min RATA

- Continued MW Lo
0-1 103
. . 103. ( 102. 103. ! 102.

92
. . 9B 90
.. 45. 16
.. 32.: 65.' 89.! 93. ( 89
. . 92 92
.. 92. ; 93. ( 93
.. 92. 93
. . 93
.. 92. : 93. : 92
.**~** 66.1 25.' 22
.. 36.( 71.: 101. : 102. 102. ( 102. : 102. : 102
_ 102. 102. ( 102. PagE

### Gro up#-Channel# Long Descri p. Short Descrip. Un i ts 

### Range 01/30/2013 14:21 01/30/2013 14:22 01/30/2013 14:23 01/30/2013 14:24 01/30/2013 14:25 01/30/2013 14:26 01/30/2013 14:27 01/30/2013 14:28 01/30/2013 14:29 01/30/2013 14:30 01/30/2013 14:31 01/30/2013 14:32 01/30/2013 14:33 01/30/2013 14:34 01/30/2013 14:35 01/30/2013 14:36 01/30/2013 14:37 01/30/2013 14:38 01/30/2013 14:39 01/30/2013 14:40 01/30/2013 14,41 01/30/2013 14:42 01/30/2013 14:43 01/30/2013 14:4 4 01/30/2013 14:45 01/30/2013 14:46 01/30/2013 14:47 01/30/2013 14:48 01/30/2013 14:49 01/30/2013 14:50 01/30/2013 14:51 01/30/2013 14:52 01/30/2013 14:53 01/30/2013 14:54 01/30/2013 14:55 01/30/2013 14:56 01/30/2013 14:57 01/30/2013 14:58 01/30/2013 14:59 0 1/30/2013 15:00 

### Date/Time Printed: G12-C2 G12-C4 G12-CII G12 -C20 2>Stk NDx

Stk NDx 

### ppm 0-150 2>Stk 02 2>NOx Mass 2>StkFlow

2. 4 B 2.4 B 2.5 B 2.4 B 2.5 B 2.5 B 2.5 B 2.5 2.6 2.5 2.6 2.6 2.6 2.7 2.5 2
. 6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.6 2.7 2.7 2.6 2.7 2.7 2.7 2.6 2.7 2.7 2.7 2.6 2.7 Stk 02 

# • 0

- 25 12.94 B 12.96 B 12.94 B 12.96 B 12.96 B 12.96 B 12.96 B 12.95 12.95 12.95 12.95 12.94 12.96 12.95 12.97 12.96 12.96 12.96 12.97 12.96 12.96 12.95 12.95 12.96 12.95 12.94 12.94 12.95 12.95 12.94 12.95 12.95 12.95 12.95 12
. 96 12.94 12.95 12.95 12.96 12.96
01/31/2013 12,21 NDx Mass 

### Ib/hr 0-100 6.20 B 6.19 B 6.21 B 6.19 B 6.19 B 6.19 B 6.19 B 6.20 6.19 6.19 6.19 6.18 6.18 6.16 6.17 6.17 6.17 6.17 6.17 6.17 6.18 6.18 6.18 6.18 6.18 6.19 6.19 6.18 6.18 6.19 6.17 6.19 6.19 6.18 6.18 6.18 6.18 6.18 6.16 6.17 StkFlow kscfh 0-300000

20251 B 2027 3 B 20280 B 20282 B 20282 B 20258 B 20284 B 20288 20238 20261 20234 20205 20232 20167 202 25 20210 20206 20 207 20224 20197 20249 20228 20231 20237 20231 20210 20212 20218 20215 20218 20197 20261 20254 20215 20243 20201 20222 20203 20167 20197 G12-C3 G12-C13 G12 -C 10 G12-C6 G12 -C7 G12-C8 G12-C18 GI2-C 2>stk CO 2>CD Mass 2>NOx Rate 2>Stk NDXc 2>Stk CDc 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO 

### ppm 0-1000

2,4 B 2.2 B 2.3 B 2.2 B 2.1 B 1. 9 B 1. 9 B 2.0 1.. 1.. 2.0 1.9 1.9 1.8 1.8 1.6 1.6 1.7 1.7 1.5 1.6 1.5 1.6 1.4 1.5 1.5 1.5 1.6 1.7 1.7 1.5 1.7 1.5 1.4 1.6 1.5 1.6 1.6 1.5 1.5 CO Mass 

### 1b/hr 0-100 3.54 B 3,54 B 3.55 B 3.54 B 2.65 B 2.65 B 2.65 B 2.66 2.65 2,65 2.65 2,65 2.65 2.64 2,64 2,64 2.64 2.64 2.64 1. 76 2.65 1. 77 2.65 1. 77 1. 77 1. 77 1. 77 2.65 2.65 2.65 1. 76 2,65 1. 77 1. 77 2.65 1. 77 2.65 2.65 1. 76 1. 76 NDx Rate Ib/mmBtu 0-1 0.007B 0.007 B 0,007 B 0.007 B 0.007 B 0.007 B 0.007 B 0,007 0.007 0.007 0.007 0.007 0.007 0.007 0,007 0,007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0,007 0.007 0,007 0.007 0.007 0.007 0.007 0.007 0,007 0.007 0.007 0.007 0.007 0.007 0.007 0,007 0.007 Stk NDXc 

### ppm 0-300 1. 78 B 1. 78 B 1. 85 B 1.78 B 1.86 B 1,86 B 1. 86 B 1. 86 1. 93 1. 86 1. 93 1. 93 1. 93 2.00 1. 86 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 2.00 1. 93 1. 93 2.00 2.00 1. 93 2.00 2.00 2.00 1. 93 2.00 2.00 2.00 1. 93 2.01 Stk CDC Gas 

### ppm 0-1000

1. 78 B 1.63 B 1.70 B 1. 63 B 1.56 B 1.41 B 1.41 B 1.48 1.41 1.41 1.48 1.41 1.41 1. 34 1. 34 1.19 1.19 1. 26 1.26 1.11 1.19 1.11 1.19 1. 04 1.11 1.11 1.11 1.19 1. 26 1.26 1.11 1. 26 1.11 1. 04 1.19 1.11 1.19 1.19 1.11 1.11 hscfh 

### hscfh 0-10000 8433 .6 B 8421. 6 B 8445,68 8425.2B 8425.2B 8415.0 B 8425.88 8438.4 8417.4 8427.0 8415.6 8414.4 8404.2 8388.0 8391.0 8395,2 8393.4 8394.0 8390.4 8389.8 8411.4 8413.2 8414.4 8406.6 8414.4 8416 .2 8417.4 8409 .0 8407.8 8419.8 8400.6 8427.0 8424.0 8407.8 8409.0 8412.6 8410 ,8 8403.0 8377.2 8389.8 NH3Inj 

### 1b/hr 0-1000 110.0 B 110.0 B 110, 

## a B 110, 

## a B 110,0 B 110. 

## a B 110. 

## a B 110,0 110.0 110,0 110.0 110.0 110.0 110 ,0 110,0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110 .0 110.0 110.0 110.0 110.0 110.0 110,0 110.0 110 .0 110.0 110.0 110.0 110,0 110.0 110.0 

### 2>Summary

- 1-Min RATA

- Continued MW Lo
0

- 1 102, : 102
.. 1 02
.. 102
.. 102. 102. ! 102. ' 103.: 102. 102 102 102 102. : 101.: 102
.. 102 .1 102. : 101,: 101
.. 102, I 102. : 102 102. : 102. 102 102. 102. : 102
. . 102.! 102.1 102.1 102.! 102
.. 102. 102. ! 102
. . 102. 102. : 102. : 102. : 

### Pag(

### Group#-Channel# Long Descrip. Short Descrip. Units Range 01/30/2013 15:01 01/30/2013 15:02 01/30/2013 15:03 01/30/2013 15:04 01/30/2013 15:05 

### Period Average Period Max Value**~** 

### Period Min Value

- Period Totals

- Period 

### % Recovery



### Dat e /Time Printed: G12

- C2 

### 2>Stk NOx

Stk NOx ppm 0

- 150 2.6 2.7 2.6 2.7 2.7 G1 2 -C4 G12

- Cl1 G12-C20 

### 2>St k 02 2>NOx Mass 2>StkFlow

Stk 02 

# • 0-25 12.95 12.95 12.95 12.95 12.95 

### NOx Mass Ib/hr 0-100 6.17 6.17 6.17 6.18 6.18 

### StkFlaw kscfh 0

- 300000

20180 20186 20189 20225 20205 G12 -C3 G12 -Cl3 GI2

- CIO G12-C6 G12-C7 G12-CB G12-C1B G12-C 

### 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 

### 2>NH3 Inj 

### 2>MW La

Stk CO ppm 0-1000

1.6 1.4 1.5 1.4 1.4 

### CO Mass Ib/hr 0-100 2.64 1.76 1. 76 1. 77 1. 76 

### NOx Rate Ib/mmBtu 0

- 1 0.007 0.007 0.007 0.007 0.007 

### Stk NOXc ppm 0-300 1.93 2.00 1.93 2.00 2.00 

### Stk CDc Gas hscfh ppm hscfh 0-1000 0-10000

1.19 8393.4 1.04 8395.8 1.11 B397.0 1.04 1.04 8412.0 8403.6 NH3Inj Ib/hr 0-1000 110.0 110.0 110
. 0 110.0 110.0 MW Lo
0-1 102.: 102.( 102.1 102. 102.: 11.2 13.2 4 21.35 19826 1.7 2.53 0.034 9.14 1.30 7994.7 109.6 96.4 61.0 15. 8 7 100.00 21261 4 .3 6.19 0.175 4 7.61 3.3 4 8525.4 110.0 104.

1. 1 12. 91 1.65 9923 0.0 0 .00 0.004 1.14 0 .00 2611.2 63.2 16. 1.2917E+) 1.5 227E + 3 2. 4 S5SE+3 2.2800E+6 2.0090E+ 2 2
. 9 099E+2 3.8710E+O 1.0515E+3 1.50 02 E+2 9.1938E+5 1.2603E+4 1.1090E+ 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100
. 0 100.0 100.0 100.

01/31/2013 12,21 

### 2>Summary

- I-Min RATA

- Continued PagE

## Appendix 

## B
. 1.3 Sentinel Unit 2 PM Testing

R0410673 

## 8-5 

# blt a.!d

# Data Summary Report Com pany : CPV SentineL LLC 

### 62575 Powerline Road 

### Desert Hot Springs, CA 92240 Source : Turbine 2 

### Data Group : Report Name: 

# SuJ\.uA tJ ,,',1- 

# Z. 

# pM 

# TRACE**~_** 

# llq\\L

-**~M- ~-**  \ Enr' ;rofl me fll a l S y s l ellls, Iflc.

S tart of Report: 

### 2:>1-Min Cales 2>Summary

- l-Min RATA 02/01/2013 14,14 End of Report, 02/01/2013 18,25 

### Validation: All Available Data 

### Group#-Chann e l# Lo ng Descrip. 

### Short Descrip
. Units Range 02/01/2013 14:14 02/01/2013 14:15 02/01/2013 14:16 02/01/2013 14:17 02/01/2013 14:18 02/01/2013 14:19 02/01/2013 14:20 02/01/2013 14:21 02/01/2013 14:22 02/01/2013 14:23 02/01/2013 14:24 02/01/2013 14:25 02/01/2013 14:26 02/01/2013 14:27 02/01/2013 14:28 02/01/2013 14:29 02/01/2013 14:30 02/01/2013 14:31 02/01/2013 14:32 02/01/2013 14:33 02/01/ 2 013 14:34 02/01/2013 14:35 02/01/2013 14:36 02/01/2013 14:37 02/01/20 1 3 14:38 02/01/2013 14:39 02/01/2013 14:40 02/01/2013 14:41 02/01/2013 1 4 :42 02/01/ 2 013 14:43


### Date/Time Printed: G12-C4 Gl2

- CII G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass



# 1., 1.. 1.. 1.8 1.8 2.0 2.0 

# 1.. 1.8 1.. 

# 1.' 1.. 1.8 

### 1.' 

# 1.. 1.' 1.8 2.2 

# 1., 2.1 2.2 2.2 2.1 2.0 2.1 2.1 2.0 2.0 2.0 2.0 Stk 02 

# • 0-25 14.37 14.35 14.35 14.37 14.36 14. 3 4 14.34 14.36 14 .36 14.36 14.35 14.35 14.36 1 4 .36 14
. 37 14.36 14.36 14.34 14
. 37 14
. 3 4 14.3 4 14.3 3 14.35 14.34 14.34 14.34 14.35 14.35 14.35 14.35
02/02/2013 12 , 40 

### NOx Mass 

### lb/hr 0-100 3.35 3.36 3.36 3.36 3.37 3.93 3.93 3.35 3.36 3.35 3.36 3.35 3.35 3.35 3.36 3.36 3.35 3.91 3.35 3.91 3.90 3.91 3.91 3.91 3.92 3.93 3.92 3.92 3.92 3.92 G12-CZO 

### 2>StkFlow

StkFlow



### kscfh 0-300000

15585 15578 15576 15589 15617 15563 15572 15558 15588 15561 15553 15532 15542 15560 15601 15586 15535 15509 15541 15510 15477 15489 15517 15514 15558 15570 15576 15546 15564 15571 GI2-C) 2>Stk CO



### Stk 

### co ppm 0

- 1000

0.3 0.2 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.3 0.3 GI2-CD Gl2-ClO G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass 

### lb/hr 0-100 0.56 0.00 0.00 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.00 0.56 0.56 NOx Rate Ib/mmBtu 0-1 0.006 0.006 0.006 0.006 0.00 6 0.007 0.007 0.006 0.006 0.006 0.006 0.006 0.006 0.006 0.006 0.006 0.006 0.007 0.006 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0
. 007 0.007 Stk NOXc 

### ppm 0-300 1. 72 1. 71 1. 71 1. 63 1. 62 1. 80 1. 80 1. 71 1. 62 1. 71 1. 71 1. 71 1. 62 1. 71 1. 72 1. 71 1.62 1. 98 1. 72 1. 89 1. 98 1. 98 1. 89 1. 80 1. 89 1. 89 1. 80 1. 80 1. 80 1. 80 G12-C7 G12-C8 

### 2>Stk CDc 2>Gas Flow

Stk CDc Gas hscfh 

### ppm hscfh 0-1000 0-10000 0.27 0.18 0.18 0.27 0
. 27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0
. 27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0
. 27 0.18 0
. 27 0.27 5324.4 5338.2 5337.6 5325.6 5343.6 5341.2 5344.2 5323.2 5333.4 5324.4 5329.8 5322.6 5317.8 5323.8 5329.8 5332.8 5315.4 5322.6 5309.4 5323.2 5311.8 5323.8 5317.2 5324.4 5339.4 5343.6 5337.6 5327.4 5333.4 5335.8 GI2-C1S 2>NH3 Inj NH3Inj



### lb/hr 0-1000 107.3 107.2 108.7 108.8 109.0 106.0 106.8 107.0 106.7 107.0 107.2 107.7 107.2 106.5 106.3 107.3 105.7 104.7 106.5 105.2 104.0 104.5 106.0 107.0 105.7 106.3 105.8 106.3 106.7 106.8 G12-C 2>MW Lo

MW Lo
0-1 54
. . 54 ' 54.' 54.: 55.1 54.: 54.: 54.' 54.' 54.' 54.' 54.: 5 4 .: 54
. ! 54.: 54.: 54 54. 54. ' 54.' 54
. 1 54.: 54 54. 54
.. 54. 54
.. 54. : 55.1 55.1 

### PagE

### Gr o up#

- Channel# Long Des c rip. S hort De s crip
. units Range 02/01/2013 14:44 02/01/2013 14:45 02/01/2013 14:46 02/01/2013 14:47 02/01/2013 14:48 02/01/2013 14:49 02/01/2013 14:50 02/01/2013 14:51 02/01/2013 14:52 02/01/2013 14:53 02/01/2013 14:54 02/01/2013 14:55 02/01/2013 14:56 02/01/2013 14:57 02/01/2013 14:58 02/01/2013 14:59 02/01/2013 15:00 02/01/2013 15:01 02/01/2013 15:02 02/01/2013 15:03 02/01/2013 15:04 02/01/2013 15:05 02/01/2013 15:06 02/01/2013 15:07 02/01/2013 15:08 02/01/2013 15:09 02/01/2013 15:10 02/01/2013 15:11 02/01/2013 15:12 02/01/2013 15:13 02/01/2013 15:14 02/01/2013 15:15 02/01/2013 15:16 02/01/2013 15:17 02/01/2013 15:1S 02/01/2013 15:19 02/01/2013 15:20 02/01/2013 15:21 02/01/2013 15:22 02/01/2013 15:23 

### Date/Time Printed: G12-C4 G12-C11 G12-C20 G12-C2 2>Stk NOx

Stk NOx 2>Stk 02 2>NOx Mass 2>StkFlow
ppm 0-150

1.. 2.0 2
. 1 2.0 2.2 2.2 2.1 2.1 2.2 2.1 1.. 2.1 2
. 1 2.1 2.2 2.1 2
. 2 2.1 2.1 2.1 2.0 2.0 2.0 2.0 2.2 2.2 2.1 2.1 2.1 2.2 2.0 2.1 2.2 2.0 2.1 2.1 2.2 2.2 2.2 2.2 Stk 02 

# • 0-25 14.36 14.35 14.3 4 14 .34 14.32 14.32 14.33 14.33 14.33 14.34 14 .35 14.33 1 4 .32 14 .32 14.32 14.33 14
. 32 1 4 .32 14.31 14.33 14.33 14 .34 14 .34 14.34 14.32 14.33 14.33 14.34 14.33 14
. 30 14.31 14.32 14 .32 14.3 4 14 .31 14.32 14.31 14.31 14.31 14.31
02/02/2013 12,40 NOx Mass 1b/hr 0-100 3.35 3.92 3.93 3.92 3.93 3.93 3.94 3.94 3.94 3.94 3.38 3.95 3.94 3.95 3.94 3.94 3.94 3.94 3.95 3.94 3.94 3.94 3.93 3.92 3.94 3.94 3.93 3.93 3.94 3.95 3.96 3.95 3.97 3.96 3.98 3.98 3.99 3.98 3.98 3.98 StkFlow kscfh 0 -3 00000

15556 15571 15570 15554 15540 15536 15586 15586 15579 15605 15637 15625 15582 15620 15585 15600 15568 15577 15596 15583 15595 15605 15596 15554 15580 15590 15569 15584 15586 15564 15617 15601 15688 156S9 15697 15711 15725 15703 15711 15722 G12-C3 G12-C13 G12-C10 G12-C6 G12-C7 G12-C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 2>NH3 Inj 2>MW La

Stk CO ppm 0-1000

0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.2 0.3 0.2 0.2 0.2 0.2 0.3 CO Mass 1b/hr 0-100 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.00 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.00 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.S6 0.56 0.57 0.56 0.00 0.00 0.57 0.00 0.00 0.00 0.00 0.57 NOx Rate lb/mmBtu 0-1 0.006 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.006 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXc ppm 0-300 1. 71 1. 80 1. 89 1. 80 1. 97 1. 97 1. 89 1. 89 1. 98 1. 89 1. 71 1. 89 1. 88 1. 88 1. 97 1. 89 1. 97 1. 88 1. 88 1. 89 1. 80 1. 80 1. 80 1. 80 1. 97 1. 98 1. 89 1. 89 1. 89 1. 97 1. 79 1. 88 1. 97 1. 80 1. 88 1. 88 1. 97 1. 97 1. 97 1. 97 Stk COc Gas ppm hscfh hscfh 0-1000 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0
. 27 0.18 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.18 0.27 0
. 27 0.27 0.27 0.27 0.27 0
. 27 0.27 0.27 0.27 0.27 0.18 0.18 0.27 0.18 0.18 O.lS 0.18 0.27 0-10000 5322.6 5335.8 5343.6 5338.2 5349.6 5348.4 5357.4 5357 .4 5355.0 5355.6 5358.6 5370
. 6 5364.0 5377
. 2 5365.2 5362.2 5359.2 5362.2 5377.2 5356.2 5360.4 5355.6 5352.6 5338.2 5363.4 5358.6 5351.4 5348
. 4 5357.4 5374.2 5384.4 5370.6 5400.6 538 4 .4 5412.0 5408.4 5421.6 5413.8 5416
. 8 5420.4 NH3Inj lb/hr 0-1000 107.7 107.0 106.2 107.0 107.0 106.8 105.2 105.8 105.7 107.3 107.3 106
. 0 106.5 106.3 106.7 106
. 7 106.8 106
. 8 107.2 107.5 107.5 106.8 107
. 2 106.2 10S.7 10S.8 107.2 104.3 106.0 107
. 0 106.7 107.2 107.3 109.0 108.8 107.8 107.5 108.2 107.8 108.8 

### 2>Summary

- I-Min RATA

- Continued MW La
0-1 54
.. 55. ! 54. 54 55.1 55
. ! 55. ! S5. ! 54. : 55. ! 54. 55. ! 55. : 55. : 55
. • 55. ! 54. : 55. : 55. : 54. : 55.: 54. : 55. ! 54. : 55. : 55.1 54. : 55. ! 55. : 55
.. 55. ! 55. 55.1 55. 56. ! 55
.. 56. : 56.1 55. ' 56 .• pagt

### Group#-Channel# Long Descrip. Short Descr i p. Units Range 02/01/2013 15:24 02/01/2013 15:25 02/01/2013 15:26 02/01/2013 15:27 02/01/2013 15:28 02/01/2013 15:29 02/01/2013 15:30 02/01/2013 15:31 02/0 1 /2013 15:32 02/01/2013 15:33 02/0l/20l3 15:34 02/01/2013 15:35 02/01/2013 15;36 02/01/2013 15;)7 02/01/2013 15;38 02/01/2013 15;)9 02/01/2013 15;40 02/01/2013 15:41 02/01/2013 15:42 02/01/2013 15:43 02/01/2013 15;44 02/01/2013 15:45 02/01/2013 15:46 02/01/2013 15:47 02/01/2013 15:48 02/01/2013 15:49 02/01/2013 15;50 02/01/2013 15;51 02/01/2013 15:52 02/01/2013 15:53 02/01/2013 15:54 02/01/2013 15:55 02/01/2013 15:56 02/01/2013 15:57 02/01/2013 15:58 02/01/2013 15;59 02/01/2013 16;00 02/01/2013 16:01 02/01/2013 16:02 02/01/2013 16:03 

### Date/Time Printed: G12 -C4 G12

- C11 G12-C20 G12-C2 2,Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02**2~NOx** Mass 2>StkFlow

2.1 2.0 2.1 2.1 2.1 2.2 2.1 2.0 2.1 2.1 2.0 2.0 2.0 2.0 2.2 2.0 2.1 2.0 2.0 2.0 2.0 2.1 2.1 2.0 2.0 2.2 2.0 2.1 2.1 2.3 2.0 2.2 2.1 2.0 2.1 2.1 2.1 2.2 2.2 2.3 Stk 02 

# • 0
.

-25 14.32 14.32 14.30 14 .31 14.31 14.31 14.32 14.32 14.32 14.33 14.32 14 .32 14 .32 14.32 14
. 32 14.32 14.33 14.32 14.33 14.34 14 .33 14.34 14
. 34 14.34 1 4 .34 14.33 14.32 14.31 14.32 14 .31 14 .31 14.31 14
. 34 14.34 14.34 14.35 14.34 14.33 14.3 2 14.32
02/02/2013 12:40 NOx Mass 

### lb/hr 0-100 3.98 3.97 3.98 3.98 3.98 3.99 3.98 3.97 3.98 3.96 3.97 3.97 3.95 3.96 3.95 3.95 3.95 3.94 3.95 3.94 3.94 3.94 3.93 3.94 3.93 3.93 3.95 3.95 3.95 4.52 3.95 3.96 3.93 3.92 3.92 3.92 3.93 3.93 3.94 4.51 StkFlow kscfh 0-300000

15723 15707 15689 15694 15722 15736 15726 15681 15733 15658 15678 15674 15625 15636 15610 15615 15630 15590 15625 15617 15583 15607 15600 15626 15591 15562 15603 15603 15610 15612 15603 15647 15586 15559 15549 15560 15561 15564 15580 15584 G12

- C3 GI2-C13 G12-CIO G12-C6 G12-C7 G12-C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 2>NH3 Inj 2>MW La

Stk CO 

### ppm 0-1000

0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.3 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.2 0.3 0.3 0.3 0.3 0.3 CO Mass 

### lb/hr 0-100 0.57 0.57 0.57 0.57 0.57 0.57 0.00 0.57 0.00 0.57 0.57 0.57 0.56 0.57 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.57 0.56 0.57 0.56 0.00 0.00 0.56 0.56 0
. 56 0
. 56 0.56 NOx Rate lb/mmBtu 0-1 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 Stk NOXc 

### ppm 0

- 300 1. 88 1. 79 1. 88 1. 88 1. 88 1. 97 1. 88 1. 79 1. BB 1. 89 1. 79 1. 79 1. 79 1. 79 1. 97 1. 79 1. 89 1. 79 1.80 1. 80 1. BO 1. 89 1. 89 1. 80 1. 80 1. 9B 1. 79 1.88 1. 88 2.06 1. 79 1. 97 1. 89 1. 80 1.89 1. 89 1. 89 1. 9B 1. 97 2.06 Stk COc Gas 

### ppm hscfh hscfh 0-1000 0.27 0.27 0.27 0.27 0.27 0.27 0.18 0.27 0.18 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0
. 27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0
. 27 0
. 27 0.27 0.18 0.18 0.27 0.27 0.27 0.27 0.27 0

- 10000 5412.6 5407.2 5417.4 5410.8 5420.4 5425.2 5413.8 5398.2 5416.2 5382.0 5397.0 5395.8 5379.0 5382.6 5373.6 5375.4 5372.4 5367.0 5370.6 5359.8 5356.2 5356.2 5353.8 5362.B 5350.8 5349.0 5371. 2 5379.6 5373.6 5382.6 5379.6 5394.6 5349.0 5340.0 5336.4 5332.2 5340.6 5349.6 5363.4 5364.6 NH3Inj 

### lb/hr 0-1000 108.3 108.3 108.7 107.8 106.8 107.8 109.3 108.5 108
. 5 107.3 108.5 108.0 108.5 106.7 106.0 106.5 106.7 107.5 106.5 107.2 107.5 107.2 107.3 107.5 105.8 105.8 107.3 106.3 106.7 106.7 106.3 105.8 106.3 106.8 105.7 106.0 105.3 105.3 105.3 106.2 

### 2>Summary

- I-Min RATA

- Continued MW La
0-1 56.1 55
.. S5. : 56.1 56
. . 55. 55. 55.l 5S. : S5
.. 55. : 55
.. SS .: 55.: 55
.**~** 5S. : 55
.. 55. : 55.: 5S .: 55.: 54. : 55.1 55.1 54. ; 55.1 55
.. 55.: 5S.1 5S. : 55
. . 55. 54.: 54.· 54.: 54.: 54.: 54.: 55. 55.· Pagt

### Gro up#- Channel # Long Des c r i p . Short De s cr i p . U

n its Range 02/01/2013 16;04 02/01/2013 16;05 02/01/2013 16;06 02/01/2013 16;07 02/01/2013 16;08 02/01/2013 16:09 02/01/2013 16:10 02/01/2013 16:11 02/01/2013 16:12 02/01/2013 16:13 02/01/2013 16:14 02/01/2013 16:15 02/01/2013 16:16 02/01/2013 16:17 02/01/2013 16:18 02/01/2013 16:19 02/01/2013 16:20 02/01/2013 16:21 02/01/2013 16:22 02/01/2013 16:23 02/01/2013 16:24 02/01/2013 16;25 02/01/2013 16:26 02/01/2013 16:27 02/01/2013 16:2B 02/01/2013 16:29 02/01/2013 16:30 02/01/2013 16;31 02/01/2013 16:32 02/01/2013 16:33 02/01/2013 16:34 02/01/2013 16:35 02/01/2013 16:36 02/01/2013 16:37 02/01/2013 16:38 02/01/2013 16:39 02/01/2013 16:40 02/01/2013 16:41 02/01/2013 16:42 02/01/2013 16:43 

### Date/Time Printed: G12 -C4 G12-C11 G12-C20 G12

- C2 2>Stk NOx

Stk NOx 

### ppm 0

- 150 2>Stk 02 2>NOx Mass 2>StkFlow

2.3 2.1 2.1 2.1 2.2 2.2 2.3 2.2 2.1 2.2 2.1 2.2 2.2 2.2 2.2 2.2 2.0 2.1 2.1 2.0 2.1 2.1 2.1 2.1 2.1 2.0 2.1 2.2 2.1 2.2 2.2 2.1 2.0 2.1 2.1 2.1 2.1 2.1 2.1 2.1 Stk 02 

# • 0-25 14.32 14.34 14.34 14 .34 14.30 14.32 14 .33 14.32 14.32 14.31 14.31 14.29 14.29 14.30 14 .28 14 .29 14.31 14.30 14.31 14.32 14.31 14.32 14.30 14.30 14.32 14.32 14.30 14 .29 14.31 14.31 14
. 30 14.32 14 .33 14.33 14.32 14 .33 14.31 14.32 14.31 14.30
02/02/2013 12,40 NOx Mass 

### Ib/hr 0

- 100 4.51 3.93 3.93 3.93 3.94 3.94 4.51 3.96 3.96 3.96 3.97 3.98 3.99 3.98 3.99 3.98 3.99 4.00 3.99 3.9B 3.99 3.98 3.98 3.99 3.97 3.96 3.98 3.99 3.98 3.99 3.99 3.97 3.96 3.95 3.97 3.95 3.9B 3.97 3.9B 3.98 StkFlow kscfh 0-300000

15587 15586 15586 15586 15529 15566 15621 15650 15655 15635 15678 15648 15718 15682 15671 15660 15739 15747 15741 15737 15748 15735 15694 15703 15704 15657 15684 15691 15704 15727 15731 15674 15674 15647 15693 15625 15696 15704 15708 15698 G12-C3 G12

- C13 G12-C10 G12

- C6 G12-C7 G12-C8 G12 -C18 G12-C 2>Stk CO 2>CO Mass 2 >NO x Rate 2>Stk NOXc 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk 

### co ppm 0-1000

0.3 0.3 0.3 0.3 0.3 0.2 0.3 0.2 0.2 0.2 0.3 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.2 0.2 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 CO Mass 

### 1b/hr 0

- 100 0.56 0.56 0.56 0.56 0.56 0.00 0.56 0.00 0.00 0.00 0.57 0.00 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.00 0.00 0.00 0.00 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.57 0.56 0.57 0.56 0.57 0.57 0.57 0.57 NOx Rate 

### Ib/mmBtu 0-1 0.008 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXe 

### ppm 0

- 300 2.06 1. 89 1. 89 1. 89 1. 97 1. 97 2.07 1. 97 1. 88 1. 97 1. 88 1. 96 1. 96 1. 97 1. 96 1. 96 1. 79 1. 88 1. 8B 1. 79 1. 88 1. 88 1. 88 1. B8 1. 88 1. 79 1.BB 1. 96 1. B8 1. 97 1. 97 1. B8 1. 80 1.89 1. 88 1. B9 1. 88 1. B8 1. 88 1. 8B Stk COe Gas hsefh 

### ppm 0-1000 0.27 0.27 0.27 0.27 0.27 0.18 0.27 0.18 0.18 0.18 0.27 0.18 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.18 0.18 0.18 0.18 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 hsefh 0 -10000 5365.8 5349.0 5349
. 0 5349.0 5362.2 5358.6 5369.4 5387.4 5389.2 5390.4 5405.4 5411.4 5435.4 5415.0 5427.6 5415.6 5426.4 5437.2 5427.0 5417.4 5429.4 5416.8 5419.2 5422.2 5406.0 5389.8 5415.6 5426.4 5414.4 5422.2 5431.8 5395.B 5387.4 5378.4 5402.4 5370.6 5411. 4 5406.0 5415.6 5420.4 NH3Inj 

### Ib/hr 0-1000 105.5 106.3 106.3 106.3 105.3 106.5 106.3 108.3 108.7 108.7 108.3 108.0 108.7 109.7 108.B 108.7 108.5 107.5 107.8 10B.3 108.3 108.7 109.2 108.7 10B.7 107.5 108.3 109.3 108.3 106.0 109.2 10B.7 107.2 108.0 106.0 107.2 107.8 107.8 107.0 107.8 

### 2>Summary

- 1-Min RATA

- Continued MW Lo
0-1 55. : 55
.. 55.: 55. : 55.: 54. : 55. : 55. : 55. 56. ( 55. 55.! 56.: 55. : 56. 56
. . 56.: 56. 56 56.1 56
. . 56.: 56.1 56. ( 56. ( 55. 56. : 56.1 56. c 56. 56. 55
.. 55.: S5
. . S5. : 55. : 56. ( 55. 56
.. 56. ( PagE

### Group#-Channel# Lo ng Descrip
. Short Descr i p. Units Range 02/01/2013 16:44 02/01/2013 16:45 02/01/2013 16:46 02/01/2013 16:47 02/01/2013 16:48 02/01/2013 16:49 02/01/2013 16:50 02/01/2013 16:51 02/01/2013 16:52 02/01/2013 16:53 02/01/2013 16;54 02/01/2013 16;55 02/01/2013 16;56 02/01/2013 16:57 02/01/2013 16;58 02/01/2013 16;59 02/01/2013 17:00 02/01/2013 17:01 02/01/2013 17:02 02/01/2013 17;03 02/01/2013 17:04 02/01/2013 17;05 02/01/2013 17;06 02/01/2013 17:07 02/01/2013 17:08 02/01/2013 17:09 02/01/2013 17;10 02/01/2013 17:11 02/01/2013 17;12 02/01/2013 17;13 02/01/2013 17:14 02/01/2013 17:15 02/01/2013 17;16 02/01/2013 17:17 02/01/2013 17:18 02/01/2013 17:19 02/01/2013 17:20 02/01/2013 17:21 02/01/2013 17:22 02/01/2013 17;23 

### Date/Time Printed: G12

- C4 G12-C11 G12-C20 G12-C2 2>Stk NOx

Stk NOx 

### ppm 0 -150 2>Stk 02 2>NOx Mass 2>StkFlow

2.2 2.1 2.2 2.2 2.2 2.1 2.0 2.0 2.0 2.1 2.0 2.0 2.1 2.1 2.2 2.2 2.1 2.1 2.2 2.1 2.1 2.1 2.1 2.1 2.1 2.1 2.2 2.1 2.0 2.2 2.2 2.1 2.2 2.1 2.0 2.1 2.0 2.0 2.0 2.0 Stk 02 % 0-25 14.31 14.31 14.30 14.29 14.30 14.32 14 .32 14.3 4 14.33 14.32 14.33 14.32 14.34 14 .34 14 .32 14.33 14 .34 14 .33 14.33 14.31 14 .32 14.32 14
. 31 14.32 14.32 14.33 14.30 14.31 14.32 14.30 14.31 14.31 14 .31 14.30 14.30 14.30 14.32 14.31 1 4. 31 14.30
02/02/2013 12,40 NOx Mass 

### lb/hr 0-100 3.99 3.99 4.00 4.01 4.00 3.98 3.97 3.95 3.95 3.95 3.94 3.94 3.92 3.93 3.94 3.93 3.94 3.95 3.95 3.97 3.97 3.96 3.95 3.95 3.96 3.96 3.96 3.96 3.95 3.97 3.96 3.9S 3.99 4.00 4.00 4.00 3.9S 4.00 4 .0 0 4.01 StkFlow ksefh 0-300000

15746 15730 1574B 15761 15774 15747 15700 15661 15633 15610 15592 15564 15535 15572 15585 15560 15628 15616 15633 15668 15695 15636 15605 15617 15639 156B1 15614 15609 15618 15654 15642 15689 15 730 15760 157BO 15769 15735 15776 15776 15806 G12-C3 G12-CD G12-C10 G12 -C 6 G12 -C7 G12-C8 G12

- C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO 

### ppm 0 -10 00

0.3 0.3 0.3 0.3 0.2 0.2 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 

## o 3 0.2 0.2 0.3 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.2 0.3 0.2 0.2 0.3 0.3 0.3 0.3 0.3 CO Mass 

### lb/hr 0-100 0.57 0.57 0.57 0.57 0.00 0.00 0.00 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.56 0.00 0.00 0.57 0.00 0.56 0.57 0.57 0.57 0.57 0.56 0.57 0.57 0.00 0.57 0.00 0.00 0.57 0.57 0.57 0.57 0.57 NOx Rate 

### Ib/mmBtu 0-1 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXe 

### ppm 0 -30 0 1. 97 1. 8S 1. 97 1. 96 1. 97 1. S8 1. 79 1. SO 1. 80 1. B8 1. BO 1. 79 1. B9 1. 89 1. 97 1. 9S 1. 89 1. 89 1. 9B 1. BB 1. 88 1. 88 1. 88 1. BS 1. B8 1. 89 1. 97 1. 88 1. 79 1. 97 1. 97 1. S8 1. 97 1. 88 1. 79 1. 88 1. 79 1. 79 1. 79 1. 79 Stk COe Gas hsefh hsefh 0

- 10000 

### ppm 0-1000 0.27 0.27 0.27 0.27 0.18 0.18 0.18 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.18 0.18 0.27 O.lS 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.18 0.27 0.18 0.18 0.27 0.27 0.27 0.27 0
. 27 5428.8 5423.4 5437.8 5450.4 5446.8 5421.0 5404.8 5374.8 5373.6 5373.6 5359.2 5358.0 5331.6 5344.2 5365.2 5348.4 5363.4 5367.6 5373.6 5401.8 5403.0 5382.6 5380.2 5376.0 5383.8 5389.8 5391.6 5381 .4 5376.6 5405 .4 5392.8 5409.0 5423.4 5442.0 5448.6 5445.0 5416.8 5439.0 5439 .0 5457.6 NH3Inj 

### lb/hr 0-1000 106.7 107.5 107.3 107.0 108.8 109.7 108.2 106.S 105.5 107.2 107.5 107.2 105.0 104.8 105.3 104.8 103.S 105.0 105.2 106.2 106.8 106.8 106.8 105.7 106.5 105.2 106.5 106.2 105.7 105.7 105 .8 105.2 105.3 108.0 107.2 107.3 108.3 108.2 108.5 108.5 

### 2>Summary

- I-Min RATA

- continued MW Lo
0-1 56. : 56.: 56
. . 56.: 56.: 56.4 56.1 55.: 55
.. 55.: 55
. . 55.: 54. : 55.4 55.: 55.1 55 ' 55.: 55. 56.4 56.1 55
. 55. 55
. . 55. 55. : 55. 55
.**~** 55
.. 55. 55. : 55. : 56. : 56. : 56.: 56.: 56 .1 5 6
.. 56
. . 56. 

### Pagf

### Group#-Channel# Long Des c r i p _ Short De sc r i p . Units Range 02/01/2013 17:24 02/01/2013 17:25 02/01/2013 17:26 02/01/2013 17:27 02/01/2013 17:28 02/01/2013 17:29 02/01/2013 17:30 02/01/2013 17:31 02/01/2013 17:32 02/01/2013 17:33 02/01/2013 17:34 02/01/2013 17:35 02/01/2013 17:36 02/01/2013 17:37 02/01/2013 17:38 02/01/2013 17:39 02/01/2013 17:40 02/01/2013 17:41 02/01/2013 17:42 02/01/2013 17:43 02/01/2013 17:44 02/01/2013 17:45 02/01/2013 17:46 02/01/2013 17:47 02/01/2013 17:48 02/01/2013 17:49 02/01/2013 17: 50 02/01/2013 17:51 02/01/2013 17:52 02/01/2013 17:53 02/01/2013 17:54 02/01/2013 17:55 02/01/2013 17:56 02/01/2013 17:57 02/01/2013 17:58 02/01/2013 17:59 02/01/2013 18:00 02/01/2013 18:01 02/01/2013 18:02 02/01/2013 18:03 

### Date/Time Printed: G12-C4 G12 -Cll G12-C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass

2.0 2.0 1.9 2.0 2.0 2.0 2.0 2.0 2.0 2.1 2.0 2.0 2.2 2.2 2.1 2.1 2.2 2.1 2.1 2.0 2.2 2.1 2.2 2.2 2.2 2.2 2 .2 2.1 2.3 2.3 2.0 2.0 2.2 2.1 2.0 2.1 2.0 2.1 2.1 2.2 Stk 02 % 0-25 14
. 30 14.31 14.31 14.30 14.31 14.33 14.32 14
. 32 14.33 14.31 14 .31 14.31 14.30 14.30 14.31 14.32 14.32 14.33 14.33 14.35 14.32 14.32 14.32 14.32 14.31 14.31 14.31 14.33 14.33 14.3 4 14.37 14.36 14.33 14.34 14.37 14 .37 14.38 14.37 14 .37 14.36
02/02/2013 12,40 NOx Mass 

### lb/hr 0-100 3.99 3.99 3.42 3.99 3.99 3.97 3.98 3.98 3.97 3.99 3.98 4.00 3.99 3.99 3.97 3.97 3.96 3.96 3.95 3.95 3.97 3.97 3.97 3.97 3.97 3.98 3.96 3.93 4.50 4.51 3.92 3.92 3.94 3.93 3.90 3.90 3.89 3.88 3.89 3.89 G12

- C20 2>StkFlow

StkFlow

kscfh 0-300000

15707 15762 15744 15724 15727 15701 15711 15730 15710 15729 15701 15777 15712 15712 15659 15676 15653 15667 15623 15664 15681 15679 15672 15699 15669 15696 15642 15553 15574 15629 15604 15586 15592 15600 15545 15541 15521 15457 15483 15481 G12 -C3 2>Stk CO

Stk CO ppm 0-1000

0.3 0.3 0.3 0.2 0.2 0.2 0.2 0.2 0.3 0.2 0.3 

## o 3 0.3 0.3 0.2 0.3 0.3 0.2 0.2 0.3 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.3 0.2 0.2 0.2 0.2 0.2 0.2 0.2 0.3 0.3 0.3 0.3 0.3 G12-C13 G12-C10 G12 -C6 2>CO Mass 2>NOx Rate 2>Stk NOXe

CO Mass 

### lb/hr 0-100 0.57 0.57 0.57 0.00 0.00 0.00 0.00 0.00 0.57 0.00 0.57 0.57 0.57 0.57 0.00 0.57 0.57 0.00 0.00 0.56 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.56 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.56 0.56 0.55 0.56 0.56 NOx Rate lb/mmBtu 0-1 0.007 0.007 0.006 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0
. 007 0.007 Stk NOXe ppm 0 -300 1. 79 1. 79 1. 70 1. 79 1. 79 1. 80 1. 79 1. 79 1. 80 1. 88 1. 79 1. 79 1. 97 1. 97 1. 88 1. 88 1. 97 1. 89 1. 89 1.80 1. 97 1. 88 1. 97 1. 97 1. 97 1. 97 1. 97 1. 89 2.07 2.07 1. 81 1. 80 1. 98 1. 89 1. 81 1. 90 1. 81 1. 90 1. 90 1. 98 G12-C7 G12-C8 2>Stk COe 2>Gas Flow

Stk COe Gas hsefh ppm hsefh 0-1000 0-10000 0.27 0.27 0.27 0.18 0.18 0.18 0.18 0.18 0.27 0.18 0.27 0.27 0.27 0.27 0
. 18 0.27 0.27 0
. 18 0.18 0.27 0.18 0.18 0.18 0.18 0.18 0.18 0.18 0.27 0.18 0.18 0.18 0
. 18 0.18 0.18 0.18 0.27 0.27 0.27 0.27 0.27 5423.4 5434.2 5428.2 5429.4 5422.2 5397.0 5408.4 5415.0 5400.0 5422.8 5413.2 5439.6 5425.2 5425.2 5398.8 5396.4 5388.6 5385.0 5370.0 5367.6 5398.2 5397.6 5395.2 5404.2 5402.4 5411.4 5392.8 5346.0 5353.2 5364.0 5331.0 5332.8 5359.2 5353.8 5310.6 5309.4 5294.4 5280.6 5289.6 5296 .8 G12 -C18 2>NH3 Inj NH3Inj



### lb/hr 0-1000 108.2 107.3 108.0 108.2 107.0 107.3 107.2 107.2 107.3 107.5 108.0 107.3 106.3 106.3 105.8 105.8 105.0 105.3 105.8 106.2 104.7 106.0 105.7 105.5 105.7 106
. 2 106.2 104.5 102.5 104.7 104.7 105.0 104.2 104.7 103.7 102.7 102.8 102.3 101.7 101.7 

### 2>Summary

- l-Min RATA

- Continued G12-C 2>MW Lo

MW Lo
0-1 56
.. 56. ! 56 .• 56. : 56
. . 55. 55. 56. t 56. t 56. : 56 .• 56.t 56. 56. ! 55
.. 55. i 55. ! 55
.. 56.l 55. 56.l 55
.. 55. i 56.l 56.l 56.l 55. : 55. : 55. l 55. : 54. 54. J 55
. . 55.l 54. : 54. : 54. ! 54. ( 54
.. 54. PagE

### Group#-Channel# Long Descri p. Short Descrip
. units Range 02/01/2013 18:04 02/01/2013 18:05 02/01/2013 18:06 02/01/2013 18:07 02/01/2013 18:08 02/01/2013 18:09 02/01/2013 18:10 02/01/2013 18:11 02/01/2013 18:12 02/01/2013 18:13 02/01/2013 18:14 02/01/2013 18:15 02/01/2013 18:16 02/01/2013 18:17 02/01/2013 18:18 02/01/2013 18:19 02/01/2013 18:20 02/01/2013 18:21 02/01/2013 18:22 02/01/2013 18:23 02/01/2013 18;24 02/01/2013 18:25 

### Period Average Period Max Value Period Min Value Period Totals 

# = Period 

### % Recovery

Date/Time Printe d: G12-C4 G12-C11 G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass

2.2 2.2 2.2 2.2 2.2 2.2 2
. 1 2.0 2.0 2.0 2.1 2.3 2.3 2.1 2.2 2.1 2.1 2.1 2.0 2.0 2.0 2.1 2.1 2.3 1.8 5.2610E+2 100.0 Stk 02 

# • 0-25 14 .35 14.35 14.35 14.36 14.36 14.37 14.37 14.38 14.38 14.38 14.36 14.33 1 4.35 14.36 14.34 14.36 14.36 14
. 36 14.38 14.38 14.37 14.36 14.33 14.38 14.28 3.6108E+3 100.0



### 02/02/2013 12:40 NOx Mass Ib/hr 0-100 3.89 3.89 3.90 3.90 3.91 3.89 3.90 3.89 3.90 3.90 3.90 4.47 4.48 3.91 3.93 3.93 3.93 3.93 3.92 3.92 3.92 3.93 3.92 4.52 3.35 9.8898E+2 100.0 G 12-C20 2>StkFlow

StkFlo w

kscfh 0-300000

15464 15440 15468 15500 15532 15506 15517 15533 15544 15546 15519 15485 15559 15558 15587 15623 15616 15614 15634 15637 15615 15617 15627 15806 15440 3.9380E+6 100.0 G12-C3 2>Stk CO

Stk co 

### ppm 0-1000

0.3 0.3 0.2 0.3 0.3 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0.3 0. 2 0.2 0.2 0.3 0.3 0.3 0.3 0.3 0.3 0.2 6.9500E+l 100.0 G12

- C13 G12-C10 G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXe

CO Mass

Ib/hr 0-100 0.56 0.56 0.00 0.56 0.56 0.00 0.56 0.56 0.56 0.56 0.5 6 0.56 0.56 0.56 0.56 0.00 0.00 0.00 0.56 0.56 0.56 0.56 0.43 0.57 0.00 1.076 1E +2 100.0 NOx 

### Rate Ib/mmBtu 0-1 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.006 1.7529E+0 100.0 Stk NOXe 

### ppm 0-300 l. 98 1. 98 l. 98 1. 98 l. 98 l. 99 1. 90 1. 81 1. 81 l.81 1. 89 2.07 2.07 l. 89 1. 98 1. 89 l. 89 1. 89 1. 81 1. 81 1. 81 1. 89 l. 87 2.07 1. 62 4.7233E+2 100.0 G12-C 7 G12-C8 G12-C18 2>Stk COe 2>Gas Flow 2>NH3 Inj

Stk COe Gas hsefh NH3Inj 

### ppm hsefh Ib/hr 0-1000 0.27 0.27 0.18 0.27 0.27 0 .18 0.27 0.27 0.27 0 .27 0.27 0.27 0.27 0.27 0.27 0.18 0.18 0
. 18 0.27 0.27 0.27 0.27 0.25 0.27 0.18 6.2550E+1 100.0 0-10000 5299.2 5290.8 5300. 4 5303.4 5314.2 5297.4 5301.0 5298 .6 5302.2 5302.8 5310.0 5322.6 5331.6 5323.2 5349.6 5345.4 53 43.0 5342.4 5332.8 5334.0 5334.6 5343.6 5372.5 5457.6 52BO.6 1.3538E+6 100.0 0 -1000 101. 8 10l. 2 102.3 101. 8 103.0 101.8 102.5 101.7 103.5 102.0 101.8 102.2 102.7 102.7 102.7 103.0 103.0 103.2 103.7 104.0 103.0 102.0 106.4 109.7 101.2 2.6B08E +4 100.0



### 2>Summary

- 1-Min RATA

- cont inu ed G12-C 2>MW Lo

MW Lo

0-1 54.: 53.1 54 54.: 54.: 54.! 54.: 54.( 54.' 54.: 54. 54.1 54.: 54.' 54 55.' 55.' 5 4.1 54.: 55.: 54.: 54.' 55.3

56. 53. 1.3941E+ 100.



### PagE

# Data Summary Repor t Company : CPV Se ntinel, LLC 62575 Powerline Road

# ~~I\.l\ 

# Ok:+ 2-

Desert Hot Springs , CA 92240 

# 7-2**I~TIl.-** PM

-

# =t~-I Source: 

### Data Group: Report Name : 

### Start of Report : 

### Turbine 2 2 >1

- Min Cales 2 >Summary

- I-Min RATA 02/01/2013 08,11 G12

- C4 End of Report, 02/01/2013 12,22 GI2-CII G12 -C13 

# fM 

# TRACE
En v ironmental Syste m"" ITIC.



### validation: All Available Data GI2-ClO G12-C6 G12

- C7 G12-Ca G12-C Group#-Channel# 

### Long Descrip. Short Descrip. unit s G12-C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass G12-C20 2>StkFlow

StkFlow

kscfh 0-300000 G12-C3 2>Stk CO

Stk CO ppm 0-1000 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COe 2>Gas Flow 

### Stk CDc Gas hscfh G12-C18 2>NlD Inj NH3Inj

Ib/hr 0-1000 2>MW Lo


### Range 02/01/2013 08:11 02/01/2013 08:12 02/01/2013 08:13 02/01/2013 08:14 02/01/2013 08:15 02/01/2013 08:16 02/01/2013 08:17 02/01/2013 08 : 18 02/01/2013 08:19 02/01/2013 08:20 02/01/2013 08:21 02/01/2013 08:22 02/01/2013 08:23 02/01/2013 08:24 02/01/2013 08:25 02/01/2013 08:26 02/01/2013 08:27 0 2 /01/2013 08:28 02/01/2013 08:29 02/01/ 2 013 08:30 02/01/2013 08:31 02/01/2013 08:32 02/01/2013 08;33 02/01/2013 08:34 02/01/2013 08:35 02/01/2013 08:36 0 2 /01/2013 08 : 37 02/01/2013 08:38 0 2 /01/ 2 013 08:39 02/01/2013 08:40


### Date/Time Printed: 1.3 1. 4 1.5 < 0.5 C 0.0 C 0.0 C 99.0 C 133.6 C 133.7 C

39
. 4 C

4.6 C 4.6 C 3
. 4 C 2.3 < 3.0 2.7 3.1 2
. 7 3
. 0 2.6 3
. 1 2.9 2.B 2
. 9 2.9 2.9 2.9 2
. 8 2.B 2.9 Stk 02 

# • 0-25 13 .39 13 .39 13
. 41< 20
. 64 C 22.45 C 22.46 C

3
. 92 C 0
. 07 C 0.06 C 0.05 C 0.0 4 C 0.0 4 C 10.96 C 13 .43 < 13 .39 13
. 42 13.3 9 13
. 44 13.39 13. 4 3 13.39 13 .3 9 13 .39 13.39 13 .38 13 .38 13.38 13
. 39 13.39 13.39
02/01/2013 16,10 NO x Mass Ib/hr 0-100 2.91 2 .90 2.91 2.90 C 0.00 C 0.00 C 89
. 61C 100
. 00C 100.00C

29.80 C

3.64 C 3.63 C 5
. 08 C 5.08 6.53 5
. 79 6.52 5.79 6.52 5.79 6.5 2 5.8 1 5.81 5
. 80 5.81 5.80 5.81 5.78 5.78 5.79 17626 17584 17662 300000 C DC DC 7810 C 6360 C 635 4 C 6346 C 6350 C 6332 C 13298 C 17676 17575 17620 17552 17659 17555 17625 17552 17 6 04 17612 17558 17584 17552 17569 175 2 5 17511 17552 1.6 2
. 6 1. 3 < 2.1 C 0.0 C 0.0 C 412.2C 891.4C 893.5 C 475.8C 9
. 7 C 9.1 C 5.8 C 2
. 5< 1.9 1.4 1.4 1.4 1.2 1.3 1.0 O.B 0.9 0
. 9 O.B 0.8 0.8 O.B O.B O
. B CO Mass 

### Ib/hr 0-100 2.18 3.63 1. 45 6
. 53 C 0.00 C 0.00 C 100.00C 100.00C 100.00C 100.00C

4
. 37 C 4.35 C 5.81 C 2
. 90 2.18 1.45 1.45 1 .4 5 1 .4 5 1. 45 1. 45 0.73 1. 45 1.45 0.73 0.73 0.73 0
. 72 0
. 72 0.72 NOx Rate Ib/mmBtu 0-1 0.00 4 0
. 004 0.004 0.004 C 0.000 C 0
. 000 C 0.123 C 0.139C 0.139 C 0.041 C 0
. 005 C 0
. 005 C 0.007 C 0.007 0.009 0.008 0.009 0
. 008 0.009 0.008 0.009 0.008 0
. 008 0
. 008 0
. 008 0.008 0
. 008 0.008 0
. 008 0.008 Stk NOXc ppm 0- 300 1. 02 1.10 1.18 < 11.35C

0.00 C 0.00 C 34
. 40C 37.84 C 37.85 C 11.15 C

1
. 30 C 1
. 30 C 2.02 C 1.82 < 2.36 2.13 2 .44 2.14 2.36 2 .05 2.44 2 .2 8 2
. 20 2.28 2
. 28 2. 2 8 2
. 28 2.20 2.20 2.28 ppm hscfh 0-1000 0-10000

1.26 2.0 4 1.02 < 47.65 C

0.00 C 0
. 00 C 143.23C 252.48 C 252
. 96C 134.64 C

2
. 74 C 2.57 C 3.44 C 1.97 < 1.49 1.10 1.10 1.11 0.94 1. 03 0.79 0
. 63 0
. 71 0.71 0.63 0.63 0
. 63 0.63 0 .6 3 0.63 6 925.2 6909
. 0 6921.0 6907.2 6913.2 6918.6 6938
. 4 6931.2 6928.2 6922.2 6930.0 6910.2 6915.6 6907.8 6905. 4 6 895.2 6896. 4 6892.2 6897.6 6888.0 6896.4 6916.8 6919.8 6898.8 6918
. 0 6905.4 6912.0 6885.6 6880
. 2 6896. 4 110
. 0 110.0 110
. 0 110.0 110
. 0 110.0 110.0 110
. 0 110.0 110
. 0 110
. 0 110.0 110.0 110
. 0 110
. 0 110.0 110
. 0 110
. 0 110
. 0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110
. 0 110
. 0 110.0 MW Lo
0-1 79.: 79.: 79. ' 79. : 79. ! 79. : 79. ! 79. ! 79
.. 79
. . 80.1 79.! 79. ! 79. ' 79. ' 79.: 79. ! 79.: 79. ! 79. ! 79. ' 80.1 80. : 80 . : 80.1 80.1 79
.. 79
. 79
.. 80
. ; 

### PagE

### Group#-Channel# Long Descrip
. Short Descrip. units Range 02/01/2013 08:41 02/01/2013 08:42 02/01/2013 08:43 02/01/2013 08:44 02/01/2013 08:45 02/01/2013 08;46 02/01/2013 08:47 02/01/2013 08;48 02/01/ 20 13 08:49 02/01/2013 OS:50 02/01/2013 08:51 02/01/2013 08:52 02/01/2013 08:53 02/01/2013 08;54 02/01/2013 08:55 02/01/2013 08;56 02/01/2013 08:57 02/01/2013 08:58 02/01/2013 08:59 02/01/2013 09;00 02/01/2013 09:01 02/01/2013 09:02 02/01/2013 09:03 0 2 /01/2013 09;04 02/01/2013 09:05 02/01/2013 09:06 02/01/2013 09:07 02/01/2013 09;08 02/01/2013 09;09 02/0 1 /2013 09:10 02/01/2013 09:11 02/01/2013 09:12 02/01/2013 09:13 02/01/2013 09:14 02/01/2013 09;15 02/01/2013 09:16 02/01/2013 09:17 02/01/2013 09:18 02/01/2013 09:19 02/01/2013 09:20 

### Date/Time Printed: G12-C4 GI2

- CII G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass

2.8 2.7 2.8 2.8 2.7 2.8 2.7 2.8 2.7 2.7 2.7 2.6 2.7 2.7 2.6 2.6 2.6 2.5 2.7 2.7 2.7 2.5 2.5 2.6 2.5 2.6 2.6 2.6 2.6 2.6 2.5 2.6 2.4 2.4 2.4 2.5 2.5 2.5 2.5 2.5 Stk 02 t 0-25 13 .40 13 .41 13 .40 13.42 13.42 13. 4 1 13.41 13. 41 13 .42 13 .40 13 .40 13 .40 13 .40 13 .39 13 .41 13.41 13.42 13 .41 13 .40 13 .41 13 .40 13.39 13 .40 13
. 39 13.40 13.41 13 .39 13 .39 13 .40 13 .41 13 .41 13 .40 13.41 13 .41 13.41 13 .41 13 .42 13 .42 13 .40 13 .41 

### 02/01/2013 16,10 NOx Mass 

### Ib/hr 0-100 5.79 5.80 5.78 5.77 5.77 5.78 5.78 5.78 5.77 5.79 5.80 5.80 5.82 5.83 5.81 5.81 5.80 5.08 5.81 5.81 5.82 5.11 5.10 5.83 5.09 5.81 5.82 5.81 5.82 5.81 5.08 5.82 5.09 5.09 5.08 5.07 5.07 5.07 5.08 5.06 G12-C20 2>StkFlow

StkFlow

kscfh 0-300000

17554 17625 17542 17543 17555 17546 17547 17547 17563 17571 17594 17608 17652 17655 17645 17647 17652 17627 17616 17642 17655 17684 17674 17662 17646 17659 17623 17604 17663 17661 17651 17655 17671 17674 17636 17592 17634 17638 17605 17581 G12-C3 2>Stk CO

Stk CO 

### ppm 0-1000

0.8 0.8 0.8 0.7 0.7 0.8 0.8 0.7 0.8 0.8 0.8 0.8 0.8 0.7 0.7 0.7 0.7 0.8 0.8 

## o.s 0.7 

## o.s 0.8 0.7 0.8 0.8 

## o .s 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.8 0.7 0.7 0.8 G12-C13 G12

- C10 G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass 

### Ib/hr 0-100 0.72 0.73 0.72 0.72 0.72 0.72 0.72 0.72 0.72 0.72 0.72 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.72 0.72 0.72 0.73 0
. 72 NOx Rate lb/mmBtu 0-1 0.008 0.008 0.008 0.008 

## o.ooa 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 

## o.ooa 0.008 0.007 0.008 0.008 0.008 0.007 0.007 0.008 0.007 0.008 0.008 O.OOB 0.008 0.008 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXc 

### ppm 0-300 2.20 2.13 2.20 2.21 2.13 2.21 2.13 2.21 2.13 2.12 2.12 2. OS 2.12 2.12 2.05 2.05 2.05 1. 97 2.12 2.13 2.12 1. 96 1. 97 2.04 1. 97 2.05 2.04 2.04 2.05 2.05 1. 97 2.05 1. 89 1. 89 1. 89 1. 97 1. 97 1. 97 1. 97 1. 97 G12-C7 G12-CS 2>Stk COc 2>Gas Flow

Stk COc Gas hscfh ppm hscfh 0-1000 0-10000 0.63 0.63 0.63 0.55 0.55 0.63 0.63 0.55 0.63 0.63 0.63 0.63 0.63 0.55 0.55 0.55 0.55 0.63 0.63 0.63 0.55 0 .6 3 0.63 0
. 55 0.63 0.63 0.63 0.55 0.55 0.55 0.55 0.55 0.55 0.55 0.55 0.55 0.63 0.55 0.55 0.63 6888.0 6906.6 6883.2 6865.2 6870.0 6875.4 6876.0 6876.0 6873.0 6894.6 6903.6 6909.0 6926.4 6936.6 6914.4 6915.0 6907.8 6907.2 6912.0 6913.2 6927.6 6948.0 6934.8 6939.6 6924.0 6919.8 6924.0 6916.8 6930.6 6920.4 6916.8 6927.6 6924.6 6925.8 6910.8 6893.4 6900.6 6902.4 6907.8 6889.2 GI2-ClS 2>NH3 Inj NH3Inj



### Ib/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued GI2-C 2>MW Lo

MW Lo
0-1 79.! 79. ' 79. 79. 79.: 79. ! 79.: 79.: 79. ! 79. : 79
.. 79. : 80
. . 80.! 80.! 80.1 80
.. 80. 80.1 80.: 80. ! 80
.. 80. ! 80. : 80
. . 80.1 

## so 80. : 80.1 80.! 80 80
.. 80 80 80. : 79
.. 80. ( 80. : 80. ( 79. ! 

### PagE

### Group#

- Channel# Long Descrip
. Sho rt Descrip
. units Range 02/01/2013 09:21 02/01/2013 09:22 02/01/2013 09:23 02/01/2013 09:24 02/01/2013 09:25 02/01/2013 09:26 02/01/2013 09:27 02/01/2013 09:28 02/01/2013 09:29 02/01/2013 09:30 02/01/2013 09:31 02/01/2013 09:32 02/01/2013 09:33 02/01/2013 09:34 02/01/2013 09:35 02/01/2013 09:36 02/01/2013 09:37 02/01/2013 09:38 02/01/2013 09:39 02/01/2013 09:40 02/01/2013 09:41 02/01/2013 09:42 02/01/2013 09:43 02/01/2013 09:44 02/01/2013 09:45 02/01/2013 09:46 02/01/2013 09:47 02/01/2013 09:48 02/01/2013 09:49 02/01/2013 09:50 02/01 /2 013 09:51 02/01/2013 09:52 02/01/2013 09:53 02/01/2013 09:54 02/01/2013 09:55 02/01/2013 09:56 02/01/2013 09:57 02/01/2013 09:58 0 2 /01/2013 09:59 02/01/2013 10:00 

### Date/Time Printed: G12-C4 G12-Cll G12-C20 G12-C2 2>Stk NOx

Stk NOx 

### ppm 0

- 150 2>Stk 02 2>NOx Mass 2>StkFlow

2.6 2.5 2.5 2.5 2.6 2.5 2.6 2.6 2.5 2.4 2.4 2.4 2.4 2.4 2.5 2.5 2.5 2.5 2.5 2.5 2.4 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.5 2.5 2
. 6 2.6 2.6 2.4 2.5 2.5 2.6 2.6 2.4 2.4 Stk 02 \ 0-25 13
. 40 13. 4 0 13.40 13 .40 13 .41 13 .41 13
. 4 0 13
. 4 1 13 .4 1 13. 4 0 13.42 13 .41 13
. 41 13
. 4 1 13
. 4 1 13 .4 0 13 .4 1 13 .41 13.41 13
. 4 0 13 .41 13 .41 13
. 41 13
. 40 13. 4 0 13.40 13.39 13
. 39 13 .40 13
. 40 13 .39 13 .39 13. 4 0 13.42 13 .41 13 .40 13.39 13.39 13
. 39 13 .40
02/01/2013 16,10 NOx Mass 

### 1b/hr 0-100 5.80 5.08 5.08 5.08 5.79 5.06 5.82 5.81 5.06 5.08 5.06 5.07 5.06 5.06 5.07 5.09 5.09 5.09 5.08 5.08 5.06 5.80 5.80 5.80 5.81 5.82 5.80 5.81 5.08 5.0B 5.81 5.B2 5.84 5 .09 5.10 5.11 5.84 5.85 5.10 5.09 StkFlow kscfh 0-300000

17602 17626 17625 17609 17589 17579 17654 17647 17582 1762B 17584 17593 17556 17572 17592 17655 17664 17664 17627 17616 17561 17621 17621 17602 17614 17646 17578 17598 17600 17611 17 6 15 17641 17712 17683 17722 17727 17704 17728 1 7650 17651 G12-C3 GI2-C13 G12 -CI0 G12-C6 G12-C7 G12-C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO 

### ppm 0-1000

0.7 0.7 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.7 0.7 0.7 0.7 0.7 0.7 0.6 0.6 0.6 0.6 0.7 0.7 0.7 0.7 0.7 0.7 0.7 0.6 0.6 0.6 0.6 0.6 0.6 0.6 0.7 0.7 0.7 0.7 0.7 0.7 0.7 CO Mass 

### 1b/hr 0-100 0.73 0.73 0.73 0.73 0.72 0.72 0.73 0.73 0.72 0.73 0.72 0.72 0.72 0.72 0
. 72 0.73 0.73 0.73 0.73 0.73 0.72 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 NOx Rate 

### Ib/mmBtu 0-1 0.008 0.007 0.007 0.007 0.008 0.007 O.OOB O.OO B 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.007 0.00 8 0.00 8 0.008 0.007 0.007 0.007 0.008 0.008 0.007 0.007 Stk NOXe 

### ppm 0-300 2.05 1. 97 1. 97 1. 97 2.05 1. 97 2.05 2.05 1. 97 1. 89 1. 89 1. 89 1. 89 1. 89 1. 97 1. 97 1. 97 1. 97 1. 97 l. 97 1. 89 2.05 2.05 2.05 2.05 2.05 2.12 2.04 1. 97 1. 97 2.04 2.04 2.05 1. 89 1. 97 1. 97 2.04 2.04 1. 89 1. 89 Stk COe Gas hscfh ppm hsefh 0-1000 0

- 10000 0.55 6906.6 0.55 6916.2 0.55 6915.6 0.47 6909.6 0.47 0.47 0.47 0
. 47 0
. 47 0.55 0.55 0.55 0.55 0.55 0.55 0. 4 7 0.47 0.47 0.47 0.55 0.55 0.55 0.55 0.55 0
. 55 0.55 0.47 0.47 0
. 47 0.47 0
. 47 0
. 47 0.47 0.55 0.55 0.55 0.55 0.55 0.55 0.55 6892.2 6888.6 6927.0 6915.0 6B89.B 6916.8 6881.4 6894.0 6879.6 6885.6 6893.4 6927.6 6921.6 6921.6 6907.2 6912.0 6881.4 6904.8 6904.8 6906.6 6911.4 6924.0 6906.6 6914.4 6906.0 6910.2 6921.0 6931.2 6949.8 6919.8 6944.4 6955.8 6955.B 6965.4 6934.8 6925.8 NH3Inj 

### Ib/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 

### 2>Summary

- 1-Min RATA

- Continued MW La
0-1 79
. . 79. 80. : 79. ! 80. ! 79
.. 79. 80. ! 79. ! 80.1 79
.. 79 79.: 79
.. 79.! 80. : 79. : 79. : 79. : 80

. 1 79. : 79. 79. : 79. : 79. ! 79.: 80. 1 79. : 79
.. 80. : 80.1 80
. . 80
.. 80.1 80.: 80.: 80. ! BO. 80. ! 80.1 

### PagE

### Group#-Chann e l# Long Descrip
. Short Descrip
. Units Range 02/01/2013 10:01 02/01/2013 10:02 02/01/2013 10:03 02/01/2013 10:04 02/01/2013 10:05 02/01/2013 10:06 02/01/2013 10:07 0 2 /01/2013 10:08 02/01/2013 10:09 02/01/2013 10:10 02/01/2013 10:11 02/01/2013 10:12 02/01/2013 10:13 02/01/2013 10;14 02/01/2013 10:15 02/01/2013 10:16 02/01/2013 10:17 02/01/2013 10:lB 02/01/2013 10:19 02/01/2013 10:20 02/01/2013 10;21 02/01/2013 10:22 02/01/2013 10:23 0 2 /01/2013 10;24 02/01/2013 10:25 02/01/2013 10;26 02/01/2013 10:27 02/01/2013 10:28 02/01/2013 10:29 02/01/2013 10:30 02/01/2013 10:31 02/01/2013 10:32 02/01/2013 10:33 02/01/2013 10:34 02/01/2013 10:35 02/01/2013 10;36 02/01/2013 10:37 02/01/ 2 013 10:38 02/01/2013 10:39 02/01/2013 10:40 

### Date/Time Printed: G12-C4 G12

- C11 G12-C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass

2.5 2.5 2.5 2.' 2.' 2.5 2.5 2.' 2.' 2.' 2.' 2.' 2.5 2.6 2.' 2.' 2.5 2.' 2.' 2.5 2.5 2.' 2.' 2.' 2.' 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.' 2.5 2.5 Stk 02 

# • 0-25 13 .41 13.40 13.41 13 .42 13. 4 2 13 .4 1 13. 4 0 13 .4 0 13 .4 1 13.41 13 .42 13.41 13.41 13 .40 13 .41 13 .41 13 .40 13.41 13.43 13. 4 2 13 .39 13
. 4 1 13.41 13
. 42 13 .41 13
. 43 13 .43 13 .43 13.43 13 .42 13.41 13 .42 13 .42 13
. 42 13 .41 13 .41 13
. 41 13 .4 1 13 .4 1 13. 4 1
02/01/2013 16,10 NOx Mass Ib/hr 0

- 100 5.10 5.09 5.09 5.09 5.10 5.11 5.11 5.11 5.10 5.10 5.08 5.08 5.07 5.BO 5.08 5.09 5.10 5.09 5. 0, 8 5.09 5.09 5.07 5.07 5.05 5.06 5.04 5.05 5.05 5.06 5.06 5.06 5.07 5.06 5.07 5.07 5.07 5.07 5.05 5
. 05 5.07 G12-C20 2>StkFlow

StkFlow

kscfh 0-300000

17693 17664 17668 17692 17716 17726 17730 17710 17716 17696 17650 17625 17598 17603 17622 17667 17674 17657 17682 17698 17613 17612 17596 17571 17569 17559 17573 17574 17599 17606 17579 17621 17600 17635 17604 17587 17595 17543 17535 17585 G12-C3 2>Stk CO

Stk CO ppm 0-1000

0.7 0.6 0.5 0.6 0.7 0.6 0.6 0.7 0.7 0.7 0.6 0.6 O.B 0.7 0.6 0.7 0.7 0.7 0.6 0.7 0.6 0.6 0.6 0.6 0.7 0.6 0.6 0.6 0.6 0.5 0.5 0.6 0.6 0.6 0.6 0.6 0.6 0
. 7 0.7 0. 7 G12-C13 G12 -C10 G12 -C6 2>CO Mass 2>NOx Rate 2>Stk NOXe

CO Mass Ib/hr 0-100 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0
. 73 0.73 0
. 73 0.73 0.72 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.73 0.72 0.72 0
. 72 0.72 0.72 0.72 0.72 0.72 0.72 0.72 0.72 0.72 0
. 72 0.72 0.72 0.72 0.72 0.72 0.72 NOx Rate lb/mmBtu 0

- 1 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 O.OOB 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 Stk NOXe ppm 0-300 1. 97 1. 97 1. 97 1. 89 1. 89 1. 97 1. 97 1. 89 1. 89 1. 89 1. 89 1. B9 1. 97 2.05 1. 89 1. 89 1. 97 1. 89 1. 90 1. 97 1. 96 1. 89 1. 89 1. 89 1. 89 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 97 1. 89 1. 97 1. 97 G12-C7 G12

- C8 2>Stk COe 2>Gas Flow

Stk COe Gas hscfh ppm hscfh 0-1000 0-10000 0.55 0.47 0.39 0.47 0.55 0
. 47 0.47 0.55 0
. 55 0.55 0.47 0.47 0.63 0.55 0.47 0.55 0.55 0.55 0.47 0.55 0.47 0.47 0.47 0.47 0.55 0.47 0.47 0.47 0.47 0.39 0.39 0.47 0.47 0.47 0.47 0.47 0.47 0.55 0.55 0.55 6933.0 6931.2 6923 . 4 6923
. 4 6933.0 6946.2 6957.0 6949.2 6942.0 6934.2 6907.2 6906.6 6895.8 6907.2 6905.4 6922.8 6934.8 6919.2 6910.2 6925.8 6920.4 6901.2 6895.2 6876.0 6884.4 6862.2 6867.6 6868.2 6877.8 6889.8 6888.6 6895.8 6887.4 6901.2 6898.2 6891.6 6894
. 6 6874.2 6871.2 6891.0 G12 -C18 2 >NH3 Inj NH3Inj



### 1b/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 l10.0 1 10.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- 1-Min RATA

- Continued G12-C 2>MW Lo

MW Lo

0-1 BO. 79. BO
. r BO 80.: 80 .: 80. ! 80. : 80.: 80
.. 80.1 80.1 79
. . 80. : 79.1 79.1 79. : 79.1 79
.. 79
.. 80 .1 79
.. 79
.. 78
. 79. ! 79.: 78. : 79.: 79. : 79
.**~** 79
.. 79. ! 79
.. 79. 79. 79. 79. 79. : 79
. 1 79.: 

### Pag{

### Group#-Chann e l# Long Descrip
. Short Descrip. Units Range 02/01/2013 10:41 02/01/2013 10:42 02/01/2013 10:43 02/01/2013 10:44 02/01/2013 10:45 02/01/2013 10:46 02/01/2013 10:47 02/01/2013 10:48 02/01/2013 10:49 02/01/2013 10:50 02/01/2013 10:51 02/01/2013 10:52 02/01/2013 10:53 02/01/2013 10:54 02/01/2013 10:55 02/01/2013 10:56 02/0 1 /2013 10:57 02/01/2013 10:58 02/01/2013 10:59 02/01/2013 11:00 02/0 1 /2013 11:01 02/01/2013 11:02 02/01/2013 11:03 02/01/2013 11:04 02/01/2013 11:05 02/01/2013 11:06 02/01/2013 11:07 02/01/2013 11:08 02/01/2013 11;09 02/01/20 13 11:10 02/01/2013 11:11 02/01/2013 11:12 02/01/2013 11:13 02/01/2013 11:14 02/01/2013 11:15 02/01/2013 11:16 02/01/2013 11:17 02/01/2013 1 1:18 02/01/2013 11:19 02/01/2013 11:20 

### Date/Time Printed: G12 -C2 G12-C4 G12-Cll 2>Stk NOx

Stk NOx ppm 0

- 150 2>Stk 02 2>NOx Mass

2.5 2.5 2.5 2.5 2.5 2.4 2.5 2.4 2.6 2.5 2.5 2.4 2.5 2.5 2.4 2.5 2.4 2.5 2.5 2.4 2.5 2.4 2 .4 2.4 2.4 2.5 2.5 2. 4 2.4 2.5 2.5 2.4 2.6 2.5 2.5 2.3 2.4 2.5 2.5 2.5 Stk 02 % 0-25 13 .41 13 .42 13 .42 13 .42 13 .42 13 .41 13 .41 13.39 13.39 13. 39 13.39 13 .41 13 .40 13 .40 13.39 13.39 13.39 13.39 13
. 39 13.39 13 .38 13 .38 13.38 13.40 13.41 13.40 13. 4 0 13 .42 13 .40 13 .40 13 .40 13.41 13.39 13 .4 0 13 .39 13 .39 13 .41 13 .40 13. 4 0 13.40
02/01/2013 16,10 NOx Mass 

### Ib/hr 0-100 5.06 5.05 5.06 5.05 5.07 5.08 5
. 10 5.11 5.86 5.14 5.14 5.12 5.13 5.14 5.15 5.16 5.16 5.15 5.16 5.15 5.15 5.15 5.14 5.12 5.13 5.14 5.12 5.10 5.13 5.13 5.13 5.12 5.85 5.13 5.16 5.15 5.12 5.11 5.11 5.10 G12

- C20 2>StkFlow

StkFlow

ksefh 0-300000

17572 17548 17577 17571 17634 17645 17720 17708 17742 17806 17809 17792 17790 17836 17823 17867 17878 17839 17855 17847 17797 17805 17779 17749 17797 17827 17758 17738 17778 17788 17772 17774 17734 17799 17870 17835 17769 17716 17721 17695 G12 -C3 2>Stk CO

Stk CO ppm 0-1000

0.9 1.0 1.1 1.1 1.2 1.5 2 '
. 4 2. 5 2.6 2.5 2.5 2
. 7 2.B 2
. 5 2.4 2.4 2.4 2.1 1.9 1.9 1.6 1.5 1.5 1.6 1.B 1.6 1.3 1.1 1.6 1.4 1.7 1.5 1.5 1.4 1.6 1.7 1.6 1.5 1.5 1.8 G12-C13 G12-CI0 G12

- C6 2>CO Mass 2>NOx Rate 2>Stk NOXe

CO Mass lb/hr 0-100 1. 45 1.44 1.44 1.44 1.45 2.18 2.92 2.92 3.66 2.94 2.94 3.66 3
. 66 2.94 2.94 2.95 2.95 2.94 2.21 2.21 2.21 2.21 2.20 2.19 2.20 2.20 1.46 1. 46 2.20 1.47 2.20 2.19 2.19 1. 47 2.21 2.21 2.19 2.19 2.19 2.19 NOx Rate lb/mmBtu 0

- 1 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXe ppm 0-300 1. 97 1. 97 1. 97 1. 97 1. 97 1. 89 1. 97 1. 89 2.0 4 1. 96 1. 96 1. B9 1. 97 1. 97 1. 89 1. 96 1. 89 1. 96 1. 96 1. B9 1. 96 1. B8 1. 88 1. 89 1. 89 1. 97 1. 97 1. 89 1.89 1. 97 1. 97 1. 89 2.04 1. 97 1. 96 1. 81 1. 89 1. 97 1
. 97 1. 97 G12-C7 G12-C8 2>Stk COe 2>Gas Flow

Stk COe Gas hsefh ppm hsefh 0-1000 0-10000 0.71 0.79 0.87 0.87 0.95 1.18 1. 89 1. 96 2.04 1. 96 1. 96 2.13 2.20 1. 97 1. 89 1. 89 1. 89 1. 65 1. 4 9 1. 49 1.26 1.18 1.18 1. 26 1.42 1. 26 1. 02 0.87 1. 26 1.10 1. 34 1.18 1.18 1.10 1. 26 1. 34 1. 26 1.18 1.18 1. 42 6885.6 6867.0 6878.4 6876.0 6900.6 6914.4 6943
. 8 6957.6 6970.8 6996.0 6997.2 6972.0 6980.4 6998.4 7002.6 7020.0 7024.2 7009.2 7015.2 7012.2 7002.0 7005.0 6994.8 6964.2 6973.8 6994.8 6967.8 6941. 4 6975.6 6979.8 6973.2 6964.8 6967.8 6984.0 7021.2 7007.4 6963.0 6951.6 6953.4 6943 . 2 G12

- C18 2>NH3 Inj NH3Inj



### Ib/hr 0

- 1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued G12-C 2>MW Lo

MW Lo
0-1 79. : 79 79
. . 79.: 79.: 79
.. 79
. . 7 9
.. 80.1 80
.. BO. BO .1 80.1 80. : 80
.. 80.: 81.1 81.1 80
.. BO. 80
.. 81.1 80. ! 80.1 80 .1 80
. . 80. ! 80.1 80
. 1 BO. BO
.. BO .1 80.: 81.: 80. : 80
.. 80.1 79
. 80.1 79
.. 

### Pagf

### Group# - Channel# Long Desc r ip . Short Descrip. Unit s Range 0 2 /01/2013 11:21 02/01/2013 11:22 0 2 /01/2013 11:23 02/01/2013 11:24 02/01/2013 11:25 02/01/2013 11:26 02/01/2013 11:27 0 2 /01/2013 11:28 02/01/2013 11:29 0 2 /01/2013 11:30 0 2 /01/ 2 013 11:31 02/01/2013 11:32 02/01/2013 11:33 02/01/2013 11:34 02/01/2013 11:35 0 2 /01/2013 11 : 36 02/01/2013 11 : 37 02/01/2013 11:38 02/01/2013 11:39 02/01/2013 11: 4 0 02/01/2013 11:41 02/01/ 2 013 11:42 02/01/2013 11:43 02/01/2013 11:44 02/01/2013 11 : 45 02/01/2013 11:46 02/01/2013 11:47 02/01/2013 11: 4 8 0 2 /01/ 2 013 11 :4 9 02/01/2013 11:50 0 2 /01/2013 11 : 51 02/01/2013 11:5 2 02/01/2013 11:53 02/01/2013 11:54 02/01/2013 11:55 02/01/ 2 013 11:56 02/01/2013 11:57 02/01/ 2 013 11:58 02/01/2013 11:59 02/0 1 / 2 013 12 : 00 

### Date/Time Printed: G12-C4 G12

- Cll G12

- C20 G1 2 -C2 2 > Stk NOx

Stk NOx 2>Stk 02 2>NOx Mass 2>StkFIow
ppm 0

- 150 2.5 2.4 2
. 6 2.4 2.5 2.5 2
. 6 2.5 2.5 2
. 4 2.6 2 .4 2.4 2
. 4 2.4 2.5 2.6 2 .5 2.4 2.6 2.5 2
. 5 2.5 2.4 2.5 2.5 2
. 6 2.5 2.6 2.6 2
. 5 2
. 5 2.5 2.6 2
. 6 2.5 2
. 5 2.5 2
. 5 2
. 4 Stk 0 2 

# • 0

- 25 13. 4 0 13 .4 1 13 .4 0 13.40 13 .4 0 13
. 39 13
. 38 13 .40 13 .40 13 .41 13. 4 1 13. 4 1 13 .4 0 13
. 4 2 13 .42 13
. 4 1 13.39 13
. 39 13 .40 13.39 13.40 13. 4 0 13.3 9 13 .40 13
. 41 13 .41 13 .41 13.40 13. 4 0 13.39 13 .39 13
. 40 13
. 4 0 13
. 40 13 .4 0 13.40 13
. 39 13.40 13 .39 13 .39
02/01/2013 16 , 10 NOx Mass Ib/hr 0-100 5
. 11 5
. 10 5.84 5.11 5.11 5
. 11 5 .84 5.10 5
. 10 5.09 5.82 5
. 08 5
. 09 5.08 5
. 09 5
. 09 5.83 5
. 10 5.09 5.84 5.08 5.08 5.10 5.07 5.08 5.09 5
. 80 5.07 5.80 5.80 5
. 08 5.06 5.07 5.79 5
. 80 5.07 5.09 5.07 5.07 5
. 08 StkFlow ksefh 0

- 300000

17715 17697 17707 1 7704 17723 17691 17677 17684 17681 17657 1 7 679 17648 17646 1767 2 17695 17665 17672 17659 17645 17697 17626 17629 17646 17586 17622 17656 17633 17571 17593 17566 17577 17559 17576 17580 17591 17585 17642 17596 17571 17586 G12-C3 G12

- C13 G12 -C10 G12 -C6 G12-C7 G12-C8 G12

- C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2 >Stk NOXc 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk 

### co ppm 0

- 1000

1.6 1.7 1.6 1.7 1.9 2
. 0 1.2 1.1 1.3 1.3 1. 2 1.0 1.0 1.1 1.3 1.1 1.3 1.4 1.1 1.0 0.8 0.9 0.8 0.8 0.7 0.6 0.6 0.6 0
. 6 0
. 6 0.6 0
. 5 0.4 0.4 0.4 0
. 3 0.3 0.2 0.1 0.2 CO Mass Ib/hr 0

- 100 2.19 2.18 2
. 19 2.19 2.19 2
. 92 1.46 1.46 1.46 1.45 1. 45 1.45 1. 4 5 1. 4 5 1. 4 5 1. 45 1.46 1.4 6 1.45 1.46 0.73 1. 45 0
. 73 0.72 0.73 0
. 73 0
. 73 0
. 72 0.72 0.72 0.73 0.72 0.7 2 0
. 72 0.72 0.72 0
. 73 0.00 0
. 00 0.00 NOx Rate Ib/mmBtu 0-1 0.007 0.007 0.008 0.007 0
. 007 0.007 0.008 0
. 007 0.007 0.007 0.008 0
. 007 0.007 0.007 0
. 007 0
. 007 0.008 0
. 007 0
. 007 0.008 0.007 0.007 0
. 007 0
. 007 0.007 0.007 0
. 008 0
. 007 0.008 0
. 008 0.007 0
. 007 0.007 0.008 0
. 008 0.007 0.007 0.007 0.007 0
. 007 Stk NO X c ppm 0-300 1. 97 1. 89 2.05 1. 89 1. 97 1. 96 2.04 1. 97 1. 97 1. 89 2.05 1. 89 1. 89 1. 89 1. 89 1. 97 2.04 1. 96 1. 89 2.04 1. 97 1. 97 1.96 1. 89 1. 97 1. 97 2 .05 1. 97 2
. 05 2.04 1.96 1. 97 1. 97 2 .05 2
. 05 1. 97 1. 96 1. 97 1. 96 1. 89 Stk CDc Gas hsefh hsefh 0-10000 ppm 0-1000

1. 2 6 1. 34 1. 26 1. 34 1. 49 1. 57 0.94 0.87 1. 02 1. 02 0
. 95 0.79 0.79 0.87 1. 03 0.87 1. 02 1.10 0.87 0.79 0
. 63 0.71 0
. 63 0
. 63 0.55 0.47 0.47 0.47 0. 4 7 0.47 0.47 0.39 0
. 31 0.31 0
. 31 0.24 0.24 0.16 0.08 0.16 6951. 0 6934.8 69 4 8.0 6946
. 8 6954.0 6951.0 6954
. 6 6939.0 6937
. 8 6919.2 6927.6 6915
. 6 692 4. 0 6915.6 6924.6 692 2 .2 6943.2 6938.4 6923.4 6953.4 6916
. 2 6917.4 6933.0 6900.6 6905.4 6918.6 6909.6 6894.6 6903
. 0 6901.8 6 906
. 0 6889.8 6896 .4 6898.2 6902.4 6900.0 6931.8 6904
. 2 6903.6 6909.6 NH3Inj Ib/hr 0-1000 110.0 110.0 110.0 110.0 110
. 0 110
. 0 110
. 0 110.0 1 1 0.0 110
. 0 110
. 0 110
. 0 110.0 110.0 110.0 110
. 0 110
. 0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110
. 0 1 1 0
. 0 1 10.0 110.0 

### 2>Summary

- I

- Min RATA

- Continued MW Lo
0

- 1 79. ! 79. 79. 79
.. 79
. . 79
. 79
. 79
.. 79. ! 79
. 79
.. 79. : 79. : 79
. . 79 . : 79
.. 80. ( 79
. : 79. ! 80. ( 79
.. 79
. . 79
. 79
. . 79. : 79. ! 79
. . 79
. . 79. : 79. : 79. : 79
. 79. : 79. : 79
. : 79
.. 79
. . 80. ( 79
.. 79 

### PagE

### Group#

- Channel# Long De s crip
. Short Descrip
. Units Range 02/01/2013 12 : 01 02/01/2013 12:02 02/01/2013 12:03 02/01/ 2 013 12:04 02/01/2013 12:05 02/01/ 2 013 12:06 02/01/ 2 013 12:07 02/01/2013 12:08 02/01/2013 12:09 02/01/2013 12:10 02/01/2013 12:11 02/01/2013 1 2 :12 0 2 /01/2013 12:13 02/01/2013 12:14 02/01/2013 12:15 02/01/2013 12 : 16 02/01/2013 12:17 0 2 /01/2013 12 : 18 02/01/2013 12:19 02/01/2013 12:20 02/01/2013 12:21 02/01/2013 1 2 :22 

### Period Average Period Max Value Period Min Value Period Totals 

## = Period % Recovery

Date/Time Printed : G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2.4 2.5 2.5 2.5 2.6 2.5 2.3 2.4 2.4 2.5 2.3 2.3 2.4 2.4 2.4 2
. 3 2.4 2.4 2.3 2.3 2.3 2.3 4.1 133.7

0.0 G12 -C4 G12-Cll G12-C20 2>stk 0 2 2>NOx Mass 2>StkFlow

stk 02 

# , 0-25 13 .40 13
. 38 13 .38 13.39 13
. 38 13.38 13.40 13
. 39 13.39 13
. 37 13 .39 13
. 40 13 .39 13 .38 13.38 13
. 39 13
. 38 13
. 39 13.40 13.40 13 .4 0 13
. 40 13 .19 2 2 .46

0.04 NOx Mass Ib/hr 0-100 5.07 5.09 5.08 5.09 5.82 5.11 5.11 5
. 11 5.10 5.12 5.11 5.10 5.10 5.09 5.09 5
. 09 5
. 11 5
. 09 5.09 5.08 5.08 5.09 6.41 100.00

0.00 StkFlow kscfh 0-300000

17568 17589 17566 17629 17618 17683 17703 17708 17655 17689 17696 1769 4 176 4 6 17616 17619 17636 17654 17642 17632 17623 17622 17638 18349 300000 

### o G12 -C3 G12 -C13 G12-CI0 G12-C6 G12-C7 G12-C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 2>NH3 Inj 2>MW 

### Lo

Stk co 

### ppm 0-1000

0.2 0
. 2 0.2 0.1 0
. 2 0.1 0.2 0
. 2 0.2 0.1 0.2 0
. 2 0.2 0.2 0
. 2 0
. 2 0.2 0.2 0.2 0.2 0.2 0.2 11. 6 893.5

0.0 CO Mass 

### lb/hr 0-100 0.00 0
. 00 0
. 00 0
. 00 0
. 00 0.00 0.00 0
. 00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0
. 00 0.00 0.00 2
. 69 100.00

0.00 NO x Rate lb/mmBtu 0-1 0.007 0
. 007 0.007 0.007 0
. 008 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0
. 007 0.007 0.007 0.007 0.009 0.139 0
. 000 Stk NOXc 

### ppm 0-300 1. 89 1. 96 1. 96 1. 96 2
. 04 1. 96 1. 81 1. 89 1. 89 1. 96 1. 81 1. 81 1. 89 1. 88 1. 88 1. 81 1. 88 1. 89 1. 81 1. 81 1. 81 1. 81 2. 4 4 37.85

0.00 stk COc Gas 

### ppm 0

- 1000 0.16 0
. 16 0
. 16 0.08 0.16 0.08 0.16 0.16 0.16 0.08 0.16 0.16 0.16 0.16 0.16 0
. 16 0
. 16 0.16 0
. 16 0.16 0.16 0.16 4 .02 252.96

0.00 hscfh hscfh 0-10000 6893.4 6919.8 6910.8 6926.4 6931.2 6957.0 6946.2 6957
. 6 6936.6 6968.4 6952.8 6942.6 6933 . 0 6930.6 6931.8 6929
. 4 69 4 5.6 6931.8 6918.6 6915.0 6914.4 6921.0 6922.9 7024.2 6862.2 NH3Inj 

### lb/hr 0-1000 110
. 0 110.0 110
. 0 110
. 0 110.0 110.0 110
. 0 110.0 110.0 110
. 0 110
. 0 110.0 110.0 110
. 0 110.0 110
. 0 110.0 110
. 0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 MW 

### Lo
0-1 79
.**~** 80.1 79. : 79
.. 80.1 80.: 80.1 80. : 79. : 80
.. 80. ! 80.: 79. : 80
.. BO 80.: BO 80.: 80.1 80.1 79
. BO. 79.8



### Bl. 7B. 1.0264E+3 3.3240E+3 1.6154E+3 4.6238E+6 2.9187E+3 6
. 7678E+2 2.22 4 9E+0 6.15 4 7E+2 1.0121E+3 1.74 4 5E+6 2
. 7720E+4 2 .0124E+ 100
. 0 100
. 0 100.0 100.0 100.0 100
. 0 100.0 100.0 100.0 100.0 100.0 100
.

02/01/2013 16 , 10 

### 2>Summary

- I

- Min RATA

- Continued PagE

# Data Summary Report Company: CPV Sentinel, LLC 62575 Powerline Road 

# z

Desert Hot Springs, CA 92240

# 5e..t\+:~\ 

# \)";+ 

# 9M**-1t~** Source: Data Group: Report Name: 

### Start of Report: 

### Turbine 2 2 > 1

- Min Cales 2>Summary

- I-Min RATA 01/30/2013 09,26 G12-C4 

# 7- 2

# (7Tf£ -I'M- /00

- 

# I

End of Report , 01/30/2013 13,34 GI2

- CII GI2-Cl3 

# TRACE
Ellvi ronmelltal 

## Systems, Illc.

Validation : All Available Data GI2-ClO G12 -C6 G12-C7 G12-C8 

### Group#-Channel# Long Descrip. 

### Short Descrip. Units G12

- C2 2:>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass G12

- C20 2>StkFlow

StkFlow

kscfh 0-300000 GI2-C) 2>Stk CO

Stk 

### co ppm 0-1000 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk CDc 2>Gas Flow G12

- C18 2>NH3 Inj NH3Inj



### lb/hr 0

- 1000 G12-C 2>MW Lo

MW Lo 

### Range 01/30/2013 09:26 01/30/ 2013 09:27 01/30/2013 09:28 01/30/2013 09:29 01/30/2013 09:30 01/30/2013 09:31 01/30/2013 09:32 01/30/2013 09:33 01/30/2013 09:34 01/30/2013 09:35 01/30/2013 09:36 01/30/2013 09:37 01/30/2013 09:38 01/30/2013 09:39 01/30/2013 09:40 01/30/2013 09:41 01/30/2013 09:42 01/30/2013 09:43 01/30/2013 09:44 01/30/2013 09:45 01/30/2013 09:46 0 1 /30/2013 09:47 01/30/2013 09:48 01/30/2013 09:49 01/30/2013 09:50 01/30/2013 09:51 01/30/2013 09;52 01/30/2013 09:53 01/30/2013 09:54 01/30/2013 09:55


### Date/Time Printed: 2.7 2.8 2.8 2.9 2.8 2.7 2.7 2.8 2.8 2.7 2.7 2 .8 2.8 2.8 2.8 2.8 2.9 2.9 2.9 2.9 2.9 2
. 8 2.9 2.8 2.9 2.8 2.8 2.8 2.8 2.8 Stk 02 % 0-25 13.03 13.02 13.03 13.03 13.04 13 .04 13
. 03 13.03 13.04 13.0 4 13.04 13.02 13.02 13.03 13.03 13.03 13.02 13.02 13.02 13.03 13.02 13 .03 13 .03 13.03 13.03 13.03 13.03 13.04 13.0 4 13.04
01/30/2013 17,58 NOx Mass Ib/hr 0-100 6.21 7.09 7.05 7.04 7.03 6.16 6.1S 7.07 7.09 6.21 6.22 7.12 7.12 7.10 7.12 7.11 7.12 7.11 7.11 7.11 7.11 7.11 7.10 7.11 7.12 7.13 7.12 7.11 7.12 7.11 20518 20469 20378 20362 20362 20381 20426 20451 20524 20553 20578 20572 20549 20541 20576 20566 20553 20537 20525 20551 20533 20563 20531 20565 20594 20618 20600 20588 20605 20597 0.2 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.1 0.2 0.2 0.2 0 .1 0.1 0.1 0.2 0.2 0.2 0.1 0.1 0.2 0.2 0.2 0.2 0.2 0.3 0.3 D.' 0.5 0.5 CO Mass Ib/hr 0-100 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 .00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.89 0.89 0.89 0.89 0.89 NOx Rate 

### Ib/mmBtu 0-1 0.007 0.008 0.008 0
. 008 O.OOS 0.007 0.007 0.008 0.008 0.007 0.007 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 Stk NOXc ppm 0-300 2.02 2.10 2.10 2.17 2.10 2.03 2.02 2.10 2.10 2.03 2.03 2
. 10 2.10 2.10 2.10 2.10 2.17 2.17 2.17 2.17 2.17 2.10 2.17 2.10 2.17 2.10 2.10 2.10 2.10 2.10 Stk COe Gas hscfh ppm 0-1000 0.15 0
. 07 0.07 0.07 0.08 0.08 0.07 0.07 0.08 0.15 0.15 0.15 0.07 0.07 0.07 0.15 0.15 0.15 0.07 0.07 0.15 0.15 0.15 0.15 0.15 0. 22 0.22 0
. 30 0.38 0.38 

### hscfh 0-10000 8448.0 8438.4 8390.4 8383.8 8373.0 8380.8 8410.2 8420.4 8439.6 8451.6 8461.8 8481. 0 8471. 4 8457.6 8472.0 8467.8 8473.2 8466.6 8461.8 8461.8 8464.8 8466.6 8453.4 8467.2 8479.2 8489.4 8481.6 8466.0 8473.2 8469.6 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 llO.O 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 llO.O 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 llO.O 0-1 102. : 102.: 102. 103.1 102. : 102. 102 102
.. 102
.. 103 103
.. 103
. . 103. ! 103.1 103. ! 103. : 103
. ! 103. ! 103.1 103.1 102. : 103. : 103.1 103.1 102. : 103. ! 103. : 102
. : 10 2 102
. . pagE

### Group#-Channel# Long Deserip. Short Descrip . Units Range 01/30/2013 09:56 01/30/2013 09:57 01/30/2013 09:58 01/30/2013 09:59 01/30/2013 10:00 01/30/2013 10:01 01/30/2013 10:02 01/30/2013 10:03 01/30/2013 10:04 01/30/2013 10:05 01/30/2013 10:06 01/30/2013 10:07 01/30/2013 10:08 01/30/2013 10:09 01/30/2013 10:10 01/30/2013 10:11 01/30/2013 10 : 12 01/30/2013 10:13 01/30/2013 10:14 01/30/2013 10:15 01/30/2013 10:16 01/30/2013 10:17 01/30/2013 10:18 01/30/2013 10:19 01/30/2013 10:20 01/30/2013 10:21 01/30/2013 10:22 01/30/2013 10:23 01/30/2013 10:24 01/30/2013 10:25 01/30/2013 10:26 01/30/2013 10:27 01/30/2013 10 :2 8 01/30/2013 10:29 01/30/2013 10 : 30 01/30/2013 10:31 01/30/2013 10:32 01/30/2013 10:33 01/30/2013 10:34 01/30/2013 10:35 

### Date/Time Printed: G12-C4 G12-C11 G12-C20 G12-C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass 2>StkFlow

2.7 2.8 3.0 2.9 2.8 2.9 2.9 2.9 2.9 2.9 2.8 2.6 2.9 3.0 3.1 3.1 3.1 3.1 3.1 3.1 3.0 3
. 0 3.0 3.0 3
. 0 2.9 2.9 2.9 3.1 3.1 3.1 3.0 3.0 3.1 3.0 2.9 3.0 3.1 3.0 3
. 0 Stk 02 

# • 0-25 13
. 04 13.03 13.03 13.03 13.03 13.03 13.03 13 .0 5 13.05 13.05 13
. 04 13.05 13.03 13
. 02 13.01 13
. 01 13.00 13.01 13
. 02 13.02 13.02 13.03 13.03 13.01 13.02 13.01 13.01 13.01 13.00 13.00 13
. 00 13.00 13.01 13 .01 13.0 2 13.01 13.00 13.00 13.01 13.01
01/30/2013 17,58 NOx Mass 

### Ib/hr 0

- 100 6.22 7.12 7.12 7.10 7.12 7.12 7.12 7.11 7
. 10 7.10 7.03 6.22 7.12 7.14 8.03 8.04 8.04 8
. 02 8.02 8.02 7.13 7.13 7.14 7.14 7
. 15 7.15 7.15 7.13 8.01 8.03 8.03 7.14 7.11 8.03 7.13 7.13 7.13 8.03 7
. 13 7.12 StkFlow ksefh 0-300000

20592 20585 20589 20534 20572 20595 20595 20601 20585 20585 20362 20601 20598 20616 20592 20611 20584 20566 20591 20585 20602 20620 20632 20597 20642 20614 20614 20566 20514 20549 20571 20553 20512 20576 20586 20562 20530 20556 20560 20546 G12-C3 G12 -C13 G12

- C10 G12-C6 G12-C7 G12-C8 G12 -C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO ppm 0-1000



## a .• 0.5 

## a .• a .• 0.4 

### a .• 0
. 3 

## a .• a .• 

## a .• 0.1 1.1 3.5 3.9 3.7 3.7 3
. 7 3.6 3.5 3.5 3.5 3.6 3.6 3.5 3.' 3.' 3.6 3
. 7 3.7 3.8 3.6 3.3 3.' 3.5 3.7 3
. 8 3.6 3.4 3.' 3.5 CO Mass Ib/hr 0-100 0.89 0.89 0.89 0.89 0.89 0
. 89 0 .8 9 0.89 0
. 89 0.89 0.00 1. 78 5.34 6.25 5.36 5.36 5.36 5.35 5.35 5.35 5.35 5.35 5.35 5.36 5.36 5.36 5.36 5.35 5.34 5 .3 5 5.36 5.35 5.33 5
. 35 5.35 5
. 35 5
. 35 5.35 5.35 5.34 NOx Rate lb/mrnBtu 0-1 0.007 0
. 008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.008 0.009 0.009 0.009 0.009 0.009 0.009 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0
. 008 0.009 0.009 0.009 0.008 0
. 008 0.009 0.008 0
. 008 0.008 0.009 0.008 0.008 Stk NOXe ppm 0-300 2.03 2.10 2.25 2.17 2.10 2.17 2.17 2.18 2.18 2.18 2.10 1. 95 2.17 2.25 2.32 2.32 2
. 32 2.32 2.32 2.32 2.25 2.25 2.25 2.24 2.25 2.17 2.17 2.17 2.32 2.32 2.32 2.24 2 .2 4 2.32 2.25 2.17 2.24 2.32 2.24 2.24 Stk COe Gas hsefh hsefh 0

- 10000 ppm 0-1000 0.30 0.37 0.30 0.30 0.30 0.30 0.22 0.30 0.30 0.30 0.08 0.83 2.62 2.92 2.77 2.77 2.76 2.69 2.62 2.62 2.62 2.70 2.70 2.62 2.55 2.54 2.69 2.77 2.76 2.84 2.69 2.46 2.54 2.62 2.77 2.84 2.69 2.54 2.54 2.62 8467.8 8475.6 8477.4 8454.6 8470.2 8479.8 8479.8 8460.6 8454.0 8454.0 8373.0 8460
. 6 8481.0 8499.0 8500.2 8508.0 8507.4 8489.4 8488.8 8486.4 8493.6 8490.0 8494.8 8502.0 8509.8 8509.2 8509.2 8489 4 8478.6 8493.0 8502.0 8494.8 8467.2 8493.6 8487.0 8487.6 8485.2 8496.0 8487.0 8481.0 NH3Inj lb/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110
. 0 110
. 0 110
. 0 110.0 110.0 110.0 110.0 110.0 110
. 0 110
. 0 110.0 110
. 0 110.0 110.0 110.0 110
. 0 110.0 110
. 0 110.0 110.0 110.0 110.0 110
. 0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- 1-Min RATA

- Continued MW Lo
0-1 102
.. 102. : 102. : 102.: 102
.. 102. 103.l 102. 102. 102. : 102. : 102. 102.: 102. : 103.: 103. I 103. : 103.l 103
.**~** 103.l 103.1 103 103. 103. : 103. : 103. 103. : 103. 103.1 103.1 103
. 103. ! 102
.. 103 103.: 103.: 103.l 103
.. 102. : 102 PagE

### Group#-Channel# Long Descrip. Short Descrip
. Units Range 01/30/2013 10;36 0 1 /30/2013 10:37 01/30/2013 10:38 01/30/2013 10 : 39 01/30/2013 10;40 0 1 /30/ 2013 10:41 01/30/2013 10:42 01/30/2013 10;43 01/30/2013 10:44 01/30/2013 10;45 01/30/2013 10;4 6 01/ 30 /2013 10:47 01/30/2013 10;48 01/30/2013 10:49 01/30/2013 10:50 01/30/2013 10;51 01/30/2013 10;52 01/30/20 1 3 10:53 01/30/2013 10;54 01/30/2013 10:55 01/30/2013 1 0:56 01/30/2013 10;57 01/30/2013 10:58 01/30/2013 10:59 01/30/2013 11:00 01/30/2013 11:01 01/ 30 /2013 11:02 01/30/2013 11:03 01/30/2013 11:0 4 01/30/2013 11:05 01/30/2013 11:06 01/30/2013 11;07 01/30/2013 11:08 0 1 /30/ 2013 11:09 01/30/2013 11 ;10 01/30/2013 11;11 01/30/2013 11:12 01/30/ 20 13 11:13 01/30/2013 11:14 01/30/2013 11:15 

### Date/Time Printed: G12-C4 G12-Cll GI2 -C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass

3.0 3.0 3.0 3.0 3.0 2.9 3.0 3.1 3.0 3.1 3.1 3.1 3.0 3.0 3.0 3.1 3.0 3.0 3.0 3.0 3.0 3.0 3.0 3.0 2.9 3.0 2.9 3.0 3.0 3.0 3.0 3.0 3.0 2.8 3.0 2.9 2.8 2.8 3.0 2.8 Stk 02 

# • 0 -2 5 13.00 13.02 13.01 13.01 13.01 13. 01 13.01 13. 01 13.02 13.01 13.02 13. 01 13.01 13.01 13 .00 13.01 13. 0 1 13.02 13.03 13. 02 13.02 13.02 13.02 13.03 13.03 13.02 13.02 13.02 13.03 13 .01 13
. 0 2 13.03 13.03 13.04 13.03 13.04 13.05 13.05 13.04 13.05
01/30/2013 17,58 NOx Mass 

### 1b/hr 0-100 7.13 7.11 7.11 7.13 7.12 7.12 7.13 8 .03 7.12 8.00 7.99 8.02 7.12 7.13 7.13 8.01 7.11 7.11 7.09 7.13 7.12 7.12 7.11 7.10 7.10 7.11 7.10 7.10 7.11 7.12 7.10 7.10 7.09 7.09 7.10 7 .08 7.07 7.06 7.06 7.05 G1l-C20 2>StkFlow

StkFlow

kscfh 0-300000

20533 20531 20502 20555 20537 20524 20576 20579 20550 20521 20514 20559 20540 20560 20534 20534 20508 20518 20500 20578 20553 20572 20530 20532 20514 20528 20492 20506 20544 20546 20511 20525 20505 20532 20540 20496 20493 20478 20 4 27 20434 G1l

- C3 2>Stk CO

Stk 

### co ppm 0-1000

3.5 3.4 3.4 3.4 3.5 3 .3 3.4 3.5 3 .5 3.4 3.2 3.2 3.3 3.4 3.5 3.3 3.' 3.2 3 .3 3.1 3.2 3.2 3.2 3.2 3.2 3.2 3.3 3.2 3.3 3.2 3.2 3.2 3
. 0 3.1 3.1 3.2 3
. 3 3.6 3.4 3.1 G12 -C13 G12-CIO G12-C6 2>CO Mass 2>NOx Rate 2>Stk N OXc CO Mass 

### 1b/hr 0-100 5.35 5.33 5.33 5.35 5.34 5 .34 5.35 5.35 5.34 5.34 4.44 4.46 5.34 5.35 5.35 5.34 5.33 4 .44 5.32 4.45 4.4 5 4.45 4.44 4.44 4.43 4.44 5.32 4.44 5.33 4 .45 4.44 4.44 4.43 4.43 4 .4 4 4.4 3 5.30 5.30 5.29 4
. 41 NOx Rate lb/mmBtu 0-1 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.009 0.008 0.009 0.009 0.009 0.008 0.008 0.008 0.009 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0
. 008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 Stk NOXc ppm 0-300 2.24 2.25 2.24 2.24 2.24 2.17 2.24 2.32 2.25 2.32 2.32 2.32 2.24 2.24 2.24 2.32 2.24 2.25 2
. 25 2.25 2.25 2.25 2.25 2.25 2.17 2.25 2.17 2.25 2.25 2.24 2.25 2.25 2.25 2.10 2.25 2.18 2. 10 2.10 2.25 2.10 G12 -C7 G12 -C8 2>Stk COc 2>Gas Flow

Stk COc Gas hscfh 

### ppm hscfh 0-1000 0-10000 2.61 2.55 2.54 2.54 2.62 2.47 2.54 2.62 2.62 2.54 2
. 40 2.39 2.47 2.54 2.61 2.47 2.54 2.40 2 .4 7 2 .32 2.40 2.40 2.40 2.40 2.40 2.40 2.47 2.40 2.47 2.39 2 .40 2.40 2.25 2.33 2.32 2.40 2.48 2. 71 2.55 2.33 8486.4 8464.2 8463.0 8484.6 8477.4 8472.0 8493.6 8494.8 8472.0 8470.8 8457.0 8486.4 8478.6 8487.0 8487.0 8476.2 8465.4 8458.8 8440.8 8483.4 8473.2 8481.0 8463.6 8454.0 8446.2 8463.0 8448.0 8454.0 8458.8 8481.0 8455.8 8451.0 84 4 2.6 84 4 3.2 8457.0 8428.2 8416.2 8410.2 8400.0 83 92.2 G12-C18 2 >NH3 Inj NH3Inj



### 1b/hr 0-1000 110.0 110.0 110.0 110.0 11 0.0 110.0 110 .0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 11 0.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 11 0.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary - I-Min RATA

- Continued G12-C 2>MW La

MW Lo
0-1 103.! 103 102.' 10 3. ! 102.' 103. ! 103
. . 102. : 102
.. 102
. . 102
. . 103 103. : 103 .• 102. : 103. : 102
. 102.J 10 2
.. 102. : 102
. 103
. . 103. ! 10 3 .
. 10 2. : 102
.. 102.: 103.: 102
.. 103. 102. : 103.1 102
.. 103. 1 102
. : 10 2 . : 102
. 102. : 102
. . 101
. .**Pag~**

### Group#-Channel# Long Descrip . Short Descrip. Units Range 01/30/2013 11:16 01/30/2013 11:17 01/30/2013 11:18 01/30/2013 11:19 01/30/2013 11:20 01/30/2013 11:21 01/30/2013 11:22 01/30/2013 11:23 01/30/2013 11:24 01/30/2013 11:25 01/30/2013 11:26 01/30/2013 11:27 01/30/2013 11:28 01/30/2013 11:29 01/30/2013 11:30 01/30/2013 11:31 01/30/2013 11:32 01/30/2013 11:33 01/30/2013 11:34 01/30/2013 11:35 01/30/2013 11:36 01/30/2013 11:37 01/30/2013 11:38 01/30/2013 11:39 01/30/2013 11:40 01/30/2013 11 :4 1 01/30/2013 11:42 01/30/2013 11:43 01/30/2013 11 :44 01/30/2013 11:45 01/30/2013 11:46 01/30/2013 11:47 01/30/2013 11:48 01/30/2013 11:49 01/30/ 2 013 11:50 01/30/2013 11:51 01/30/2013 11:52 01/30/2013 11:53 01/30/2013 11:54 01/30/2013 11 , 55 

### Date/Time Printed : G12-C4 G12 -Cll G12-C20 G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass 2>StkFlow

3.0 2.8 3
. 1 2.8 2.9 2.8 2
. 9 2
. 9 2.9 2.8 2.9 3.0 2.9 2.9 2.9 3.0 2.9 2.9 2.8 3.0 3.0 2.9 3.0 3.0 3.1 3
. 0 2.9 2.9 2.9 2.9 3.0 3.0 2.9 2.9 2.9 2.9 2.9 2.9 3.0 3.0 Stk 02 % 0-25 13.04 13.05 13
. 02 13.04 13.05 13
. 06 13.06 13
. 05 13.04 13
. 03 13.03 13
. 02 13
. 03 13.02 13.03 13.03 13.03 13.02 13.02 13.02 13.02 13
. 02 13.01 13
. 02 13.00 13
. 00 13.01 13.01 13.01 13.02 13.01 13
. 02 13.02 13
. 02 13
. 02 13.02 13.02 13.01 13.00 13.00
01/30/2013 17,58 NOx Mass 

### lb/hr 0-100 7.06 7.07 7.96 7.05 7.08 7
. 07 7
. 08 7.08 7.08 7.09 7.09 7.10 7.08 7.0B 7.06 7.0B 7.07 7.09 7.09 7.09 7.09 7.09 7.08 7.0B 7.99 7.10 7.0B 7.09 7.0B 7.0B 7.07 7.0B 7.0B 7.06 7.07 7.07 7.06 7.06 7.08 7.09 StkFlow kscfh 0-300000

20430 204B3 20425 20419 20515 20512 20541 205 16 20494 204B6 20499 204B7 20476 20435 20409 20463 2044B 20479 20476 20485 20476 20469 20432 20457 20465 20439 20415 20437 20421 20451 20389 20 44 1 20434 20393 20407 20428 203B4 2 0371 20380 20409 G12-C3 G12-C13 G12-CI0 G12

- C6 G12

- C7 G12 -C8 G12 -C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk 

### co ppm 0-1000

3.2 2.9 3
. 4 2.4 3.5 3.7 3.7 3.5 3.0 3.0 2.9 2.9 2.8 2
. 8 3.0 2.9 2
. 8 2.8 2.8 2.7 2.8 2.8 2.8 2.8 2.7 2.8 2.8 2.7 2.7 2.9 2
. 8 2.7 2
. 7 2.8 2.7 2.8 2.8 2.8 2.7 2.7 CO Mass 

### lb/hr 0-100 4.41 4.42 5.30 3
. 53 5.31 5.30 5.31 5.31 4.42 4.43 4.43 4.43 4.43 4. 4 2 4.41 4.42 4.42 4.43 4.43 4.43 4 .4 3 4.43 4 .43 4.43 4.44 4.44 4.42 4.43 4.43 4.43 4.42 4.42 4.42 4.41 4.42 4.42 4.41 4.41 4.42 4.43 NOx Rate lb/mmBtu 0-1 O.OOB 0.008 0.009 O.OOB 0.008 O
. OOB 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0
. 008 0.008 0.008 0
. 008 0.008 O.OOB 0.008 O.OOB 0.009 O
. OOB O.OOB 0
. 008 O.OOB O.OOB 0.008 0.008 0.008 0.008 0.008 0.008 0
. 008 0
. 008 0.008 0.008 Stk NOXc 

### ppm 0-300 2.25 2.10 2.32 2.10 2
. 18 2.11 2.1B 2.18 2
. 18 2.10 2.17 2 .2 5 2.17 2.17 2
. 17 2 .25 2.17 2.17 2.10 2.25 2.25 2.17 2.24 2.25 2.32 2
. 2 4 2.17 2.17 2.17 2
. 17 2 .24 2.25 2
. 17 2.17 2
. 17 2
. 17 2.17 2.17 2.2 4 2.24 Stk COc Gas ppm 0-1000 hscfh hscfh 0-10000 2. 4 0 2.1B 2.55 1. 80 2.63 2.7B 2.7B 2.63 2.25 2.25 2
. 17 2
. 17 2.10 2.10 2.25 2.17 2.10 2.10 2.10 2
. 02 2.10 2.10 2.09 2.10 2.02 2.09 2.09 2.02 2.02 2.17 2. 09 2.02 2.02 2.10 2.02 2.10 2.10 2.09 2.02 2.02 8401.2 B412
. 0 8420.4 B396.4 8425
. 2 8413.2 8 42 5.2 8425
. 8 B427
. 6 8434.8 B440.2 B446.2 8430 .6 B424.6 8403.0 B425.2 8419.2 8442.6 8441.4 8445.0 8441.4 843B.4 8434.2 8433.6 8458.2 8447.4 8427.0 8436
. 0 8429.4 8431 .2 8416.2 8427.0 B424
. 0 B

4 07.2 B413.2 B421.6 B403.6 8409.0 8423.4 8435.4 NH3Inj 

### lb/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued MW Lo
0-1 102. 10 2
.. 102
. . 102
. 1 10 2 .
. 102.1 102
. 1 102. ' 102. : 102
. 1 102. : 102
. . 102
.. 102
.. 102.1 102.**~** 102
.. 102
.. 102
.**~** 102. 102 102
. . 102
.. 102
.. 102. 103.1 102. 102. J 102. 103
.. 102. : 102. : 102
. . 102.**~** 102
. . 102
. . 102
.. 102
.**~** 102
. . 102
. : Pag(

### Group#-Channel# Long Descrip
. Short Descr i p . Units Range 01/30/2013 11:56 01/30/2013 11:57 01/30/2013 11:58 01/30/2013 11:59 01/30/2013 12:00 01/30/2013 12:01 01/30/2013 12:02 01/30/2013 12:03 01/30/2013 12:04 01/30/2013 12:0S 01/30/2013 12:06 01/30/2013 12:07 01/30/2013 12:08 01/30/2013 12:09 01/30/2013 12 , 10 01/30/2013 12:11 01/30/2013 12:12 01/30/2013 12:13 01/30/2013 12:14 01/30/2013 12:15 01/30/2013 12:16 01/30/2013 12:17 01/30/2013 12:18 01/30/2013 12:19 01/30/2013 12:20 01/30/2013 12:21 01/30/2013 12:22 01/30/2013 12:23 01/30/2013 12:24 01/30/2013 12:25 01/30/2013 12:26 01/30/2013 12:27 01/30/2013 12:28 01/30/2013 12:29 01/30/2013 12:30 01/30/2013 12:31 01/30/2013 12:32 01/30/2013 12:33 01/30/2013 12:34 01/30/2013 12:35 

### Date/Time Printed: G12-C4 G12-C11 G12 -C2 2>Stk NOx

stk NOx 

### ppm 0 -150 2>Stk 02 2>NOx Mass

3.0 3.0 2 .• 3.0 2.' 3.0 3.0 2.' 2 .• 2.9 2.' 3.0 2.' 2.' 3.0 2.' 3.0 3.0 2.' 3.1 3.1 3.1 3.0 3.1 3.0 3.0 3.0 3.0 3.0 2 .• 2.' 3.0 3.0 3.0 2.' 3.0 2 .• 3.0 3.0 3.0 Stk 02 \ 0-25 13.00 13.01 13.02 13.00 13.01 13.00 12.99 13.01 13.00 13.00 12.99 13.00 12.99 12.99 12
. 98 13.00 12.98 12.97 12.98 12.98 12.97 12.97 12
. 97 12.96 12.97 12.96 12.97 12.97 12.98 12
. 98 12.98 12.97 12.97 12.98 12.98 12.98 12.98 12.96 12.96 12.95


### 01/30/2013 17,58 NOx Mass 

### lb/hr 0

- 100 7.08 7.09 7.07 7.10 7.09 7.10 7.11 7.10 7.09 7.09 7.09 7.09 7.11 7.10 7.12 7.10 7.13 7.14 7.12 8 .00 7.14 7.13 7.14 7.15 7.13 7.13 7.13 7.12 7.10 7.10 7.11 7.12 7. 1 2 7.10 7.11 7.09 7.10 7.11 7.13 7.12 G12 -C20 2>StkFlow

StkFlow

kscfh 0-300000

2 0401 20448 20422 20456 20459 20441 20462 20469 20430 20431 20407 20421 20440 20430 20442 20460 20477 20494 20456 20429 20490 20447 20477 2 0489 20452 20429 20465 20425 20387 20393 20423 20428 20439 20407 20440 20378 20407 20377 20 4 21 20385 G12-C3 2>Stk CO

Stk CO 

### ppm 0-1000

2.7 2.7 2 .• 2.6 2 .• 2.6 2.6 2.7 2.6 2.7 2.6 2.7 2.5 2.7 2.' 2.6 2.5 2.5 2.6 2.' 2.6 2.3 2.7 2.5 2.7 2.5 2.7 2.6 2 .• 2.7 2 .• 2.6 2.7 2.5 2.7 2.7 2.7 2.7 2.6 2.6 G12-C13 G12-CI0 G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass



### lb/hr 0-100 4.43 4.43 4.42 3.55 4.43 3.55 3.56 4
. 4 4 3.55 4.43 3.55 4.43 3.55 4.44 3.56 3.55 3.56 3.57 3.56 3.56 3.57 3.56 4.46 3.57 4.45 3.56 4.46 3.56 4.44 4.44 4.44 3.56 4.45 3.55 4.45 4.43 4.44 3.56 3.56 3.56 NOx Rate lb/mmBtu 0-1 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 

### 0.00. 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.00 9 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.00 8 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.00 8 0.008 0.008 Stk NOXc 

### ppm 0-300 2.24 2.24 2.17 2.24 2.17 2.24 2.24 2.17 2.17 2.17 2.16 2.24 2.16 2.16 2.23 2
. 17 2.23 2.23 2.16 2.31 2.31 2.31 2.23 2.30 2.23 2.23 2.23 2.23 2.23 2.16 2.16 2.23 2.23 2.23 2.16 2.23 2.16 2.23 2.23 2.23 G12-C7 G12-C8 2>Stk CDc 2>Gas Flow

Stk COc Gas hscfh ppm hscfh 0-1000 2.02 2.02 2.10 1. 94 2. 09 1. 94 1. 94 2.02 1. 94 2.02 1. 94 2.02 1. 86 2
. 01 1. 79 1. 94 1. 86 1. 86 1. 94 1. 79 1. 93 1. 71 2.01 1. 86 2.01 1. 86 2.01 1. 93 2.09 2.01 2.09 1. 93 2.01 1. 86 2.01 2.01 2.01 2 .01 1. 93 1. 93 0-10000 8431.8 8440.8 8419.2 8454.6 8445.0 8448.6 8467.8 8449.2 8443.8 8444.4 8445.0 8440.2 8458.8 8454.6 8470.2 8456.4 8484.6 8502.6 8476.2 8464.8 8500.8 8482.8 8495.4 8511.0 8485.2 8486.4 8490.6 8473.8 8447.4 8449.8 8462.4 8475.0 8479.8 8455.8 8469.6 8443.8 8455.8 8464.8 8482.8 8478.6 G12 -C18 2>NH3 Inj NH3Inj



### lb/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued G12-C 2>MW Lo

MW Lo
0-1 102. : 102 102. : 103.: 102
.. 102
.**~** 103. : 102.: 102
. : 102.**~** 102. 102. 103.1 103
.. 103. 

### 102 103
.. 104.1 103. 103. : 103. 103. : 103. : 103
. . 103
. . 103. 103.: 103
.**~** 102. ! 102. : 103
.. 103
. . 103. : 103. 103
.. 10 3.1 103.1 103
. . 102 103
.. 

### PagE

### Group#-Channel# Long Descrip. Short Descrip. units Range 01/30/2013 12:36 01/30/2013 12:37 01/30/2013 12:38 01/30/2013 12:39 01/30/2013 12:40 01/30/2013 12:41 01/30/2013 12:42 01/30/2013 12:43 01/30/2013 12:44 01/30/2013 12:45 01/30/2013 1 2:46 01/30/2013 12:47 01/30/2013 12:48 01/30/2013 12:49 01/30/2013 12:50 01/30/2013 12:51 01/30/2013 12:52 01/30/2013 12:53 01/30/2013 12:54 01/30/2013 12:55 01/30/2013 12:56 01/30/2013 12:57 01/30/2013 12:58 01/30/2013 12:59 01/30/2013 13:00 01/30/2013 13:01 01/30/2013 13:02 01/30/2013 13:03 01/30/2013 13:04 01/30/2013 13:05 01/30/2013 13:06 01/30/2013 13:07 01/30/2013 13:08 01/30/2013 13:09 01/30/2013 13,10 02/30/2013 1 3:1 1 01/30/2013 13:12 01/30/2013 13:13 01/30/2013 13:1 4 01/30/2013 13:15
Date/Time Printed: G12-C4 G12-C11 G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass

3.0 3.0 2.9 2.9 3.0 3.0 3.0 2.9 3.0 2.9 3.0 3.1 3.0 2.9 2.9 3.0 3.0 3.0 2.9 2.9 2.9 3.0 3.0 3.0 3.0 2.9 3.0 2.9 2.9 2.8 2.9 2.9 2.8 2.8 2.8 2.8 2.8 2.9 2.8 2.8 Stk 02 

# • 0-25 12.96 12.96 12.96 12.96 12.96 12.98 12 .96 12.98 12.97 12.97 12.97 12 .95 12.95 12.96 12.96 12.96 12.97 12.97 12.98 12.97 12.97 12.98 12.96 12.96 12.96 12.96 12.95 12.96 12.94 12.94 12.94 12.95 12.97 12.96 12.96 12.96 12.95 12.94 12.96 12.95
01/30/2013 17,58 

### NOx Mass 

### Ib/hr 0-100 7.13 7.13 7.12 7.12 7.12 7.11 7.12 7.10 7.10 7.11 7.11 7.13 7.12 7.11 7.10 7.12 7.09 7.10 7.10 7.11 7.09 7.10 7.12 7.11 7.10 7.09 7.11 7.09 7.13 7.11 7.12 7.10 7.09 7.11 7.11 7.10 7.12 7.13 7.11 7.11 G12-C20 2>StkFlow

StkFlow

kscfh 0-300000

20422 20427 20408 20419 20392 20433 20399 20401 20387 20405 20402 20414 20388 20389 20357 20390 20355 20381 20387 20396 20357 20404 20396 20388 20362 20314 20346 20315 20378 20336 20354 20324 20338 20379 20388 20356 20375 20384 20366 20359 G12-C3 2>Stk CO

Stk 

### CO ppm 0-1000

2.3 2.5 2.4 2.7 2.5 2.7 2.5 2.8 2.7 2.5 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.5 2.6 2.8 2.6 2.8 2.5 2.6 2.6 2.8 2.9 2.5 2.7 2.7 2.5 2.6 2.5 2.5 2.6 2.5 2.6 2.5 2.6 2.6 G12-C13 G12 -C 10 G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc



### CO Mass 

### Ib/hr 0-100 3.56 3.56 3.56 3.56 3.56 4.45 3.56 4.44 4.44 3.56 3.55 3.57 3.56 3.56 3.55 3.56 3.55 3.55 3.55 4.44 3.55 4.44 3.56 3.56 3.55 4.43 4.44 3.54 3.56 3.56 3.56 3.55 3.54 3.56 3.56 3.55 3.56 3.57 3.55 3.56 

### NOx Rate Ib/mmB tu 0-1 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 Stk 

### NOXC ppm 0-300 2.23 2.23 2.15 2.15 2.23 2.23 2 .23 2.16 2.23 2.16 2.23 2.30 2.23 2.15 2. 15 2.23 2.23 2.23 2.16 2.16 2.16 2.23 2.23 2.23 2.23 2.15 2.23 2.15 2.15 2.08 2.15 2.15 2.08 2.08 2.08 2.08 2.08 2.15 2.08 2.08 G12-C7 G12-C8 2>Stk COc 2>Gas Flow

Stk 

### CDc Gas hscfh ppm hscfh 0-1000 0-10000

1. 71 1. 86 1. 78 2.01 1. 86 2.01 1. 86 2.09 2.01 1. 86 1. 93 1. 93 1. 93 1. 93 1. 93 2.01 1. 93 1. 86 1. 94 2.08 1. 93 2.09 1. 86 1. 93 1. 93 2.08 2.15 1. 86 2.00 2.00 1. 85 1. 93 1. 86 1. 86 1. 93 2. 86 1. 93 1. 85 1. 93 1. 93 8483.4 8485.2 8477.4 8482.2 8470.8 8466.6 8473.8 8453.4 8458.2 8465.4 8464.2 8490.6 8479.8 8469.6 8456.4 8470.2 8445.0 8455.8 8447.4 8461.8 8445.6 8454.6 8472.6 8469.0 8458.2 8438.4 8462.4 8439.0 8486.4 8469.0 8476.2 8453.4 8437. 8 8465.4 8469.0 8455.8 8474.4 8488.8 8460.0 8467.8 G12-C18 2>NH3 Inj NH3Inj



### Ib/hr 0-1000 110.0 110 .0 110 .0 110 .0 110.0 110.0 110.0 110 .0 110.0 110.0 110 .0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 2>Summary

- I -M in RATA

- Continued G12-C 2>MW Lo

MW Lo
0-1 103. ! 103
. . 103.: 103.: 103 102. 103.**~** 103
. : 102
. . 103
.. 103. : 103. : 103
.. 103.1 103.1 103
. . 102
.. 103.1 102
. . 103. 1 102
.. 102
.. 103.1 103.1 103
.. 102. : 102
.. 102. 104.1 103
.. 103.1 103.1 102
.. 102 103. 1 103
.. 103
. . 103
.. 103.1 103
.. PagE

### Group #- Channel# Long Descrip_ short Descrip. Units Range 01/30/ 2 013 13:16 01/30/2013 13:17 01/30/2013 13:18 01/30/2013 13:19 01/30/2013 13:20 01/30/ 2 013 13:21 01/30/2013 13:22 01/30/2013 13:23 01/30/2013 13:24 01/30/2013 13:25 01/30/2013 13:26 01/30/ 2 013 13: 2 7 01/30/ 2 013 13:28 01/30/2013 13:29 01/30/2013 13:30 01/30/2013 13:31 01/30/2013 13 : 32 01/30/ 2 013 13:33 01/30/2013 13:34 

### Period Average Period Max Value Period Min Value Period Totals 

## = Period 

### % Recovery



### Date/Time P r inted : G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2.7 2.8 2.8 2.8 2.8 2.8 2.8 2.7 2
. 8 2.7 2.8 2. 7 2 .9 2.9 2
. 8 2.9 2.9 2.9 2.9 2.9 3.1 2.6 G12 -C4 G12

- C11 G12

- C20 2>Stk 02 2>NOx Mass 2>StkF1ow

Stk 02 

# • 0-25 1 2. 96 12
. 95 12
. 94 12
. 94 12.95 1 2 .96 12.96 12.96 12
. 96 12.96 12
. 96 12
. 97 12
. 94 1 2.91 12.93 12.93 1 2. 93 12.92 12.92 13.00 13
. 06 12.91 NOx Mass 

### Ib/hr 0 -1 00 6.22 7.10 7.11 7.09 7.10 7
. 09 7.08 6.20 7.08 6.20 7
. 08 6.19 7.12 7
. 16 7.15 7.14 7
. 15 7.14 7.14 7.13 8.04 6
. 16 StkFlow 

### kscfh 0

- 300000

20360 20309 20325 20274 20327 20310 20304 20302 20288 20317 20285 20308 2 0368 20395 20400 20391 20414 20370 20363 20 4 69 20642 20274 G12-C3 G12 -C13 G12

- C10 G12 -C6 G12-C7 G12

- C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW La



### Stk CO 

### ppm 0-1000

2.8 2.6 2.9 2
. 7 2.7 2.7 2.8 2
. 8 2.7 3.0 2.7 2. 9 2.9 2.6 2.8 2.6 2.6 2 .8 2
. 5 2
. 5 3.9 0
. 1 CO Mass 

### Ib/hr 0-100 4.44 3.55 4.44 3.55 3.55 3.54 4 .43 4.43 3
. 5 4 4
. 43 3.5 4 4. 4 2 4
. 45 3
. 58 4.47 3.57 3.58 4. 47 3.57 3
. 71 6
. 25 0.00 NOx Rate 1b/mmBtu 0-1 0.007 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.007 0.008 0
. 007 0
. 008 0
. 008 0
. 008 0
. 008 0
. 008 0.008 0.008 0.008 0
. 009 0
. 007 Stk NOXe 

### ppm 0-300 2
. 01 2
. 08 2.08 2
. 08 2.08 2.08 2
. 08 2.01 2.08 2.01 2
. 08 2.01 2.15 2
. 14 2.07 2
. 15 2
. 15 2.14 2.14 2
. 19 2.32 1. 95 

### stk CDc Gas hsefh 

### ppm hscfh 0-1000 0

- 10000 2.08 8457.6 1.93 8446.8 2.15 8464.2 2.00 8443.2 2.00 8454.6 2.01 8436.6 2
. 08 8434
. 2 2
. 08 8433.6 2.01 8427.6 2.23 8439.6 2.01 8426
. 4 2.16 8425.2 2.15 8482
. 2 1.92 8525
. 4 2
. 07 8506.2 1
. 92 8502.6 1.92 8512
. 2 2.07 8504.4 1.85 8501.4 1.86 8459.2 2.92 8525.4 0
. 07 8373
. 0 NH3Inj lb/hr 0 -1 000 110.0 110.0 110.0

63
. 2 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 109.8 110.0

63.2 MW Lo
0-1 102 102." 103
. : 102.' 102
. ' 103
. 1 102.' 102. ' 102.' 102.' 102.! 102
. ' 103
. 104.' 103
. 103
. 103.' 103
. 103. ' 102.9

104
. 101. 7
. 2880E+2 3
. 2371E+3 1.7764E+3 5.0968E+6 6.1970E+2 9.2486E+2 2.0000E+0 5.4432E+2 4.6265E+2 2.1063E+6 2.7343E + 4 2.5627E+ 100.0 100.0 100
. 0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.

01/30/2013 17,58 

### 2>Summary

- 1-Min RATA

- Continued Pag(

# Data Summary Company :

S o urce : 

### Data Group: Report Na me: 

### Start of Report : 

# Report 

# csN**~~A1.\** 

# U-

. +2**fl ~** **\<;~5"-** 

# \t"'-' CPV Sentinel, LLC 62575 Powerline Road 

### Desert Hot Springs, CA 92240 Turbine 2 2>1-Min Cales 

### 2>Summary

- I-Min RATA 

### 01/30/2013 13 , 45 

# 5-

# 2/~ft. -eM-TOO-£..

End of Report , 01/30/2013 17,51 G12-C4 GI2 -CII G12-C13 

# TRACE
En/'i ro llm e nlai S y s te m s , In c.

Validation : All Available Data GI2 -CIO G12

- C6 G12-C7 G12

- C8 

### Group#-Channel# Long Descrip. 

### Short Descrip
. 

### Units G12-C2 2>Stk NOx

Stk NO x ppm 0-150 2 >St k 02 2 >NOx Mass G12

- C20 2>StkF!ow

StkFlow



### kscfh 0

- 300000 G12-C3 2>Stk CO

Stk CO ppm 0

- 1000 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk CDc 2>Gas Flow G12-C18 2>NH3 Inj NH3Inj

Ib/hr 0 -1 000 G12-C 2>MW Lo

MW Lo 

### Range 01/30/ 2 013 13:45 01/30/2013 13:46 01/30/2013 13:47 01/30/2013 13:48 01/30/2013 13:49 01/30/2013 13:50 01/30/2013 13:51 01/30/2013 13:52 01/30/2013 13:53 01/30/2013 13:54 01/30/2013 13:55 01/30/2013 13:56 01/30/2013 13:57 01/30/2013 13:58 01/30/2013 13:59 01/30/2013 1 4 :00 01/30/2013 14:01 01/30/2013 14:02 01/30/2013 14:03 01/30/2013 14:04 01/30/2013 14:05 01/30/2013 14:06 01/30/2013 14:07 01/30/2013 14:08 01/30/2013 14:09 01/30/2013 1 4 :10 01/30/2013 14:11 01/30/ 2 013 14:12 01/30/ 2 013 14:13 01/30/ 2 013 14:14


### Date/Time Printed: 2.8 44.4 B 61.0 B 60.1 B 21.1 B

1. 3 B 6.9 B 16.1 B 51.3 B 57.0 B 54.5 B 56.1 B 56.8 B 57.0 B 57.1 B 57.3 B 57.1 B 57.2 B 57.6 B 57.4 B 57.7 B 57.4 B 42.7 B

3.8 B 2.9 B 1.1 B 2.88 3.2 B 2.4 B 2.3 B Stk 02 

# • 0- 2 5 12
. 95 13
. 2 7 B 13.3 4 8 13.38 B 14.11 B 15.878 15.61 B 14.54 B 13.858 13.808 13
. 83 B 13.808 13. 8 0 B 13 .8 0 B 13
. 7 9 B 13
. 78 B 13.78 B 13.77 B 13.768 13.76 B 13
_75 8 13.778 14.07 B 15.13 8 15. 6 4 B 15
. 23 B 14.078 13. 3 8 B 13
. 30 B 13 .3 18


### 01/31/2013 12,03 NOx Mass 

### Ib/hr 0-100 7.10 100.00B 100.00 B 100.00B

34.41B

1.65 B 10.59 B 33.04 B 100.00 B 100.00B 100.00B 100.008 100.00B 100.00B 100.00B 100.00B 100.00 B 100.00 B 100.00 B 100.00B 100.008 100.00 B

87.35 B

5.09 B 3.85 B 1
. 66 B 5.90 B 7.85 B 6.19 B 6.19 B 20332 19339 20090 19248 13568

9923 13012 17194 19835 20470 20046 20483 20483 20564 20459 20484 20424 20492 20434 20402 20422 20365 17119 11462 11109 13325 17470 21125 21188 21199 

### 3
. 0 1.58 0.0 B 

### o. a B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B O. 

### a B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.0 B 0.48 2.6 B 4.3 B 3.9 B CO M a ss 

### 1b/hr 0-100 4 .4 4 2.43 B 0.00 B 0.00 B 0.00 B 0.00 B 0.00 B 0.00 B 0.00 B 0
. 00 B 0.00 B 0.00 B 0.00 B 0.00 B 0
. 008 0.00 B 0.00 B 0.00 B 0.00 B 0.00 B 0.008 0.008 0.008 0_ 008 0.008 0.008 0. 6 6 B 4.368 6.198 6.19 B 

### NOx Rate Ib/mmBtu 0-1 0.008 0.126 B 0.175 B 0.174 B 0.068 B 0.006 B 0.0288 0.0558 0.158 B 0.174 B 0.1688 0.1728 0.174 B 0.174 B 0.175 B 0.175 B 0.1748 0.174 B 0.175 B 0 .17 5 B 0.175 B 0.175 B 0.136 B 0.014 B 0.012B 0.0048 0.0098 0.0098 0.007 B 0.0078 Stk NO X c ppm 0

- 300 2.08 34.33 B 47.61 B 47.158 18.338

1.528 7.70 8 14.948 42.93 B 47.378 45.488 46.62B 47
. 20 B 4 7.37B 47.388 47.48 B 47.32 B 47.338 47.60 B 47.43 B 47.618 47.508 36.89 B

3.89 B 3 .2 5 B 1.14 B 2.428 2.51 B 1.868 1.798 Stk CDc Gas 

### hscfh p p m 0-1000 2.23 1.16 B 0.00 B 0.00 B 0.00 B 0.00 B 0.00 B 0.00 B 0.00 B 0.00 B 0
. 008 0.00 B 0
. 00 B 0
_00 8 0.00 B 0
. 00 B 0
. 008 0.00 B 0.00 B 0.00 B 0.00 B 0
. 00 B 0.00 B 0
. 00 B 0.00 B 0.00 B 0
. 358 2
. 04 B 3
. 3 4 B 3
. 03 B 

### hscfh 0 -1 0000 8456.4 7719.6 7945.8 7572.6 4819.8 2611. 2 3601.2 5721.0 7315.8 7603.8 7414.8 7608.6 7608.6 7638.6 7610.4 7630.2 7608.0 7644.0 7633.2 7621. 2 7639.2 7596.6 6117.0 3460.2 3057.0 3952.8 6242.4 8311.2 8424.6 8418.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 1 10.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 0-1 

### 102

92
. . 98 90. 45. : 16.: 32. : 65
. ! 89. c 93. ( 89
.. 92
. 92
. . 9 2. : 93. ( 93
. . 92. : 93. 93.: 92. : 93. 92
. 66. ( 25. ! 22
. . 36. ( 71.: 101.: 102 102. ( pagE

### Group#-Channel# Long Descrip. Short Descrip. Units Range 01/30/2013 14:15 01/30/2013 14:16 01/30/2013 14:17 01/30/2013 14:18 01/30/2013 14:19 01/30/2013 14:20 01/30/2013 14:21 01/30/2013 14:22 01/30/ 20 13 14:23 01/30/2013 14:24 01/30/2013 14:25 01/30/2013 14:26 01/30/2013 14:27 01/30/2013 14:28 01/30/2013 14:29 01/30/2013 14:30 01/30/2013 14:31 01/30/2013 14:32 01/30/2013 14:33 01/30/2013 14:34 01/30/2013 14:35 01/30/2013 14:36 01/30/2013 14:37 01/30/2013 14:38 01/30/2013 14:39 01/30/2013 14:40 01/30/2013 14:41 01/30/2013 14:42 01/30/2013 14:43 01/30/2013 14:44 01/30/2013 14:45 01/30/2013 14:46 01/30/2013 14:47 01/30/2013 14:48 01/30/2013 14:49 01/30/2013 14:50 01/30/ 2 013 14:51 01/30/ 2013 14:52 01/30/2013 14:53 01/30/2013 14:54 

### Date/Time Printed: G12-C4 G12 -Cll G12-C20 G12

- C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass 2>StkFlow

2.2 B 2.2 B 2.1 B 2.3 B 2.2 B 2.2 B 2.4 B 2.4 B 2.5 B 2.4 B 2.5 B 2.5 B 2.5 B 2.5 2.6 2.5 2.6 2.6 2.6 2.7 2.5 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.6 2.7 2.7 2.6 2.7 2.7 2.7 Stk 02 

# • 0-25 13.3 2B 13.31B 13.32B 13.29 B 13.23 B 12.96 B 12.94 B 12.96 B 12 .94 B 12.96 B 12.96 B 12.96 B 12.96 B 12.95 12.95 12. 95 12.95 12.94 12.96 12.95 12.97 12.96 12 .96 12.96 12.97 12.96 12.96 12.95 12.95 12.96 12.95 12.94 12.94 12.95 12.95 12.94 12.95 12.95 12.95 12.95 

### 01/31/2013 12,03 NOx Mass 

### Ib/hr 0-100 5.31 B 5.31 B 5.31 B 6.21 B 5.31 B 5.31 B 6.20 B 6.19 B 6.21 B 6.19 B 6.19 B 6.19 B 6.19 B 6.20 6.19 6.19 6.19 6.18 6.18 6.16 6.17 6.17 6.17 6.17 6.17 6.17 6.18 6.18 6.18 6.18 6.18 6.19 6.19 6.18 6.18 6.19 6.17 6.19 6.19 6.18 StkFlow ksefh 0-300000

21235 21242 21261 21234 20986 20288 20251 2027 3 20280 20282 20282 20258 20284 20288 20238 20261 20234 20205 20232 20167 20225 20210 20206 20207 20224 20197 20249 20228 20231 20237 20231 20210 20212 20218 20215 20218 20197 20261 20254 20215 G12

- C3 G12-C13 G12-C10 GI2 -C6 G12-C7 G12-C8 G12 -C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW La

Stk CO ppm 0

- 1000

3.2 B 2
. 8 B 3.0 B 2.6 B 2.4 B 2.6 B 2.4 B 2.2 B 2.3 B 2.2 B 2.1 B 1. 9 B 1. 9 B 2.0 1.9 1.9 2.0 1.9 1.9 1.8 1.8 1.6 1.6 1.7 1.7 1.5 1.6 1.5 1.6 1.4 1.5 1.5 1.5 1.6 1.7 1.7 1.5 1.7 1.5 1.4 CO Mass 

### Ib/hr • 0-100

5.31 B 4.43 B 4.43 B 4.44 B 3.54 B 3.54 B 3.54 B 3.54 B 3.55 B 3.54 B 2.65 B 2.65 B 2.65 B 2.66 2.65 2
. 65 2.65 2.65 2.65 2.64 2.64 2.64 2.64 2.64 2.64 1. 76 2.65 1. 77 2.65 1. 77 1. 77 1. 77 1. 77 2.65 2.65 2.65 1. 76 2.65 1. 77 1. 77 NOx Rate 

### Ib/mmBtu 0-1 0.006 B 0.006 B 0.006 B 0.007 B 0.006 B 0.0068 0.007 B 0.00 7 B 0 .0 078 0.007 B 0.007 B 0.007 B 0.007 B 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 Stk NOXe ppm 0-300 1.71 B 1. 71 B 1.63 B 1. 78 B 1.69 B 1. 63 B 1.78 B 1.78 B 1.85 B 1.78 B 1.86 B 1. 86 B 1.86 B 1. 86 1.93 1. 86 1. 93 1. 93 1. 93 2.00 1. 86 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 2.00 1. 93 1. 93 2.00 2.00 1. 93 2.00 2.00 2.00 Stk COe Gas ppm 0-1000 hscfh hsefh 0-10000 2.4 9 B 2.18 B 2.34 B 2.02 B 1.85 B 1.93 B 1. 78 B 1. 63 B 1.70 B 1.63 B 1.56 B 1.41 B 1.41 B 1. 48 1.41 1.41 1. 48 1.41 1.41 1.34 1.34 1.19 1.19 1.26 1. 26 1.11 1.19 1.11 1.19 1. 04 1.11 1.11 1.11 1.19 1.26 1.26 1.11 1.26 1.11 1. 04 8421.0 8434.8 8431.2 8454.0 8421.0 8427.6 8433.6 8421. 6 8445.6 8425.2 8425.2 8415.0 8425.8 8438.4 8417.4 8427.0 8415.6 8414.4 8404.2 8388.0 8391.0 8395.2 8393.4 8394.0 8390.4 8389.8 8411. 4 8413.2 8414.4 8406.6 8414.4 8416.2 8417.4 8409.0 8407.8 8419.8 8400.6 8427.0 8424.0 8407.8 NIB Inj 

### Ib/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 1 10.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued MW La
0-1 102
.. 102
.. 102. 102 102.1 102. : 102
. 102
.. 102
. 102
.. 102. : 102.**~** 102
.. 103. : 102 ' 102
.. 102
. : 102. : 102.: 101. : 102.: 102.1 102. : 101. : 101.
. 102. 1 102.: 102.: 102.: 102
. ! 102. ! 102. : 102. : 102
. . 102. 102.1 102.1 102 102
.. 102.**~ Pag~** 

### Group#-Channel# Long Descrip. Short Descr i p . U

n its Range 01/30/2013 14:55 01/30/2013 14:56 01/30/2013 14:57 01/30/2013 14:5S 01/30/2013 14:59 01/30/2013 15:00 01/30/2013 15:01 01/30/2013 15:02 01/30/2013 15:03 01/30/2013 15:04 01/30/2013 15:05 01/30/2013 15:06 01/30/2013 15:07 01/30/2013 15:0S 01/30/2013 15:09 01/30/2013 15:10 01/30/2013 15:11 01/30/2013 15:12 01/30/2013 15:13 01/30/2013 15:14 01/30/2013 15:15 01/30/2013 15:16 01/30/2013 15:17 01/30/2013 15:18 01/30/2013 15:19 01/30/2013 15:20 01/30/2013 15:21 01/30/2013 15:22 01/30/2013 15:23 01/30/2013 15:24 01/30/2013 15:25 01/30/2013 15:26 01/30/2013 15:27 01/30/2013 15:28 01/30/2013 15:29 01/30/2013 15:30 01/30/2013 15:31 01/30/2013 15:32 01/30/2013 15:33 01/30/2013 15:34 

### Date/Time Printed: G12-C4 G12

- Cll G12-C2 2>stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass

2.6 2.7 2.7 2.7 2.6 2.7 2.6 2.7 2.6 2.7 2.7 2.6 2.7 2.7 2.7 2.6 2.6 2.6 2.6 2.7 2.6 2.7 2.7 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.8 2.7 2.7 2.7 2.7 2.8 2.8 2.7 Stk 02 

# • 0-25 12.96 12.94 12.95 12.95 12.96 12.96 12.95 12.95 12.95 12.95 12.95 12.96 12
. 96 12.97 12.96 12.96 12
. 96 12.96 12.96 12.95 12.96 12.94 12.94 12.95 12.95 12.95 12.95 12.95 12.95 12.95 12.94 12.96 12.93 12.93 12.92 12.93 12.93 12
. 91 12.9 2 12.92
01/31/2013 12,03 NOx Mass 

### Ib/hr 0 -1 00 6.18 6.1S 6.1S 6.18 6.16 6.17 6.17 6.17 6.17 6.18 6.18 6.16 6.17 6.16 6.17 6.17 6.16 6.1S 6.17 6.1S 6.16 6.18 6.19 6.17 6.1S 6.17 6.1S 6.18 6.18 6.18 6.19 6.1S 7.0S 6.20 6.20 6.20 6.20 7.10 7.10 6.21 G12-C20 2>StkFlow

StkFlow

ksefh 0-300000

20243 20201 20222 2020) 20167 20197 20180 20186 20189 20225 20205 20174 20204 20204 20200 20220 20182 20236 20197 20203 20190 20175 2 0208 20172 20203 20184 20213 20231 20202 20222 2 0223 20239 20216 20230 20215 20220 20227 20214 20235 20225 G12-C3 2>Stk CO

Stk CO 

### ppm 0-1000

1.6 1.5 1.6 1.6 1.5 1.5 1.6 1., 1.5 1., 1.' 1., 1.5 1., 1.3 1.5 1.3 1.4 1.5 1.4 1.6 1.3 1.4 1.3 1.4 1.3 1.3 1.5 1.3 1.5 1.4 1.7 1.5 1.5 1.5 1.7 1.7 2.0 1.6 1.9 G12-Cl3 G12 -C10 G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXe

CO Mass



### Ib/hr 0-100 2.65 1. 77 2.65 2.65 1. 76 1. 76 2.64 1. 76 1. 76 1. 77 1. 76 1. 76 1. 76 1. 76 1. 76 1. 76 1. 76 1. 77 1. 76 1. 76 2.64 1. 76 1. 77 1. 76 1. 76 1. 76 1. 77 1. 77 1. 76 1. 77 1.77 2.65 1.77 1. 77 1. 77 2.66 2.66 2.66 2.66 2.66 NOx Rate 

### Ib/mmBtu 0-1 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.008 0.008 0.007 stk NOXc 

### ppm 0-300 1. 93 2.00 2.00 2.00 1. 93 2.01 1. 93 2.00 1. 93 2.00 2.00 1. 93 2.01 2.01 2.01 1. 93 1. 93 1. 93 1. 93 2.00 1. 93 2.00 2.00 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 2.00 1. 93 2.07 2.00 2.00 2.00 2.00 2.07 2.07 2.00 G12-C7 G12

- CS 2>Stk COe 2>Gas Flow

Stk COc Gas hscfh 

### ppm hsefh 0-1000 0-10000

1.19 1.11 1.19 1.19 1.11 1.11 1.19 1. 04 1.11 1. 04 1. 04 1. 04 1.11 1. 0 4 0. 9 7 1.11 0.97 1. 04 1.11 1.04 1.19 0.96 1. 04 0.96 1. 04 0.96 0.96 1.11 0.96 1.11 1. 04 1.26 1.11 1.11 1.11 1. 26 1. 26 1. 4 S 1.18 1. 40 8409.0 8412.6 S410.8 8403.0 8377.2 8389.8 8393.4 8395.8 8397.0 8412.0 8403.6 8380.2 8392.8 8382.0 8391. 

### a 8399.4 8383.8 8406. 

## a 8389.8 8403.0 8386.8 8401.8 8415.6 8389.8 8403.0 8395.2 8407.2 8414.4 8402.4 8410.8 8421.6 8407.2 8429.4 8435.4 8439.6 S431. 2 8434.2 8449.8 8448.0 8443.8 G12-C1S 2>NH3 Inj NH3Inj



### 1b/br 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110. 

## a 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued G12-C 2>MW Lo

MW Lo
0-1 102
.**~** 102
.. 102. 102. 102
. . 102. : 102
.. 102. ( 102. ! 102. ! 102. : 101.
. 102.c 101.1 102
. . 102. : 102. c 102. ! 102.**~** 102
. . 102. c 102. ! 102. : 102. : 102. ! 102.! 102
. . 102. 102.: 102.: 102
. ! 102.! 103.: 102. : 102 102 102.: 102.: 103.' 103.! pagE

### Group #-Cha nnel# Long Descrip . Short Descrip . Un i ts Range 01/30/2013 15:35 01/30/2013 15:36 01/30/2013 15:37 01/30/2013 15:38 01/30/2013 15:39 01/30/2013 15 : 40 01/30/2013 15:41 01/30/2013 15:42 01/30/2013 15:43 01/30/2013 15:44 01/30/2013 15:45 01/30/2013 15:46 01/30/2013 15:47 01/30/2013 15:48 01/30/2013 15:49 01/30/2013 15:50 01/30/2013 15:51 01/30/2013 15:52 01/30/2013 15:53 01/30/2013 15:54 01/30/2013 15:55 01/30/2013 15:56 01/30/2013 15:57 01/30/2013 15:58 01/30/2013 15:59 01/30/2013 16:00 01/30/2013 16:01 01/30/2013 16:02 01/30/2013 16:03 01/30/2013 16:04 01/30/2013 16 : 05 01/30/2013 16:06 01/30/2013 16:07 01/30/2013 16;08 01/30/2013 16:09 01/30/2013 16;10 01/30/2013 16;11 01/30/2013 16;12 01/30/2013 16;13 01/30/2013 16:14 

### Date/Time Printed: G12 -C2 G12-C4 G12

- CII 2:>Stk NOx

Stk NOx 

### ppm 0

- 150 2:>Stk 02 2:>NOx Mass

2.7 2.8 2.7 2.8 2.7 2.7 2.8 2.7 2.8 2.8 2.7 2.9 2.8 2.8 2.8 2.8 2
. 7 2.8 2.8 2.8 2.7 2.8 2.8 2.8 2.7 2.7 2.7 2.7 2 .7 2.7 2.7 2
. 7 2.7 2.8 2.7 2.7 2.7 2.7 2.7 2.7 Stk 02 

# • 0-25 12.91 12.91 12.92 12.91 12.91 12
. 91 12.89 12.90 12.90 12.90 12.91 12.89 12.89 12
. 88 12.89 12.89 12.92 12.91 12.91 12.91 12.93 12.92 12.91 12.92 12.93 12.92 12.93 12.93 12.93 12.94 12.93 12
. 93 12.93 12.93 12.93 12.94 12
. 94 12.92 12.93 12.93 

### 01(31(2013 12 , 03 NOx Mass lb/hr 0-100 6.21 7.12 6.22 7
. 12 6
. 23 6
. 22 7.14 6.24 7.14 7.13 6.23 7.13 7.14 7.16 7.14 7.15 6
. 22 7.11 7.12 7.12 6.21 7.10 7.11 7.11 6.20 6.20 6.19 6.18 6.20 6.18 6.20 6.19 6.21 7.09 6
. 19 6.18 6.20 6.21 6.20 6.20 G12-C20 2:>StkFlow

StkFlow

ksefh 0-300000

20227 20264 20254 20271 20279 20257 20281 20296 20305 20276 20293 20262 20274 20323 2027 4 20305 20255 20260 20287 20290 20259 20255 20257 20271 20239 20215 20197 20176 20220 20182 20243 20212 20262 20236 20203 20202 20261 20239 20227 20216 G12

- C3 2:>Stk CO

Stk CO 

### ppm 0-1000

1.7 1.8 1.5 1.3 1.7 1.5 1.9 1.9 

### 2
. 1 2.3 2
. 4 2.4 

### 2.2 2.4 2.2 2.2 

### 2.3 2.4 2.4 2.4 2.4 2.7 2.8 2.5 2.7 2.7 2.9 2.8 2.7 2.7 2.6 2.8 2.7 2.8 2.7 2.8 2.9 2.8 2.9 2.9 GI2

- CD G12-CIO Gl2 -C6 2:>CO Mass 2:>NOx Rate 2:>Stk NOXe

CO Mass 

### 1b(hr 0-100 2
. 66 2.67 1. 78 1. 78 2.67 1. 78 2.68 2.68 2
. 68 3
. 56 3.56 3.57 3.57 3.58 3
. 57 3.57 3.55 3.56 3.56 3.56 3.55 3.55 4.45 3.55 3.54 3.54 4.42 4.42 3
. 54 3.53 3.55 4.42 3.55 4.43 3.54 4.42 4.43 4
. 44 4.43 4.43 NOx Rate lb/mmBtu**0~1**

0.007 0.008 0.007 0.008 0.007 0.007 0.008 0.007 0.008 0.008 0.007 0.008 0.008 0.008 0.008 0
. 008 0.007 0.008 0.008 0.008 0.007 0.008 0.008 0
. 008 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.008 0.007 0
. 007 0
. 007 0
. 007 0.007 0.007 Stk NOXe 

### ppm 0-300 1. 99 2.07 2.00 2.07 1. 99 1. 99 2.06 1. 99 2.07 2.07 1. 99 2.14 2.06 2.06 2.06 2.06 2.00 2.07 2.07 2.07 2.00 2.07 2.07 2.07 2.00 2. 00 2.00 2
. 00 2.00 2.00 2
. 00 2.00 2
. 00 2
. 07 2.00 2.00 2.00 2
. 00 2.00 2.00 G12 -C 7 G12 -C8 2:>Stk COe 2>Gas Flow

Stk COe Gas hsefh 

### ppm hscfh 0

- 1000

1. 26 1. 33 1.11 0.96 1. 26 1.11 1. 40 1. 40 1. 55 1. 70 1. 77 1. 77 1. 62 1. 77 1. 62 1. 62 1. 70 1. 77 1. 77 1. 77 1. 78 2.00 2
. 07 1. 85 2.00 2.00 2
. 15 2.07 2
. 00 2.00 1. 92 2.07 2
. 00 2
. 07 2.00 2.08 2.15 2
. 07 2.15 2.15 0

- 10000 8 4 55.2 8470.8 8455.8 8473.8 8476.8 8467
. 8 8499.0 8494.8 8498
. 4 8486.4 8482
. 8 8491 2 8496.0 8527
. 2 8496
. 0 8509
. 2 8456.4 8469
. 0 8480
. 4 8481.6 8447.4 8456.4 8467.8 8463.0 8439.0 8439.6 8421.6 8412.6 8431.2 8404.8 8440.8 8427.6 8448
. 6 8437
. 8 8424.0 8413.2 8437
. 8 8449
. 8 8434
. 2 8429.4 G12-C18 2>NH3 Inj NH3Inj



### 1b(hr 0-1000 110
. 0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110
. 0 110
. 0 110
. 0 110
. 0 110
. 0 110.0 110
. 0 110
. 0 110
. 0 110.0 110.0 110
. 0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110
. 0 110.0 110.0 110
. 0 110.0 110.0 110
. 0 

### 2:>Summary

- I-Min RATA

- Continued G12-C 2>MW Lo

MW Lo**~1**

103.1 103
.. 103. : 103. : 103. : 103. : 

### 103 103
. : 103
. . 103. ! 103
.. 104
. ( 104
. 1 104. ' 103. : 104.: 103,1 103. : 103. ! 103
.. 102. : 103.: 103. ! 103.1 103, : 103. ( 102. ' 102. ( 102. : 102
.. 102. ! 102. ; 102. ! 102
.. 102. 102,
. 102
. 103. I 102
.. 103. I pag(

### Group#-Channel# Long Descrip. S hort Descrip . Units Range 01/30/2013 16:15 01/30/2013 16:16 01/30/2013 16:17 01/30/2013 16:18 01/30/2013 16:19 01/30/2013 16:20 01/30/2013 16:21 01/30/2013 16 : 22 01/30/2013 16:23 01/30/2013 16:24 01/30/2013 16:25 01/30/2013 16:26 01/30/2013 16:27 01/30/2013 16:28 01/30/2013 16:29 01/30/2013 16:30 01/30/2013 16:31 01/30/2013 16:32 01/30/2013 16:33 01/30/2013 16:34 01/30/2013 16:35 01/30/2013 16:36 01/30/2013 16:37 01/30/2013 16:38 01/30/2013 16:39 01/30/2013 16:40 01/30/2013 16:41 01/30/2013 16:42 01/30/2013 16:43 01/30/2013 16:44 01/30/2013 16:45 01/30/2013 16:46 01/30/2013 16:47 01/30/2013 16:48 01/30/2013 16:49 01/30/2013 16:50 01/30/2013 16:51 01/30/2013 16 : 52 01/30/2013 16:53 01/30/2013 16:54 

### Date/Time Printed: G12

- C4 G12

- C 1 1 G12-C20 G12-C2 2>Stk NOx

Stk NOx 2>Stk 02 2>NOx Mass 2>StkFlow
ppm 0-150 2.7 2.7 2.8 2.6 2.7 2.8 2.7 2.8 2.7 2.7 2.7 2.7 2
. 7 2.7 2.7 2.8 2.7 2.6 2.6 2.6 2.7 2.7 2.7 2
. 7 2.7 2.7 2.8 2.7 2.8 2.B 2.B 2.7 2.8 2.7 2.7 2.7 2.6 2.6 2.7 2.6 Stk 02 

# • 0-25 12.91 12.92 12
. 91 12.94 12.94 12.93 12.93 12.93 12.94 12.94 12.93 12.93 12.93 12
. 93 12
. 92 12 .9 1 12.93 12.93 12.93 12.94 12.94 1 2 .93 12.94 12.94 12.93 12.92 12.91 12
. 91 12.91 12.90 12.90 12.91 12.90 12
. 92 12.93 12.93 12.95 12.94 12.94 12.96
01/31/2013 12,03 NOx Mass 1b/hr 0

- 100 6.21 6.21 7.11 6.18 6.18 7.09 6.20 7
. 09 6
. 19 6
. 19 6
. 20 6.21 6.19 6.20 6.21 7.10 6.20 6.20 6.20 6.19 6
. 20 6.21 6.19 6.21 6.20 6.23 7.11 6
. 23 7.13 7.14 7.13 6.22 7.12 6.23 6.22 6 .2 2 6.20 6.21 6.21 6.19 StkFlow ksefh 0-300000

20205 20239 20243 20182 20191 20252 20219 20233 20210 20237 20240 20252 20206 20243 20249 20221 20226 20213 20216 20218 20248 20260 20224 20277 20236 20291 20260 20293 20310 20305 20272 20251 20243 20303 20301 20308 20287 20276 20277 20260 G12-C3 G12-C13 G12-C10 G12-C6 G12

- C7 Gl2-C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO ppm 0-1000

2.8 2.9 2.8 2.9 3.0 3.0 3.0 2.9 2.9 2.9 3.0 3.1 3.1 3.1 3.2 3.1 3.2 3.3 3.3 3.2 3.4 3.2 3.1 3.2 3.2 3.2 3.1 3.2 3.1 3.3 2.9 3.1 3.0 3.1 3
. 1 3.2 3.3 3.3 3.1 3
. 4 CO Mass lb/hr 0-100 4.43 4.44 4.44 4.41 4
. 41 4.43 4.43 4.43 4.42 4.42 4.43 4.43 4.42 4
. 43 4.44 4.44 4.43 4.43 4.43 4.42 5.31 4.44 4
. 42 4.43 4.43 4.45 4.45 4.45 4.46 4.46 4.45 4.44 4.45 4.45 4.44 4.45 4.43 4.43 4
. 43 5.30 NOx Rate lb/mmBtu 0-1 0
. 007 0.007 0.008 0.007 0.007 0.008 0.007 0.008 0.007 0.007 0.007 0
. 007 0
. 007 0.007 0.007 0.008 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0
. 007 0
. 008 0.008 0.008 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXe ppm 0-300 1. 99 2.00 2.07 1. 93 2.00 2.07 2.00 2.07 2.00 2.00 2
. 00 2
. 00 2.00 2.00 2.00 2.07 2.00 1. 92 1. 92 1. 93 2.00 2
. 00 2.00 2.00 2.00 2.00 2.07 1. 99 2.07 2.07 2.07 1. 99 2
. 07 2.00 2.00 2.00 1. 93 1. 93 2.00 1. 93 Stk COe Gas hsefh ppm hscfh 0

- 1000 0

- 10000 2.07 8446.2 2.14 8449.8 2.07 8461.8 2.15 8404
. 8 2.22 8408.4 2.22 8444
. 4 2.22 8430
. 6 2.15 8436.6 2.15 8416.2 2.15 8427.6 2.22 8439.6 2.29 8444
. 4 2.29 8425
. 2 2.29 8440
. 8 2.37 8454.0 2.29 8452.8 2.37 8433.6 2.44 8428.2 2.44 8429.4 2.37 8419.8 2.52 8432.4 2.37 8448.0 2.30 8422.2 2.37 8444.4 2.37 8437.8 2.37 8471.4 2.29 8469.0 2.36 8482.8 2.29 8490.0 2.43 8498.4 2.14 8484
. 6 2.29 8465.4 2.21 8472.6 2.29 8476.2 2.29 8464.8 2.37 8467.8 2.45 8437.8 2.45 8443.8 2.30 8444.4 2.53 84 1 6
. 2 NH3Inj Ib/hr 0

- 1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 1 10.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- I

- Min RATA

- Continued MW Lo
0-1 102
. 103.1 103. ( 101.
. 102. ! 103.1 102
.. 102
.. 102.1 102.: 103.: 102
.. 102. : 103 102
. 102. : 102. 102. 102
. . 102.: 102. 102. ! 102
. . 102
. . 102
. . 103. : 103
. : 103.1 103. ! 1 03. : 103. 1 103. ( 103.( 103. 1 102
.. 102. 102. : 102
.. 102
.. 102.1 PagE

### Group#-Channel# Long Descrip
. Short Descr i p . Units Range 01/30/2013 16:55 01/30/2013 16:56 01/30/2013 16:57 01/30/2013 16:58 01/30/2013 16:59 01/30/2013 17:00 01/30/2013 17:01 01/30/2013 17:02 01/30/2013 17:03 01/30/2013 17:04 01/30/2013 17:05 01/30/2013 17:06 01/30/2013 17:07 01/30/2013 17:08 01/30/2013 17:09 01/30/2013 17:10 01/30/2013 17:11 01/30/2013 17:12 01/30/2013 17:13 01/30/2013 17:14 01/30/2013 17;15 01/30/2013 17:16 01/30/2013 17;17 01/30/2013 17:18 01/30/2013 17:19 01/30/2013 17:20 01/30/2013 17:21 01/30/2013 17:22 01/30/2013 17:23 01/30/2013 17:24 01/30/2013 17:25 01/30/2013 17:26 01/30/2013 17;27 01/30/2013 17:28 01/30/2013 17:29 01/30/2013 17:30 01/30/2013 17:31 01/30/2013 17:32 01/30/2013 17:33 01/30/2013 17:34 

### Date/Time Printed: G12 -C2 G12 -C4 G12 -C11 G12

- C20 2;:.Stk NOx

Stk NOx ppm 0

- 150**2~Stk** 02**2~NOx** Mass 2;:.StkFlow

2.7 2.6 2.7 2.6 2.6 2.6 2.7 2.7 2.7 2.7 2.6 2.7 2.7 2.8 2.7 2.7 2.6 2.7 2.6 2.7 2.7 2.7 2.7 2.7 2.7 2
. 7 2.7 2.7 2.6 2.7 2.7 2.6 2.7 2.7 2.6 2.7 2.7 2.8 2.7 2.7 Stk 02 

# • 0-25 12.95 12.97 12.96 12.97 12.96 12.95 12.94 12
. 93 12.93 12.93 12.93 12.92 12.93 12
. 92 12.93 12.91 12.92 12.92 12.93 12.93 12
. 93 12.92 12.9 2 12
. 92 12.93 12.93 12.91 12.93 12.92 12.94 12.93 12.93 12.93 12.93 12.93 12
. 9 2 12.91 1 2 .91 12.91 12.92
01/31/2013 12,03 NOx Mass Ib/hr 0-100 6.18 6.16 6.16 6.16 6.16 6.18 6.20 6.21 6.21 6.21 6.23 6.24 6.23 7.13 6.23 6.25 6.25 6.24 6.24 6.22 6.23 6.24 6.23 6.25 6.23 6.24 6.25 6.25 6.24 6.23 6.23 6.23 6.23 6.23 6.24 6.25 6.25 7.16 6.24 6.24 StkFlow kscfh 0-300000

20215 20189 20174 20195 20184 20208 20238 20255 20255 20255 20321 20323 20334 20321 20340 20342 20353 20343 20345 20291 20322 20340 20316 20362 20325 20377 20336 20383 20347 20351 20318 20325 20322 20314 20358 20367 20339 20378 20317 20340 G12-C3 G12 -CD G12-C10 G12-C6 G12-C7 G12

- C8 G12-C18 G12-C 2;:.Stk CO 2;:.CO Mass 2;:.NOx Rate 2;:.Stk NOXc**2~Stk** COc 2;:.Gas Flow 2;:.NH3 Inj 2;:.MW La

Stk CO ppm 0-1000

3.4 3.4 3.9 3.7 3.6 3.7 3.6 3.3 3.3 3.3 3.5 3.4 3.6 3.3 3.6 3.5 3.6 3.6 3.6 3.8 3.9 3.7 3.8 3.8 3.6 3.8 3.6 3.8 3.6 3.7 3.7 3.6 3.7 3.6 4.0 3.8 3.8 3.4 3.8 3.6 CO Mass lb/hr 0-100 5.30 5.28 5.28 5.28 5.28 5.30 5.31 4.43 4.43 4.43 5.34 5.35 5.34 4.45 5.34 5.36 5.35 5.35 5.34 5.33 5.34 5.35 5.34 5.36 5.34 5
. 35 5.36 5
. 35 5.35 5.34 5.34 5.34 5.34 5.34 6.24 5.36 5.36 5.37 5.35 5.35 NOx Rate lb/mmBtu 0

- 1 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 Stk NOXc ppm 0

- 300 2.00 1. 93 2.01 1. 93 1. 93 1. 93 2.00 2.00 2.00 2.00 1. 92 2.00 2.00 2.07 2.00 1. 99 1. 92 2.00 1. 92 2.00 2.00 2.00 2.00 2.00 2.00 2.00 1. 99 2.00 1. 92 2.00 2.00 1. 92 2.00 2.00 1. 92 2.00 1. 99 2.07 1. 99 2.00 Stk COc Gas ppm hscfh hscfh 0-1000 2.52 2.53 2.90 2.75 2.68 2.75 2.67 2 .44 2.44 2.44 2.59 2.51 2
. 66 2.44 2.66 2.58 2.66 2.66 2.66 2.81 2.89 2 , .74 2.81 2.8 1 2
. 66 2.81 2.66 2.81 2.66 2.74 2.74 2.66 2.74 2.66 2.96 2.81 2.81 2
. 51 2.81 2.66 0-10000 8407.8 8376.0 8380.2 8378.4 8384.4 8404.8 8428.2 8445.6 8445.6 8445.6 8473.2 8484.6 8478.6 8484.0 8481.0 8503.2 8497.2 8493.0 8483.4 8460.6 8473.8 8491. 8 8481.6 8500.8 8475.0 8496.6 8500.8 8499.0 8494.8 8475.0 8472.0 8475.0 8473.8 8470.2 8488.8 8503.2 8502.0 8518.2 8493.0 8491
. 8 NH3Inj 

### 1b/hr 0-1000 110.0 llO .0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 1 10.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued MW La
0-1 102. : 101. ! 101. 101. 102.1 102
. : 102.: 103
. ! 103.J 10) .J 103.J 103. ! 103. : 104.1 102. 103.: 103
.**~** 103. ! 103.: 102. : 103.: 103.1 103.1 103. : 103. ! 103.: 103. ! 103 103. 103.1 102. 102. 103.1 103.: 103
.. 103.! 103.! 103. : 103
.. 103
. . 

### Pagf

### Group #-Channel# Long Descrip
. Short Descrip
. Units Range 01/30/2013 17:35 01/30/2013 17:36 01/30/2013 17:37 01/30/2013 17:38 01/30/2013 17:39 01/30/2013 17:40 01/30/2013 17:41 01/30/2013 17:42 01/30/ 2 013 17:43 01/30/2013 17:44 01/30/2013 17:45 01/30/2013 17:46 01/30/2013 17:47 01/30/2013 17:48 01/30/2013 17:49 01/30i 2 013 17:50 01/30/2013 17:51 

### Period Average Period Max Value Period Min Value Period Totals 

# = Period 

### % Recovery



### Date/Time Printed: G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2.8 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2.8 2.7 2.7 2.6 2.6 2.6 2.7 2.6 6.7 61. 0

1.1 G12-C4 G12-C11 G12-C20 2>Stk 02 2>NOx Mass 2>StkFlow

Stk 02 % 0-25 12
. 91 12.93 12.93 12.92 12.92 12.92 1 2.91 12.91 12.92 12.92 12.91 12.91 12.93 12 .9 3 12.9 4 12.94 12
. 96 13.07 15.87 12.88 NOx Mass 

### lb/hr 0-100 7.15 6.24 6.25 6.26 6.26 6.27 6.28 6.27 6.26 7.15 6.27 6.25 6.24 6.23 6.23 6.23 6.20 13 .29 100.00

1. 65 StkFlow kscfh 0-300000

20356 20361 20393 20400 20405 20428 2 0429 20424 20409 20379 20401 20339 20367 2 0317 20342 20346 20323 20054 21261

9923 G12-C3 G12-C13 GI2-CI0 G12-C6 G12

- C7 G12-CS G12 -CIS G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO 

### ppm 0-1000

3.7 3.7 3.9 3.7 3.7 3.8 3.6 4.0 3.7 4.0 3.8 3.8 3.7 3
. 9 3.9 3.8 4.0 2.4 4.3 0.0 CO Mass lb/hr 0-100 5.36 5.35 5.36 5.37 5.37 5.37 5.38 6.27 5.37 6.25 5.37 5.36 5.35 5.34 5.34 5.34 6.20 3.40 6.27 0.00 NOx Rate lb/mmBtu 0-1 0.008 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0
. 007 0.007 0.007 0.007 0.007 0 .0 0 7 0.007 0.019 0.175 0.004 Stk NOXc 

### ppm 0-300 2.07 2.00 2.00 2.00 2.00 2.00 1. 99 1. 99 2.00 2.07 1. 99 1. 99 1. 92 1. 92 1. 93 2.00 1. 93 5.31 47.61

1.14 Stk CDc Gas 

### ppm 0-1000 hscfh 

### hsefh 0-10000 2.73 2
. 74 2.S9 2.74 2.74 2.S1 2 .6 6 2.95 2. 74 2.96 2.81 2.8 1 2.74 2.89 2.89 2.82 2.97 1. 75 3.34· 0.00 8509.2 8490.0 8503.2 8517.0 8518.8 8528.4 8539.8 8537.4 8520.6 8508.0 8527.8 8502.0 8492.4 8471 4 8471.4 8473.2 8442.0 8239.1 8539.8 2611.2 NH3Inj 

### lb/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 MW Lo
0-1 103 103. 104.1 103. 104. ! 104. : 10 4
. 103
.. 104. ! 103. ! 103
.. 103
.. 103. 103
. . 102
.. 103.1 102. : 99.8 104.

16. 1. 6448E+3 3.2285E+3 3.2827E+3 4.9533E+6 5.8170E+2 8.3991E+2 4.8029E+0 1.3127E+3 4.3164E+2 2.0350E+6 2.7170E+4 2.4671E+ 100.0 100
. 0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.



### 01/31/2013 12,03 

### 2>Summary

- l-Min RATA

- Continued 

### Pag{

# Data Summary Report C

o mpany : CPV Sentinel, LLC 62575 Powerline Road 

### Desert Hot Springs, CA Source : Turbine 2 Data Group:**2>1~Min** 

### Cales Report Name: 

# CPJ**')~, Ul\~t**  

# 2-

# ~ \**3~~** 

# - I'':)' \(A't-, b**~A4** 

# TRACE

92240 

# 5- Z/trr'l-**_~fA.-** 100-1 Ellviro n me llt a l S yst e m s, Ill c.

Start of Report : 2>Summary

- I-Min RATA 01/30/2013 13,45 

### End of Report: 01/30/2013 17:51 validation: Valid Data Only 

### Group#-Channel# Lo ng Descrip
. 

### Short Descrip
. Units Range 01/30/2013 13:45 01/30/2013 13:46 01/30/2013 13:47 01/30/2013 13:48 01/30/ 2 013 13:49 01/30/2013 13:50 01/30/2013 13:51 01/30/2013 13:52 01/30/2013 13:53 01/30/2013 13:54 01/30/2013 13:55 01/30/2013 13:56 01/30/2013 13:57 01/30/2013 13:58 01/30/2013 13:59 01/30/2013 14:00 01/30/2013 14:01 01/30/2013 14:02 01/30/2013 14:03 01/30/2013 14:04 01/30/ 2 013 14:05 01/30/2013 14:06 01/30/2013 14:07 01/30/2013 14:08 01/30/2013 14:09 01/30/2013 14:10 01/30/2013 14:11 01/30/2013 14:12 01/30/2013 14:13 01/30/2013 14:14


### Date/Time Printed: G12-C2 G12-C4 G12-Cll 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass

2.8 Stk 02 % 0-25 12.95

01/31/2013 12,03 

### NOx Mass 1b/hr 0-100 7.10 GI2 -C20 2>StkFlow



### StkFlow

kscfh 0-300000

20332 19339 20090 19248 13568

99 2 3 13012 17194 19835 20470 20046 20483 20483 20564 20459 20484 20424 20492 20434 20402 20422 20365 17119 11462 11109 13325 17470 21125 21188 21199 GI2-C) 2>Stk CO

Stk CO 

### ppm 0-1000

3.0 GI2-Cl3 GI2-CIO G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXC

CO Mass NOx Rate Stk NOXc 

### Ib/hr Ib/mmBtu ppm 0-100 0-1 0-300 4.44 0.008 2.08 G12-C7 G12-CB 2>Stk CDc 2>Gas Flow



### Stk COc Gas hscfh ppm 0-1000 2.23 

### hscfh 0-10000 8456.4 7719.6 7945.8 7572.6 4819.8 2611.2 3601.2 5721.0 7315.8 7603.8 7414.8 7608.6 7608.6 7638.6 7610.4 7630.2 7608.0 7644.0 7633.2 7621.2 7639.2 7596.6 6117.0 3460.2 3057.0 3952.8 6242.4 8311.2 8424.6 8418.0 GI2-CIS 2>NH) Inj NH3Inj



### Ib/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110. 0 110.0 110.0 110.0 110.0 110.0 110 .0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 G12-C 2>MW La

MW La
0-1 102.

92
.. 98. : 90. : 4S. : 16
.. 32. : 65. 89.1 93.1 89
.. 92.1 92
.. 92 93.1 93
. . 92. : 93. : 93.: 92. : 93
. . 92. ! 66.1 2S. ' 22
.. 36.1 71.: 101.: 102. 102.1**Pag~**

### G:; oup#-Channel# Long Descrip. Short Descrip
. Units Range 01/30/2013 14:15 01/30/2013 14:16 01/30/2013 14:17 01/30/2013 14:18 01/30/2013 14:19 01/30/2013 14:20 01/30/2013 14:21 01/30/2013 14:22 01/30/2013 14:23 01/30/2013 14:24 01/30/2013 14:25 01/30/2013 14:26 01/30/2013 14:27 01/30/2013 14:28 01/30/2013 14:29 01/30/2013 14:30 01/30/2013 14:31 01/30/2013 14:32 01/30/2013 14:33 01/30/2013 14:34 01/30/2013 14:35 01/30/2013 14:36 01/30/2013 14:37 01/30/2013 14:38 01/30/2013 14:39 01/30/2013 14:40 01/30/2013 14:41 01/30/2013 14:42 01/30/2013 14:43 01/30/2013 14:44 01/30/2013 14:45 01/30/2013 14:46 01/30/2013 14:47 01/30/2013 14:48 01/30/2013 14:49 01/30/2013 14:50 01/30/2013 14:51 01/30/2013 14:52 01/30/2013 14:53 01/30/2013 14:54
Date/Time Printed: G12-C4 G12

- Cl1 G12-C2 2>Stk NOx

Stk NOx 

### ppm 0

- 150 2>Stk 02 2>NOx Mass

2.S 2.6 2.S 2.6 2.6 2.6 2.7 2.S 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.6 2.7 2.7 2.6 2.7 2.7 2.7 Stk 02 % 0-25

12.95 12.95 12.95 12.95 12.94 12.96 12.95 12.97 12.96 12.96 12.96 12.97 12.96 12.96 12.95 12.95 12.96 12.95 12.94 12.94 12.95 12.95 12.94 12.95 12.95 12.95 12.95 

### 01/31/2013 12,03 NOx Mass 

### 1b/hr 0-100

6.20 6.19 6.19 6.19 6.18 6.18 6.16 6.17 6.17 6.17 6.17 6.17 6.17 6.18 6.18 6.18 6.18 6.18 6.19 6.19 6.18 6.18 6.19 6.17 6.19 6.19 6.18 G12-C20 2>StkFlow

StkFlow

kscfh 0

- 300000

21235 21242 21261 21234 20986 20288 20251 20273 20280 20282 20282 20258 20284 20288 20238 2026 1 20234 20205 20232 20167 20225 20210 20206 20207 20224 20197 20249 20228 20231 20237 20231 20210 20212 20218 20215 20218 20197 20261 20254 20215 G12-C3 2>Stk CO

Stk 

### co ppm 0-1000

2.0 1.9 1.9 2.0 1.9 1.9 1.8 1.8 1.6 1.6 1.7 1.7 loS 1.6 1.5 1.6 1.4 1.5 1 5 loS 1.6 1.7 1.7 1.5 1.7 1.5 1.4 G12-C13 G12 -ClO G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass 

### 1b/hr 0-100

2.66 2.65 2.65 2.65 2.65 2.65 2.64 2.64 2.64 2.64 2.64 2.64 1. 76 2.65 1. 77 2.65 1. 77 1. 77 1. 77 1. 77 2.65 2.65 2.65 1. 76 2.65 1. 77 1. 77 NOx Rate 

### Ib/mmBtu 0-1

0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXc 

### ppm 0-300

1. 86 1. 93 1. 86 1. 93 1. 93 1. 93 2.00 1. 86 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 2.00 1. 93 1. 93 2.00 2.00 1. 93 2.00 2.00 2.00 G12-C7 G12

- C8 2>Stk COc 2>Gas Flow

Stk COc Gas hscfh ppm hscfh 0-1000 0-10000

1.48 1.41 1.41 1 48 1.41 1.41 1. 34 1. 34 1.19 1.19 1. 26 1 26 1.11 1.19 1.11 1.19 1. 04 1.11 1.11 1.11 1.19 1. 26 1. 26 1.11 1. 26 1.11 1. 04 8421.0 8434.8 8431.2 8454.0 8421.0 8427.6 8433.6 8421
. 6 8445.6 8425.2 8425.2 8415.0 8425.8 8438.4 8417.4 8427.0 8415.6 8414.4 8404.2 8388.0 8391.0 8395.2 8393.4 8394.0 8390.4 8389.8 8411. 4 8413.2 8414.4 8406.6 8414.4 8416.2 8417.4 8409.0 8407.8 8419.8 8400.6 8427.0 8424.0 8407.8 G12

- C18 2>NH3 Inj NH3Inj



### 1b/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 l10.0 110.0 110.0 l10.0 110.0 110.0 110.0 110.0 110.0 110. 

## a 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 1 1 0.0 110.0 110.0 110.0 110.0 110.0 110.0 2>Summary

- I-Min RATA

- continued G12-C 2>MW 

### Lo

MW 

### Lo
0-1 102.: 102
.. 102.: 102.: 102. ! 102. ! 102. : 102. ' 102
.. 102
.. 102. : 102. 102. 103. : 102. 102
.. 102 102
.. 102.: 101. 102. : 102. ! 102. : 101. : 101
.. 102.1 102.: 102. : 102.: 102.**~** 102. 102. 102. 102
. . 102. 102.1 102. I 102
.**~** 102
.. 102. PagE

### G j:.-oup#-Channel# Long Descrip. Short Descrip
. Units Range 01/30/2013 14:55 01/30/2013 14:56 01/30/2013 14:57 01/30/2013 14:58 01/30/2013 14:59 01/30/2013 15:00 01/30/2013 15:01 01/30/2013 15:02 01/30/2013 15:03 01/30/2013 15:04 01/30/2013 15:05 01/30/2013 15:06 01/30/2013 15:07 01/30/2013 15:08 01/30/2013 15:09 01/30/2013 15:10 01/30/2013 15:11 01/30/2013 15:12 01/30/2013 15:13 01/30/2013 15:14 01/30/2013 15;15 01/30/2013 15:16 01/30/2013 15:17 01/30/2013 15:18 01/30/2013 15:19 0 1 /30/2013 15:20 01/30/2013 15:21 01/30/2013 15:22 01/30/2013 15:23 01/30/2013 15:24 01/30/2013 15:25 01/30/2013 15:26 01/30/2013 15:27 01/30/2013 15:28 01/30/2013 15:29 01/30/2013 15:30 01/30/2013 15:31 01/30/2013 15:32 01/30/2013 15:33 01/30/2013 15:34
Date/Time Printed: G12-C4 G12-Cll G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass

2.6 2.7 2.7 2.7 2.6 2.7 2.6 2.7 2.6 2.7 2.7 2.6 2.7 2.7 2.7 2.6 2.6 2.6 2.6 2.7 2.6 2.7 2.7 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.7 2.6 2.8 2.7 2.7 2.7 2.7 2.8 2.8 2.7 Stk 02 % 0-25 12.96 12.94 12.95 12.95 12.96 12.96 12.95 12.95 12.95 12.95 12.95 12.96 12.96 12.97 12.96 12. 96 12.96 12.96 12.96 12.95 12.96 12 .94 12.94 12 .9 5 12.95 12.95 12.95 12.95 12.95 12 .9 5 12 .94 12.96 12.93 12.93 12.92 12.93 12.93 12.91 12.92 12
. 92
01/31/2013 12,03 NOx Mass 

### 1b/hr 0-100 6.18 6.18 6.18 6. 1 8 6.16 6.17 6.17 6.17 6.17 6.18 6.18 6.16 6.17 6.16 6.17 6.17 6.16 6.18 6.17 6.18 6.16 6.18 6.19 6.17 6.18 6.17 6.18 6.18 6.18 6.18 6.19 6.18 7.08 6.20 6.20 6.20 6.20 7.10 7.10 6.21 G12-C20 2>StkFlow

StkFlow

kscfh 0-300000

20243 20201 20222 20203 20167 20197 20180 20186 20189 20225 20205 20174 20204 20204 20200 20220 20182 20236 20197 20203 20190 20175 20208 20172 20203 20184 20213 20231 20202 20222 20223 20239 20216 20230 20215 20220 20227 20214 20235 20225 G12-C3 2>Stk CO

Stk CO 

### ppm 0-1000

1.6 1.5 1.6 1.6 1.5 1.5 1.6 1.4 1.5 1.4 1.4 1.4 1.5 1.. 1.3 1.5 1.3 1.4 1.5 1.4 1.6 1.3 1.4 1.3 1.4 1.3 1.3 1.5 1.3 1.5 1.4 1.7 1.5 1.5 1.5 1.7 1.7 2.0 1.6 1.9 G12 -C13 G12-ClO G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass Ib/hr 0-100 2.65 1. 77 2.65 2.65 1. 76 1. 76 2.64 1. 76 1. 76 1. 77 1. 76 1. 76 1. 76 1. 76 1. 76 1. 76 1. 76 1. 77 1. 76 1. 76 2.64 1. 76 1. 77 1. 76 1. 76 1. 76 1. 77 1. 77 1. 76 1. 77 1. 77 2.65 1.77 1. 77 1. 77 2.66 2.66 2.66 2.66 2.66 NOx Rate Ib/mmBtu 0-1 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.008 0.008 0.007 Stk NOXc 

### ppm 0-300 1. 93 2.00 2.00 2.00 1. 93 2.01 1. 93 2.00 1. 93 2.00 2.00 1. 93 2.01 2.01 2.01 1. 93 1. 93 1. 93 1. 93 2.00 1. 93 2.00 2.00 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 1. 93 2.00 1. 93 2.07 2.00 2.00 2.00 2.00 2.07 2.07 2.00 G12 -C7 G12 -C8 2>Stk COc 2>Gas Flow

Stk COc Gas hscfh ppm hscfh 0-1000 0-10000

1.19 1.11 1.19 1.19 1.11 1.11 1.19 1. 0 4 1.11 l. 04 1. 04 1. 04 1.11 1. 04 0.97 1.11 0.97 l. 04 l.11 1. 04 1.19 0.96 l. 04 0.96 l. 04 0.96 0.96 1.11 0.96 1.11 1. 04 1. 26 1.11 1.11 1.11 1. 26 1. 26 1. 48 1.18 1. 40 8409.0 8412.6 8410.8 8403.0 8377.2 8389.8 8393.4 8395.8 8397.0 8412.0 8403.6 8380.2 8392.8 8382.0 8391. 0 8399.4 8383.8 8406.0 8389.8 8403.0 8386.8 8401.8 8415.6 8389.8 8403.0 8395.2 8407.2 8414.4 8402.4 8410
. 8 8421.6 8407.2 8429.4 8435.4 8439.6 8431.2 8434.2 8449.8 8448.0 8443.8 G12-C18 2>NH3 Inj NH3Inj



### 1b/hr 0-1000 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 1 10.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 2>Summary

- I-Min RATA

- Continued G12-C 2>MW Lo

MW Lo

0-1 102. 102
.. 102. ; 102
.. 102. 102
. . 102. : 102.1 102. t 102. 102. : 101. ' 102
. t 101. : 10 2. : 102
. : 102.1 102. 102. 102.: 102.1 102. ! 102. : 102
.. 102, ' 102. 102. : 102. 102
.. 102. : 102. ! 102. 103
.. 102. : 102
.. 102
.. 102. : 102. : 103
.. 103. t PagE

### G:!" oup#-Channel# Lo ng Descrip. Short Descrip. units Range 01/30/2013 15,35 01/30/2013 15:36 01/30/2013 15:37 01/30/2013 15:38 01/30/2013 15:39 01/30/2013 15:40 01/30/2013 15:41 01/30/2013 15:42 01/30/2013 15:43 01/30/2013 15:44 01/30/2013 15:45 01/30/2013 15:46 01/30/2013 15:47 01/30/2013 15:48 01/30/ 2 013 15:49 01/30/2013 15:50 01/30/2013 15:51 01/30/2013 15:52 01/30/2013 15:53 01/30/2013 15:54 01/30/2013 15:55 01/30/2013 15:56 01/30/ 2 013 15:57 01/30/2013 15:58 01/30/2013 15:59 01/30/2013 16:00 01/30/2013 16: 01 0 1/30/2013 16:02 01/30/2013 16:03 01/30/2013 16:04 01/30/2013 16:05 01/30/2013 16:06 01/30/2013 16:07 01 /30/20 13 16:08 01/30/2013 16;09 01/30/2013 16:10 01/30/2013 16:11 01/30/2013 16:12 01/30/2013 16:13 01/30/2013 16:14 

### Date/Time Printed : G12-C4 G12-C11 G12 -C20 G12-C2 2:>Stk NOx

Stk NOx 

### ppm 0-150 2:>Stk 02 2:>NOx Mass 2:>StkFlow

2.7 2 .• 2.7 2 .• 2.7 2.7 2 .• 2.7 2 .• 2 .• 2.7 2.9 2 .• 2 .• 2 .• 2 .• 2.7 2 .• 2 .• 2 .• 2.7 2 .• 2 .• 2 .• 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2 .• 2.7 2.7 2.7 2.7 2.7 2.7 Stk 02 % 0-25 12.91 12.91 12.92 12.91 12.91 12.91 12 .8 9 12
. 90 12.90 12.90 12.91 12.89 12.89 12.88 12.S9 12
. B9 12.92 12.91 12.91 12.91 12.93 12.92 12. 9 1 12.92 12.93 12.92 12.93 12.93 12.93 1 2 .94 12. 9 3 12.93 12.93 12.93 12.93 12.94 12.94 1 2 .92 12
. 93 12.93 

### 01/31/2013 12,03 NOx Mass 

### lb/hr 0-100 6.21 7.12 6.22 7 .12 6.23 6.22 7.14 6.24 7.14 7.13 6.23 7.13 7.14 7.16 7.14 7.15 6
. 22 7.11 7 .1 2 7.12 6.21 7.10 7.11 7.11 6.20 6.20 6.19 6.1S 6.20 6.18 6.20 6.19 6.21 7.09 6.19 6.18 6.20 6.21 6.20 6.20 StkFlow ksefh 0-300000

20227 20264 20254 20271 20279 20257 20281 2 0296 20305 20276 20293 20262 20274 20323 20274 2 0305 20255 20260 20287 20290 20259 20255 20257 20271 20239 20215 20197 20176 20220 20182 202 4 3 2 0212 20262 20236 20203 20202 2 0261 20239 20227 20216 G12-C3 GI2-C13 GI2-CI0 G12-C6 G12-C7 G12 -C8 G12-C18 GI2-C 2:>Stk CO 2 :>CO Mass 2:>NOx Rate 2:>Stk NOXe 2:>Stk COc 2:>Gas Flow 2:>NH3 Inj 2:>MW Lo

Stk 

## co ppm 0-1000

1.7 I.. 1.5 1 3 1.7 1.5 1.9 1.9 2.1 2.3 2.' 2.' 2.2 2.' 2.2 2.2 2.3 2.' 2.' 2.' 2.' 2.7 2 .• 2.5 2.7 2.7 2.9 2.8 2.7 2.7 2.6 2.8 2.7 2.8 2.7 2.8 2.9 2.8 2.9 2.9 CO Mass lb/hr 0 -100 2.66 2.67 1. 78 1. 78 2.67 1. 78 2.68 2.68 2.68 3.56 3.56 3.57 3.57 3.58 3.57 3.57 3.55 3.56 3.56 3.56 3.55 3.55 4.45 3.55 3.54 3.54 4.42 4.42 3.54 3.53 3.55 4.42 3.55 4.43 3.54 4.42 4.43 4.44 4.43 4.43 NOx Rate lb/mmBtu 0-1 0.007 0.008 0.007 0.008 0.007 0.007 0.008 0.007 O.OOB 0.008 0.007 0.008 O.OOS O.OOB O.OOB O
. OOB 0.007 0.008 O.OOB 0.008 0.007 0.008 0
. 008 O.OOB 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0
. 007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXc 

### ppm 0 -3 00 1. 99 2.07 2.00 2.07 1. 99 1. 99 2.06 1. 99 2.07 2.07 1. 99 2.14 2.06 2.06 2.06 2.06 2.00 2.07 2.07 2.07 2.00 2.07 2.07 2.07 2.00 2 .00 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.07 2.00 2.00 2.00 2.00 2.00 2.00 Stk COe Gas hscfh ppm hscfh 0-1000 0

- 10000

1
. 26 8455.2 1.33 8470.B 1.11 84 55.8 0.96 8473.8 1.26 8476.8 1
. 11 8467.8 1.40 8499.0 1.40 8494.8 1.55 8498.4 1.70 8486.4 1.77 8482.8 1.77 8491.2 1.62 8496.0 1.77 8527.2 1
. 62 8496.0 1
. 62 8509.2 1.70 8456.4 1.77 8469.0 1.77 8480.4 1.77 8481 .6 1.78 8447.4 2.00 8456.4 2. 07 8467.8 1
. 85 8463.0 2.00 8439.0 2.00 8439.6 2.15 8421.6 2.07 8412.6 2
. 00 8431.2 2
. 00 8404.8 1
. 9 2 B440.8 2.07 8427.6 2.00 8448.6 2.07 8437.8 2.00 8424.0 2.08 8413.2 2.15 8437.8 2.07 8449.8 2.15 8434.2 2.15 8429.4 NH3Inj Ib/hr 0-1000 110.0 110.0 110. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued MW Lo
0-1 103.1 103.: 103.· 103.· 103.: 103."**103.~** 103./ 103.·**103.~** 103.: 104.1 104.! 104.: 103.: 104.· 103.1 103.·**03.~** 1 03.: 102.: 103.· 103.' 103.1 103 103.1 102. 102.1 102.: 102.: 102.! 102.: 102. 102.'**102.~** 102.: 102.' 103.1 102. 103.! Pag(

### Gr.oup#-Channel# Long Descrip. Short Descrip . Units Range 01/30/2013 16:15 01 / 30/2013 16:16 01/30/2013 16:17 01/30/2013 16:18 01/30/2013 16:19 01/30/2013 16:20 01/30/2013 16:21 01/30/2013 16:22 01/30/2013 16:23 01/30/2013 16:24 01/30/2013 16:25 01/30/ 2013 16:26 01/30/2013 16:27 01/30/2013 16:28 01/30/2013 16:29 01/30/20 13 16:3 0 01/30/2013 16:31 01/30/2013 16:32 01/30/2013 16:33 01/30/2013 16:34 01/30/2013 16:35 01/30/2013 16:36 01/30/2013 16:37 01/30/2013 16:38 01/30/2013 16:39 01/30/2013 16:40 01/30/2013 16:41 01/30/2013 16:42 01/30/20 13 16:43 01 / 30/2013 16:44 01/30/2013 16 :45 01/30/2013 16:46 01/30/2013 16:47 01/30/2013 16:48 01/30/2013 16:49 01/30/2013 16:50 01/30/2013 16:51 01/30/2013 16:52 01/30/2013 16:53 01/30/2013 16:54 

### Date/Time Printed: G12

- C4 G12-C11 G12-C20 G12

- C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2 >NOx Mass 2>StkFlow

2.7 2.7 2.B 2.6 2.7 2 .B 2.7 2.B 2.7 2.7 2 .7 2.7 2.7 2.7 2.7 2.B 2.7 2.6 2.6 2.6 2.7 2.7 2.7 2.7 2.7 2.7 2.B 2.7 2.B 2.B 2.B 2.7 2.B 2.7 2.7 2.7 2.6 2.6 2.7 2
. 6 Stk 02 

# • 0-25 12.91 12.92 12.91 12.94 12.94 12.93 12.93 12 .93 12 .94 12.94 12.93 12.93 12.93 12.93 12.92 12.91 12.93 12.93 12.93 12.94 12.94 12.93 12.94 12.94 12. 93 12.92 12.91 12.91 12.91 12.90 12.90 12.91 12.90 12.92 12.93 12.93 12. 9 5 12.94 12 .94 12.96
01/31/2013 12,03 NOx Mass 

### Ib/hr 0-100 6.21 6.21 7.11 6.18 6.18 7.09 6.20 7.09 6.19 6.19 6.20 6.21 6.19 6.20 6.21 7.10 6.20 6.20 6.20 6
. 19 6.20 6.21 6.19 6.21 6.20 6.23 7.11 6.23 7.13 7.14 7.13 6.22 7.12 6.23 6.22 6.22 6.20 6.21 6.21 6.19 StkFlow 

### kscfh 0

- 300000

20205 20239 20243 20182 20191 20252 20219 20233 20210 20237 20240 20252 20206 20243 20249 20221 20226 20213 20216 20218 20248 20260 20224 20277 20236 20291 20260 20293 20310 20305 20272 20251 20243 20303 20301 20308 20287 20276 20277 20260 G12 -C3 G12 -C13 G12-C10 G12

- C6 G12-C7 G12-C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 2>NH3 Inj 2>MW Lo

Stk CO 

### ppm 0-1000

2.B 2.9 2.B 2.9 3.0 3.0 3.0 2.9 2.9 2.9 3.0 3.1 3.1 3 .1 3.2 3.1 3.2 3.3 3.3 3.2 3.4 3.2 3.1 3.2 3.2 3.2 3.1 3.2 3.1 3.3 2.9 3
. 1 3.0 3.1 3.1 3.2 3.3 3.3 3.1 3.4 CO Mass 

### lb/hr 0-100 4.43 4.44 4.44 4.41 4.41 4.43 4.43 4.43 4.42 4.42 4.43 4.43 4.42 4.43 4.44 4.44 4.43 4.43 4.43 4.42 5.31 4.44 4.42 4.43 4.43 4.45 4.45 4.45 4.46 4.46 4.45 4.44 4.45 4.45 4.44 4.45 4.43 4.43 4.43 5.30 NOx Rate 

### Ib/mmBtu 0-1 0.007 0.007 0.008 0.007 0.007 0.008 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.008 0.008 0.008 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXc 

### ppm 0-300 1. 99 2.00 2.07 1. 93 2.00 2.07 2.00 2.07 2.00 2.00 2.00 2.00 2.00 2.00 2.00 2.07 2.00 1. 92 1. 92 1. 93 2.00 2.00 2.00 2.00 2.00 2.00 2.07 1. 99 2.07 2.07 2.07 1. 99 2.07 2.00 2.00 2.00 1. 93 1. 93 2.00 1. 93 Stk COc Gas 

### hscfh ppm hscfh 0-1000 0-10000 2.07 2.14 2.07 2
. 15 2 .2 2 2.22 2
. 22 2.15 2.15 2.15 2.22 2.29 2.29 2.29 2.37 2.29 2.37 2.44 2.44 2.37 2
. 52 2.37 2.30 2.37 2.37 2.37 2.29 2.36 2.29 2.43 2.14 2.29 2.21 2.29 2.29 2.37 2.45 2.45 2.30 2.53 8446.2 8449.8 8461.8 8404.8 8408.4 8444.4 8430.6 8436 .6 8416.2 8427.6 8439.6 8444.4 8425.2 8440.8 8454.0 8452.8 8433.6 8428.2 8429.4 8419.8 8432.4 8448.0 8422.2 8444.4 8437.8 8471. 4 8469.0 8482.8 8490.0 8498.4 8484.6 8465.4 8472.6 8476.2 8464.8 8467.8 8437.8 8443.8 8444.4 8416.2 NH3Inj 

### Ib /hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110 .0 110.0 110 .0 110.0 110.0 11 0.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110 .0 110 .0 110.0 110.0 110.0 110.0 110.0 110.0 llO. 

### a 110.0 

### 2>Summary

- I-Min RATA

- Continued MW Lo
0-1 102. ; 103.1 103.1 101
.. 102. 103.1 102
. . 102
.. 102. ! 102.: 103.· 102.' 102. · 103.: 102.' 102. ; 102. ! 102
. . 102. : 102
.. 102. 102 102
. . 102
.. 102. 103 103. : 103. I 103. 103
.. 103. r 103. I 103. I 103. I 102
.. 102. ' 102.: 102.' 102.' 102.1 

### PagEGr oupfr-Channel# Long Descrip
. Short Descrip
. Units Range 01/30/2013 16:55 01/30/2013 16:56 01/30/2013 16:57 01/30/ 2 013 16:58 01/30/ 2013 16:59 01/30/2013 17:00 01/30/2013 17:01 01/30/2013 17:02 0 1/30/2013 17:03 01/30/2013 17:04 01/30/ 2013 17:05 01/30/ 2013 17:06 01/30/2013 17:07 01/30/2013 17:08 01/30/20 1 3 17:09 01/30/2013 17:10 01/30/2013 17:11 01/30/2013 17:12 01/30/ 2013 17:13 01/30/2013 17:14 01/30/2013 17 :1 5 01/30/2013 17:16 01/30/2013 17:17 01/30/2013 17:18 01/30/2013 17:19 01/30/ 2013 17:20 01/30/2013 17:21 01/30/2013 17:22 0 1 /30/2013 17:23 01/30/2013 17:24 01/30/2013 17:25 01/30/2013 17:26 01/30/2013 17:27 01/30/ 2 013 17:28 01/30/2013 17:29 01/30/2013 17:30 01/30/2013 17:31 01/30/2013 17:32 01/30/2013 17:33 01/30/2013 17:34 

### Date/Time Printed: G12-C4 G12 -C11 G12-C20 G12-C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass 2>StkFlow

2.7 2.6 2.7 2.6 2.6 2.6 2.7 2.7 2.7 2.7 2
. 6 2.7 2.7 2.B 2.7 2.7 2.6 2.7 2.6 2.7 2.7 2.7 2.7 2.7 2.7 2
. 7 2.7 2.7 2.6 2.7 2.7 2.6 2.7 2.7 2.6 2.7 2.7 2.B 2.7 2.7 Stk 02 

# • 0-25 12.95 12.97 12.96 12
. 97 12.96 12.95 12.94 12.93 12.93 12.93 1 2.93 12.9 2 12 .9 3 12.92 1 2.93 12.91 12.92 1 2 .9 2 12.93 12.93 12.93 12 .92 12.92 12.92 12.93 12.93 12.91 12.93 12.92 12.94 12. 93 12.93 12.93 12
. 93 12 .93 12.92 12,

- 91 12.91 12.91 12.92
01/31/2013 12,03 NOx Mass 

### Ib/hr 0 -100 6.18 6.16 6.16 6.16 6.16 6.18 6.20 6.21 6 .21 6.21 6.23 6.24 6.23 7.13 6.23 6.25 6.25 6.24 6.24 6.22 6.23 6.24 6.23 6.25 6.23 6.24 6.25 6.25 6.24 6.23 6.23 6.23 6.23 6.23 6.24 6.25 6.25 7.16 6.24 6.24 StkFlow kscfh 0 -30 0000

20215 20189 2017 4 20195 20184 20208 20238 20255 20255 20255 20321 20323 20334 20321 20340 20342 20353 20343 20345 20291 20322 20340 20316 20362 20325 20377 20336 20383 20347 20351 20318 20325 20322 20314 20358 20367 20339 20378 20317 20340 G12-C3 G12

- C13 G12 -CI0 G12 -C 6 G12-C7 G12-C8 G12-C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 2>NH3 Inj 2>MW Lo

stk CO ppm 0-1000

3.4 3.4 3.9 3.7 3.6 3 .7 3.6 3.3 3.3 3.3 3.5 3 .4 3.6 3.3 3.6 3.5 3.6 3.6 3.6 3.B 3.9 3.7 3.B 3.B 3.6 3.B 3.6 3.B 3.6 3.7 3.7 3.6 3
. 7 3.6 4.0 3.B 3.B 3 .4 3 .B 3.6 CO Mass 

### Ib/hr 0-100 5.30 5.28 5.28 5.28 5.28 5.30 5
. 31 4.43 4.43 4.43 5.34 5.35 5.34 4 .45 5.34 5.36 5.35 5.35 5.34 5.33 5.34 5 .3 5 5.34 5.36 5.34 5 .3 5 5.36 5.35 5.35 5.34 5.34 5.34 5.34 5.34 6.24 5.36 5.36 5.37 5.35 5.35 NOx Rate lb/mmBtu 0-1 0.007 0.007 0.007 0.007 0.007 0.007 0 .0 07 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 Stk NOXc ppm 0-300 2.00 1. 93 2.01 1. 93 1. 93 1. 93 2.00 2.00 2.00 2.00 1. 92 2.00 2.00 2.07 2.00 1. 99 1. 92 2.00 1. 92 2.00 2.00 2.00 2.00 2.00 2.00 2.00 1. 99 2.00 1. 92 2.00 2.00 1. 92 2.00 2.00 1. 92 2.00 1. 99 2.07 1. 99 2.00 Stk COc Gas hscfh hscfh 0-10000 ppm 0-1000 2.52 2.53 2.90 2. 75 2.68 2.75 2.67 2
. 44 2.44 2.44 2. 59 2 .51 2.66 2.44 2.66 2.58 2.66 2.66 2.66 2.81 2.89 2.74 2.81 2.8 1 2.66 2.81 2.66 2 .81 2.66 2.74 2.74 2.66 2. 74 2.66 2.96 2.81 2.81 2.51 2.81 2.66 8407.8 8376.0 8380.2 8378.4 8384.4 8404.8 8428.2 8445.6 8445.6 8445.6 8473.2 8484.6 8478.6 8484.0 8481
. 0 8503.2 8497.2 8493.0 8483.4 8460
. 6 8473.8 8491.8 8481. 6 8500.8 8475.0 8496.6 8500.8 8499.0 8494.8 8475.0 8472.0 8475.0 8473.8 8470.2 8488.8 8503.2 8502.0 8518
. 2 8493.0 8491. 8 NH31I1j 

### Ib/hr 0-1000 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 l10.0 110.0 110 .0 110.0 110.0 l10. 0 110.0 110.0 110.0 110.0 110
. 0 110
. 0 110.0 110 .0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110 .0 110.0 

### 2>Summary

- 1-Min RATA

- Continued MW La
0-1 102. : 101. ! 101.! 101. : 102. t 102. : 102
. . 103.1 103
. t 103.1 103. t 103.! 103. : 104.1 102. 103. : 103. ! 103. ' 103
. : 102 103. : 103. t 10 3. t 103 103. ! 103.: 103. ! 103. : 103.! 103.1 102. : 102. : 103. t 103.: 103. 103.! 10 3 .' 103.: 103.· 103.: PagE

### G:::-oupfr

- Channel# Long Descrip
. Short Descrip
. units Range 01/30/2013 17:35 01/30/2013 17:36 01/30/2013 17:37 01/30/2013 17:38 01/30/2013 17:39 01/30/2013 17:40 01/30/2013 17: 41 01/30/2013 17:42 01/30/2013 17:43 01/30/2013 17:44 01/30/2013 17:45 01/30/2013 17:46 01/30/2013 17:47 01/30/2013 17:48 01/30/2013 17;49 01/30/2013 17:50 01/30/2013 17:51 

### Period Average Period Max Value Period Min Value Period Totals = 

### Period 

### % Recovery

Date/Time Printed: G12-C4 G12 -C11 G12-C20 G12-C3 G12 -CD GI2-CI0 G12 -C6 G12-C7 G12-C8 G12-C18 G12-C G12-C2 2>Stk NOx

Stk NOx 2>stk 02 2>NOx Mass 2>StkFlow 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 2>NH3 Inj 2>MW Lo


### ppm 0-150 2.8 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2.8 2.7 2.7 2.6 2.6 2.6 2.7 2.6 Stk 02 

# • 0-25 12.91 12.93 12.93 1 2.92 12.92 12
. 92 12.91 1 2.91 12.92 12.92 12 .91 12. 91 12.93 12.93 12.9 4 12. 94 12.96 NOx Mass 

### 1b/hr 0- 1 00 7.15 6.24 6.25 6.26 6.26 6.27 6.28 6.27 6.26 7.15 6.27 6.25 6.24 6.23 6.23 6.23 6.20 StkFlow kscfh 0-300000

20356 20361 20393 20400 20405 20428 20429 20424 20409 20379 20401 20339 20367 20317 20342 20346 20323 Stk CO 

### ppm 0-1000

3.7 3.7 3
. 9 3.7 3
. 7 3.8 3.6 4.0 3.7 4. 0 3.8 3.8 3.7 3.9 3.9 3.8 4.0 2.7 12.93 6.36 20054 2.6 2.9 12.97 7.16 21261 4.0 2.5 12.88 6.16 9923 1.3 5.5080E+2 2.6511E+3 1.3028E+3 4.9533E+6 5.3740E+2 83.3 83 .3 83.3 100.0 83.3

01/31/2013 12,03 CO Mas s lb/hr 0-100 5.36 5.35 5.36 5.37 5.37 5.37 5.38 6.27 5.37 6.25 5.37 5.36 5.35 5.34 5.34 5.34 6.20 NOx Rate lb/mmBtu 0

- 1 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.007 0.007 0.007 0.007 0.007 Stk NOXc 

### ppm 0

- 300 2.07 2.00 2.00 2.00 2.00 2.00 1. 99 1. 99 2.00 2.07 1. 99 1. 99 1. 92 1.92 1. 93 2.00 1. 93 3.77 0.007 1.99 6.27 0.008 2.14 1.76 0.007 1 .8 6 7.7227E+2 1.4689E+O 4.0786E+2 83.3 83.3 83.3 Stk COc Gas hscfh 

### ppm 0-1000 2.73 2.74 2.89 2. 74 2.74 2.81 2.66 2.95 2.74 2.96 2 .81 2.81 2.74 2.89 2.89 2.82 2.97 hscfh 0-10000 8509.2 8490.0 8503.2 8517.0 8518.8 8528.4 8539.8 85 37 .4 8520.6 8508.0 8527.8 8502.0 8492.4 8471.4 8471. 4 8473.2 8442.0 NH3Inj lb/hr 0

- 1000 l10.0 110.0 110.0 110.0 110.0 110.0 110
. 0 l10.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 MW 

### Lo
0-1 103.: 103. 104
. 1 103.' 104.1 104.: 10 4 .: 10 3. ' 10 4. 1 103 103.' 103.' 103.' 103.' 102.' 103.1 102.: 1
. 9 4 8239.1 110.0 99.8 2 .97 8539.8 110.0 104. 0.96 2611.2 110.0 16. 3.9779E+2 2.0350E+6 2.7170E+4 2.4671E+ 83.3 100.0 100.0 100
.



### 2>Summary

- I-Min RATA

- Continued PagE

# Data Summary Repor t Company : CPV Sentinel, LLC 62575 Powerline Road 

### Desert Hot Springs, CA 92240

# c~**~(()'** 

# \J ;',f-1..



# _ TRACE

- Source : Turbine 2 D

ata Group : 2>1-Min Cales

# ~ 

# .,**5-L/~(L-** fM- 

# toO-3 Ellvi ro nm e nlal S y s l e m s, Ill c.
Report Name : 

### Start of Report : 2>Summary

- I-Min RATA 

### 01/31/2013 OS,33 G12-C4 

### End of Report, 01/31/2013 12,39
GI2-Cll G12-C20 G12-C3 G12-C13 

### validation: All Available Data GI2-Cla G12-C6 G12-C7 G12-Ca GIZ-C18 G12-C 

### Group#-Channel# Long De sc rip. 

### Short Descrip. Units G12-C2 2>Stk NOx

Stk NOx 

### ppm 0

- 150 2>Stk 02 2>NOx Mass 2>StkFlow 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXc 2>Stk COc 2>Gas Flow 2>NH3 Inj 2>MW La


### Range 01/31/2013 08:33 01/31/2013 08:34 01/31/ 2 013 08:35 01/3 1 /2013 08:36 01/31/2013 08:37 01/31/2013 08:38 01/31/2013 08:39 01/31/2013 08:40 01/31/2013 08:41 01/31/2013 08:42 01/31/2013 08:43 01/31/2013 08:44 01/31/2013 08:45 01/31/2013 08:46 01/31/2013 08:47 01/31/2013 08:48 01/31/2013 08:49 01/31/2013 08:50 01/31/2013 08:51 01/31/2013 08:52 01/31/2013 08:53 01/31/2013 08:54 01/31/2013 08:55 01/31/2013 08:56 01/31/2013 08:57 01/31/2013 08:58 01/31/2013 08:59 01/31/2013 09:00 01/31/2013 09:01 01/31/2013 09:02


### Date/Time Printed: 2.8 2.7 2 .8 2.8 2.8 2.8 2.7 2.7 2.7 2.7 2.8 2.7 2. 8 2.7 2.7 2.8 2.7 2.8 2.7 2.7 2.7 2.8 2
. 8 2.8 2.7 2.6 2.7 2.8 2.7 2.7 Stk 02 

# • 0-25 13.20 13.21 13. 2 0 13.20 13.21 13 .20 13 .20 13
. 19 13 .19 13 .20 13 .19 13.19 13 .19 13.20 13 .20 13.20 13.21 13
. 1 9 13 .1B 13 .18 13 .19 13 .19 13 .18 13 .1 8 13 .18 13 .19 13.20 13 .19 13
. 19 13
. 20


### 01/31/2013 13,29 NOx Mass Ib/hr 0-100 6.96 6.93 6.95 6.94 6.95 6.96 6.95 6.96 6.95 6.94 6.96 6.96 6.95 6
. 95 6.9 4 6.94 6.96 6.97 6.99 6.99 6.97 6.98 6.97 6.97 6.96 6.06 6.93 6.94 6.96 6.94 

### StkFlow kscfh 0-300000

20554 20499 20526 20518 20566 20554 20546 20535 20499 20517 20532 20527 20503 20546 20524 20517 20584 20578 20612 20600 20575 20606 20551 20548 20501 20445 20485 20491 20530 20509 Stk CO 

### ppm 0-1000

3.2 2.9 2.6 2.7 2.9 2.9 2.9 2.6 2.7 2.7 2.S 2.8 2.6 2.4 2.7 2.3 2.8 2.5 2.3 2.4 2.6 2.5 2.4 2.4 2.5 2.S 2.6 2.7 2.7 2.7 CO M ass 

### 1b/hr 0

- 100 4.35 4.33 3.47 4.34 4.34 4.35 4.35 3.48 4.34 4.34 3.48 4.35 3.47 3.48 4.34 3.47 4.35 3.49 3.50 3.49 3.49 3
. 49 3.49 3.49 3.48 3.46 3.47 4.34 4.35 4.34 NOx Rate 

### Ib/mmStu 0-1 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 O.OOB 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0
. 008 0
. 008 0.008 0.007 0.008 O.OOB 0.008 0.008 Stk NOXc 

### ppm 0-300 2.15 2.07 2.15 2.15 2.15 2.15 2.07 2
. 07 2.07 2.07 2.14 2.07 2.14 2.07 2.07 2.1S 2.07 2.14 2
. 06 2.06 2.07 2.14 2.14 2.14 2.06 1. 99 2.07 2
. 14 2.07 2.07 stk CDc Gas 

### ppm 0-1000 2.45 2.22 1. 99 2.07 2.22 2.22 2.22 1. 99 2.07 2.07 1. 91 2.14 1. 99 1. 84 2.07 1. 76 2.15 1. 91 1. 76 1. 83 1. 99 1. 91 1. 83 1. 83 1. 91 1. 91 1. 99 2.07 2
. 0 7 2
. 07 

### hscfh hscfh 0-10000 8280.0 8247.0 8268 .6 8265
. 6 8274.0 8280.0 8277.0 8283.0 8268.6 8265.0 8281. 8 8280.0 8270.4 8277
. 0 8268
. 0 8265.0 8281. 2 8300.4 8325.0 8320
. 2 8299.2 8311.8 8300.4 8299
. 2 8280.0 8247.0 8252.4 8265
. 6 8281 .2 8262.0 NH3Inj 

### Ib/hr 0-1000 110.0 110.0 110
. 0 110.0 110.0 110.0 110
. 0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 MW La
0-1 100.1

99. 99. 99
.. 99. : 99. 100
.. 100.

99
. . 99
.. 100
.. 100
..

99
.. 100
..

99
.. 100.1 100. ! 100 100
.. 100
.. 100.: 100
.. 100
. . 100. ! 100
..

99
.. 99. 100.1

99. 99
. . 

### pagE

### Group#-Chann e l# Long Descrip
. Short De s c r ip
. U

nits Range 01/31/2013 09:03 01/31/2013 09:04 01/31/2013 09:05 01/31/2013 09:06 01/31/2013 09:07 01/31/2013 09:08 01/31/2013 09:09 01/31/2013 09:10 01/31/2013 09:11 01/31/2013 09:12 01/31/2013 09:13 01/31/2013 09:14 01/31/2013 09:15 01/31/2013 09:16 01/31/2013 09:17 01/31/2013 09:18 01/31/2013 09:19 01/31/2013 09:20 01/31/2013 09:21 01/31/2013 09:22 01/31/2013 09:23 01/31/2013 09:24 01/31/2013 09:25 01/31/2013 09:26 01/31/2013 09:27 01/31/2013 09:28 01/31/2013 09:29 01/31/2013 09:30 01/31/2013 09:31 01/31/2013 09:32 01/31/2013 09:33 01/31/2013 09:34 01/31/2013 09:35 01/31/2013 09:36 01/31/2013 09:37 01/31/2013 09:38 01/31/2013 09:39 01/31/2013 09:40 01/31/2013 09:41 01/31/2013 09:42 

### Date/Time Printed: G12 -C4 GI2

- Cll G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>stk 02 2>NOx Mass

2.7 2.8 2.8 2.7 2.6 2.7 2.7 2.7 2.7 2.8 2.7 2.7 2.8 2.7 2.7 2.8 2.9 2.7 2.8 2.8 2.8 2.7 2.8 2.7 2.8 2.8 2
. 7 2.7 2.8 2.7 2.7 2.7 2.7 2.8 2.6 2.8 2.7 2.6 2.7 2.7 Stk 02 

# • 0-25 13.20 13 .18 13 .18 13 .18 13.18 13 .19 13 .19 13.18 13 .17 13 .17 13 .18 13 .18 13 .17 13 .1B 13
. 1B 13 .18 13 .14 13 .13 13 .14 13 .14 13 .15 13 .15 13 .16 13 .17 13 .16 13 .17 13 .17 13 .17 13 .17 13 .19 13 .2 0 13.21 13.21 13 .19 13 .19 13 .19 13 .19 13.1B 13
. 19 13 .1B 

### 01/31/2013 13,29 NOx Mass 

### 1b/hr 0-100 6.95 7.00 7.00 7.00 6.11 6.9B 6.9B 6.98 6.99 6.98 6.97 6.97 6.97 6.97 6.97 6.96 7.06 7.06 7.05 7.05 7.02 7.01 7.00 7.00 6.98 6.98 6.97 6.96 6.96 6.95 6.93 6.92 6.91 6.95 6.07 6.95 6.95 6.08 6.94 6.94 G12-C20 2>StkFlow

StkFlow

kscfh 0-300000

20530 20619 20631 20642 20597 20600 20608 20582 20573 20533 20554 20542 20516 20530 20542 20523 20716 20662 20686 20662 20621 20572 20585 20603 20525 20557 20516 20483 20490 20509 20481 20479 20457 20505 20484 20520 20506 20492 20489 20453 G12-C3 2>Stk CO

Stk CO 

### ppm 0

- 1000

2.8 2.S 2.6 2.S 2.6 2.7 2.E:! 2.7 2.7 2.7 2.9 3.0 2.7 2.9 3.0 2.8 2.9 2.7 2.6 2.7 2.S 2.9 3.2 3.3 3.4 3.S 3.S 3.6 3.3 3.6 3.9 3.9 3.8 3.S 3.7 3.8 3.8 3
. 7 3.8 3.8 G12

- C13 G12-C10 G12

- C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass lb/hr 0-100 4.34 3.50 3.50 3.50 3.49 4.36 3.49 4
. 36 4.37 4.36 4.36 4.36 4.36 4.35 4.36 4.35 4.42 4.41 3.53 4.40 3.51 4.38 4.38 5.25 5.24 5.24 5.23 5.22 5.22 5.21 6.06 6.06 6.05 5.21 5.21 6.08 6.08 5.21 6.07 6.07 NOx Rate Ib/mmBtu 0-1 0.008 0.008 0.008 0.008 0.007 0.008 0
. 008 0
. 008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 O.OOB 0.008 0.008 0.008 0.008 0.008 0.008 0.008 O.OOB 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.008 0.007 0.008 0.008 Stk NOXc 

### ppm 0

- 300 2.07 2.14 2
. 14 2.06 1 : 99 2.07 2.07 2.06 2.06 2.14 2.06 2.06 2.14 2.06 2.06 2.14 2.20 2.05 2.13 2.13 2.13 2.06 2.13 2.06 2.13 2.14 2.06 2.06 2.14 2.07 2.07 2.07 2.07 2.14 1. 99 2.14 2.07 1. 99 2.07 2.06 G12-C7 G12-C8 2>Stk COe 2>Gas Flow

Stk COe Gas hsefh ppm hsefh 0-1000 0

- 10000 2.15 1. 91 1. 99 1. 91 1. 99 2.07 1. 99 2.06 2.06 2.06 2.22 2.29 2.06 2.22 2
. 29 2.14 2.20 2.05 1. 98 2.05 1. 90 2.21 2. 4 4 2.52 2.59 2.67 2.67 2.75 2.52 2.75 2.99 2.99 2.92 2.68 2.83 2.91 2.91 2.83 2.91 2.90 8270.4 8328.0 8332.8 8337.0 8319.0 8309.4 8312.4 8313.0 8320.2 8304.0 8301.6 8296.8 8296.8 8292.0 8296.8 8289.0 8410.2 8399.4 8398.2 8388.6 8361.0 8341.2 8335.8 8332.2 8311.2 8313.6 8296.8 8283.6 8286.6 8272.8 8250.6 8239.2 8230.2 8271.0 8262.6 8277.0 8271.6 8276.4 8264.4 8260.8 G12-C18 2>NH3 Inj NH3Inj



### 1b/hr 0-1000 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 1l0.0 1l0. 

## a 110.0 110.0 110.0 110.0 110.0 110.0 1l0.0 

### 2>Summary

- I-Min RATA

- Continued G12-C 2>MW Lo

MW Lo
0-1 99
.. 100. 100
. . 101.1 100. :

99. : 100
. 100
.. 100. 100. : 100
. .

99. ; 100. t

99. : 100. : 100.: 101.
. 101
.. 101. 101. 101 100. : 100. 101
.. 100. : 100
..

99. : 100 .: 100
..

99
.. 99. 99. 99.1 99.: 99. ! 100. t

99. : 99.! 99
.. 99. ! Pag(

### Group#-Chann e l # Long Descrip . Short Descrip . Units R

ange 01/31/2013 09:43 01/31/2013 09:44 01/31/2013 09:45 01/31/2013 09:46 01/31/2013 09:47 01/31/2013 09:48 01/31/2013 09:49 01/31/2013 09:50 01/31/2013 09:51 01/31/2013 09:52 01/31/2013 09:53 01/31/2013 09:54 01/31/2013 09:55 01/31/2013 09:56 01/31/2013 09:57 01 / 31/2013 09:58 01/31/2013 09:59 01/31/2013 10:00 01/31/2013 10:01 01/31/2013 10:02 01/31/2013 10:03 01/31/2013 10:04 01/31/2013 10:05 01/31/2013 10:06 01/31/2013 10:07 01/31/2013 10:08 01/31/2013 10:09 01/31/2013 10:10 01/31/2013 10:11 01/31/2013 10:12 01/31/2013 10:13 01/31/2013 10:14 01/31/2013 10:15 01/31/2013 10:16 01/31/2013 10:17 01 / 31/2013 10:18 01/31/2013 10:19 01/31/2013 10:20 01/31/2013 10:21 01/31/2013 10:22 

### Date/Time Printed: G12-C4 G12-Cl1 G12

- C20 G12-C2 2>Stk NOx

Stk NOx 2>Stk 02 2 >NOx Mass 2 > StkFlow
ppm 0-150 2.9 2.7 2.7 2.7 2.8 2.7 2.7 2.6 2.7 2.7 2.8 2.8 2.7 2.7 2.7 2.7 2.8 2.7 2.8 2.7 2.7 2.7 2.7 2.7 2.7 2.8 2.8 2.8 2.7 2.8 2.7 2.6 2.7 2.7 2.7 2.7 2.7 2.7 2.6 2.7 stk 02 

# • 0-25 13 .17 13 .17 13 .18 13 .19 13 .19 13 .19 13 .19 13 .19 13 .18 13 .19 13 .19 13 .19 13 .18 13 .19 13 .17 13 .18 13 .18 13 . 17 13 .17 13 .17 13 .17 13 .16 13 .16 13 .16 13 .17 13 .16 13.15 13 .15 13 .14 13 .15 13 .16 13 .16 13 .16 13
. 17 13 .16 13.17 13.16 13.17 13 .16 13 .17
01/31/2013 13,29 NOx Mass Ib/hr 0

- 100 6.96 6.95 6.94 6.93 6.94 6
. 93 6.93 6.07 6.95 6
. 92 6.95 6.94 6.93 6.93 6.95 6
. 95 6.96 6.98 6.99 6.98 7.00 6.99 7.01 7.00 6.98 6.99 6.99 7.01 7.00 7.00 6.99 6.11 6.98 6.97 6.98 6.96 6.97 6.96 6.07 6.92 StkFlow ksefh 0 -30 0000

20489 20450 20449 20447 20483 20463 20463 20465 20486 20432 20503 20496 20438 20445 20458 20487 20518 20532 20578 20548 20594 20548 20608 20565 20556 20554 20535 20575 20538 20557 20545 20538 20510 20510 20508 20502 20488 20486 20397 20384 G12-C3 GI2-C13 G12

- CI0 G12-C6 G12-C7 G12-C8 G12

- C18 G12-C 2>Stk CO 2>CO Mass 2>NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2 >NH3 Inj 2 > MW La stk 

### co ppm 0

- 1000

3.8 3
. 8 3
. 8 3.9 3.7 3.8 4.0 4.0 3.9 3.8 4
. 0 4.0 3.9 3.9 3.7 3.7 3.7 3.7 3.4 3.2 3.6 3.6 3.6 3.7 3.5 3.4 3.5 3.4 3.5 3.5 3.4 3.6 3.6 3.6 3.6 3.6 3.3 3.1 2.8 2.4 CO Mass 

### Ib/hr 0- 100 6.09 6.08 6.07 6.06 5.21 6.07 6.07 6.07 6.08 6
. 06 6.08 6.08 6.07 6
. 06 5.21 5.21 5.22 5.23 5.24 4
. 36 5.25 5.24 5.26 5.25 5.24 5.24 5.25 5.26 5.2S 5.25 5.24 5.24 5.23 5.23 5.23 5.22 5.23 4.35 4.34 3.46 NOx Rate lb/mmBtu 0-1 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 Stk NO Xe ppm 0-300 2.21 2.06 2.06 2.07 2.14 2.07 2.07 1. 99 2.06 2.07 2.14 2.14 2.06 2.07 2.06 2.06 2.14 2.06 2
. 14 2.06 2.06 2.06 2.06 2.06 2.06 2.13 2.13 2.13 2.05 2.13 2.06 1. 98 2.06 2.06 2.06 2.06 2.06 2.06 1. 98 2.06 Stk COe Gas hsefh hsefh 0

- 10000 ppm 0-1000 2.90 2.90 2.90 2.98 2.83 2.91 3.06 3.06 2.98 2.91 3.06 3.06 2
. 98 2
. 98 2.82 2.83 2.83 2.82 2.60 2.44 2.75 2.74 2
. 74 2.82 2.67 2.59 2.66 2
. 59 2.66 2
. 66 2.59 2.74 2.74 2.75 2.74 2.75 2.52 2.37 2.13 1. 83 8286.0 8270.4 8259.0 8247.6 8262.0 8254.2 8254.2 8254.8 8274.0 8241.6 8270.4 8267
. 4 8254.8 8247.0 8273.4 8274.6 8287
. 2 8303
. 4 8322.0 8310.0 8328.6 8320.8 8344.8 8327.4 8313.0 8323.2 8326.2 8342.4 8338.2 8335.2 8319.6 8316.6 8305.2 8294.4 8304.6 8291.4 8296.2 8284
. 8 8259.6 8243
. 4 NH3Inj Ib/hr 0-1000 110.0 110.0 110.0 110.0 110.0 1 10.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 l10.0 110.0 l10.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Cont i nued MW Lo
0

- 1 99. , 99. : 100.1

99. 100.1

99.1 99. ! 99. 99
.. 99. : 99. : 99
. . 99.: 99
.**~** 99
.. 99
. . 100
. : 100. : 101.: 100.**~** 100. : 100. : 100
. : 101.: 100. : 100. : 100. ! 100. : 100.: 101.1 100
. . 100.**~** 100. :

99. 100. : 100
.**~** 100
. . 100. : 100.1 100 . : pagE

### Group#-Channel# Long Descrip. Short Descrip
. Units Range 01/31/2013 10:23 01/31/2013 10:24 01/31/2013 10:25 01/31/2013 10:26 01/31/2013 10:27 01/31/2013 10:28 01/31/2013 10:29 01/31/ 2 013 10:30 01/31/2013 10:31 01/31/2013 10:32 01/31/2013 10:33 01/31/2013 10:34 01/31/2013 10:35 01/31/2013 10:36 01/3 1 /2013 10:37 01/31/2013 10:38 01/31/2013 10:39 01/31/2013 10:40 01/31/2013 10:41 01/3 1 /2013 10:42 01/31/2013 10:43 01/31/2013 10:44 01/31/2013 10:45 01/31/2013 10: 46 01/31/2013 10:47 01/31/2013 10: 48 01/31/2013 10:49 01/31/2013 10:50 01/31/2013 10:51 01/31/2013 10:52 01/31/2013 10:53 01/3 1 /2013 10:54 01/31/2013 10:55 01/31/2013 10:56 01/31/2013 10:57 01/31/2013 10:58 01/31/2013 10:59 01/31/2013 11:00 01/31/2013 11:01 01/31/2013 11:02 

### Date/Time Printed: G12-C4 G12 -C1 1 G12 -C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx M ass

2.7 2.7 2.7 2.7 2 .• 2.7 2.7 2.6 2.7 2.6 2.6 2.6 2.7 2.6 2.6 2.7 2.6 2.7 2.7 2.6 2.7 2.6 2.6 2.7 2.6 2.6 2.6 2.6 2.7 2.6 2.6 2.7 2.7 2.7 2.7 2.6 2.7 2.7 2.6 2.6 Stk 02 

# • 0-25 13 .17 13 .16 13 .17 13 .17 13 .17 13 .18 13 .17 13
. 18 13 .18 13 .19 13 .17 13 .18 13 .18 13
. 18 13 . 1 8 13 .18 13.17 13 .18 13 .17 13 .18 13.19 13 .19 13 .18 13
. 18 13 .18 13 .18 13 .19 13 .18 13 .1 7 13 .1 7 13 .17 13 .17 13 .1 7 13 .18 13 .17 13 .19 13 .18 13 .16 13.18 13
. 19
01/31/2013 13,29 NOx Mass 

### lb/hr 0

- 100 6.91 6.92 6.91 6.92 6.93 6.92 6 .9 4 6.04 6.93 6.05 6.06 6.04 6.91 6.04 6.03 6.90 6.05 6.91 6.91 6
. 03 6.88 6.03 6.04 6.90 6.03 6.03 6.03 6.05 6.92 6.06 6.05 6.92 6.91 6.91 6.92 6.02 6.91 6.91 6.03 6.01 G12-C20 2>StkFlow

StkF low

kscfh 0

- 300000

20352 20337 20351 20363 20407 20 404 20436 20361 20419 20393 20381 20354 20361 20359 20297 20349 20345 20357 20341 20327 20309 20350 20351 20348 20306 20309 20332 20365 20382 20373 20358 20372 20348 20355 20360 20309 20362 20317 20313 20279 G12-C3 2>Stk CO

Stk 

### co ppm 0-1000

2.3 2.1 2.1 2.0 1.9 1.6 1.6 1.5 1.. 1.5 1 4 1.4 1.2 1 4 1
. 3 1.5 1.6 1.3 1.1 1.4 1.7 1.8 2.6 3.0 3.1 3.2 3.2 3.3 2 .• 2.9 2 .• 2.9 2.6 2 .• 2.9 3.0 3.1 2.9 2.8 2 .• G12

- C13 GI2 -CIO G12-C6 2>CO Mass 2>NDx Rate 2>Stk NOXc

CO Mass 

### Ib/hr 0-100 3.46 3.46 3.46 2.59 2.60 2.60 2.60 2.59 2.60 2. 59 1. 73 1. 73 1. 73 1. 73 1. 72 2.59 2.59 1. 73 1. 73 1. 72 2.58 2.59 3.45 4.31 4.31 4.31 4.31 5.18 4.33 4.33 4.32 4.33 3.46 4.32 4.32 4.30 4.32 4.32 4.3 1 4.29 NDx Rate 

### Ib/mmBtu 0-1 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.007 0.007 0.007 0.008 0.007 0.007 0.008 0.007 0.008 0.008 0.007 0.008 0.007 0.007 0
. 008 0.007 0.007 0.007 0.007 0.008 0.007 0.007 0.008 0.008 0.008 0.008 0.007 0.008 0.008 0.007 0.007 Stk NOXc 

### ppm 0-300 2.06 2.06 2.06 2.06 2.14 2.06 2.06 1. 99 2.06 1. 99 1. 98 1. 99 2.06 1. 99 1. 99 2.06 1. 98 2.06 2.06 1. 99 2.07 1. 99 1. 99 2.06 1. 99 1. 99 1. 99 1. 99 2.06 1. 98 1. 98 2.06 2.06 2.06 2.06 1. 99 2.06 2.06 1. 99 1. 99 G12-C7 GI2 -C 8 2>Stk CDc 2>Gas Flow

Stk COc Gas hscfh 

### ppm hscfh 0-1000 0-10000

1. 76 1.60 1. 60 1. 53 1.45 1.22 1.22 1.15 1.38 1.15 1. 07 1. 07 0.92 1. 07 0.99 1.15 1. 22 0.99 0.84 1. 07 1.30 1. 38 1. 99 2.29 2.37 2.45 2.45 2.52 2.14 2.21 2.14 2.21 1. 98 2.14 2.21 2
. 30 2.37 2.21 2.14 2.14 8230.8 8235.0 8230.2 8235.0 8253.0 8241.0 8264.4 8223.6 8247.0 8226.0 8242.2 8220
. 6 8223.6 8223.0 8197.8 8218.8 8227.8 8221.8 8226.0 8209.8 8191.8 8208.6 8219.4 8218.2 8201.4 8202.6 8201.4 8225.4 8242.8 8239.2 8233.2 8238.6 8229.0 8221.2 8233.8 8191.8 8224.2 8227.2 8204.4 8179.8 GI2-C18 2>NH3 Inj NH3Inj



### 1b/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110 .0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110 .0 110.0 110.0 110.0 110.0 110.0 1 10.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary

- 1-Min RATA

- Continued G12-C 2>MW Lo

MW Lo
0-1 100. :

99
. . 99. 100
. 100.: 100
.. 100
..

99. 100. : 100.: 100.1

99.**~** 99
.. 100.:

99.: 99.**~** 99
.**~** 99
.. 100
.

99. 99
. . 99
.. 99. : 99. ! 99
.. 99
.. 99.: 99
. . 100
. .

99.: 99
. . 100.: 100 .1 100. 100.1

99. 99. 9 9. ! 99
.. 99. PagE

### Group#-Channel# Long Descrip
. Short Descrip. Units Range 01/31/2013 11;03 01/31/2013 11;04 01/31/2013 11;05 01/31/2013 11;06 01/31/2013 11;07 01/31/2013 11;08 01/31/2013 11;09 01/31/2013 11;10 01/31/2013 11;11 01/31/2013 11;12 01/31/2013 11;13 01/31/2013 11;14 01/31/2013 11;15 01/31/2013 11;16 01/31/2013 11;17 01/31/2013 11;18 01/31/2013 11;19 01/31/2013 11;20 01/31/2013 11:21 01/31/2013 11:22 01/31/2013 11:23 01/31/2013 11:24 01/31/2013 11;25 01/31/2013 11;26 01/31/2013 11:27 01/31/2013 11:28 01/31/2013 11:29 01/31/2013 11:30 01/31/2013 11:31 01/31/2013 11:32 01/31/2013 11:33 01/31/2013 11:34 01/31/201 3 1 1:35 01/31/2013 11;36 01/31/2013 11:37 01/31/2013 11:38 01/31/2013 11:39 01/31/2013 11:40 01/31/2013 11:41 01/31/2013 11:42 

### Date/Time Printed: G12-C4 G12-Cll G12-C2 2>Stk NOx

Stk NOx 

### ppm 0-150 2>Stk 02 2>NOx Mass

2.6 2.6 2.6 2.7 2.7 2.8 2.7 2.7 2.7 2.6 2.8 2.7 2.7 2.7 2.7 2.6 2.7 2.6 2.8 2.7 2.7 2.6 2.8 2.6 2.8 2.6 2.7 2.6 2.7 2.7 2.6 2.6 2.6 2.7 2.7 2.7 2.7 2.7 2.5 2.6 Stk 02 

# • 0-25 13 .19 13 .19 13 .18 13 .17 13 .16 13 .15 13 .16 13 .16 13 .16 13 .16 13 .15 13
. 15 13 .16 13 .17 13 .18 13 .18 13 .17 13 .18 13 .18 13 .17 13 .16 13 .16 13
. 15 13 .16 13 .16 13 .18 13 .16 13 .17 13 .15 13 .15 13 .17 13 .17 13 .17 13 .16 13
. 15 13
. 15 13 .16 13 .15 13 .17 13 .16
01/31/2013 13,29 NOx Mass 

### Ib/hr 0-100 6.02 6.03 6.03 6.91 6.93 6.94 6.92 6.94 6.91 6.04 6.93 6.92 6.92 6.92 6.91 6.04 6.91 6.04 6.90 6.92 6.93 6.06 6
. 94 6.05 6.92 6.04 6.93 6.05 6.93 6.94 6.05 6.05 6.04 6.92 6.93 6.92 6.9 1 6.93 6.04 6.04 G12 -C20 2>StkFlow

StkFlow

kscfh 0-300000

20291 20323 20297 20348 20368 20365 20359 20397 20320 20307 20340 20318 20342 20357 20377 20330 20332 20337 20343 20367 20363 20347 20392 20334 20334 20337 20365 20342 20338 20389 20339 20341 20332 20331 20341 20303 20307 20343 20314 20310 G12-C3 2>Stk CO

Stk 

### co ppm 0-1000

2.8 2.9 2.' 2.9 2.9 3.2 2.7 2.8 2.8 2.9 2.9 2.7 2.6 2.' 3.1 3.0 2.' 3.1 3.0 2.9 2.9 3.1 3.1 2.9 3.2 3.3 3.1 3.4 3.1 3.3 3.2 3.2 3.5 3.5 3 .4 3.4 3.2 3.3 3.4 3.2 G12-C13 G12 -ClO G12-C6 2>CO Mass 2>NOx Rate 2>Stk NOXc

CO Mass 

### Ib/hr 0-100 4.30 4.30 4.30 4.32 4.33 4.34 4.33 4.34 4.32 4.32 4.33 4.33 3.46 4.32 4.32 4.31 4.32 4.31 4.31 4.32 4.33 4.33 4. 34 4.32 4.32 5.18 4.33 5.18 4.33 5.21 4.32 4.32 5.18 5.19 5.20 5.19 4.32 5.20 5.18 4.32 NOx Rate 

### Ib/mmBtu 0-1 0.007 0.007 0.007 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.007 0.008 0.008 0.008 0.007 0.008 0.007 0.008 0.007 0.008 0.007 0.008 0.008 0.007 0.007 0.007 0.008 0.008 0.008 0.008 0.008 0.007 0.007 Stk NOXc 

### ppm 0-300 1. 99 1. 99 1. 99 2.06 2.06 2.13 2.06 2.06 2.06 1. 98 2.13 2.06 2.06 2.06 2.06 1. 99 2.06 1. 99 2.14 2.06 2.06 1. 98 2.13 1. 98 2.13 1. 99 2.06 1. 98 2.06 2.06 1. 98 1. 98 1. 98 2.06 2.06 2.06 2.06 2.06 1. 91 1. 98 G12-C7 G12-C8 2>Stk COc 2>Gas Flow

Stk COc Gas hscfh ppm hscfh 0-1000 0-10000 2.14 2.22 2.22 2.21 2.21 2.44 2.06 2.13 2.13 2.21 2.21 2 .06 1. 98 2.21 2.37 2.29 2 .21 2.37 2.29 2.21 2.21 2.36 2.36 2.21 2.44 2.52 2.36 2.60 2.36 2.51 2.44 2.44 2.67 2.67 2.59 2.59 2.44 2.51 2.60 2.44 8184.6 8197.8 8197.8 8229.0 8247.6 8257.2 8244. 

## a 8259.6 8228.4 8223.0 8247.0 8238.0 8237.4 8232.6 8230.2 8211.0 8222.4 8214.0 8216.4 8236.8 8245.8 8239.2 8268.0 8233.8 8233.8 8214.0 8246.4 8226.6 8246.4 8266.8 8225.4 8226.0 8222.4 8232.6 8247.6 8232.0 8223.0 8248.2 8215.2 8224.2 G12 -C18 2>NH3 Inj NH3Inj

1b/hr 0-1000 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 

### 2>Summary - 1-Min RATA

- Continued G12-C 2>MW Lo

MW Lo

0-1 99. c 99.: 99.: 100.1 100. 100. 100. 100
.. 100. (

99. 100. :

99. ; 9 •. 99. 1 00.1 1 00. r

99.! 99
.. 99
.. 100
.. 100,
.

99, ' 100. '

99, ' 99, ; 99. ! 100. : 100,1 100.1 101,1 100
. .

99. 99, ' 99. ' 100.

99, ! 99.' 100.1

99
. 100." 

### PagE

### Group#-Channel# Long Descrip . Short Descrip . Units 

### Range 01/31/2013 11;43 01/31/2013 11
. 44 01/31/2013 11:45 01/31/2013 11;46 01/31/2013 11;47 01/31/2013 11:48 01/31/ 2 013 11:49 01/31/ 2 013 11:50 01/31/ 2 013 11:51 01/31/2013 11:52 01/31/2013 11:53 01/31/2013 11:54 01/31/2013 11:55 01/31/2013 1 1 :56 01/31/2013 11:57 01/31/2013 11:58 01/31/2013 11:59 01/31/ 2 013 12:00 01/31/2013 12:01 01/31/2013 12:02 01/31/2013 12:03 01/31/2013 12:04 01/31/ 2 013 1 2 : 05 01/31/2013 12:06 01/31/2013 12:07 01/31/2013 12:08 01/31/2013 12:09 01/31/2013 12:10 01/31/2013 12:11 01/31/2013 12:12 01/31/2013 12:13 01/31/2013 12:14 01/31/2013 12:15 01/31/2013 12:16 01/31/ 2 013 12:17 01/31/2013 12:18 01/31/ 2 013 12:19 01/31/ 2 013 12:20 01/31/ 2 013 12:21 01/31/2013 12:22 

### Date/Time Printed: G12-C4 G12 -C l1 G12

- C2 2>Stk NOx

Stk NOx ppm 0-150 2>Stk 02 2>NOx Mass

2.6 2.6 2.6 2.6 2.7 2.6 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2.6 2.7 2.6 2.7 2.7 2.6 2.7 2.7 2.7 2.7 2.6 2.6 2.7 2.6 2.6 2.7 2.7 2.7 2.6 2.7 2.6 2.7 2.6 2.7 2.6 2.6 2.7 Stk 02 

# • 0-25 13 .17 13 .17 13
. 17 13 .16 13 .15 13
. 14 13
. 1 4 13
. 1 4 13
. 13 13
. 13 13
. 13 13 .14 13 .14 13 .15 13 .13 13 .13 13 .13 13 .13 13 . 13 13
. 11 13 .11 13 .12 13
. 13 13
. 14 13
. 13 13 .1 4 13 .14 13 .14 13
. 15 13.14 13 .13 13.14 13.13 13.14 13 .13 13
. 14 13 .14 13 .1 5 13 .14 13
. 14
01/31/2013 13,29 NOx Mass 

### 1b/hr 0-100 6.03 6.03 6.04 6.04 6.92 6.06 6.93 6.93 6.94 6.94 6.95 6.95 6.92 6.05 6.94 6.06 6.93 6.93 6.07 6.96 6.96 6.95 6.94 6.06 6.06 6.92 6.06 6.05 6.91 6.91 6.91 6.03 6.92 6.04 6.92 6.04 6.90 6.02 6.02 6.89 G12-C20 2 >StkFlow

StkFlow

ksefh 0-300000

20292 20298 20324 20283 20327 20296 20317 20320 20317 20326 20344 20376 20306 20312 20317 20298 20308 20301 20302 20324 20325 20322 20310 20312 20286 20289 20297 20265 20279 20262 20249 20210 20259 20238 20258 20240 20221 20216 20182 20218 G12-C3 2>Stk CO

Stk 

### co ppm 0-1000

3.6 3.3 3.3 3.2 3.3 3
. 4 3.4 3.1 3
. 1 3.0 3
. 3 3.2 3.2 3.4 3.4 3.1 3.1 3.1 3.0 2.8 3.3 3.1 2.9 2.9 3
. 1 3.1 3.2 3.2 3.4 3.3 3
. 4 3.5 3.2 3.2 2.7 3.1 3.0 2.8 3.0 3.1 GI2

- C13 G12-C10 G12-C6 2>CO Mass 2 >NOx Rate 2>Stk NOXe

CO Mass lb/hr 0-100 5.17 5.17 5.18 4.31 5.19 5.19 5.20 4.33 4
. 34 4.34 5.21 4.34 4.33 5.19 5.20 4.33 4.33 4.33 4.33 4
. 35 5.22 4
. 3 4 4 .33 4 .33 4.33 4.32 4.33 4.32 5.18 5.18 5.19 5.17 4.32 4.31 4.32 4.31 4. 31 4.30 4
. 30 4 .31 NOx Rate lb/mmBtu 0-1 0.007 0.007 0.007 0.007 0.008 0.007 0.008 0.008 0.008 0.008 0.008 0.008 0.008 0.007 0.008 0.007 0.008 0.008 0.007 0.008 0.008 0.008 0.008 0
. 007 0.007 0.008 0.007 0.007 0.008 0.008 0.008 0.007 0.008 0.007 0.008 0.007 0.008 0.007 0.007 0.008 Stk NOXe ppm 0-300 1. 98 1. 98 1. 98 1. 98 2.06 1. 98 2
. 05 2.05 2.05 2.05 2.05 2.05 2.05 1. 98 2.05 1. 97 2.05 2.05 1. 97 2.04 2.04 2
. 05 2.05 1
. 98 1. 97 2.05 1. 98 1. 98 2.06 2.05 2.05 l. 98 2.05 1. 98 2.05 1. 98 2.05 1. 98 1. 98 2.05 G12-C7 G12-C8 2>Stk COe 2>Gas Flow

Stk COe Gas hsefh ppm hscfh 0-1000 0-10000 2.75 2.52 2
. 52 2.44 2.51 2
. 59 2.59 2. 3 6 2.35 2.2 8 2
. 51 2 .4 3 2.43 2.59 2.58 2.35 2.35 2.35 2.28 2.12 2.50 2 .35 2 .20 2 .2 0 2
. 35 2.36 2.43 2.43 2.59 2.51 2.58 2
. 66 2.43 2
. 43 2.05 2.36 2 .28 2.13 2
. 2 8 2.36 8206.2 8208
. 6 8219.4 8213.4 8241.6 8239
. 8 8248.2 8249.4 8259.0 8262.6 8269.8 8272.2 8244.0 8235.6 8259.0 8251.2 8255.4 8252.4 8253.0 8283.0 8283.6 8271.6 8256.0 82 4 6.4 8246.4 8236.8 8240.4 8227.2 8222.4 8226.0 8231.4 8205.0 8235.6 8216.4 8235.0 8217.0 8209.2 8196.6 8193.6 8208.0 G12 -C18 2>NH3 Inj NH3Inj



### 1b/hr 0-1000 110.0 llO.O 110.0 110.0 110.0 110.0 110
. 0 1 1 0.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 1 1 0.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110
. 0 110
. 0 110.0 110.0 110.0 

### 2>Summary

- I-Min RATA

- Continued G12-C 2>MW Lo

MW Lo
0-1 99
. ! 99.: 99
. . 100.1 100.1 100
. : 100. : 100
. : 100
. 100
. . 100. 100.

99. 99
. . 99. 100. 100. 100. ! 100.: 100
. . 100
.. 100. : 100. ! 100. ( 100
. : 100. ( 100. 1

99
. . 100.1 100. : 100
. .

99
. . 99
.. 99. 99. 99
.. 99
. . 99
.. 98. 99
.. pagE

### Group#-Channel # Long Descrip
. S h o r t De sc rip
. Un its Range 01/31/2013 12:23 01/31/2013 12:24 01/31/2013 12:25 01/31/2013 12:26 01/31/2013 12:27 01/31/2013 12:28 01/31/2013 12:29 01/31/2013 12:30 01/31/2013 12:31 01/31/2013 12:32 01/31/2013 12:33 01/31/2013 12:34 01/31/2013 12:35 01/31/2013 12:36 01 / 31/2013 12:37 01/31/2013 12:38 01/31/2013 12:39 

### Peri o d Av e rag e Period Max Val ue P e ri o d Min Valu e Period Total s 

# = Period 

### % Recovery



### Date/Time Printed: G12-C4 G12

- C11 G12

- C20 G12

- C2 

### 2>Stk NOx

Stk NOx 

### ppm 0

- 150 

### 2>Stk 02 2>NOx Mass 2>StkF!ow

2.7 2.7 2.8 2.7 2.7 2.6 2.7 2.7 2.6 2.7 2.8 2.7 2.7 2.7 2.6 2.7 2.6 2.7 2.9 2.5 6.6540E+2 100.0 

### Stk 02 

# • 0-25 13.13 13 .13 13.10 13 .11 13 .10 13
. 11 13 .10 13 .12 13 .11 13 .11 13 .10 13 .12 13 .11 13 .13 13 .11 13 .12 13 .11 13 .17 13.21 13 .10 3.2518E+3 100
. 0



### 01/31/2013 13,29 

### NOx Mass 

### 1b/ hr 0

- 100 6.93 6.92 6.94 6.94 6.94 6.07 6.93 6.92 6.06 6.92 6.94 6.93 6.92 6.92 6.05 6.90 6.05 6.72 7.06 6.01 1.6602E+3 100.0 

### StkFlow ksefh 0-300000

20283 202 57 20261 20268 20246 20249 20212 20241 20216 20213 20232 20267 20227 20254 20193 20189 20203 20411 20716 20182 5.0416E+6 100.0 G12-C3 G12 -Cl3 G12

- C10 G12 -C6 G12-C7 G12

- C8 G12

- C18 G12-C 

### 2>Stk CO 2>CO Mass 2 > NOx Rate 2>Stk NOXe 2>Stk COe 2>Gas Flow 2>NH3 Inj 2>MW La Stk CO 

### ppm 0-1000

3.0 2.9 2.8 2.8 3.0 3.0 2.9 2.7 3.0 3.3 3.0 2.9 3.0 2.6 

### 3.2 3.1 3.1 

### 3.0 4.0 1.1 7.3600E+2 100.0 

### CO Mass 

### 1b/ hr 0-100 4.33 4.32 4.34 4.34 4.34 4.33 4
. 33 4.33 4.33 5.19 4.33 4.33 4.33 3.46 4.32 4.31 4.32 4.41 6.09 1. 72 1
. 0895E+3 100.0 

### NOx Rate 

### Ib/mmBtu 0-1 0.008 0. 0 08 O.OOB O.OOB O.OOB 0.007 O.OOB O.OOB 0.007 O.OOB O.OOB 

### 0.008 O.OOB 0.008 0.007 0.008 0.007 O.OOB 0.008 0.007 1.9139E+0 100.0 

### Stk NOXe 

### ppm 0-300 2.05 2.05 2.12 2.04 2.04 1. 97 

### 2.04 2.05 1. 97 2.04 2.12 2.05 2.04 2.05 1. 97 2.05 1. 97 2.05 

### 2.21 1. 91 5.0755E+2 100.0 

### Stk COe Gas hsefh 

### ppm hsefh 0-1000 0-10000 2.28 2.20 2.12 2.12 2.27 2.27 2
. 19 2.05 2.27 2.50 2.27 2.20 2.27 1. 97 2.42 2.35 2.35 2.27 3.06 0.84 5.6129E+2 100.0 8245.2 8234.4 8268.0 8260.2 8262.0 8252.4 8248.2 8238.6 8239.2 8238.0 8256.0 8249.4 8243.4 8233.2 8229.6 8217.6 8233.8 8259.7 8410.2 8179.8 2.0401E+6 100.0 

### NH3Inj 

### 1b/hr 0

- 1000 110.0 110
. 0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 110.0 2.7170E+4 100.0



### 2>Summary

- 1-Min RATA

- Continued MW Lo
0-1 100. 100.

- 100. : 100. : 100. : 100. 100. ( 100
. ( 100. ( 100. ( 100.: 100
..

99. 100. :

99
.. 99. : 99
. . 100.0

101.



### 98. 2.4714E+ · 100.

pagE

## Appendix B.2 Fuel Analysis Data



## R0410673 B-6

# Saybolt A COli( U UR A lDIlJ[S (8ttPAMY 

### SAYBOLTLP 21730 S. Wilmington Avenu e Suite 201 Carson, CA 90810 3 10-518-4400 Telephone 3 10-518-4455 Facs imile 

## Fast To The Point 

# Saybolt LP
Certificate of Analysis DELTA AIR QUALITY SERVICES BOB FINKEN 1845 N

. CASE ORANGE, CA 92865 Report Date : 2/6/2013 Job No : 13091-00008592 Sample Number : 1300103-03 Client Ref : Gemma Test Refinery Gas Analysis Hydrogen Carbon Dioxide Carbon Monoxide Nitrogen Oxygen Methane Ethylene Ethane Propane Propylene Isobutane n-Butane 1-Butene Isobutylene t-2-Butene c-2-Butene 1 , 3-Butadiene Isopentane n-Pentane Hexanes Plus Total Molar Mass Ratio Relative Density Compressability Factor Gross Heating Value (Dry-Ideal) Gross Heating Value (Dry-Real) Gross Heating Value (Wet-Ideal) Net Heating Value (Dry-Ideal) Method ASTM 01945/ 01946 ASTM 01945/ 01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/ 01946 ASTM 01945/ 01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 0-3588 ASTM 0-3588 ASTM 0-3588 ASTM 0-3588 ASTM 0-3588 ASTM 0-3588 ASTM 0-3588 Date Sampled : 2/1/2013 Product: Natural Gas Location: NG line - 2 Sample 10 : Test #S2/NG line-Fuel Sulfur-1 Vessel: Result Units
<0
. 001 mole% 0.538 mole % <0
. 001 mole % 4.778 mole% 0.037 mole% 89.675 mole% <0.001 mole% 4.360 mole% 0.480 mole% <0.001 mole% 0
. 034 mole% 0
. 057 mole% <0
. 001 mole% <0.001 mole% <0.001 mole % <0.001 mole% <0.001 mole% 0
. 012 mole% 0.009 mole% 0.020 mole% 100
. 000 mole% 0
. 60710 0
. 60927 0
. 996 1000 BTU /cf 1004 BTU/cf 983 BTU /cf 900 BTU /cf isslier warrants that II has**e~er~ised** due diligence and care with r espc<:l to the infonnal;on and professIOnal Jl>dgments embodied In this .epan . This repa" renCCts only the findings al the lime and place of inspection and lestlnS
.**Iss~ r**  cKpressly disclaims 111)1 further indemnity of any k.llld
. This feJl(lrt is nol. guarlr'llee or polley ofmsuran ce WIth res pec t to the goods or the conlracwal performance of any party Any perwn relYing upon Ihls ,epon should be aware that issuer's activities are carried 0111 under their lIeneral terms and oonditions
. "PrCClsion parameters apply In the evaluation of the tes t results specified above
. Please also r efer t o ASTM 03244**(ex~pt** for analysis of RFG) and I? 367 with respect to the ulIlluuion of the test data to deteflTllne co nf ormance with specifications," 

### Page 7 of 12

### SAYBOLTLP 21730 S
. Wilmington Avenue Suite 20 I 

## Fast To The Point 

## 5aybolt: C arson, CA 90810 310-518-4400 Telephone 3 10-518-4455 Facsimile A [ORt l"BORATOIIJ[S CO I1 P"'1Y



### OEL TA AIR OUALITY SERVICES BOB FINKEN 1845 N. CASE ORANGE, CA 92865 Report Oate : 2 /6/ 2013 

### Job No : 13091-00008592 Sample Number : 1300103-03 Client Ref : Gemma Test Refinery Gas Analysis Pressure Base Ethylene Ethane Propane Propylene Isobutane n-Butane 1-Butene Isobutylene t-2-Butene c-2-Butene 1,3-Butadiene Isopentane n-Pentane Hexanes Plus Total Carbon Hydrogen Nitrogen Oxygen Gross Heating Value Fuel Factor (FD) Average Molecular Weight Sulfur Speciation Hydrogen SUlfide Carbonyl SUlfide SUlfur Oioxide Methyl Mercaptan 

# Certificate of Analysis

Oate Sampled: Product: Location : Sample 10: Vessel : Method Result ASTM 0-3588 14
. 696 ASTM 0-3588 <0.001 ASTM 0-3588 1
. 163 ASTM 0-3588 0
. 132 ASTM 0-3588 <0.001 ASTM 0-3588 0.011 ASTM 0-3588 0.Q18 ASTM 0-3588 <0.001 ASTM 0-3588 <0.001 ASTM 0-3588 <0.001 ASTM 0-3588 <0.001 ASTM 0-3588 <0.001 ASTM 0-3588 0.004 ASTM 0-3588 0.003 ASTM 0-3588 0
. 008 ASTM 0-3588 1
. 339 ASTM 0-3588 68.986 ASTM 0-3588 22.353 ASTM 0-3588 7.614 ASTM 0-3588 1
. 047 ASTM 0-3588 21192 ASTM 0-3588 8847 ASTM 0-3588 17
. 58 AOMO 307/ASTM 05504 <0.1 AOMO 307/ASTM 05504 <0.1 AOMO 307/ASTM 05504 <0.1 AOMO 307/ASTM 05504 <0.1 

# Saybolt LP

2/1/2013 

### Natural Gas NG Line - 2 Test #S2/ NG 

### Line-Fuel SU lfur-1
Units psi GPM GPM GPM GPM GPM GPM GPM GPM GPM GPM GPM GPM GPM GPM GPM wt% wt% wt% wt% 

### BTU/lb SCF/mm BTU

ppm v/v ppm v/v ppm v/v ppm v/v issuer warnnlS IMI il has exerdsed due diligence and care with respect to the**II'I o~tion**  and professional judgments embodied in this report . This report reflects only m efindings althe time and place of inliJH:CtHlII and testing. Issuer elCpfes$ly dIsclaims any further indemnity or any kind
. This report is not l guaran t ee or policy of insurance ""th respect to the good$ or the canltlC l lla! performance of any party Any person rdying upon th is report should be aware that ,ssuets activities are earned ()UI WIder their genaallemtS an d conditions
. "Precision parameters apply in the evaluatiOn of the test rcsults 5ptcified**abo~ .**  Please also ref e r to ASTM 03244 (except for analysis ofRFG) and IF 361 with respect to the utilization of the test dati to determine conformance with specifications ," 

### Page 8 

### of 12

### SAYBOLTLP 21730 S. Wilmington Avenue Suite 201 

## Fast To The Point 

## 5iJyboit II CO il E tAB DII A TClI l ES CO M P ANY 

### Carson, CA 90810 310-518-4400 Te lephone 310-518-4455 Fac s imile 

# Certificate of Analysis DELTA AIR QUALITY SERVICES BOB FINKEN 1845 N. CASE ORANGE, CA 92865 

# Saybolt LP

Date Sampled : 

### 2/1/2013 Report Date : 

### 2 /6/ 2013 Job No : 13091-00008592 Sample Number : 1300103-03 Client Ref: Gemma Test Sulfur Speciation Ethyl Mercaptan Dimethyl Sulfide Carbon Disulfide 2-Propanethiol tert-Butyl Mercaptan 1-Propanethiol Thiophene Diethyl Sulfide n-Butyl Mercaptan Dimethyl Disulfide tetra-Hydro Thiophene n-Pentanethiol Diethyl Disulfide Total Unknown Mercaptan Total Reduced Su lfur Product: Location: Sample ID : Vessel : Method Result AQMD 307/ ASTM D5504 <0.1 AQMD 307/ASTM D5504 <0
. 1 AQMD 307/ ASTM D5504 <0.1 AQMD 307/ ASTM D5504 <0.1 AQMD 307/ASTM D5504 <0
. 1 AOMD 307/ASTM D5504 <0.1 AOMD 307/ASTM D5504 <0.1 AOMD 307/ ASTM D5504 <0.1 AOMD 307/ ASTM 05504 <0.1 AOMO 307/ASTM D5504 <0
. 1 AOMO 307/ASTM 05504 <0
. 1 AOMO 307/ASTM 05504 <0.1 AOMD 307/ASTM 05504 <0.1 AOMO 307/ASTM 05504 0
. 2 AOMO 307/ASTM 05504 0
. 2

Approved By: Natural Gas NG Line - 2 Test #S2ING Line-Fuel Sulfur-1
Units
ppm v/v ppm v/v ppm v/v ppm v/v ppm v/v ppm v/v ppm v/v ppm v/v ppm v / v ppm v/v ppm v/v ppm v/v ppm v/v ppm v/v ppm v/v

Signature On File Francine Hanby Laboratory Manager

Issuer warrants thai il has ex ercised due dlhgence and care with respecllO the Inform.hOlland professional judgments embodied in this

. epo<t .**TI uS~!1**  .efleets only the findings aI the time Uld place oftn!ip«!ion and testing. Issuer ClqIressly dl$Ci aJn1$ any further llldemnily of any kind. Th,s .eporl is 1101 a**guarant~** Or policy of illsurance WIth respect to rhe goods or the contraClu al perfofTTW1ce arany party . Any person relying upon this .epon should be .ware that I$SUO::r'S a<;:bVlties M e earned out \II1der their general terms and conditions
. "Preeis ion p arameters apply in the evillualiOll of tile lest results specifIed .wove . Pl ease al so refer to ASTM 03244 (exUPI for analysis of RFG) and IP 367 WIth respect to the utiliu t ion of the leS I dal. 1 0**determi~** tonfonnance with specification s . " 

### Page 9 of 12

# Saybolt: A (01£ LAIOR"TDJlU:S CG J'l PA NJ 

### SAYBOLTLP 21730 S. Wilmington Avenue Suite 201 Carson, CA 90810 3 10-518-4400 Teleph o ne 310-518-4455 Facsimile 

## Fast To The Point 

# Saybolt LP
Certificate of Analysis DELTA AIR QUALITY SERVICES BOB FINKEN 1845 N

. CASE ORANGE, CA 92865 Report Date : Job No : Sample Number : Client Ref : Test 2/6/2013 13091-00008592 1300103-04 Gemma
Refinery Gas Analysis Hydrogen Carbon Dioxide Carbon Monoxide Nitrogen Oxygen Methane Ethylene Ethane Propane Propylene Isobutane n-Butane 1 - Butene Isobutylene t-2-Butene c-2-Butene 1 , 3-Butadiene Isopentane n-Pentane Hexanes Plus Total Molar Mass Ratio Relati ve Density Compressability Factor Gross Heat i ng Va l ue (Dry-Ideal) Gross Heat ing Va l ue (Dry-Rea l) Gross Heat ing Va l ue (Wet-Ideal) Net Heating Value (Dry-Idea l) Method ASTM 01945 /01946 ASTM 01945/ 01946 ASTM 01945 /01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945 /01946 ASTM 01945/ 01946 ASTM 01945/ 01946 ASTM 01945/ 01946 ASTM 01945/ 01946 ASTM 01945/ 01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 01945/01946 ASTM 0-3588 ASTM 0-3588 ASTM 0-3588 ASTM 0-3588 ASTM 0-3588 ASTM 0 - 3588 ASTM 0-3588 Date Sampled : 2/1/2013 Product: Location: Sample 10 : Vessel : Result
<0001 0.555 <0.001 2.475 0
. 015 91.836 <0.001 4.481 0.494 <0.001 0
. 036 0
. 058 <0.001 <0.001 <0
. 001 <0.001 <0.001 0.013 0.014 0.022 99
. 999 0.59853 0
. 60068 0
. 996 1025 1029 1007 923 Natural Gas NG Line - 2 Test #S2/NG Line-Fuel Sulfur-2
Units
mole % mole % mole % mole % mole% mole% mole% mole% mole % mole% mole % mole % mole% mole% mole % mole % mole% mole% mole% mole% mole%

BTU /cf BTU /cf BTU /cf BTU /cf Issuer warrants thaI it lias exercised due diligence and care with**r~** 10 the informllion and pl"ofcssional j...ogments embodied in this report . This rcpo" renecl5 only the findings at the bmc and place ofinspeclion and testing
. Issuer expre:;sly disclaims 8/\)1 further indemnity o f My kind. nus repo!1 is noll guarantee or policy of insurance with respect to the goods or the confractual performance of any party . Any per$Oll relying upon this Tepo" should be aware that issuer's acrivities are carried OUI under their generillerms and conditions
. "Precision parameters apply In the evaluation of the lest resul ts specified above
. Pl ease also refer 10 A STM 03244 (except for analysis ofRFG) and IP 367 wlIh respecllo Ihe uulization of the le5t data to determine confonmance 'Him spedficllions
. " 

### Page10of12

### SAYBOLTLP 2 173 0 S
. Wi lmin gto n Avenue Suite 201 

## Fast To The Point 

## Saybolt. A CORE lA.80RAiUR[[S CDI1PAHY 

### Carson, CA 90810 3 10-518-4400 Te leph o ne 3 10-518-4455 Facs imile 

# Certificate of Analysis DELTA AIR QUALITY SERVICES BOB FINKEN 1845 N. CASE ORANGE, CA 92865 

# Saybolt LP

Date Sampled : 2/1/2013 

### Report Date : 2/ 6/

2013 

### Job No : 1 3091-00008592 Sample Number : 1300103-04 C l ient Ref: Gemma Test Refinery Gas Analysis Pressure Base Ethylene Ethane Propane Propylene Isobutane n-Butane 1-Butene Isobutylene t-2-Butene c-2-Butene 1 , 3-Butadiene Isopentane n-Pentane Hexanes Plus Total Carbon Hydrogen Nitrogen Oxygen Gross Heating Value Fuel Factor ( FO) Average Molecular Weight Sulfur Speciation Hydrogen Sulfide Carbonyl Sulfide Sulfur Dioxide Methyl Mercaptan Product: Natural Gas Location : NG Line - 2 Sample 10 : Test #S2 / NG 

### Line-Fuel Sulfur-2 Vessel : Method Result Units
ASTM 0-3588 14
. 696 psi ASTM 0-3588 <0
. 001 GPM ASTM 0-3588 1.196 GPM ASTM 0-3588 0
. 136 GPM ASTM 0-3588 <0
. 001 GPM ASTM 0-3588 0.012 GPM ASTM 0-3588 0.018 GPM ASTM 0-3588 <0
. 001 GPM ASTM 0-3588 < 0
. 001 GPM ASTM 0-3588 <0
. 001 GPM ASTM 0-3588 <0
. 001 GPM ASTM 0-3588 <0
. 001 GPM ASTM 0-3588 0
. 005 GPM ASTM 0-3588 0
. 005 GPM ASTM 0-3588 0
. 009 GPM ASTM 0-3588 1
. 381 GPM ASTM 0-3588 71
. 719 wt % ASTM 0-3588 23.229 wt% ASTM 0-3588 4.001 wt% ASTM 0-3588 1.052 wt% ASTM 0-3588 22029 BTUllb ASTM 0-3588 8823 SCF / mm 

### BTU ASTM 0-3588 17
. 34 AQMO 307 / ASTM 05504 

### <0
. 1 ppm v/v AQMO 307/ASTM 05504 

### <0
. 1 ppm v/v AQMO 307/ASTM 05504 

### <0
. 1 ppm v/v AQMO 307 / ASTM 05504 

### <0
. 1 ppm vlv**S5~r** warrants thaI il has exerCised due**dih~ce** and care willi respect 10 lIle in ronnalion and professional judgments embodied in this report. This repon refleets only the findings atlhe lime and place of insp«tion Uld testing. Issuer expressly dlsclaims
.... y further indemnity of any kind
. This lepan is no l a guarantee or policy o [insuran ce with respect \0 rhe goods or the conlractuaJ perfonnance of any part)'
. Any person relying upon this repo " should be aware**thallssue~5** activities are carried 01,11 under the,r general terms and conditions
. "Precision parameters apply in the evall.lltion of the teSI results specified**abo~ .**  Ple..se 11150 re f er t

o ASlM 03244 (except for analysis of RFG) and IP 367 with rcspecllO the utilization of the test dati to detennine conformllflGe with specificallon s ," 

### Page 11 of 12

### SAYBOLTLP 21730 S. Wilmington Avenue Suite 201 

## Fast To The Point 

# 5aybolt II COM( lAURATORI£S COMPA.NY 

### Carson, CA 90810 3 10- 518-4400 Telepho ne 310-518-4455 Facs imil e 

# Certificate of Analysis DELTA AIR QUALITY SERVICES BOB FINKEN 1845 N. CASE ORANGE , CA 92865 

# Saybolt LP

Date Sampled: 2/1/2013 

### Report Date : 2/6/2013 

### Job No : 13091-00008592 Sample Number : 1300103-04 Client Ref : Gemma Test Sulfur Speciation Ethyl Mercaptan Dimethyl Sulfide Carbon Disulfide 2-Propanethiol tert-Butyl Mercaptan 1-Propanethiol Thiophene Diethyl Sulfide n - Butyl Mercaptan Dimethyl Disulfide tetra-Hydro Thiophene n-Pentanethiol Diethyl D isulfide Total Unknown Mercaptan Total Reduced Sulfur Product: Location: Sample ID : Vessel: Method Result AQMD 307 / ASTM 

### D5504 <0.1 AQMD 307/ASTM 

### D5504 <0.1 AQMD 307/ASTM 

### D5504 <0.1 AQMD 307/ASTM 

### D5504 <0.1 AQMD 307/ASTM 

### D5504 <0.1 AQMD 307/ASTM 

### D5504 <0.1 AQMD 307/ASTM 

### D5504 <0.1 AQMD 307/ASTM 

### D5504 <0.1 AQMD 307/ASTM 

### D5504 <0.1 AQMD 307 / ASTM 

### D5504 <0.1 AQMD 307 / ASTM 

### D5504 <0
. 1 AQMD 307 / ASTM 

### D5504 <0
. 1 AQMD 307 / ASTM 

### D5504 <0
. 1 AQMD 307 / ASTM 

### D5504 0
. 2 AQMD 307/ASTM 

### D5504 0
. 2

Approved By: Natural Gas NG Line - 2 Test #S2/NG 

### Line-Fuel Sulfur-2
Units
ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv ppm vlv

Signature On File Francine Hanby Laboratory Manager

ISSlIer WBJT8111S that il has exercised du-e diligenc e and care with respec t 10 !he informahon and professional j udgmmts embodied in this reporl. TIlls report 

### .,nCClS only the findings al the rime and plac e of inspection and tesllng
. ISliuer expressly disclaims any further indemnity o f any kind
. This repon 15 1101 a llUaranlee or policy of insurance 'Hith res pecl lO the goods o r the ronlr.cwa! performance of any party . Any pc:r$OO relying upon this report sho uld be aware thaI issuer's activities are carried out under thell general t erm.s and conditions
. "Precision parameters IIjlPty in the evaluation or m e lest results specified above
. Please alS(l refer to ASTM 03244 (exce pt for analysis ofRfG) iUld IP 367 with ICSp« t to the utilization of the leSI data to detennine confonTIlII1ce with specifications
. " 

### Page 12 of 12

## APPENDIXC TEST DATA

R041 0673 C-1 

# Delta /'!.,.



# .. """

# ..... :.... 

# .. ..-

# ..

## Appendix C.1 Stratification and Preliminary Flow Rate Tests

R0410673 

## C-2

### 12-POINT STRATIFICATION CHECK Gemma 

### 2 1/30/2013 

### 02 CO2 NOx CO Port Point % % ppm ppm

W 3 13.52 4
. 24 1
. 59 0
. 09 W 2 13
. 53 4.24 1.58 0.17 W 13
. 56 4.23 1
. 64 0
. 20 N 3 13.48 4
. 29 1
. 78 0.16 N 2 13.48 4.29 1.81 0.23 N 1 13.43 4.32 1.87 2.40 

## E 3 1307 4.54 2.27 1
. 94 

## E 2 13
. 08 4.53 2.35 1
. 91 

## E 1 13.08 4
. 54 2.27 1
. 69 

## S 3 13.08 4
. 54 2.34 1.12 

## S 2 13.08 4
. 55 2.40 0.60 

## S 1 13.07 4.55 2.53 0.57 Average 13.3 4.4 2.0 0.9 Maximum 13.6 4.6 2.5 2.4 Minimum 13
. 1 4.2 1.6 0.1 Maximum Difference from Average 0.3 0
. 2 0
. 5 1.5 Max Difference (% of average) 2.0% 3.9% 24.2% 159
. 6%
Criteria:

If < 

### 10%, use single point. Action Taken :

12-point traverse used for RATA runs Runs in conjunction with NH 3 

### test , use 12-point traverseRELATIVE ACCURAC Y TEST DATA AND WORKSHEET CPV Sentinel-2 -C EMS-103·STRAT TEST CONSTANTS Stat i on : CPV Sentinel Unit : 2 Perfonned By : AA. SP. SS. JM Cp' 0
.84 Tref : 68 

### ' F Stack Area : 143
. 14 ft' MeterYd : 0
.992 METHOD 2.1 DATA dP Temp Vel. Point (in. H 2O ) sqrt(dP) 

### O F (Ips) 4 1
. 50 1
.2247 758 105
. 25 3 1
. 80 1
.3416 759 115
. 34 2 2 .00 1.4142 760 121
. 63 1 2
. 10 1.4491 760 124
. 63 4 1
. 30 1 .1 402 764 98.22 3 1.40 1
. 1632 763 1 01.89 2 1
. 50 1
.2247 764 105.51 1 1.80 1
.3416 763 115
. 53 4 1
. 50 1.2247 760 1 05.33 3 1
. 80 1
.3416 766 115
. 67 2 2
. 20 1
.4832 76 6 127
.88 1 3.00 1
. 7321 766 149
. 33 4 1
.60 1.2649 758 108
. 70 3 1
. 70 1
.3038 759 112
. 09 2 1
. 80 1 .34 16 766 11 5.67 1 2.80 1
.6733 766 144 .27 Average 1.8369 1
.3553 762.4 116.68

Stack Flow Rate : 1 ,002
. 1 kwacfm Stack Flow Rate : 397
. 9 kdscfm 

### Dry Gas Meter T ime Vol. Tm(in) T m(o ut) #/Matl. Start 411
. 600 74 70 H,O 75 71 H,O 76 71 Empty End 431 .290 

### I SG line Rinse Total 19
. 690 72.8 Total

NO x ppm NO x , ppm@ 15% O 2 NO x I blMMBtu N O x Iblhr CO ppm CO, ppm@15%0 2 CO Iblhr O 2 % Stack Flow dscfh CT Fuel Flow hscfh Turbine Water Inject ion gpm



## 8./18 RlrQUII1lY5.MCIIS 1845 N

. Case Street O range, California 92865 714-279-6777 CT load MW SCR NH3 I nject ion Iblhr N Ox I blMMSCF CO IbJMMBlu CO Ib/MMSCF TEST VARIABLES Start Date : 1/ 30

/ 20 1 3 StarVEnd Time : 8 , 30 Load (MW)lReplicate# 103 Barom. Pressure : 29
. 80 Ps ta ck: 2.10 Pstack: 29.95 MW: 26.30 METHOD 100.1 DATA 

### 0, Co, Analyzer Range 20 10 Cal Gas Value 9
. 98 4
. 96 Pre -T est Direct Zero 0
. 12

-0
.02 Pre-Test Direct Span 10
. 1 0 5.02 Pre -Test System Zero 0
. 13 -0
.01 Pre-Test System Span 9
.98 5
.05

Post-Test System Zero 0
. 18 0
.07 Post-Tes t System Span 10
.01 5
. 13 Post-Test D i rect Zero 0
. 10 0
. 10 Post -T est Direct Span 10 .09 5.22 Average 13
. 29 4.41 Corr

. results 13 .32 4
. 29 Pre - test zero bias 0.1% 0.2% Pre-test span bias -0
. 6% 0
.3% Post-test zero bias 0.4 % -0
. 3% Post-lest span bias -0.4% -0
. 9% Zero drift 0
. 2 % 0 .7 % Span drift 0
. 1% 0
. 6% METHOD 4.1 DATA Impingers End Sta rt Diff

. 811.1 679.2 131
. 9 Meter Pressure : 664.4 664
.3 0.1 563.4 583.4 0 .0 Sample Volume : 885
. 9 881.4 4
.5 H 20 Volume: 100
.0 -100
.0 Mo i sture Content: 36
. 5 RESULTS Ref. Meth CEMS Diff

. Ditt

. % 2
.06 2
.00 0.06 3.1'% 161 1 .5 0 0.11 6
. 6% 0
. 006 0.006 0
. 000 0.0% 5
. 89 4
. 96 0.93 1 5 .7 % 0
. 77 0
.90 -0
. 13 -16.9% 0
. 60 0
.66

-0
. 06
- 10
. 2% 1
.34 1.29 0
. 05 3.4% 13
. 32 13.20 0.12 0
. 9% 23,676,927 21,076,000 2.800 .9 27 11
. 7%



## - 8,490.2 

## -

- 

## -

- 103


### -



## - 110
. 0 

## - 6
.93 0.001 

## - 1.41 

## - 9 ,02 STAAT iwg "H9 Ib/l b-mole NO , CO

5 10 4
. 62 4
. 49 0
.00 0.Q1 4
.81 4
. 50 0.00 0
. 25 4
. 77 4
.55

### ~ 0
. 10 4 .7 5 4
. 51 -0
.01 0
.04 4 .7 6 4 .5 3 2
.04 0
. 92 2.06 0
. 77 -0
. 1% 2.5%

-0
. 9% 0.5% 0.2% 0
.6% -0.4% -0.2% 0
.0% - 1
. 5% -0.4% -0.4%

1
. 6 iwg 19
. 362 dscf 1 .72 3 scf

8
.2 %

Sent i nel Unit 2 RATA.xls 217120 1 3 4 : 12 PM

### Port Point Angle W 4 2 W 3 0 W 2 4 W 1 

## 6 N 4 3 N 3 4 N 2 

## 5 N 1 2 

## E 4 4 

## E 3 1 

## E 2 3 

## E 1 0 S 4 2 S 3 1 S 2 4 S 1 4 Average 2.8 Average Angle < 10 deg

. ? Yes No Points w/Reverse Flow? Yes Less Than 4 Points> 30 Oeg.? Yes PASS

## FLUE GAS VELOCITY DATA AND WORKSHEET 

## CLIENT: Gq 

## 61'" M ,::, 

## PERFORMED BY: s? S P LOCATION: SeN \ \ f\J 

## A L 

## BAR. PRESSURE:--'Z"-'qi-.

. 

# '6"'D,,-.::=---------- UNIT: \J I\.J \ 

## T 

# :>- STATIC PRESSURE:

__**"'-,2.~~~I**

# ______ _ TEST DATE: I! 

# 30 \ (7) 

## TC READOUT 

# 10:-->1;.... '**·1.:....:::..V->_<.--'5~**______ _ 

## TEST NUMBER: S
- 

# "'-Sn<-

- '-'II.- 

# ioo:i TC 

# 10: \ \ LEAK CHECK PRE- ./ POST-_/=---

# PITOT'""T:::-U'-::BC=E:--:I~D-:

# ,&---r;Q7.9:- , ------- tlP INDICATOR TYPE:**<'~ (o.o\\.lAt'~**  

## PITOT TUBE COEFFICIENT:....:D=-:.!-'D"'-'t-l-·---,

___ _ tlP INDICATOR 

# 10: P' < 

## ZERO: v' 

## LEVEL:----".-/==----

___ _ Yaw Angle, tlP, Temperature, Time Port Point Degrees(1) inches H2 

## O OF 

# o£qo tV 1-)



# ... 2

- 0 

# t ' 'S""" '7 

# <;7" , '7, < 

# v' D \

- 'b-**I.'~;** 

# '1 

# -z.. 

# -l-\ , O**~,O** 

# 'l C9C7 

# >-C? -cJ 'J. ' \ 'l 

# ron**l~** Lj-

## ~]**,** 

# 0 

# t ' -:;,**I~'--f** 

# :> -r-L 

# +.0 

# \
- '-i l 4>:) L.,



# ... tf;'D**~,** 

# l.S- I l,-t..{ \ 'i- ;) 

# .0 

# 1. 0 

# '7403 E::: t. 

# .. '-\ "



### - 0 

# t ,S /l"U --; 

## -1-),0 

# 'L'b '/ r:ct/, 

# L
... 3-0 ;;l, ,

# d--. 'ltD0 

# I 

# I--b·0 

# 3
. 0 7/_ (-, 

# :5 y i.) <D 

# 'Lw I 

# <i<-6 CJ.. 

# "'l.O l , 

# 1 

# "S'l 2-

... <1--\ 

# . D {d:? 

# "'\ ("-<r I ..,.-L 

# -u ,;,z.E? cG(P

Comments: 1) Positive yaw angles correspond to clockwise rotation of the probe.



# J1eIta L\ ""--- Date of last revision 

### 11/13/08 D8834033 Master Document 8torageiFormsiDatasheetsiFieid Datasheets

## WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET CLIENT : 

# 6:! 

# c {(\ {(\ ('r 

### AMBIENT TEMPERATURE : 

# '78 0 

### LOCATION : 

## c,,, ,,1<
.. ,.,,,.... BAROMETRIC PRESSURE- : 

## """' :J.. """""

g'-':7() -------- DATE : I) 

## Je l'?> I 

### ASSUMED MOISTURE : . RUN NO : <; -.l. -91"1<

- 

### NH,, ' - Ic6 - 

### .p. . ,- 

# tJ· PITOT TUBE COEFF

. C ' -p-

:**;:-:- -,** **7...,A .---------**  OPERATOR:**s. S~!V\**  1 - PROBE ID NO/MATERIAL:

__ 

## -tZ '--
______ _ METER BO X 

### NO : 

# S p",,- P 

### PROBE LENGTH : 

# 7 METER dH@: 

### tj\';'L NOZZLE ID NO/ M:-:A-=T=ER=-I:-:-A-:-L:--: ,v :T / r ;"' -------- METER Yd :

### O.~"2: NOZZLE DIAMETER : 

# 7 STACK AREA ,

## FT~**:** FILTER NOffYPE : 

# ---, 7,L--

-------- TRAVERSE POINTS, MIN/POINT :

## ~ 

# xl**~p** PRE-TEST LEAK RATE :: < " ,et?L CFM@ / 

### '5" in

. Hg

. d H=

__ 

### X d P : POST-TEST LEAK RATE: :.(o <'C7 

### CFM@ I 

### 5" in

. Hg

. Probe Cond ition , pre/ post test: P ITOT LEAK CHECK
- PRE : I'" 

## /.+ POST : AI

### ~ Silica Gel Expended , YIN : CHAIN OF CUSTODY : SAMPLE CUSTODIAN • 

## .-;::Y' Filter Condition after Test: 

# Z SAMPLER 

## '"3'5**~** Check Weigh t: 

# 7 SAMPLE CUSTODIAN -,.LLL Meter Point 

## I Time 

## I Volume , ft 3 

# -p 

# I OCOX' 

# I '-H\. i. 6(J 

## 7 DV):J. 

# /.-ffi)

# ~~~ :3 

# 1 (')**~"?R** 

# I '-'di", , 

# '-rz.v 7**(~eJ**



### I 

## I Ofl,"n. V i i? 

# s T o iA9:;;: 1 \,-\ 2. 

# r · i'fL t. 

## 166Yt1 i 

## I 

# Ot¢:5t V 

# I 0 'f.:,<;,,) .-; 1 

## 0 

# "081 1 

# L\ :2 c..>. 

# 'i7tC**~** 

# l "'Wi b C,o\ 

### I) 1 0QO?;**I-\~"l.** 

## 'Z'1o**Aver~e :**  

### d P in

. H , O d H in. H , O



### (,y;.!,



# t · 

# '6

' l , '() Stack Temp. OF



# 1'-'1'"

/- J( Probe Temp , OF



## t"A**~** 

### Filter Temp , O F IV 

### I r 

# I

1 Imp. Out Temp, OF



# rf/l, S§
'3'5 Imp

. 

### # Contents Post-Test - Pre-Test = Difference 

# V,i tl 

# \·hS:>-/ 

# ,fIr \ 

# rcl'1 ·Z.
__ ':2- 

## DIN l is'»'**Ctv~·y(** 

# 1 .4 ·3 c 

# '3 w'\**5vl'3.~S'63 ,**  

# 1 , 

# l**~ ~**  

# !r&>S , 1 B 0 1,Lj, 

# vr \t-.s,o \"" 1 ,'12 \2.,'\.Se"

- 

## \DO

Tota l:

____________ _ Meter Temp , O F In lOut 

# 1'-\ 1 

## ·-(U

7'> 1 

## l \.

,c" I "1( Vacuum in. Hg

. 

### "",.0



## "il 0 , % Pstatic in

. H , O

Comments :

____________________________________________________________________________________________________________ _



### Date of last revision 

### 11 /13 / 08 D5834048 Master Document 5torage i FormsiDatasheets i Fieid Datasheets

## Appendix 

## C.2 CEM Data

R0410673 

## C-3 

# De/ta b. """"",,"",,, ,, 

# ..

# _ ...

## Appendix C.2.1 CEM Quality Assurance Measurements

R0410673 C-4 

# Delta l'1 ,,""- 

## ....... ,

# ..

# -

### Client: Gemma 

# DeltaAIr QualfIY Services CEMS PERFORMANCE DATA SHEET
Location : CPV Sentinel Unit 2 Date : 

### 1 / 30

/ 2013 Performed By : AA, SP , SS, JM CEMS ID# : ..=5--=-C:.,:E::;.M;:.:S=--

__________ _ Analyzer: O 2 CO 2 NO , CO Manufacturer : AMI CAl CAl TECO Serial Number : 021119-3 W06004-M V10043 CM0490048 CEMS Probe : Material: S

. S

. Length: 8' Heated Line Material : Teflon Length : 6' Sample Conditioner : Type: Universal CEMS Line : Material : Teflon Length : 200' Bias Line: Material: Teflon Length : 200' Upscale Response Time : 30 Downscale Response Time :

Sample Pressure (psi) : 6 TECO Vacuum (oo 

### Hg) : Sample Flow Rate : 8 SCFH S02



# --
Gas Temp : 780 

### of Gas Temp : 275 

### of Gas Temp: 32 

### of

30 seconds NA

Sent i nel Unit 

### 2 CEMS QA.xls 

### 2/7/2013 4:40 

### PM

### GAS Zero Zero NO NO N0 2 

### N0 2 

# DllhaAIrqua/flY S/ltv/C/IS
N02 

### to NO Converter Efficiency Test Analyzer Manufacturer : Analyzer Model : Analyzer Serial Number : Date : ANALYZER MODE

NO , NO NO, NO NO NO ,

Abs

. Value C o -C,: Abs. Value C 2 

### -C ,: C,/C 2 

### CE 

## = 0,10, • 100 %: Gemma CPV SentinEIIIOrUl<l! Gas Value: 4.82 600CLD V10043 1/

30

/ 13



### 3
. 9 3
. 7 2% 93% N0 2 

### Cal Gas Value : 4
. 02



### ANALYZER RESPONSE 0
. 00 0
. 00 4
. 82 4
. 84 0.08 3.73

Label

0 , 

## O

2 

### 0 3 

### Performed By : AA CEMS 

### 10# : 5-CEMS CAL CORRECTED LABEL

0
. 1 3.7
Requirement

<5% >90% C, C 2



### Sentinel Unit 2 CEMS QA.xls 2/7/2013 

### 4:40 PM

### GAS Zero Zero NO NO NO, NO, 

# OBllaAir Quality SBlfllcBS NO, to NO Converter Efficiency Test Analyzer Manufacturer: Analyzer Model: Analyzer Serial Number: Date: ANALYZER MODE

NO, NO NO , NO NO NO,

Abs. Value Co-C, : Abs. Value C,-C, : 

### C,/C, CE 

## = 

## 0,/0, • 100%: Gemma CPV SentinEIIIOr1ila! Gas Value: 4.82 600CLD V10043 

### 1/31/13

4
. 0 3
. 8 0% 96% NO, Cal Gas Value: 4.02

ANALYZER RESPONSE -0.01 -0.02 4.82 4
. 83 0.00 3.85

Label



## 0, 0, 0 3 

### Performed By : 

## AA CEMS 

## 10#: 5-CEMS CAL CORRECTED LABEL

0
. 0 3.9
Requirement

<5% >90% C, C,

Sentinel Unit 2 CEMS QA.xls 

### 2/7/2013 4:40 PM

### GAS Zero Zero NO NO NO , NO, 

## OeltJl AI, qualllY SeN/CBs NO, to NO Converter Efficiency Test Analyzer Manufacturer: Analyzer Model: Analyzer Serial Number: Date : ANALYZER MODE

NO , NO NO , NO NO NO,

Abs. Value Co -C, : Abs

. Value C , -C , : 

### C,/ C, CE 

# =0,10 , • 100 %: Gemma CPV SentimlllOrUla! Gas V alue : 4
. 82 600CLD V10043 

### 2

/ 1/13

4.0 3
. 8 1 % 96 % NO , Cal Gas Value: 4
. 02

ANALYZER RESPONSE -0
. 03

- 0
. 03 4
. 81 4.82 -0
. 01 3
. 85

Label

0, 0 , 0 3 

### Performed By : 

## AA CEMS 

### 10# : 5-CEMS CAL CORRECTED LABEL

0
. 0 3
. 9
Requirement

<5 % >90 % C , C,

Sentinel Unit 2 CEMS QA.xls 

### 2/7/2013 4 : 40 PM

# DeltaAirQualllY Services SPAN GAS RECORD AND SCAQMD CALIBRATION ERROR/LINEARITY CLiENT/LOCATION: Gemma CPV 

### Sentinel Unit 2

TRUCK/CEM 1.0 .: .:::5....::-C::.:E"'M"'S'--

__________ _ DATE : 

### 1/30/13 BY : AA , BF , SS,ME,JM Exp. Vendor 

### %of Gas Cylinder 

### # Value Date 

### 10 Range ZERO Low CC93915 0.0 

### 10/6/17 F22012



## 0, Mid CC72997 9.98 

### 11/16/15 F22012 49.9% 

## 0, High CC199067 18.90 

### 4/4/15 F22012 94.5% CO, Mid CC72997 4.96 

### 11 /16 /15 F22012 49
. 6% CO, High CC199067 9.62 

### 4 / 4

/ 15 F22012 96 .2% NO, Mid CC321491 2.58 

### 1130/13 F22012 51
. 6 % NO, High CC362309 4.82 

### 5/24/14 F22012 96.4% NO, NO, CC113404 4.02 

### 7/9113 F22013 80.4% CO Mid CC325462 4.49 

### 2/20/13 F22012 44.9% CO High CC313840 9.47 

### 8/16/15 F22012 94.7% PRE-TEST INSTRUMENT CALIBRATION ERROR ANALYZER 

## 0, CO, NO, CO Analyzer Range 20 10 5 10 Zero Gas Value 0.0 0.0 0.0 0.0 Analyzer Reads 0.12 -0.02 0.00 0.01 Error (% 

### of scale) 0
.6% -0.2% 0
. 1% 0
. 1%

High Gas Value 18.90 9.62 4.82 9.47 Analyzer Reads 18.97 9.64 4.81 9.51 Error (% 

### of scale) 0.3% 0.2% -0.2% 0.4%

Mid Gas Value 9.98 4.96 2.58 4.49 Analyzer Reads 10.10 5.02 2
. 56 4.50 Error (% 

### of scale) 0.6% 0
.6% -0.3% 0.0% Linearity at Mid Point 0.2% 0
. 6% -0.3% -0 .2% POST-TEST INSTRUMENT CALIBRATION ERROR ANALYZER 

## 0, CO, NO, CO Analyzer Range 20 10 5 10 Zero Gas Value 0.0 0.0 0.0 0
. 0 Analyzer Reads 0.10 0
. 12 -0.01 0.01 Error (% 

### of scale) 0.5% 1.2% -0.2% 0
. 1%

High Gas Value 18.90 9.62 4.82 9.47 Analyzer Reads 18.87 9.67 4.78 9.48 Error (% 

### of scale) -0.1% 0
. 5% -0
. 9% 0.1%

Mid Gas Value 9
.98 4.96 2
. 58 4.49 Analyzer Reads 10.07 5
. 13 2.54 4.49 Error (% 

### of scale) 0
.4% 1.7% -0.8% 0.0% Linearity at Mid Point 0.3% 0.9% -0.2% -0.1% STATUS



## --

-- PASS



# --



# -- PASS



## --

-- PASS PASS

STATUS



# --

-- PASS



# --

-- PASS



## --



# -- PASS PASS Sentine l Unit 2 CEMS QA,xls 2/7/2013 4:39 PM

# 00/18 Air QualllY SOMCOS SPAN GAS RECORD AND SCAQMD CALIBRATION ERROR/LINEARITY CLiENTILOCATION: Gemma CPV Senlinel Unit 2

TRUCK/CEM I.D.:**-,,5~-C~E::!:M:::S~**

### __________ _ DATE : 1131/13 BY : AA,BF ,S S,ME,JM Exp. Vendor 

### %01 Gas Cylinde r 

### # Value Date 10 Range ZERO Low CC93915 0.0 10/6/17 F22012



## 0, Mid CC72997 9.98 11/16115 F22012 49.9% 

## 0, High CC199067 18.90 4 1 4 11 5 F22012 94.5% CO, Mid CC72997 4.96 11 / 16 1 15 F22012 49.6% CO, High CC199067 9.62 4 14 1 15 F22012 96.2% NO, Mid CC321491 2.58 1130/13 F22012 51.6% NO, High CC362309 4.82 5124/14 F22012 96.4% NO, NO, CC113404 4
.02 719113 F22013 80.4 % CO Mid CC325462 4.49 2 120 / 13 F22012 44.9% CO High CC313840 9.47 8116/15 F22012 94 .7% PRE-TEST INSTRUMENT CALIBRATION ERROR ANALYZER 

## 0, CO, NO, CO STATUS Analyzer Range 20 10 5 10 Zero Gas Value 0.0 0.0 0 .0 0 .0 

# -- Analyzer Reads 0.11 0.06 -0.01 0.00 

# - Error (% of scale) 0
. 5% 0.6% -0.3% 0.0% PASS

High Gas Value 18.90 9.62 4
.82 9.47 

## -- Analyzer Reads 18
.98 9.66 4
. 79 9.44 

# -- Error (% of scale) 0.4% 0.4% -0.6% -0 .3% PASS

Mid Gas Value 9.98 4.96 2.58 4.49 

## -- Analyzer Reads 10.10 5.09 2.54 4.46 

## -- Error (% of scale) 0
. 6% 1.3% -0.8% -0.3% PASS Linearity at Mid Point 0.2% 0
. 8% -0.3% -0.2% PASS POST-TEST INSTRUMENT CALIBRATION ERROR ANALYZER 

## 0, CO, NO , CO STATUS Analyzer Range 20 10 5 10 Zero Gas Value 0 .0 0.0 0.0 0.0 

# -- Analyzer Reads 0.09 0.09 0.04 -0.07 

## -- Error (% of scale) 0
. 5% 0
. 9% 0
. 8% -0
. 7% PASS

High Gas Value 18
.90 9.62 4 .8 2 9 .4 7 

## -- Analyzer Reads 18 .79 9
. 67 4.76 9
. 35 

# -- Error (% of scale) -0
. 5 % 0.5% -1.3% -1
. 2% PASS

Mid Gas Value 9.98 4.96 2.58 4.49 

## -- Analyzer Reads 10
. 04 5.13 2.54 4 .3 9 

## -- Error (% of scale) 0.3% 1.7 % -0
.8% -1 .0% PASS linearity at Mid Point 0
. 3% 1
.0% -0.5% -0
. 1% PASS Note. NOx analyzer linearity IS 

### greater than the SCAQMD Method 100.1 speclficallon of 

## +I-d %**b~~** 

### c within the uncertainty (+1-2%) of the best available calibration standards available fa the rangg'irri'

## usn~'.2**EM;/~O~ ;**  4 : 39 PM

# DeltaA1rqualfIY So/VIces SPAN GAS RECORD AND SCAgMD CALIBRATION ERROR/LINEARITY CLiENT/ LOCATION: Gemma CPV Sentinel Unit 2

TRUCK/CEM 1.0 .: ..::5c.:-C"'E:::M"'S=-

__________ _ DATE: 

### ..::.2 /,::

1 :..: 11:::3:-::-::-:-=--::-:-_ 

### BY : AA , BF, SS, ME, JM Exp, Vendor 

### %of Gas Cylinder 

### # Value Date 

### 10 Range ZERO Low CC93915 0.0 

### 10 /6/ 17 F22012 O 2 

### Mid CC72997 9.98 

### 11 / 16/15 F22012 49.9% O 2 

### High CC199067 18
. 90 

### 4 / 4

/1 5 F22012 94.5% CO 2 

### Mid CC72997 4.96 

### 11 / 16 /15 F22012 49.6% CO 2 

### High CC199067 9
. 62 

### 4 / 4

/ 15 F22012 96.2% NO, Mid CC321491 2.58 

### 1/30/13 F22012 51 .6% NO, High CC362309 4.82 

### 5 /24/ 14 F22012 96.4 % N0 2 

### N0 2 

### CC113404 4.02 

### 7/9113 F22013 80.4% CO Mid CC325462 4.49 

### 2/20/13 F22012 44
. 9 % CO High CC313840 9.47 

### 8 /16/ 15 F22012 94
. 7 % PRE -TEST INSTRUMENT CALIBRATION ERROR ANALYZER O 2 

### CO 2 

### NO, CO Analyzer Range 20 10 5 10 Zero Gas Value 0
. 0 0 .0 0.0 0
. 0 Analyzer Reads 0.10 -0
. 02 -0
.02 -0
. 03 Error (% of scale) 0
. 5 % -0.2% - 0.4 % -0.3%

High Gas Value 18.90 9.62 4
. 82 9.47 Analyzer Reads 19.14 9.66 4
. 79 9.45 Error (% of scale) 1.2% 0.4% -0.7% -0 .2%

Mid Gas Value 9.98 4
. 96 2.58 4.49 Analyzer Reads 10.19 5
.05 2.54 4.52 Error (% of scale) 1
. 1 % 0.9% -0.8% 0 .3% Linearity at Mid Point 0 .2% 0.8% -0 .3% 0 .5% POST-TEST INSTRUMENT CALIBRATION ERROR ANALYZER O 2 

### CO 2 

### NO, CO Analyzer Range 20 10 5 10 Zero Gas Value 0
. 0 0
. 0 0
.0 0
.0 Analyzer Reads 0
. 10 0.03 -0.02 -0 .0 4 Error (% of scale) 0.5% 0.3 % -0.4% -0.4%

High Gas Value 18
. 90 9.62 4.82 9
.47 Analyzer Reads 19.02 9.70 4.77 9.43 Error (% of scale) 0
. 6% 0
. 8 % -1.1% -0.4%

Mid Gas Value 9
. 98 4 .9 6 2.58 4
. 49 Analyzer Reads 10
. 13 5
. 11 2.52 4.43 Error (% of scale) 0
. 8% 1 .5% -1.1% -0.6% Linearity at Mid Point 0.2% 0
. 9 % -0.4 %
- 0 .2% STATUS



## --



# -- PASS



## --

-- PASS



# --



# -- PASS PASS

STATUS



# --

-- PASS



## --

-- PASS



# --

-- PASS PASS Sentinel Unit 2 CEMS QA.xls 21712013 4 :3 9 PM

### Source Test Date
AETB Name AETB Phone Number AETB e-mail QI Last Name QI F i rst Name QI Middle Initia l QI Exam Date Exam Provider Exam Contact Gemma CPV Sentinel Unit 2 1/

30 / 2013 

### Delta Air Quality Services , I n c . 714-279-6777 contact@deltaags

. com Aleshaiker Ali 

## M November 21 , 2008 Source Evaluation Society gstiprogram@gmail

.com

## Appendix 

## C.2.2 NO x and CO Compliance

R0410673 

## C-5COMPLIANCE TEST DATA AND WOR K S H EET CPV S e nt l n e l- 2 -CEMS-5 0 -1 TEST CONSTANTS Station: CPV Sentinel Unit 2 Perfo r med By : AA , SP, SS, JM Cp: 0
.99 Tref : 60 of Stack Area : 1 4 3
. 14 ft' Meter Y d : 0
.992 METHOD 2.1 DATA dP Temp Vel. Point (in. H 2 O) sqrt(dP) of (fps) 4 0.61 0
.7810 774 79
.99 3 0
.65 0
. 8062 773 82
. 54 2 0
. 72 0
. 8485 772 86.B3 1 0
. 75 0.8660 772 88.63 4 0.60 0
. 7746 770 79
. 20 3 0.59 0.768 1 773 78.64 2 0.63 0
. 7937 776 8'-36 1 0
. 65 0
.8062 775 82
.61 4 0
.60 0
. 7746 771 79
. 24 3 0.63 0.7937 770 81
. 1 6 2 0
. 72 0
.8485 776 86.98 1 0.83 0
. 9110 777 93.42 4 0
. 71 0
. 8426 774 86
. 30 3 0
.88 0
. 9381 777 96
. 19 2 0.95 0
. 9747 778 99
. 99 1 0.85 0
.9220 779 94
. 62 Average 0
. 7066 0
.8406 774.2 86
. 11

Stack Flow Rate : 739
. 5 kwacfm Stack Flow Rate : 282.3 kdscfm Dry Gas Meter Time Vol. Tm(in) Tm(out) #/Matl. S tart 924.138 80
.5 77.9 H,O 84
. 0 79
. 0 H,O End 972
. 196 83
. 0 79.0 Empty 82.0 80
.0 SG Total 48.05 8 80.7 Total

NO

.. ppm**NO~,** p pm @ 15% O 2 NO

.. IblMMBtu NO

.. Iblhr CO ppm CO, p pm @ 1 5% O 2 CO Ib/hr 0, % Stack Flow dscfh CT Fuel F l ow hscfh Turbine Water Injection gpm



## 8,118AllQua/flY StlIIIICls 1845 N

. C ase St ree t O ran g e , Ca l if o rn ia 92 86 5 7 1 4-279-6777 CT Load MW SCR NH3 Inj ect i on lblhr NO

.. IblMMSCF CO Ib/M MB tu CO Ib/MMSCF TEST VARIABLES Start Date : 2/1/13 Start/End Time: 1 4:20 1 5:35 Load (MW)/Replicate# 50 1 Barom
. Pressure : 29
. 69 Pslack : Ps tack: MW:
Analyzer Range Cal Gas Value Pre-Test Direct Zero Pre-Test Direct Span Pre-Test System Zero Pre-Test System Span

Post-Test System Zero Post-Test System Span Post -Test Direct Zero Post-Tes t Direct Soan Average Corr

. results Pre-test zero bias Pre-test span bias Post-test zero bias Post-tes t span bias Zero drift Soan drift METHOD 4
. 1 DATA I mp i ngers End Start Diff

. 861.4 682
. 7 178 .7 666
.8 663
. 2 3
.6 583
. 3 582
. 5 0.8 916.8 900
.6 16
. 2

Ir 100 99.3 RESULTS Ref

. Meth CEMS

2.20 2
. 10 1.99 1
. 85 0.007 0.01 4 .5 2 3
. 84 0
. 26 0
. 30 0
. 23 0.26 0
.32 0.48 14
. 38 14
.33 16 , 936,600 15,604.000



## - 5,361 55



### - 107 8.44 

### - 0,00 1 

## - 0.55 

## - 2
. 10 mg 29.84 "H9 28.1 4 lb/lb-mole METHOD 100.1 DATA 0, CO, NO, CO 20 10 5 10 9.98 4.96 4
. 82 4.49 0
.07 0.25 -0.03 -0
.03 1 0
. 04 5.40 4
. 73 4.44 0
. 17 0
. 31 -0
. 02 0
. 14 10.04 5.39 4.71 4
. 39

0
. 21 0.31 -0
. 03 0
.08 10.03 5.36 4.69 4
.39 0.09 0
.25 -0
.04 -0
. 04 1 0.09 5
. 40 4
. 74 4.43 14.38 4.09 2
. 14 0
.35 1 4.38 3.70 2.20 0.26 0.5% 0
. 6% 0
. 3% 1
. 7% 0
. 0% -0
. 2% -0.4% -0 .5% 0.6% 0.6% 0
. 1% 1
. 2% -0.3% -0.4% -1.0% -0.4% 0.2% 0
. 0% -0
. 2% -0.6% -0
. 1% -0.2% -0
. 4% 0
. 0%

Meter Pressure : 1
. 8 iwg Sample Volume: 45
. 700 dscf H 2

0 Volume : 4
. 616 scf Mo i sture Content: 9.2 %

Sentinel Unit 2 50% NOx · NH3-RO G Compliance. xis 2/7/2013 4 : 18PMCOMPLIANCE T EST DAT A AND WOR K SHEET CPV S e n U n e l- 2 -CEMS -SO -2 TEST CONSTANTS Station : CPV Sentinel Unit: 2 Performed By : M , SP , SS , JM Cp : 0
.99 Tref: 60 " F Stack Area : 143.14 

## tt' Meter Y d : 0
. 992 ME T HOD 2. 1 DATA dP Temp Vel. Point (in.H.p) sqrt(dP) "F (Ips)

4 0.63 0.7937 780 61 . 55 3 0.85 0.9220 782 9 4 .60 2 0.95 0 .97 4 7 781 100 . 1 6 1 0
. 90 0 .9467 780 97.47 4 0.59 0 , 7661 779 76 . 66 3 0 . 64 0 .6000 780 82 . 19 2 0.80 0
.8944 780 91
. 89 1 0
. 80 0 .8944 78 1 91 . 93 4 0.59 0 . 7681 777 78
. 82 3 0
.55 0 . 74 1 6 778 76. 1 3 2 0 . 63 0 . 7937 774 81 . 35 1 0
. 60 0.7746 779 79 . 55 4 059 0 .7 661 780 78 . 92 3 0.60 0 . 7746 781 79.61 2 0
.69 0 .8307 78 1 85
. 38 1 0.79 0
.8888 781 91 . 35 Average 0 . 6947 0
.8335 779
.6 85
. 63

Stack Flow Rate : 735.4 kwacfm Stack F low Ra t e: 27 8 .4 k d scfm Dry Gas Meter Time Vol. T m ( in) T m (out) # / Matl . Start 975.178 80 78 H,O 80 76 H,O End 1 0 1 9.529 80 78 Empty 80 75 SG Tota l 44 . 351 78 .4 Total**NO~** ppm**NO~,** pp m @ 15% O2**NO ~**  fb/MMBtu**NO~** Iblhr CO ppm CO , ppm@ 1 5% O 2 CO Iblh r O2 % Stack F l ow dscfh CT Fue l Flow hscfh Turbine Water I njection gpm



## DlltaAIrqualitySIMCIS 1 8 4 5 N. Case S treet O r

ange, Ca lifornia 92 8 6 5 71 4 -279-6777 CTLoad MW SCR NH3 Inject ion Iblh r NO. Ibl M MSCF CO IblMMBtu CO IblMMSCF TEST VARIABLES Start Date : 211113 Start/End Time : 1 5 :53 17:09 Load (MW)lReplicale# 50 2 Barom . Pressure : 29
.69 Pstack : Pstack: MW:
Analyzer Range Cal Gas Value P r

e-Test D irect Z e ro Pre-T est Direct Span Pre-Test System Zero Pre-Test Svstem Span

Post · Test System Zero Post-Test Svstem Span Post·Test Direct Ze r o Post-Test Direct !?pan Average Carr . results Pre-test zero bias Pre-test span bias Post-lest zero bias Post- test span bias Zero drift §pan drift METHOD 4.1 DATA Impingers End Start Oiff . 787.3 606
.6 160 . 7 706.8 703
.5 3.3 657.8 656A lA 968
.9 958
. 3 10.6

Ir 100 96 .0 RESULTS Ref . M et h CEMS 2.27 2 . 1 0 2.0 5 1
.90 0008 0 .0 1 4
.59 3
.99 0
. 30 0
. 30 0
.27 0
. 25 0.37 0.44 14 . 36 14
. 32 16,701 , 357 15,653,000 5,391



### -



## - 56



### - 1 07 8.52 0.00 1 0 . 64 2 , 10 "9 29.84 'H9 26. 1 0 Ib/lb - mole METHOD 1 00
. 1 DATA 

### 0, CO , NO, CO 20 1 0 5 10 9.98 4
.96 4
.82 4 .49 0
.09 0
. 25 -0.04 -0
.04 1 0.09 5.40 4 .7 4 4.43 0 .21 0 . 31 -0.03 0
. 08 10 .03 5 . 36 4 .69 4 . 39

0 . 2 1 0 . 19 -0.01 0 . 13 10 . 11 5 .24 4.72 4 .38 0 . 10 0 . 1 4 -0
.02 -0 .04 10 . 11 5
. 25 4 . 77 4.43 14.40 4 . 03 2.20 0
.39 1 4.36 3.7 1 2 . 27 0
.30 0 .6% 0 . 6% 0.1% 1.2% -0
. 3% -0.4% -1 .0% -0.4% 0
. 5% 0
.6% 0 . 2% 1 . 7% 0 .0% 0.0% -1.0% -0
. 5% 0 .0% -1 . 1% 0 . 5% 0 .5% 0.4% - 1 .2% 0.5% 0 .0%

Meter Pressure : 1 . 6 iwg Sample Volume : 42.332 dscf H 20 Vo lume : 4. 4 63 scf Moisture Content 9.5 %

Sentinel Uni t 2 50% NOx-NH3·ROG Complianc e .xls 21712013 4 : 18PMCOMPLIANCE TEST DATA AND WORKSHEET CPV Sentinel-2-CEMS -7 5-1 TEST CONSTANTS Station: CPV Sentinel Unit: 2 Performed By : M,SP,SS , JM Cp' 0
.99 Tref : 60 "F Stack Area : 143
. 14 

### f1' MeterY,, : 0
.992 METHOD 2.1 DATA dP Temp Vel. Point (in. H 2O) sqrt(dP) "F ( I ps)

4 0.65 0
.6062 790 63
.05 3 0.61 0
. 9000 769 92
.66 2 0.95 0.97 47 790 100.41 1 1 .20 1
. 0954 790 11 2.85 4 0.66 0
. 8246 766 64
.68 3 0.68 0
.6246 767 84
.85 2 0
. 71 0
.6426 769 86.77 1 0.72 0
. 6465 769 67
.38 4 0.65 0
. 6062 766 82.99 3 0 .72 0.8485 769 67 .38 2 0
. 63 0
.91 1 0 790 93
.65 1 095 0
.9747 790 100.4 1 4 0
. 78 0
.8832 790 90
.98 3 1 .20 1
. 0954 791 112
. 69 2 1 .20 1 .0 954 792 112
. 94 1 1 .00 1 .0 000 792 103.1 0 Average 0.6477 0
.9207 789
. 6 94
.64

Stack Flow Rate : 814
. 5 kwacfm Stack Flow Rate : 306 .8 kdscfm Dry Gas Meter Time Vol

. T m (in) T m( oul) # / Ma ll. Start 822
.650 70.6 72.3 H,O 76
.3 74
.2 H,O End 666
. 694 63
.5 77
.7 Emp ty 69
. 2 84
.7 SG Total 44
. 244 76
. 6 To tal

NO x ppm NO., ppm@ 15% O 2 NO

. IblMMBtu NO K tblhr CO ppm CO , ppm@ 15% O 2 CO I blhr O 2 % Stack F low dscfh CT Fue l Flow hscfh Turb i ne Water I njection gpm



## DB/18All

# qua/flY SBtrlCilS 1845 N

. Case Street Orange, California 92865 714-279- 6777 CTLoad MW SCR NH3 Injectio n Iblhr NOx IbfMMSCF CO IblMMBtu CO IblMMSCF TEST VARIABLES Start Date : 2/1/13 Start/End Time : 9 , 10 10:34 Load (MW)/Repticate# 75 1 Barom

. Pressure : 29
. 69 Pstack : Pstack : MW :

Ana l yze r Range Cal Gas Value Pre-Test Direct Zero Pre-Test Direct Span P re-Test Sys tem Zero Pre-Test System Span

Post-Test System Zero Post -T est System Span Post-Test Direct Zero Post -T est Direct Span Average Corr

. results Pre - test zero bias Pre-test span bias Po s l -test zero bias Post - test span bias Zero drift Span drift METHOD 4
. 1 DATA Impingers End S ta rt Diff

. 859
. 1 660
. 5 178 .6 674.6 671.4 3.2 579.9 579.0 0.9 932.5 922
.6 9
. 9

Ir 100 92.6 RESULTS Ref. Meth CEMS

2.66 2
.50 2.27 1
.96 0
.006 0.007 6.36 5
. 24 0
.47 0.70 0.36 0 .5 1 0
. 63 0
. 73 13.47 1 3.41 18.407 , 808 17 ,635,000



## - 6,912



### -



## - 60



## - 110 9
.23 

## - 0
. 001 

## - 0.66 

## - 2
. 10 iwg 29.64 "H g 26
. 1 6 Jb/l b- mo l e METHOD 100.1 DATA 

### 0, CO, NO, CO 20 10 5 10 9
.96 4
. 96 4 .82 4
.49 0. 1 0 -0
.02 -0
. 02 -0.03 10
. 19 5.05 4.79 4.52 0
. 17 0.11 -0.03 0
. 16 10
.04 5
.06 4 .7 4 4.45

0
. 22 0
. 18 -0 .02 0
. 16 10
. 10 5
. 25 4 .7 1 4.43 0
. 10 0
. 1 3 -0.03 -0
.02 10
.07 5
. 26 4 .7 6 4.45 13
. 53 4.43 2.80 0
.62 1 3.47 4 .2 4 2.66 0.47 0
. 3% 1
. 3% - 0.2% 1.9% -0
. 8% 0 .3 % -1
. 0% -0
. 7% 0
.6% 0
. 5% 0
. 3% 2
.0% 0
. 2% -0
. 1% -0.9% -0
.2% 0
. 3% 0
. 7% 0.2% 0
. 2% 0
. 3% 1
. 7% -0.5% -0. 2%

Meter Pressure : 1 .9 iwg Sample Volume : 42.226 dscf H 20 Volume : 4
. 304 scf Moisture Content: 9
.3 %

Sentinel Un i t 2 75% NOx
- NH3-R OG Complianc e .xls 2(7/2013 4 : 18 PMCOMPLIANCE TEST DATA AND WORKSHEET CPV Sentlnel·2-CEMS·75-2 TEST CONSTANTS Station : CPV Sentinel Unil: 2 Performed By : AA. SP. SS

. JM Cp' 0.99 Tref : 60 'F Stack Area : 143
. 14 ft' MelerYd: 0.992 METHOD 2.1 DATA dP Temp Vel. Point (in

. H 2 O) sQrt(dP) 'F (fps)

4 0
. 73 0
. 8544 797 88,41 3 1
. 20 1
.0954 798 11 3.40 2 1
. 20 1.0954 798 113
.40 1 1.10 1
.0488 799 108
. 62 4 0
. 65 0.8062 796 83.40 3 0.70 0
.8367 796 86.54 2 1.10 1.0488 795 108.45 1 1.20 1
.095 4 794 113 .22 4 0
. 63 0
.7937 795 82
. 07 3 0
. 65 0
. 8062 794 83
.33 2 0
. 63 0
. 7937 794 82
. 04 1 0
. 65 0
. 8062 793 83 .30 4 0.68 0
. 8246 794 85.23 3 0
. 72 0.8485 795 87
. 74 2 0
. 83 0.9 11 0 795 94.20 1 0 .90 0
. 9487 795 98.09 Average 0
. 8343 0.9134 795.5 94.46

Stack Flow Rate : 8 11 .3 kwacfm Stack Flow Rate : 301.4 kdscfm Dry Gas Meter Time Vol. Tm(in) Tm(out) #/Matl. Start 868
. 920 86
. 0 80
. 9 H,O 86.5 80.5 H,O End 917
. 834 85
. 0 77
. 5 Empty 85
. 0 80
. 5 SG Total 48
. 914 82
. 7 Tolal**NO~** ppm**NO~,** ppm@ 1 5% O 2**NO~** IblMMBtu**NO~** Iblhr CO ppm CO, ppm@ 15% O 2 CO Iblhr O 2 

### % Slack Flow dscfh CT Fuel F lo w hscfh Turbine Water Injection gpm



## 8,ItaAhQu.,/tYS,rr1C8I 1845 N

. Case Street Orange, California 92865 7 14-279-6777 CT Load MW SCR NH3 In 'ection Iblhr**NO ~**  IblMMSCF CO IbfMMBtu CO IblMMSCF TEST VARIABLES Start Dale : 211 1 13 Start/End Time : 11 : 05 12 : 15 Load (MW) / Replicate# 75 2 Barom

. Pressure : 29.69 Pstack : Pstack : MW:
Analyzer Range Cal Gas Val ue Pre-Test Direct Zero Pre-Test Direct Span Pre-Test System Zero Pre-Test System Span

Post-Test System Zero Pos t-Test System Span Post-Test Di r ect Zero Post·Test Direct Span Average Carr

. results Pre-test zero bias Pre-test span bias Post-test zero bias Post- test span bias Zero drift Span drift METHOD 4.1 DATA Impingers End Start Diff. 882.4 684
.3 198.1 669.4 666
.4 3
. 0 488
. 5 487
. 5 1
. 0 960
. 9 95 1
. 2 9.7

I , 100 111 ,8 RESULTS Ref

. Meth CEMS 2.78 2
. 50 2
. 16 1 .95 0.008 0
. 007 6 .09 5
. 09 0
. 86 0
. 90 0
. 67 0 .72 1,13 1
. 12 13
.32 13.40 18,083,506 17,671,000



### - 6.936



## - I 80 • 

## - 110 8.78 

## - 0
. 002 

### - 1
.58 

## - 2.10 iwg 29
. 84 "Hg 28
. 06 Ib/lb-mo le METHOD 100.1 DATA 

### 0 , CO, NO, CO 20 10 5 10 9
. 98 4
.96 4
. 82 4,49 0
. 10 0.13 -0
. 03 -0
.02 10
. 07 5.26 4
. 76 4
. 45 0
. 22 0.18 -0
. 02 0
. 18 10
. 1 0 5.25 4.71 4.43

0
. 20 0.25 -0
. 01 0
. 15 1 0
. 12 5
. 32 4
. 71 4
.43 0
. 09 0
. 20 -0.04 -0
. 02 10 .06 5.34 475 4.43 13.41 4
. 55 2.71 0.98 13 .32 4.25 2
. 78 0.86 0
. 6% 0.5% 0
. 3% 2
. 0% 0
.2% .Q

. 1% ·0
. 9% -0
.2% 0
.5% 0
.5% 0
. 6% 1
. 7% 0
.3% -0.2% ·0
. 8% -0
. 1% -0
. 1% 0.7% 0
.3% -0
. 3% 0
. 1% 0.7% .Q

. 1 % 0
. 0%

Meter Pressure: 2 , 1 iwg Sample Volume: 46
. 369 dscf H20 Vol u me : 5
. 197 scf Moisture Conlent: 1 0
. 1 %

Sentinel Unit 2 75% NOx-NH3 · ROG Compl i ance. xis 217/2013 4 : 18 PMCOMPLIAN C E TEST DATA AND WOR K SHEET CPV Sen t in e l- 2 -C EMS-100-1 TEST CONSTANTS Station : CPVSentinel Unit: 2 Performed By : AA. 5P. 55. JM Cp o 0
. 99 Tref : 60 of Stack Area · 143.14 ft' Meter Y,, : 0.992 ME T HOD 2
. 1 DATA dP Temp Vel. Point (in. H2 O) sqrt(dP) of (fps)

4 1.20 1
.0954 773 1 12
. 1 2 3 1
.60 1
. 2649 774 1 29
. 52 2 1
. 60 1.2649 775 129
. 58 1 1.30 1
. 1402 774 116
. 75 4 0
.80 0.8944 775 9 1 .62 3 0.91 0
. 9539 772 97.60 2 1
.30 1
. 1402 772 116
. 66 1 1
.20 1
. 0954 773 112
. 12 4 0
. 70 0
. 8367 770 85
.53 3 0
. 85 0
.9220 770 94.25 2 0
.95 0
.9747 770 99
.64 

# , 1
.00 1
.0000 771 102
. 27 4 0
. 72 0
.8485 772 86.82 3 0
. 74 0
. 8602 771 87.98 2 1.00 1.0000 772 102.31 

# , 1. 1 0 1.0488 772 107
. 31 Average 1
. 0430 1.02 1 3 772
. 3 104.51

Stack Flow Rate : 897
. 5 kwacfm Stack Flow Rate : 339.7 kdscfm Dry Gas Meter Time Vol. Tm(in) Tm(ou t) #/Matl. Start 435.850 81 77 H,O 77.5 72
. 5 H,O End 485
. 200 79 73 Empty 75 72 5G Total 49
. 350 75
. 9 Total**NO~** ppm NO x , ppm @ 15% O 2**NO~** Ib/MM8tu**NO~** Iblhr CO ppm CO , ppm @ 15% O 2 CO Ibfhr O 2 % Stack Flow dscfh CT Fue l Flow hscfh Turb i ne Water Injection gpm



## 881taAIrQua/flY S8nt1CIIS 1 845 N

. Case St ree t Ora n g e , California 92865 7 1 4·27 9· 6777 CT Load MW SCR NH3 Injection Iblhr**NO ~**  IbfMMSCF CO IblMMBtu COlblMM5C F TEST VARIABLES Start Oate : 1/30/13 Start/End Time : 11 :0 1 12 : 17 Load (MW)lReplicate# 1 00 1 Barom. Pressure : 29
.80 Pstack: Pstack: MW:
Analyzer Range Cal Gas Val u e Pre-Test Direct Zero Pre-Test Direct Span Pre-Test System Ze ro Pre-Test System Span

Post-Test System Zero Post-Test Svstem Span Post-Test Direct Zero Post-Test Direct Span Average Carr. results Pre-test zero bi as Pre-test span bias Post - test zero bias PosHest span bias Zero drift Span drift METHOD 4
. 1 DATA Impingers E n d S tart D iff

. 887.1 689
. 3 197.8 669
. 0 6632 5
.8 490
. 3 489
. 9 0
.4 944
. 8 930.4 1 4.4

I, 1 00 118.4 RESULTS Ref

. Meth CEM5

3.34 2.49 0
.009 8
. 25 2.96 2
. 21 4
. 39 12.98 20,384,677

· 8. 4 3B 

## · 

## r

· 1 03 

## · 110 9.78 

## · 0
. 005 

## · 5
. 19 · 2.00 iwg 29.95 "H9 2B.06 I b/lb-mole ME T HOD 100
. 1 DATA 

### 0, CO, NO, CO 20 10 5 10 9
.98 4.96 4
. 82 4
. 49 0
. 10 0
. 10 · 0
.0 1 0
.04 10
.09 5.22 4.76 4
.53 0
. 12 0.12 -0
.01 0.25 10
.09 5
. 22 4.74 4
.53

0
. 12 0
. 15 -0
. 01 0
. 19 9
.99 5
.25 4
. 71 4.49 0
. 10 0
. 12 -0.01 0
.06 9
.94 5.25 4
. 79 4
.54 13
.02 4
.66 3.27 3
. 05 12.98 4. 40 3
. 34 2.96 0
. 1% 0
. 2% 0.0% 2
. 1% 0
. 0% 0
. 0% -0
.5% 0
. 0% 0
. 1% 0.3% 0
.0% 1.3% 0
. 2% 0
.0% -1
.5% -0
. 5% 0
.0% 0
. 3% -0
. 1%

-0
. 6% -0.5% 0.3% -0
.6% -0.3%

Meter Pressure: 1
.8 iwg Sample Volume: 47
. 521 dscf HzOVolume : 5
. 504 scf Moisture Content: 10.4 %

Sentinel U nit 2 1 00% NOx-NH3-ROG Com p liance

. xls 217/ 2 013 4:18 PMCOMPLIANCE TEST DATA AND WORKSHEET CPV Sentlnel-2-CEMS-100-2
Stat i on : Unit: CPV Sentine l 2 Performed By : AA , SP , SS, JM 0
.99 Cp : Tre f : Sta ck Area : Meter

3 0 .90 2 0.99 1
. 30 4 0
. 70 3 0
. 82 2 0.90 0
. 85 4 085 3 1.00 2 1
. 30 1 1
. 50 4 1
. 10 3 1 .50 2 1.60 Average

Flow Rate : I

Time Start 48 6
. 580
E nd 534.400 0.9487 0.9950 1
. 14 02 0
.6367 0
.9055 0
.9487 0.9220 0
.9220 1
.0000 1
. 1402 1
.2247 1
.0488 1
.2247 1 .26 49 60 143 , 14 0
. 992

774 775 776 775 775 776 778 775 776 778 779 777 778 780 

### OF ft'

97
. 1 2

1 01.90 116
.82 85.69 92
. 74 97
. 20 94
. 54 94.42 102.45 116
. 91 125
. 63 1 07
. 50 125 .58 129.81

91 1
. 7 kwaefm

#/Matl

. 69 69 H 2O 69 67 H 2O 67 68 Empty

NO x ppm 3.03 NO x , ppm@ 15% O2 2
.25 NO x IbIMMBtu 0
.008 NO x I blh r 7
.58 CO ppm 2
. 12 CO, ppm@ 15 % O2 1
.58 CO Ib/hr 3
. 18 O 2 % 12
. 97 I Turb in e Water Injectio n gpm CTLoad MW SCR NH3 I Ib/hr NO x Ib/MMSCF 8
. 98 CO I blMMBtu 0
.004 

## 8.118111'QualItY S8111fC6S 1845 N

. Case Street Orange. California 92865 

### 714 ·279·6777 Date : S ta rt/End T i me : 13 : 11 15:05 Load ( MW) / Replicate# 100 2 Ba rom . Pressure : 29
.80 Pstaek: 2.00 iwg Pstaek : 29.95 ·Hg MW:

Pre-test zero bias 0
. 1% 0.3% 0
.0% 1
.3% Pre -les t span bias 0.2% 0
.0% -1
.5%
- 0
. 5% Post-test zero bias 0
. 1% 0 .2% 0
. 2% 2
.0% Post-test span bias 0 ,0% 0
.0% -0.2% 0 .1 % drift 0.0% 0
. 9% 0,2% 0
. 1%

Pressu re : 2
.0 iwg 46 .802 dscf 5.392 sef Content: 10
. 3 %

Sentinel Unit 2100% NOx-NH3 -ROG Compliane e.x ls 217/2013 4 : 18PMPort 

## s 

## s s s s s 

## s s s s s s s s 

## s E E E E E E E E E E E E E E E N N N N N N N N N N N N N N N 

## w w w w 

## w w w w w 

## w w 

## w w w w Average Point 3 3 3 3 3 2 2 2 2 2

3 3 3 3 3 2 2 2 2 2

3 3 3 3 3 2 2 2 2 2

3 3 3 3 3 2 2 2 2 2 Date 2/1/2013 2/1/2013 21112013 211/20 13 211/20 13 211/20 13 211 / 2013 211/2013 211/2013 2/1/2013 2/1/20 13 21112013 2 1 112013 2/ 1 / 2013 21 1 1 2013 211 / 2013 211/20 13 211/2013 2/1/2013 21112013 211 / 2013 21112013 211/20 13 21112013 211/2013 211/20 13 211/2013 2/1/2013 2/1/2013 211120 13 211/2013 211/20 13 21 1

/ 2013 21 1/ 2013 211/2013 211/2013 211/2013 2/1/2013 2/1/2013 21112013 21 1 / 2013 21112 013 21112013 21112013 211/2013 211/2013 211/2013 211/2013 21112013 211/2013 21112013 211/2013 21112013 211/201 3 2/1/2013 2/1/2013 2/1/2013 21 1 1 2013 21 1

/ 2013 211120 13 

## IlIhaA/rOua/1IY SIIMellS 1845 N . Case Street Orange, California 92865 714·279·6777 Time 14 :21 14:22 14 :23 14:24 14:25 14 : 26 14 : 27 14 : 28 14:29 14:30 14:31 14:32 14:33 14:34 14 : 35 14 :40 14:41 14:42 14:43 14:44 14:45 14:46 14 :47 14 :48 14 :49 14 : 50 14:51 14:52 14:53 14:54 15 : 02 15:03 15 : 04 15 :05 15:06 15:07 15:08 15:09 15:10 15:11 15:12 15:13 15:14 15:15 15:16 15:21 15:22 15:23 15 : 24 15 :2 5 15 : 26 15:27 15:2 8 15:29 15:30 15 : 31 15 : 32 15:33 15 : 34 15:35 REFERENCE METHOD 1·MINUTE AVERAGE DATA 14
. 364 4.112 1.941 0.271 14
. 373 14
. 397 14
. 394 14
. 383 14.368 14.368 14.363 14
. 363 14
. 372 14
. 366 14
.38 14.371 14.382 14
. 359 14 .38 14
. 382 14 .3 85 14 .392 14
. 385 14.387 14.391 14.375 14.377 14
. 368 14 . 341 14
. 306 14
. 308 14
. 299 14
. 304 14.35 14
. 345 14 .342 14.349 14.345 14.344 14 .3 45 14 .348 14
. 342 14
. 342 14
. 348 14
. 349 14
. 344 14
. 346 14.345 14.398 14.391 14
. 39 14 .392 14
. 398 14.421 14.434 14.427 14.44 14.427 14.437 14.44 14.462 14.452 14.465 14.38 4.106 4.095 4
. 098 4
. 104 4
. 11 4
. 108 4.113 4.111 4.101 4 .103 4.093 4
. 098 4 .087 4
. 097 4.077 4.076 4.076 4 .07 2 4.074 4.075 4
. 072 4
.083 4
. 081 4.082 4 .098 4.123 4.119 4
. 124 4.124 4.094 4
. 098 4 .104 4.093 4.101

4.1 4 .097 4 .097 4.106 4.106 4 .099 4.096 4
. 101

4.1 4.103 4.071 4.077 4.075 4.073 4
. 07 4.057 4
.053 4
.057 4.05 4
.055 4 .048 4.043 4 .0 31 4
. 037 4
. 03 4.09 1
.949 1
. 798 1 . 759 1
.854 1.937 1
. 909 1.918 1.995 1
.866 2
.007 2
.048 2
.309 1.847 2
. 148 2.178 2.227 2.201 2.127 2.166 2.18 2.155 2
. 263 2 .2 53 2 .1 9 2
. 38 2.492 2.426 2.382 2.437 2
. 286 2.247 2.314 2
. 259 2.256 2.27 2.267 2.236 2.404 2.47 2.219 2.417 2.333 2.326 2.206 2.106 2.197 2
. 127 2
. 109 2
.081 2
.041 1.976 2
.056 2
.012 2.072 2
.083 1.937 1
. 771 1
. 883 1
. 856 2.14 0.274 0
. 288 0
. 299 0
. 284 0.251 0.246 0.223 0 .214 0.222 0.235 0
. 274 0.261 0.244 0.247 0.389 0.387 0.392 0 .386 0.386 0.4 0.424 0.405 0.397 0.417 0.395 0.329 0.343 0.338 0.328 0.402 0.402 0 .397 0.403 0.422 0.406 0.405 0.392 0
. 394 0.379 0.4 06 0
. 388 0.379 0.375 0.393 0.36 0
. 353 0 .367 0.365 0.385 0
. 399 0.413 0
. 396 0.418 0.408 0.4 0.385 0.379 0.383 0.385 0.35 02-ln 13 .7 39 13
. 756 NOx-ln 27.104 26.95 CO-In 37.882 38.289 THe - In 1
.32 1.341 13.768 26.752 39.693 1.475 13 .76 1 26.95 39 .1 94 1.386 13
. 76 27
. 018 38.333 1
.337 13
.768 26
.875 39 .1 91 1.473 13
. 773 26
. 847 39
. 739 1.511 13.766 27.01 38.604 1.405 13.776 26.912 38.716 1.345 13
.766 27.001 38.914 1.313 13
. 78 26.826 39.202 1
. 378 13 .77 3 26.865 40
. 37 1.573 13
. 784 26.862 39.48 1
. 397 13
. 773 27.017 39
.234 1.311 13 .7 62 27
. 12 38.314 1
.239 13
. 763 27.231 38
.224 1.446 13
.766 27.153 38.161 1
. 375 13.77 27.149 37.983 1
. 189 13.773 27.159 38.242 1 .308 13.776 27.08 38.126 1.369 13
.777 27
. 065 38.494 1.366 13
.775 27 .11 3 38.466 1.311 13
.763 27
. 286 37.651 1. 181 13.769 27.161 37.782 1 .243 13.76 27
.208 38
. 142 1
. 233 13
. 746 27.345 37
. 251 1 .05 8 13.761 27.22 37.407 1 .1 26 13
. 758 27.083 38.494 1.199 13 .7 48 27.279 37.513 1.27 13 .7 47 27
. 191 37.852 1.277 13.749 27
. 16 37
.82 1
. 341 13.749 27
. 145 38 .137 1
. 365 13.744 27.248 37 .5 16 1 .2 82 13 .7 55 27.084 38 .054 1.378 13
. 741 27.174 38.146 1.374 13.756 27.057 38.464 1
. 394 13.763 27.067 38.588 1.439 13.744 27.262 38.266 1.278 13 .7 38 27
. 389 36.944 1
. 119 13 .7 47 27
. 242 37.471 1
.259 13 .7 57 27
. 083 38.553 1 .397 13.754 27
. 129 38.348 1
. 331 13
. 732 27.326 37.732 1.287 13
. 742 27.238 37.566 13.736 27.395 37.278 13.722 27.643 35
.563 13.733 27 .5 32 35
. 75 13 .7 34 27
. 582 35.904 13
. 747 27.51 36.075 13 .7 34 27
. 584 36.084 13 .756 27
. 373 36.662 13 .7 38 27.533 36.441 13
. 748 27.469 36.331 13.751 27.408 36.565 13.731 27.576 36.39 13.747 27.493 36
. 357 1.158 1.108 0.959 0.953 1.089 1 .0 91 1.144 1.175 1.105 0.99 1
. 171 1.236 1
. 176 13
. 76 27
. 38536
. 6921
. 163 13.749 27.422 36
. 805 1.226 13
. 755 27.465 36
. 29 1
. 044 13 .75 7 27
. 354 37.083 1
. 056 13.76 27
. 20 37
. 81 Sentinel Unit 2 50% NOx-NH3-ROG Compliance .xls 217/2013 4 :18 PMPort 

## s s 

# s s s s s s 

# s s s s s s s E E E E E E E E E E E E E E E N N N N N N N N N N N N N N N 

## w w w w w w w w 

## w w w w 

## w w 

## w Average Point 3 3 3 3 3 2 2 2 2 2

3 3 3 3 3 2 2 2 2 

### 2

3 3 3 3 3 2 2 2 2 2

3 3 3 3 3 2 2 2 2 2 Oate 21112013 2/1 / 2013 2/1/2013 21112013 211 / 2013 211 / 2013 2/1 / 2013 21112013 2/1/2013 2/1/2013 211 / 2013 211 / 2013 21112013 211 / 2013 211/2013 2/1/2013 211 1 2013 211 / 2013 211 / 2013 211 / 2013 2/1/2013 21112013 2 1 1

/ 2013 211 1 2013 21 112013 211 / 2013 211/2013 21112013 2 1 1

/ 2013 211 1 2013 21 1/ 2013 21 1/ 2013 211 / 2013 211/2013 211 1 2013 21 1/ 2013 21 112013 2 / 1/

2013 21 1 1 2013 211/2013 211 / 2013 211 / 2013 21112013 211 / 2013 211 / 2013 211/20 13 211/2013 211 / 2013 21 1/ 2013 21 1/ 2013 211 / 2013 211/2013 211/2013 2 1 112013 21 112013 21 112013 211 / 2013 211/2013 211/2013 21 1/ 2013 

## Oeh8AlrQual/lyS8rr1C8S 1845 N . Case Street 

### Orange , California 92865 714-279-6777 Time 15 :54 15 :55 15:56 15:57 15 :58 15 :59 16 :00 16 :01 16:02 16:03 16:04 16 :05 16 :06 16 :07 16:08 16:13 16 : 14 16 : 15 16 : 16 16 : 17 16 : 18 16:19 16 : 20 16 : 21 16 : 22 16 : 23 16 : 24 16 : 25 16 : 26 16 : 27 16 : 35 16 :36 16 : 37 16 : 38 16 : 39 16 :40 16 :41 16:42 16:43 16:44 16 :45 16 :46 16 :47 16 :48 16:49 16:55 16:56 16:57 16 :58 16 : 59 17 : 00 17:01 17 :02 17 :03 17 :04 17 :05 17:06 17:07 17 :08 17 :09 REFERENCE METHOD 1-MINUTE AVERAGE DATA 14.396 4
. 056 2
. 033 0.434 14.389 14.407 14.4 14.412 14.439 14.466 14.474 14.46 14.452 14.453 14.473 14.464 14.501 14.474 14.364 14.367 14.356 14.361 14.349 14.344 14.345 14.343 14.353 14.353 14.317 14.319 14.326 14.318 14.323 14
. 383 14
. 367 14.37 14.384 14.4 14.4 14
. 385 14.37 14.367 14.379 14
. 347 14
. 369 14
. 369 14
. 365 14
. 36 14.43 14.435 14.44 14.443 14.439 14.444 1 4 .479 14.462 14.471 14 .463 14.456 14.465 14.484 14.481 14.484 14.40 4
. 062 4.054 4.06 4
. 056 4
. 039 4
. 025 4.02 4
. 028 4
. 03 4
. 027 4
. 017 4
.019 4.003 4.014 4
. 068 4
. 068 4
. 074 4
.071 4
.079 4
.085 4
. 08 4
.084 4
.072 4.077 4.106 4.103 4.099 4
. 104 4
.096 4
.046 4
. 053 4
. 049 4
. 039 4
. 028 4
. 025 4
.03 4
.04 4
. 039 4
. 031 4
. 049 4
.03 4
. 029 4.03 4
. 032 3.985 3
. 981 3
. 978 3
. 974 3
. 978 3.974 3
. 953 3
. 959 3
. 952 3
. 951 3
.953 3
.948 3
. 936 3
. 936 3
. 933 4
. 03 2
. 236 1
. 935 2
. 165 2
. 096 1
. 975 2
.009 1.981 2.012 2
. 038 2
. 074 2
. 067 2
. 128 1
. 96 1
.999 2.428 2.253 2
. 373 2.267 2.331 2.44 2.395 2.381 2.343 2
. 306 2.389 2.486 2.373 2.402 2.39 2
. 326 2
. 394 2
. 32 2
. 232 2
. 309 2
. 223 2
. 294 2
. 31 2
. 392 2
. 266 2
.369 2
. 384 2
. 339 2
. 333 2
. 389 2
. 103 2
.071 2
.008 2
.084 2
. 158 2.177 2.164 2
. 129 2
. 106 2
. 13 1 2
.035 2
. 002 1.936 1
. 945 1
. 937 2
. 20 0.392 0.412 0.418 0.423 0.424 0.431 0.445 0.44 0.441 0.437 0
. 391 0
. 374 0
. 396 0.4 0.336 0
. 345 0
. 343 0
. 352 0.342 0
. 338 0
. 348 0
. 335 0
. 353 0
. 365 0.329 0.333 0
. 338 0
. 325 0
. 34 0.401 0.387 0.37 0
. 384 0
. 392 0.413 0.414

0.4 0
. 373 0.409 0.379 0.394 0.415 0
. 388 0
. 387 0.395 0.4 0.407 0.412 0.422 0.41 0.428 0.444 0.449 0
.456 0
.446 0.413 0.411 0.402 0.408 0 .3 9 02-ln 13.75 13.764 13.761 NOx-ln 27
.261 27.057 27.094 CO-In 37.89 38
. 359 38.81 THC-In 1 . 174 1.273 1.324 13.762 27.066 38.861 1
.352 13
.766 27
.021 39.447 1
. 344 13
.769 27.032 39
.615 1
.256 13
. 785 27
.007 39
.743 1
. 286 13.783 27
.003 39
. 802 1
. 236 13.764 27
. 126 39.609 1.299 13.765 27
. 127 39
. 775 1
. 332 13.764 27
. 344 38.172 1
. 236 13
.761 27.491 37.66 1 .1 97 13
. 786 27
. 105 38.802 1
. 227 13
. 764 27.347 39
. 089 1
. 301 13.761 27.574 37.555 1.142 13.764 27
.674 36.426 1.168 13
.76 27
.699 36.741 1
. 129 13.764 27
.547 36
. 977 1
.223 13
.751 27
.681 36.628 1
. 193 13 .742 27 .711 36.509 1 .08 13.744 27
. 783 35.825 0
. 986 13
. 743 27
. 776 35.943 1
. 054 13
. 761 27
.71 35.932 1
. 143 13
. 765 27.458 36
.674 1
. 145 13
. 765 27
. 344 37
. 616 1.211 13
.765 27
. 398 37.347 1.176 13
.771 27.403 37.194 1.258 13
. 766 27.423 37.223 1.278 13.77 27.431 36
. 923 1
. 105 13
. 772 27
. 575 36
. 663 1.198 13
.767 27
. 549 36
.971 1
. 207 13.774 27
. 57 36.443 1
.246 13
. 80427.33437.4881
.354 13.809 27
.239 38
.064 1.358 13
. 81 27
. 181 38
. 667 1
.344 13.794 27.289 38
. 226 1
. 252 13.783 27
. 383 37
.818 1
. 393 13
. 773 27.448 37
. 199 1.25 13
. 793 27
.282 37.9 1
. 305 13.765 27
.506 37
. 329 1
. 196 13.778 27
. 355 37.432 1
.327 13.777 27
. 355 37
. 657 1. 292 13
. 773 27
. 38 37
. 679 1
. 333 13
. 771 27
.50537.0791.294 13
. 763 27
. 701 35.826 1
.042 13
. 779 27.321 37.866 1.366 13
. 78527
.24938
. 164 1
.271 13
. 787 27
.218 38
. 231 1
. 218 13
.81 27
.052 39.247 1
. 362 13
.785 27
. 163 38.876 1
. 36 13.799 27.17 38.407 1
. 324 13
.803 27.06 39.26 1.48 13
. 795 27.077 39.083 1
. 325 13
. 783 27
. 135 39.192 1
. 376 13.771 27
. 257 38
.655 1
. 3 13.765 27.437 37
. 7 1
. 255 13.765 27
. 313 37.85 1
. 225 13.766 27.313 38.072 1.25 13
.766 27.277 38.207 1.251 13.766 27
.251 38.323 1
. 36 6 13.77 27
. 34 37
. 88
Sentinel Unit 2 50 % NOx-NH3-AOG Compliance

. xis 217/2013 4 : 18 PMPort 

## w w w w w 

## w w w w w w w 

## w w 

## w N N N N N N N N N N N N N N N E E E E E E E E E E E E E E E 

## s s s s s s s s 

## s S S S S S S Average Point Date 3 2/1/2013 3 2/112013 3 2/1/2013 3 2/112013 3 2/112013 2 2/1/2013 2 2/1/2013 2 2 1 1 / 2013 2 2/112013 2 2/1/2013 2/1/2013 2/1 / 2013 2/1/2013 2/11 2013 2/1/2013 3 2/1/2013 3 2/1/2013 3 211/2013 3 2/1/2013 3 2/1/2013 2 2/ 1 / 2013 2 2/ 1 /2 013 2 2/1/2013 2 2/112013 2 2/112013

3 3 3 3 3 2 2 2 2 2

3 3 3 3 3 2 2 2 2 2 2/1/2013 211/2013 2/112013 2/1/2013 2 11/ 2013 2/1/2013 2/1120 13 2/1/20 1 3 2/ 1/ 2013 2/1/2013 2/1/2013 211/2013 2/ 1

/2013 2/112013 2/1/2013 2/ 1 12013 2/112013 2/112013 2/1/2013 2/1/2013 2/1/2013 2/1/2013 211/2013 2/112013 2/ 1

/ 2013 2/ 1

/2 013 2/ 1/2 013 2/1/2013 2111201 3 211/2013 211/2013 211/201 3 211/2013 21112013 211/20 13 

## 88ItaAl,Qual/fY SIlMen 1845 N. Case Street Orange, California 92865 714-279-6777 Time 9:11 9:12 9:13 9:14 9:15 9 : 16 9:17 9:18 9:19 9:20 9 : 21 9 : 22 9 : 23 9 : 24 9 : 25 9:28 9 : 29 9 : 30 9:31 9:32 9:33 9:34 9 : 35 9:36 9:37 9:38 9:39 9:40 9 :41 9 :42 9 :45 9 :46 9 :47 9 :48 9 :49 9 : 50 9:51 9 : 52 9:53 9 :54 9 :5 5 9 : 56 9:57 9:59 10 :00 10 : 20 10:21 10:22 10 :23 10 :24 10 :2 5 10:26 10:27 10:28 10:29 10 :30 10:31 10 : 32 10:33 10 : 34 REFERENCE METHOD 1-MINUTE AVERAGE DATA 

### 0, 13.438 13.45 13.437 13.445 13
.45 13.476 13.486 13.492 13.493 13.494 13.482 13.483 13 .478 13.468 13.471 13.626 13.624 13.627 13.64 13
. 63 13
. 521 13.492 13.4 97 13.467 13.436 13.427 13.43 13.43 13.427 13.428 13.463 13.473 13.491 13
. 508 13.497 13.449 13.421 13.414 1 3.406 13.417 13.424 13.448 13.429 13.422 16.266 13.492 13.493 13.477 13.475 13.478 13.475 13.49 13.488 13.49 13.499 13.487 13.479 13.468 13.473 13.469 13.53 CO, 4.451 4.449 4.455 4 .453 4.453 4.445 4.443 4.441 4.444 4 .445 4.451 4.454 4.457 4.461 4.461 4.359 4.357 4.356 4.348 4.351 4.419 4.436 4.432 4.449 4.462 4.472 4.471 4.468 4.471 4.471 4.449 4.446 4.435 4.426 4.428 4.462 4.482 4.485 4.491 4.484 4.479 4.463 4.475 4.484 2.879 4.48 4.483 4.489 4.492 4.489 4.488 4
.479 4.481 4.481 4.477 4.482 4.488 4.499 4.496 4
. 497 4
.43 NO, 2.847 2
. 84 2
.888 2
.772 2.685 2.716 2.825 2.854 2.911 2.886 2.888 2
. 924 2
. 885 2.813 2
. 816 2.788 2
. 931 2
. 844 2.71 2.788 2.781 2.83 2
.815 2
.875 2
.883 2.954 2.914 2
.866 2
. 838 2
. 777 2
. 886 2.94 1 2.948 2.939 2
. 867 2.701 2.874 2. 79 2
.822 2
.836 2.922 2.707 2.859 2.949 1.897 2.594 2
. 575 2
. 787 2
. 623 2
. 598 2
.665 2
. 649 2
. 753 2.794 2.802 2
. 795 2
.739 2
. 748 2
. 767 2
. 735 2
. 80 CO 0.765 0.773 0.73 0
. 713 0
. 706 0.718 0
. 763 0.752 0.759 0.746 0.746 0
.683 0.636 0.631 0.64 0
.601 0.605 0.615 0.627 0.627 0.645 0.677 0.631 0.631 0.642 0.632 0.621 0.622 0
. 623 0.653 0.488 0
. 507 0.502 0
.475 0.495 0.473 0.409 0.413 0.392 0.403 0.413 0.42 0.416 0.393 0.365 0.733 0
. 698 0.739 0.681 0
.667 0
. 724 0
. 707 0
. 736 0.715 0.702 0.695 0.637 0
.527 0
.601 0
. 634 0.62 02-ln 13 .3 24 13 .3 29 13
. 318 13 .3 36 13
.334 13
. 339 13
. 343 13 .3 44 13.345 13
. 346 13 .3 46 13
.346 13
. 346 13.343 13.345 13 .3 44 13.345 13
. 345 13 .3 42 13.341 13.344 13.344 13
. 344 13
. 345 13
. 342 13
. 339 NOx-ln CO-In THC-In 29.999 51
.869 6
.504 30.002 52.16 4 6
. 678 30.25 49
.41 6.1 30
. 237 49.472 5
. 687 30
. 261 48
. 573 5
.83 30.113 49
.668 6.007 29
.994 52
. 707 6
. 804 29.966 50
.984 6.293 30.064 50.475 6
. 219 30
. 035 50
. 274 6.063 29.968 51.089 6
. 246

30
. 3 49
. 837 6.137 30.245 48 .1 05 5.758 30.278 48
.08 5
.675 30.385 47
. 915 5.711 30.466 46
. 102 5
. 278 30.584 45.441 5
. 243 30.37 47
. 557 5.895 30.393 46
. 574 5.445 30.379 47
.29 5.566 30.225 48.08 5 .71 8 30.216 48
.66 5.738 30.2 8 47
. 917 5.623 30.347 47
.854 5.741 30.353 47
. 533 5.584

30.5 48.207 5.823 13
. 346 30.396 47 .962 5.841 13.342 30.462 46
. 927 5.505 13.343 30
. 297 48
.268 5
. 912 13
.344 30.268 49
. 052 6 .0 6 13.335 30.455 47
. 93 5.76 13
. 344 30.472 46
.5 5.431 13
. 344 30.486 47
. 273 5
. 77 13
.345 30.495 46.707 5.576 13
.342 30.497 47
. 025 5.484 13
. 342 30.504 48
. 292 5.691 13
. 344 3M8 48 .838 6.084 13.333 30.622 46 .853 5.745 13.34 30.669 46
. 952 5.654 13.336 30.658 46
. 727 5
.598 13 .34 5 30
. 534 46.855 5
.524 13 .35 30
.379 48
. 915 5
.981 13
. 339 30
.558 48
. 111 5
.799 13
. 331 30.736 47.053 5
. 65 13.334 30 .70 3 46.979 5.726 13
. 334 30
. 264 48.649 5.441 13.33 1 30.276 47.543 4.97 13.312 30.44 50 .7 25 6
. 144 13
. 319 30.499 46.567 5
. 084 13
.322 30.284 47
. 717 5
. 544 13
. 319 30
. 268 46
. 611 4
. 912 13
. 319 30
. 13 47.982 5 .0 68 13.325 30.242 47.013 4
. 774 13.326 30.208 48
. 217 5
. 269 13.328 30.125 46
. 092 4
. 714 13
. 329 30.159 46
. 179 5.027 13
. 315 30.429 44.313 4.591 13
. 316 30.452 40
. 961 3
. 793 13
. 318 30
. 25 46.279 4
. 94 13 .3 16 30.342 45 .1 57 4
.879 13
. 34 30.34 47.92 Sentinel Unit 2 75% NOx-NH3-ROG Compliance .x ls 217/2013 4:18 PMPort 

## w w w w w w w w w w 

## w w w w w N N N N N N N N N N N N N N N E E E E E E E E E E E E E E E 5 S S S S 

## s s S S S 

## s S S S S Average Point 3 3 3 3 3 2 2 2 2 2

3 3 3 3 3 2 2 2 2 2

3 3 3 3 3 

### 2 2 2 2 2

3 3 3 3 3 2 

### 2 2 2 2 Date 211/2013 211/2013 21112013 21112013 21112013 21112013 2 1 1 / 2013 211 1 2013 211/2013 211/2013 211/2013 211 / 2013 21112013 21112013 21112013 211 / 2013 211 / 2013 211/2013 211/2013 21112013 2 / 1/

2013 211 1 2013 211 / 2013 211 / 2013 211 / 2013 211 / 2013 211/2013 21112013 21112013 211 / 2013 21112013 21112013 21112013 211 / 2013 211 / 2013 2/1/2013 2/1/2013 21112013 21112013 21112013 211 / 2013 21112013 21112013 211 / 2013 211/2013 211/2013 211/2013 211/2013 21 112013 21112013 21112013 211 12 013 211/2013 21112013 211/2013 2/1/2013 2 / 1/2013 211 1 2013 211 / 2013 21 1

/ 2013 

## D.1IaAll

# qua/flY S.MCIIS 1845 N. Case Sireel 

### Orange, California 92865 714-279-6777 REFERENCE METHOD l-MINUTE AVERAGE DATA 11:06 13.44 4.505 2
.647 1
. 73 11:07 11 :08 11 :09 11 : 10 11 : 11 11 : 12 11 : 13 11 :14 11 :15 11 :16 11 :17 11 :1 8 11 : 19 11:20 11 :23 11 :24 11 :25 11 :26 11 :27 11 : 28 11 : 29 11 : 30 11 : 31 11 :32 11 : 33 11:34 11 : 35 11 : 36 11 : 37 11 :43 11 :44 11 :45 11 :46 11 :47 11 :48 11:49 11 : 50 11 : 51 11 : 52 11 :53 11 : 54 11 : 55 11 : 56 11 :57 12:01 1 2:02 12:03 12 :04 12 :05 12 :06 12 :07 12:08 12:09 12:10 12:11 12 : 12 12 : 13 12 : 14 1 2 : 15 13.433 13.432 13.44 13
.45 13.441 13.438 13.445 13.452 13.45 13.444 13.437 13.44 13.437 13.438 13.423 13.425 13.418 13.416 13.41 13.406 13.405 13.404 13.407 13.418 13.409 13.405 13.407 13.412 13.413 13.428 13
.423 13
.422 13.428 13.427 13.43 13.431 13
.434 13.429 13
.428 13.424 13.417 13.413 13.411 13.407 13.391 13.392 13.401 13.381 13
. 387 13
. 382 13.36 13.365 13
. 378 13.372 13.384 13.381 13
.391 13
. 394 13
. 39 13.41 4.516 4.519 4
. 512 4
. 51 4.515 4.517 4.513 4.513 4
. 515 4.52 4
. 524 4
. 522 4
. 521 4
.521 4.531 4.532 4.537 4.537 4
. 543 4 . 545 4
. 547 4
. 545 4
. 541 4.534 4
. 541 4.543 4.543 4.543 4.543 4.537 4
.543 4
. 546 4
. 539 4.539 4.539 4.539 4
.541 4
. 543 4.547 4
.552 4.561 4.567 4
. 57 4.571 4.582 4.587 4
. 583 4
. 595 4
. 594 4
.602 4.615 4
.614 4
. 61 4.615 4
. 605 4
. 608

4
.6 4
.602 4
.608 4.55 2
.65 2
. 754 2
.678 2
. 549 2
. 666 2
. 74 2
. 738 2
. 719 2
. 753 2
. 762 2
. 703 2
. 556 2
.675 2
. 731 2
. 767 2.76 2
. 836 2.772 2.861 2
.893 2.868 2
.842 2
.815 2
. 751 2
. 917 2.667 2.702 2.667 2
.734 2.672 2
.676 2
.609 2.512 2.687 2
.646 2.81 2.704 2
.808 2
. 76 2
. 658 2
.651 2
. 707 2
. 736 2.667 2.615 2.573 2
. 548 2
. 643 2
. 671 2
. 784 2
.848

2.6 2.622 2
. 726 2
. 733 2
. 862 2
. 618 2
. 576 2
. 724 2.71 2.014 1
. 639 1
. 341 1.393 1.715 1.627 1.743 1.627 1.727 1.439 1
. 539 1
. 76 1.605 1.488 1.518 1.669 1.564 1.692 1.909 1
. 693 1
. 159 1
. 095 1
. 273 1
. 317 1
. 17 0.945 1
. 005 1.09 1
. 152 1.039 1
. 098 0
. 949 0
. 97 0
. 853 0
. 848 0
. 871 0
. 821 0
. 812 0
. 761 0
. 754 0
.662 0
. 507 0
. 522 0.497 0.187 0.23 0.217 0
. 185 0
. 16 0
. 183 0
. 125 0
. 102 0.129 0.128 0.171 0.145 0.158 0
. 153 0.147 0.98 02·ln NOx-ln CO-In THe-In 13
. 308 28.739 107
.595 26.957

13
. 3 29.032 115
.202 30. 1 9 13
. 296 29
. 5 92.548 21
. 102 13
. 326 29
.445 74
. 547 13
.655 1 3
. 322 28.71 94
. 037 22
. 019 1 3
. 315 29
. 232 95
. 323 20
.86 13
. 297 28
. 867 10 1. 647 24
. 023 13
. 323 29
. 024 100
. 126 23
. 144 13
. 313 29.298 95
. 121 21
. 555 13
. 321 29
.22 98
.681 22
. 929 13
. 313 29
. 312 87
. 169 18.653

13
. 3 29
. 061 99
.09 23.474 13
. 328 29
. 128 105
. 013 24
.077 13
. 321 29
. 179 99.934 23
. 17 13
. 318 29.27 99
.652 23
.815 13
. 326 29
. 051 101
. 824 23
. 389 13
. 323 29.085 107.064 25
.849 13
. 322 28.807 106
. 946 26
. 343 13.318 28.66 112
. 242 28
.279 13
. 324 28.553 126.77 33.989 13
. 319 29.602 97
. 873 21.071 13
. 311 29.828 78
. 667 16
. 033 13
. 318 29.477 78
. 114 1 5
.8 13
. 325 29
. 351 88.364 19.965 13
. 323 29.425 92
.317 22.339 13
. 319 29.804 67.984 11.727 13.32 29.601 68.443 13.155 13.318 29.464 70.408 13.872 13
. 327 28.981 84
. 936 19
.335 13
. 33 29.358 78
. 027 16.474 13
. 318 29
.643 66
. 384 12
.494

13
.3 30. 1 82 59
. 793 9
. 953 13
. 316 30.139 55
. 33 9
. 305 13
. 318 30.185 56.124 9
. 505 13.315 30.395 48.409 6
.858 13
. 318 30.291 48.56 7
. 219 13.322 30.328 46
. 691 6
.857 13
. 309 30.457 45.08 6.448 13
.31 30.413 44
. 597 6
. 132 13.315 30.586 42.47 5
.524 13
. 307 30
. 513 43
. 225 5
. 82 13
. 315 30.621 39
. 274 4
.627 13
. 309 30.764 33
. 251 2.752 13
. 305 30.707 35.344 3.5 13.315 30.649 34.69 3.314

13.3 30.847 23.7 1.135 13
. 308 30.822 25.729 1
. 326

13
.3 31
. 002 23.716 1
. 137 13
.293 31.122 21
.546 0
. 71 13
.292 31.162 20
.933 0
. 57 13
.291 31
.023 24
.653 1
.462 13
.27 31.403 21.163 0.672 13
. 303 31.075 20.389 0.634 13.287 31.133 21.551 0.827 13.278 31.061 22.458 13
.294 31
. 108 21
.938 0
.779 13
.277 31.323 19
. 982 0
. 518 13.3 31.034 20
. 528 0
.53 13
. 297 31.069 20
.7 0
. 606 13
. 298 31.146 20
. 3 1 6 0
. 563 13.31 29.97 64.24 Sent i nel Unit 2 75% NOx-NH3-ROG Comp l iance. xis 217/2013 4:18 PMPort 

## w w w w w w 

## w w w w w w w 

## w w N N N N N N N N N N N N N N N E E E E E E E E E E E E E E E 

## s s s s
s s 

## s s s s s s s Average Point 3 3 3 3 3 2 2 2 2 2

3 3 3 3 3 2 2 2 2 

### 2

3 3 3 3 3 2 2 2 2 2

3 3 3 3

2 2 2 

### 2 Oate 113012013 113012013 113012013 113 0 12013 113012013 113012013 1130 1 2013 1 13012013 113012013 113012013 113012013 1 130 1 2013 113012013 113012013 113012013 1 130 1 2013 1 13012013 113012013 1 130120 13 113012013 1130120 13 113012013 113012013 113012013 113012013 1 130 1 2013 113012013 113012013 113012013 113 0 1 2013 1130 12 013 113012013 113012013 113 0 120 13 113 0 120 13 113012013 113012013 113012013 1 13012013 113012013 113012013 113012013 1 13012013 1 13012013 113012013 113012013 113012013 1 130 1 2013 1130 1 2013

1 13012013 1 13 0 120 13 113012013 113012013 113012013 1 13012013 1 1

30 1 2013 113012013 113012013 

## DtIII8A1rQuaIIlYSI",clI$ 1845 N. Case Street Orange, California 92865 714-279-6777 Time 11 : 02 11 : 03 11 : 04 11 :05 11 :06 11 : 07 11 : 06 11 :09 11 : 10 11 : 11 11 : 12 11 ;1 3 11 :14 11 :15 11 : 16 1 1 : 27 11 :26 11 :29 11 :30 11 : 31 11 :32 11 :33 11 :34 11 :35 11 : 36 11 : 37 1 1 :36 11 :39 11 :40 11 :41 11 :46 11 :47 11 :46 11 :49 11 :50 11 :5 1 11 :52 11 :53 11 :54 11 :55 1 1 :56 11 :57 11 :56 11 :59 12:00 12:03 12 :04 12 :05 12 :06
12:09 1 2:10 12:11 12: 12 12 : 13 12 : 14 12:15 12:16 12:17 REFERENCE METHOD 1-MINUTE AVERAGE DATA 13
. 106 4.644 3
. 274 3
. 612 13.066 13.091 13.069 13.061 13.074 13 .0 91 13 .0 69 13 .092 13.066 13.069 13 .0 94 13
. 106 13.102 13.093 13 .095 13
. 102 13.11 13.096 13
. 104 13
. 091 13
. 067 13.071 13.061 13
. 052 13
. 043 13.017 13.013 13.016 13
. 006 13
. 056 13 .051 13.061 13
. 062 13
. 064 13.06 13.056 13.051 13
. 033 13
. 012 12.99 12.962 12.979 12
. 975 12
. 956 12 .92 1 12
. 915 12
. 922 12.919
12.696 12
. 905 12
. 691 12
. 692 12.697 12
.666 12
. 666 12 .661 12.677 13.02 4 .65 4.646 4.647 4
.653 4.655 4 .64 4 4.643 4.643 4.646 4.644 4
.641 4.635 4 .636 4
.639 4
.662 4
.663 4 .659 4 .664 4
.657 4
.66 4
.659 4 .667 4 .666 4
.671 4.67 4.675 4.676 4.665 4
.676 4.666 4.666 4.66 4.661 4
.657 4.66 4.656 4.656 4
.656 4
.656 4.667 4.666 4
.662 4
.661 4
.666 4.67 4 .673 4 .666 4
.666

4 .67 9 4
.677 4
. 666 4.667 4.662 4
.694 4
. 691 4
. 696 4
. 696 4.66 3
. 319 3
. 32 3.371 3.362 3.46 3
. 522 3.514 3.477 3.5 3
.437 3.357 3
.262 3.441 3.491 3
.259 3.204 3.166 3.246 3
. 137 3
. 341 3
. 321 3 .329 3.134 3.203 3.249 3.266 3.246 3.236 3.366 3.231 3.253 3.161 3.247 3
. 229 3
. 297 3.332 3.296 3.247 3
. 334 3.247 3.205 3.24 3.251 3.234 3 .096 3.125 3
. 057 2.957
3
. 177 3. 16 3
. 356 3.105 3.212 3 . 341 3 .154 3.267 3.311 3.27 3
. 726 3.763 3.791 3.745 3
. 667 4
.063 3
.961 3 .654 3.902 3
. 637 3
.659 4.022 4.033 3.666 3.134 3 .046 2.906 3.027 3.046 3.144 3.003 2.972 2.911 2
.699 2
. 656 2.91 2.635 2
. 9 2
. 714 3.247 3.307 3.076 3.09 3.096 3.12 3 .173 3.115 3
. 209 3.172 3.014 2 .696 2 .662 2.937 2 .91 6 2.536 2
.564 2
. 602 2.606

2
.046 2.174 2.166 2.153 2 .204 2 .1 14 2 .1 39 2 .035 2.127 3.05 02-ln NOx-ln 13.027 31.705 121.99 22
. 93 13 .006 31.706 119.331 21.613 13.007 31.46 120.927 22
. 063 13.001 31
. 373 121
. 192 22
. 366 12.99 31.476 120 .6 61 22.422 12
.977 31.524 120
. 006 21
. 726 12.991 31.399 123.032 23
. 153 12
. 967 31.626 116.207 21
. 646 12.966 31.601 116.526 20
.969 12.963 31
. 796 116.133 21
. 505 12.966 31.692 116
. 336 21
. 107 12
.997 31.454 122. 6 14 22
. 607 12.996 31.196 126.066 24
. 119 12.995 31.364 130.774 25.41 12.993 31
. 744 116.054 21
. 614 12.994 32.607 11 1.62 1 20
. 053

13 32.651 110.02 19.719 13.009 32.636 1 05.023 16.399 12.996 32.503 109.341 19.641 13.009 32.296 109.762 16.663 13.002 32.366 11 3.377 20.54 12.977 32.592 106.65 19
.059 12 .956 32.674 110.151 20
.006 12.951 32.705 107.414 16 . 22 12.942 32.65 106
.426 16
.771 12.931 32.622 106.013 16
. 761 12.925 32.666 106.304 16.456 12
. 919 32.766 107
.666 16
.766 12.923 32.576 106.246 19
.073 12.912 32.694 102 .1 95 17.493 12.939 32.616 111.534 19
.941 12.939 32.492 113.034 20.464 12.946 32.497 107 .914 19.093 12.95 32.663 107 .236 19
. 173 12.956 32.713 105 .445 16.161 12.944 32.671 105 .6 16.195 12 .935 32.913 104
.66 17
. 421 12 .93 32.902 103.726 17
. 625 12
. 92 32
. 74 105 .60 1 16 .613 12.915 32.677 104.199 17.612 12.693 32.929 104.464 17.459 12.663 33.056 104.353 17
. 503 12.666 33.056 101.123 17
. 166 12.675 32 .9 16 105.176 16.274 12.65 32.996 103.649 17.661 12.626 33.256 97.522 16.402 12 .621 33.096 100
. 253 16
. 66 12
.62 33.066 99
. 925 17
. 316 12
. 621 32.656 99
.669 17
. 257
12.606 33
. 217 95 .1 03 15
. 904 12
.613 32
. 936 96
.956 15
. 943 12.791 33.39 97.446 16
. 294 12.797 33.025 96
. 209 15.966 12.769 33.006 96
. 901 17.067 12.763 33
.27 93.463 15
. 104 12
. 769 32
. 926 97.263 16
.246 12.761 33.51 94.062 15
. 365 12.757 33.333 95
. 644 15.426 12.92 32.52 106
. 31
Sentinel Unit 2100% NOx-NH3·ROG Compliance. xis 217/2013 4:19 PMPort 5 S S S


## s s s
s s s S E E E E
E E E
E E E E N N N N
N N N
N N N N 

### w 

## w w w 

## w w w 

## w w w 

## w w w w 

## w Average Point 3 3 3 3

2 2 2

3 3 3 3

2 2 2

3 3 3 3

2 2 2

3 3 3 3 3 2 2 2 2 2 Date 1 / 3012 0 13 1 / 30

/ 2013 1/30/2013 1 / 30/2013

1 / 30

/ 2013 1 / 30

/2 013 1/30/2013

1 / 30

/ 20 1 3 1 / 30

/ 2013 1 / 30

/ 2013 1/30/2013 1/30/2013 1 / 30

/ 2013 1 / 30

/ 2013 1 / 30

/ 2013
1130/2013 1 / 30

/ 2013 11 30 1 2013
1130 / 2013 1/30/2013 1 / 30/2013 1/

3012 0 13 11 3012013 11 3012 0 13 1130 / 2013 1130/2013

1 / 30

/ 2013 1 / 30

/ 2013 1 / 30/2013

1130 / 2013 1130 / 2013 1 / 30

/ 2013 1 / 30

/ 2013 1 /30/2013 1 / 30

/ 2013 1 / 3012013 1/

3012013 1 / 3012013 1 / 30

/ 2013 1/30/2013 1/30 / 2013 1/

30

/ 2013 11 3012013 1 / 30

/ 2013 1 / 30

/ 20 1 3 1/30/2013 1 / 30/2013 1130 1 2013 

## D,I18A1,QualllY S,rrlC6I 1845 N
. Case Sireel Orange, California 92865 714-279-6777 Time 13 : 12 13 : 13 13 : 14 13 : 15
13 : 18 13 : 19 13 : 20
13 :23 13 : 24 13 : 25 13 :26 13:31 13 : 32 13 : 33 13 : 34
13 : 37 13 : 38 13 : 39
13 :42 13 :43 13 :44 13 :45 14 : 29 14 : 30 14 : 31 14 : 32
14 : 35 14 : 36 14 : 37
14 :40 14 :41 14 :42 14 :43 14 :5 1 14 :52 1 4 : 53 14 :54 14 :55 14 :56 14 : 57 14 : 58 14 : 59 15 :00 15 :01 15 :02 15:03 15 : 04 15 :05 REFERENCE METHOD 1-MINUTE AVERAGE DATA 1 2. 873 4.763 2
. 976 2
. 529 12
. 879 12.862 12.872
12
.868 12.868 12.863
12
.886 12
.882 12
.868 12
.88 12
.886 12
. 889 12
. 891 12
.886
12.895 12
. 911 12
. 915
12.923 12
. 921 12
. 925 12
. 918 12
. 95 12
. 95 12
. 958 12.96
12
. 969 12
. 984 12.979

12
. 98 12
.974 12.973 12.969 12.979 12
.981 12
. 981 12
. 978 12
. 98 12
. 989 12
. 983 12
. 979 12.982 12
. 99 3 12
. 994 12
. 996 12.993 12.996 12.996 12
. 93 4.762 4.775 4
. 772
4
.782 4 . 764 4
. 787
4
. 776 4 . 764 4
. 795 4
. 789 4
. 795 4
. 787 4 .7 89 4 .7 95
4
. 792 4.783 4 .7 84
4.783 4.785 4.782 4
.789 4
.806 4
.809 4
.806 4
.806
4
.805 4.798 4
.804
4
. 807 4
. 812 4.815 4
.82 4
. 819 4.819 4
.818 4
.822 4
.822 4.816 4.823 4.823 4.823 4
.817 4
.817 4.816 4.819 4
. 816 4
. 816 4.80 2.896 3
. 032 2
. 989
2
. 96 9 3
. 001 3
. 089
3
. 113 2
. 967 2
. 975 2
. 984 3
. 135 3
. 089 3
. 16 3
. 134
3
. 082 3
.059 3
.088
2.95 2.987 2.939 2
.914 2
.83 2
.868 2
. 797 2
. 903
2
.896 2.774 2.871
2
.787 2
. 849 2
. 771 2
.829 2
. 953 2
. 919 2
. 864 2
. 989 2
. 951 3
. 051 3
. 053 3
. 103 3
. 167 3. 017 2
. 993 3
. 036 2.969 2
.95 3
.039 2
. 97 2
.642 2.486 2
.645
2
. 1 2 . 227 2
. 242
2.232 2
. 292 2 . 111 2
. 213 2.83 2
.943 2
.679 2
.982
2.943 3.034 2.734
3.031 2.837 3.068 2
.931 1. 951 2
. 089 1.881 1.979

1
. 769 1
. 77
1
. 796 1
. 684 1
. 668 1
. 656 1.927 1.697 1
. 816 1.785 1
. 713 1
. 768 1
. 988 1.815 1
. 926 1
.839 1.741 1
. 762 1.791 1.632 1
.621 2
. 22 02-ln 12.757 12
. 758 NOx-ln 33
.806 33
. 647 CO-In 90
. 76 92.728 THC-In 14.408 14
.825 12
. 752 34
. 016 88
. 842 12.945 12
. 754 33
. 869 93
. 807 14
. 6
12
. 773 33
. 7 92
.09 14
.647 12
. 775 33.41 98
. 843 16
.63 12
. 777 33.524 97.093 14
. 989
12
. 79 33
.682 97
.675 16
.075 12
.803 33
. 554 102.762 16
.603 12.797 33
.865 99
. 041 16
. 349 12.803 33
.626 100.764 16.627 12
. 777 34
.627 90.333 14.122 12
. 789 34
.659 93.374 14
. 561 12
.802 34
. 718 83
.801 12
. 296 12
.79 34.478 93
. 158 14
.967
12.801 34
. 261 92.283 14
. 664 12
.817 34
. 203 94
.009 14.4 12
.815 34.436 84.498 1 2 .6 63
12.832 33.819 97.343 15
. 782 12.839 34
. 014 93.227 14.428 12
.838 33
. 834 101
. 378 16
. 594 1 2
.832 34 .1 01 96
. 702 1 5
. 289 12
.869 34
.653 71
.963 1 0
. 735 12
.873 34
. 81 74.991 11
. 895 12.873 34
.64 68.522 9
. 369 12.888 34.47 75.477 11.402
12
.887 34
. 77 8
.663 12.915 34.468 60.818 7
.968 12.903 34
. 735 60.686 8
.095
12
. 903 34.494 62.488 8
. 242 12
. 888 34
.852 59
. 106 7
. 514 12
. 883 34
. 813 57
. 773 7
. 073 12
. 885 34
. 932 57
. 922 7
. 362 12.884 34.814 63.811 8.915 12
. 878 34.995 55.375 6.724 12
. 877 34
. 80 5 57.066 6
. 975 12
. 882 34
.927 55.592 7
.097 1 2. 877 35
. 139 54
. 355 6
.65 12
. 895 34.839 53.057 6
.01 12
. 878 34
. 931 58.171 7
. 316 12.877 34
. 986 53.845 6
. 177 12
.88 35
. 04 3 56
. 125 6
. 823 1 2. 904 34
. 966 55
. 121 6
. 914 12
. 906 34
. 808 55.775 6
. 618 12
. 894 34
. 839 54.248 5
.966 12
.891 35
. 099 54
.214 6
. 572 12.903 34
. 782 56
.66 7
. 1 12
. 901 34
. 995 53
. 572 6
. 688 12
. 84 34
. 40 77.00
Se ntinel Un it 2100 % NOx-NH3-ROG Compliance. xis 217/2013 4 : 19PM

## Appendix 

## C.2.3 One Minute Data Logger Data

R0410673 

## C-6Date 1/30/2013 1/30/2013 1/30/2013 1 / 30/ 2013 1 / 30/ 2 0 13 1 / 30/ 2013 1/ 30/ 2013 1/ 30/ 2013 1/30/2013 1/30/2013 1/30/2013 1/ 30/2013 1/ 30/ 2013 1/ 30/ 2013 1/ 30/ 2013**~ ~** **N~** 

### W**~ N~**  Ti me % % PPM PPM % PPM 7:19:00 0
. 148 0.237 -0.007

-0.431 0.044 0.177 7:20 :00 0.123 0.091

-0.001 -0.268 0.042 0
. 194 7:21 :00 0
. 119 -0.01 -0.004 0
.007 0.039 0.189 7 : 22 :00

### ~0i;-**:;.,11;,:,8_--; 0:-;** **0;:;1.;.6+...,0;- 0;,0;;;1-t-i;0-;:** **0:i;05;-~0i;-'0i::3;::7,...,** 0
. 192 7 :23 :00**L...0; ~1;;:16:-_-O;.** **:::0;,23;:,..J** 3 .724 0
.008 0.038 3.483 7 : 24 :00 8 .7 83 4
.706 4
. 822 1
. 623 6.427 4
. 876 7 : 25 :00 19 .243 9
. 66 4
. 822 9
. 224 19
. 315 4
.868 7 : 26 :00 18
. 966 9.654 4
. 817 9.56 18
. 96 4.867 7:27 :00 18967 9 65 4 824 9 522 18959 4
.881 7:28 :00 4.889 7:29 :00 1.903 7 : 30 :00 0
. 26 7 : 31 :00 10
. 118 5
.028 0
.063 7
. 835 10
.08 7 0
. 261 7 : 32 :00 10
. 108 5
.022 3.557 4.54 10.071 0
. 257 7 : 33 :00 '"I -:1"0;,:
. 1;04:-....;;5"
.0,;.19:---=3;.;
.7;;;3;;4---,4-:
.4"'95,.....--=1"0"
.0"'7"'"' 0
. 251 1 / 30/2013 7 : 34 :00 10
.078 5
.021 2
. 688 4.506 7.608 0.376 1/30/2013 7 : 35 :00 10
.06 5.022 0.Q15 4.492 0.Q78 0.522 1/30/2013 7:36:00 10
.058 5.019 0.006 4.461 0.036 0.521 1/30/2013 7 : 37 :00 10
.051 5
.016 0.005 4.44 0
.023 1.001 1/ 30/2013 7 : 38 :00 10
.052 5
.01 0
.006 4
.42 0.022 2. 525 1/ 30/ 2013 7:39 :00 10
.053 5
.008 0.009 4.391 0
. 527 0
. 206 1 / 30/ 2013 7 :40 :00 10
.054 5
.004 0
.003 4
. 384 0
.019 0
.047 1 / 30/ 2013 7 :41 :00 10.058 5 0
. 368 4
. 348 0
.02 0.061 1/ 30/ 2013 7 :42 :00 10
.06 4
.996 4
. 854 4.327 0
.0 22 0
.051 1/30/2013 7:43 :00 10
.06 3 4.991 4
. 812 4
. 312 9.929 0
.051 1/30/2013 7:44 :00 10
.068 4.987 4.447 4
. 293 20
. 886 2.001 1/30/2013 7:45 :00 10
.071 4.982 3.035 4.264 20.909 4
.725 1/30/2013 7 :46 :00 10
.079 4
. 977 2.584 4
. 245 20
. 909 4
. 817 1 / 30/ 2013 7 :47 :00 10
.087 4
.974 2.563 4
. 226 20
. 909 4
. 858 1 / 30/ 2013 7 :48 :00 10
.095 4
. 967 2 .445 4
. 206 20
. 908 4
. 868 1/ 30/ 2013 7 :49 :00 10
.098 4
. 961 0
. 879 4
. 189 20
. 908 1.379 1/ 30/ 2013 7 :50:00 10
. 106 4.955 0.4 4
. 161 20
. 907 0
.076 1/30/2013 7 :51 :00 10
. 108 4.947 0
. 297 4
. 132 20
. 907 2
. 614 1/30/2013 7:52:00 10
. 115 4.94 0.277 4
. 117 20.907 3.805 1/30/2013 7:53 :00 10
. 121 4.931 0.251 4
.085 20.865 0.926 1/30/2013 7:54 :00 10
. 128 4.922 0.234 4
.069 20.857 0.063 

### W THe PPM PPM -0.234 0.844 -0.12 0 .85 N2/NOx Mode 0.163 0
. 878 0.154 1.183 NO / NO Mode 0.159 -0 . 649 Ca l Zero 1.549 0
.003 186.631 I 0
.011 ITHe Zefo ; NO/ NO , Mode 245.437 0
.013 244.606 45
. 104 239.82 83.368 NO/NO Mode I 240.102 

# I 83
. 584 Cat High

239.924 83
. 659 N02/ NO Mode 135.45 84
. 321 136
. 159 85
. 1 2 THe H i gh ""'13:';6"'.9;;;5;;;5+-:8;';5;;;.0;:';1;"3.JN02/ NO, Mode ; Mid

119.951 50.231

7.43 46.946 0.13 46
. 84 N02/NO Mode 0.12 46
. 827 0.12 46.809 ITHC Mid 0.112 41
. 305 0 . 114 25 . 588 NOx Cal Zero 0
. 113 25.493 N2/ NO, Mode 0.117 25
.4 ITHC Low 0.138 22.827 NO, Cat High; N2/ NO Mode 0.393 2.682 0.425 2.368 0.424 2.228 NO/NO, Mode 0
.426 2
. 269 NO, Mid 0
. 373 2
. 251 NO/ NO Mode 0
. 362 2
. 163 0
. 358 2.417 N0 2/NO Mode 0.388 2
. 569 0.412 2.503 N02/NO, Mode 0
. 31 2
.499 0.35 2 .481 NOx Cal Zero 1/ 30/ 2013 7 :55 :00 10
. 134 4
. 911 0
. 238 4
.049 19.949 12
.465 17
. 961 10
. 595 78
. 895 19
. 631 1/ 30/ 2013 7 :56 :00 10
. 144 4
. 902 0
. 215 4
.027 16
. 314 46
.049 426.311 1/ 30/ 2013 7 :57 :00 1 0. 144 4
. 894 0
. 296 3
. 999 16
.485 48
. 268 107.835 1 / 30/ 2013 7:58 :00 10
. 144 4.886 0.302 3
. 996 16.491 48.422 7 5
. 577 1/30/2013 7:59 :00 10
. 144 4.879 0
. 354 3
. 969 16
.489 16
.447 76
. 336 1/30/2013 8:00 :00 10
. 144 4.87 0.363 3.948 16.495 22.89 77.537 1/30/2013 8:01:00 10
. 15 4
. 864 0.239 3
. 942 15
. 67 24
. 229 54.812 1/30/2013 8:02:00 10
. 204 4
. 856 0
. 136 3.911 14
.4 2 9 24
. 351 1181.994 1/ 30 / 2013 8 :03:00 13.479 0
. 606 0
.054 3.437 13.408 24
. 327 416.549 1/ 30 / 2013 8 :04 :00 20
. 615 0
.012 0
.027 0
. 861 12.953 45
. 523 23.077 1/ 30/ 2013 8 :05 :00 20
. 655 0 .007 0
.029 0
. 311 12
. 89 47
.436 6
. 214 1/ 30 / 2013 8 :06 :00 20
. 669 0
.006 0
.01 7 0
. 316 12.937 48
. 839 5.759 1 / 30/ 2013 8 :07:00 20
. 682 0
.006 0
.009 0.254 12.835 44
. 136 6.595 1/30/2013 8:08:00 20.622 0
.008 0
.006 0.265 12.886 44
. 211 6.213 1/30/2013 8:09:00 10.229 4.573 0
.001 0.178 10.527 6
. 886 3.529 1/30/2013 8 : 10:00 9
. 993 5
.04 -0.006 -0.288 9.927 0
. 389 -0.207 1/ 30/2013 8 : 11 :00 1,....;9;.;.9;;8"'3--;5;;;.0;,48::---0;;;.;;:00;;;2;.., -0
. 321 9
. 927 0
. 276 -0
. 215 1/ 30/ 2013 8 : 12 :00 3
. 273 1.425 3
. 11 7 -0
.096 5
. 3 25 11.443 0
. 162 1/ 30/ 2013 8 : 13 :00 0
. 149 -0
.004 4
.761 0
. 226 0
.046 24
. 548 0
. 262 1 / 30/ 2013 8 : 14 :00

### 1~0i;-**~12;:;7---;-0:-;.00~5-...,4:" 7;;6,;7--i;0..,;** **2~54::-~0;- 0;;,1;':'6--2~4~** **.5;';5:::8-""0i;- 1~44;7-,**  1/ 30 / 2013 8 : 15 :00 0.127

-0.005 2.348 1.509 0
.014 12
. 531 27.324 1 / 30/2013 8:16 :00 0
. 126 -0.003 -0
.004 4
.412 0
.009 0
. 185 133.067 4.433 NOx Cal High 4
.069 3
. 97 2.292 40 .585 NOx M id

87
. 3 3
. 133 1.259 0
. 838 0.786 0.64 0.428 0
. 101 0 .02 02 bias 0
.068

-0
.01 2 -0 .012 NOx bi as -0
.011 -0
.007

### 0, % CO 2**NO~** CO O2 NO, CO THC Date Time % PPM PPM % PPM PPM PPM 1/30/2013 8:17:00 1/30/2013 8:18:00 1/30/2013 8:19:00 1/30/2013 8 :20 : 00 1/30/2013 8:21 : 00 1/30/2013 8:22 : 00 1/30/2013 8:23:00 1/30/2013 8:24:00 1/30/2013 8:25:00 1/30/2013 8:26:00 1/30/2013 8:27:00 1/30/2013 8:28:00 1/30/2013 8 :29:00 1/30/2013 8:30 :00 1/30/2013 8:31:00 1/30/2013 8:32:00 1/30/2013 8:33:00 1/30/2013 8:34:00 1/30/2013 8:35:00 1/30/2013 8:36:00 1/30/2013 8:37:00 1/30/2013 8:38:00 1/30/2013 8:39:00 1/30/2013 8:40:00 1/30/2013 8:41:00 1/30/2013 8:42:00 1/30/2013 8:43:00 1/30/2013 8:44:00 1/30/2013 8:45 :00 1/30/2013 8:46 : 00 1/30/2013 8 : 47 : 00 1/30/2013 8:48:00 1/30/2013 8:49:00 1/30/2013 8:50:00 1/30/2013 8:51:00 1/30/2013 8:52:00 1/30/2013 8:53:00 1/30/2013 8:54:00 1/30/2013 8:55 : 00 1/30/2013 8:56 : 00 1/30/2013 8:57:00 1/30/2013 8 :58:00 1/30/2013 8:59:00 1/30/2013 9:00:00 1/30/2013 9:01:00 1/30/2013 9:02:00 1/30/2013 9:03:00 1/30/2013 9:04 :00 1/30/2013 9:05:00 1/30/2013 9:06:00 1/30/2013 9:07:00 1/30/2013 9:08:00 1/30/2013 9:09:00 0.126 10.677 20.58 20.607 20.613 20.606 20 .6 21 20 .62 8 20
. 641 20.651 20.656 20.279 13
. 667 13.525 13.517 13.512 13.53 13.528 13.558 13.558 17
. 395 17 .3 09 13.481 13
.477 13
.467 13
.479 13.456 13.43 13.075 17.19 13.111 13 .0 65 13.075 13.08 13.078 13.077 13.085 17
. 945 17 .753 13.096 13.09 13.084 13.093 13.084 13.074 13.072 13
.08 16
.059 20.719 19.863 0.628 0.147 0.124 o -0.001 4.546 0.011 0
. 14 

# I 136.439 

# I -0.007 CO bias 0.023 -0 .002 3.35 8.777 23.792 105.568 0.043 0.022 0 .3 79 14
. 177 23.313 53.357 0
.045 0.018 0.235 13.33 30 .26 42.322 0
. 047 0.D35 0 .2 41 12.74 39 .9 1 22.294 0.05 0.034 0.242 12 .7 68 41 .27 7.437 0.052 0.006 0 .2 43 12 .7 99 41.259 7.192 0.054 0.014 0.231 12.874 40.541 7.445 0.056 0.005 0.228 12.942 38.997 8.36 0.058 0.003 0.22 12.963 37.848 9.584 0.06 0.005 0.211 12.968 38.011 10.17 0.347 0.052 0
. 224 12.972 38.479 9.426 4.212 1.543 0.067 12.969 38.86 9.13 4.232 1.596 0
.092 12
. 97 38
. 924 8.989 4.241 1.588 0.093 12
. 961 38
. 686 9.007 4.249 1.553 0.144 12.961 37.294 9.975 4.24 1.582 0.167 12.962 36.577 11.492 4.246 1.657 0.184 12.962 36.694 11.541 4
. 234 1.644 0
. 198 12.968 36.602 ll.419 4.238 1.681 0.193 12
. 96 36.804 10.95 1.882 0.817 0.192 12.963 36.775 10.923 2.178 0.775 0.163 12.964 36
. 674 10.983 4.292 1.759 0
. 177 12.959 36.785 11.129 4.294 1 .7 82 0.163 12.961 36
. 708 10.835 4.296 1.816 0
. 193 12.962 36.67 11.57 4.29 1.814 0.226 12.962 36 .5 97 11.562 4.299 1.786 0.811 12.955 33
. 904 30.107 4.315 1.872 2.396 12.964 31.932 84.183 4.534 1.944 1.121 12.95 36
. 574 42.257 2.099 0.935 0 .204 12.949 36
. 168 13.295 4.532 2.08 1.177 12
. 96 33 .209 45.589 4.536 2.271 1.94 12
. 96 32
. 751 73.851 4.534 2.273 1
. 846 12
. 961 32.891 70.347 4.533 2.346 1.912 12.968 32.922 69.71 4.538 2.386 1.723 12.963 33.202 66.195 4.538 2.272 1.69 12.977 33.105 66.22 4.535 2.266 1.628 12.989 32
. 955 66.892 1.564 0.905 1.141 12.98 33.094 66.07 1.948 0.803 0
.413 12
. 98 33.097 65.946 4.536 2.376 1.337 12
. 974 33.423 64.144 4.536 2.314 1.228 12.977 33 .6 63 56.081 4.54 2.343 1.118 12.98 33.781 56.524 4.537 2.394 0.693 12.986 34.226 41.641 4.546 2.4 0.604 12.983 34.339 38.9 4.551 2.517 0
. 605 12.99 33.802 45.454 4.553 2.529 0.568 12.978 34.279 46.105 4.55 2.599 0.421 12.983 34.308 36.172 2.684 1.717 0 .37 12.981 34
.448 34.277 0.101 0 .0 15 0 .2 19 12.978 34
.484 34.458 0
. 111 0.012 0
. 257 11.84 33.319 30.49 0.055 0
.006 3.414 0.179 1.295 102.896 0.051 0
.003 4.496 0.026 0.452 136.686 0.049 0
.001 4.507 0.007 0.316 136.62 1/30/2013 9:10:00 4
. 811 2.62 -0.006 3.233 5
. 972 0
. 933 101.55 1/30/2013 9 :11:00 9
. 991 5.122 -0.002 -0.146 9.919 0.271 2
. 538 1/ 30/2013 9 :12 :00

## "1-:;10":'.0;;;1;--':;5c;.1;'::3~2-"";'''0=' -0.339 9
. 923 0
. 246 -0.24 1/30/2013 9 : 13:00 7
. 943 3.928 0.835 -0.299 6.901 6.013 -0.244 1/30/2013 9:14 :00

## "1-;;'0.~17;;5"""'-;0;';.0;;;6~9--4~**~74;;5"""'--;O~.1:;;0-i'1--0;':'.~04~4;-"";24:;'.~38;';6"""'-:::-0.';:;02:::6"'"** 1/30/2013 9:15:00 0.123 0.057 4.759 0.21 0.01 24.443 0.128 0.057 5.151 2.468 2
. 155 0.214 0.161 0.26 0.244 0.299 0.32 0.29 0.298 0.318 Start Strat 0.361 0.227 0
. 334 0.359 0.451 0
. 309 0.279 0.329 0.317 0
. 258 0
. 362 0
. 352 2.696 13.51 6.713 0.452 5
. 173 11.474 10.674 10
. 331 9.615 9.632 9.727 9.606 9
. 622 9.36 7.216 7.553 4.521 4.103 5
.082 5
. 805 3.501 3
. 335 3.173 2
.776 0
. 687 -0.007 -0.007 CO bias 0 .02 1 -0.014 -0 .0 14 02/C0 2 bias -0.015 -0.014 NOx bias -0.014Date Time 1/30/2013 9:16:00 1/30/2013 9:17:00 1/30/2013 9:18:00 1/30/2013 9 : 19:00 1/30 / 2013 9:20:00 1/30 / 2013 9 :21 :00 1/30 / 2013 9:22:00 1/30/2013 9:23:00 1/30/2013 9:24:00 1/30/2013 9:25:00 1/30/2013 9:26:00 1/30/2013 9 :27: 00 1/ 30/2013 9 :28:00 1/ 30 /2013 9 :29: 00 1/30 /2013 9 :30 : 00 1/30/2013 9 :31 : 00 1/30/2013 9:32 : 00 1/30/2013 9:33:00 1/30/2013 9:34 : 00 1/30/2013 9:35 : 00 1/30/2013 9:36 : 00 1/30/2013 9 : 37 : 00 1/30/2013 9 : 38 : 00 1/30/2013 9:39 : 00 1/30/2013 9:40 : 00 1/30/2013 9:41 : 00 1/30/2013 9:42:00 1/30/2013 9:43:00 1/30/2013 9:44 : 00 1/30/20 13 9 : 45 : 00 1/30 / 2013 9 : 46 : 00 1/30 / 2013 9:47 : 00 1/30/2013 9 : 48:00 1/30/2013 9:49 : 00 1/30/2013 9:50 :00 1/30/2013 9:51:00 1/30/2013 9:52:00 1/30/2013 9 :53:00 1/ 30/2013 9 :54:00 1/30/2013 9 :55:00 1/30/2013 9:56:00 1/30/2013 9:57:00 1/30/2013 9:58:00 1/30/2013 9:59:00 1/30/2013 10:00:00 1/30/2013 10:01:00 1/30/2013 10 : 02:00 1 /3 0 / 2013 10 : 03 :00 1/30/2013 10 : 04:00 1/30/2013 10:05:00 1/30/2013 10:06:00 1/30/2013 10:07:00 1/30/2013 10:08:00 1/30/2013 10:09 : 00 1/30/2013 10:10 : 00 1/30 /2013 10 :11 : 00 1/30/2013 10 :12 : 00 1/30/2013 10:13 : 00 1/30/2013 10:14 : 00 

### 0, % 0.123 0
. 122 14
. 836 20.724 20.752 20.748 20.756 20.761 20.723 20
. 757 20
. 731 20.721 20.404 13 .2 76 13
. 104 13
. 103 13
. 10 6 13 .103 13.082 13
. 082 13.083 13.08 13.073 13.057 13
. 061 13.057 13.057 13.057 13
.05 13.054 13.055 13.048 13.056 13
.04 13.052 13.037 13
.037 13.03 13
.044 13.044 13.056 13.063 13.079 13.077

13
. 1 13.114 13
. 119 13
. 126 13.139 13
. 133 13
. 127 13.113 13
. 118 13.086 13
. 06 13.054 13.051 13.036 13.019 CO , % 0.053 0.051 0.079 0.087 0
.088 0.091 0
.089 0.089 0
. 106 0.09 0.102 0.109 0.341 4.529 4.543 4.544 4.542 4.544 4.552 4.554 4
. 552 4.555 4.56 4.568 4 .563 4.566 4.566 4.565 4.571 4.567 4
. 563 4.565 4.559 4.565 4.559 4.566 4.566 4.568 4.565 4.569 4.567 4.571 4.57 4.579 4.575 4
. 574 4.577 4.58 4.576 4.578 4.578 4.583 4.576 4.589 4.6 4.6 4.6 4
. 604 4.606 NO , PPM 4.766 4 .764 1.443 0.012 0.01 0.009 0
.002 0.007 0.017 0.01 0
.017 0
.021 0
.074 3.078 3.114 3
. 148 3
. 022 2
. 974 3.04 3.092 3.054 2
. 996 3
. 144 3.156 3.06 3.068 3.067 3
. 233 3.257 3
. 198 3
. 234 3 .2 27 3.135 3.202 3.089 3.157 3.168 3
. 16 3.061 3.125 3.064 3.158 3.006 3
. 241 3.303 3
. 17 3
. 224 3 .245 3
. 208 3
. 11 3
. 159 3.142 3.028 3.009 3.356 3 .37 4 3
. 386 3.419 3.449 

## co PPM 0.224 0.224 0.218 0.206 0.258 0
. 221 0
. 195 0
. 198 0.204 0.209 0
. 2 0.198 0
. 202 0.086 0.099 0.088 0.131 0.15 0.144 0.206 0
. 272 0
. 317 0
. 274 0
. 238 0.232 0.244 0.225 0
. 253 0.226 0
. 203 0
. 207 0
. 196 0
. 27 0.23 0.278 0
. 308 0.45 0.518 0.564 0
. 655 0
. 668 0.521 0.564 0.579 0.492 0.445 0
. 55 0
. 495 0.51 0.604 0.497 0.512 0
.712 3.37 4
. 229 4 .2 23 4
. 193 4
. 128 4
.087 

### 0 , % 0
.009 0.009 10.284 12.95 12
. 938 12
. 953 12
. 947 12
. 953 12.94 12.949 12.954 12.952 12 .953 12 .952 12
. 955 12.954 12.957 12.956 12 .953 12 .954 12.955 12.951 12
. 936 12.906 12.931 12.939 12.93 12
. 925 12.914 12
. 921 12
. 931 12 .926 12.925 12.929 12.938 12 .927 12.939 12
. 924 12
. 944 12
. 946 12
. 96 12
. 966 12
. 973 12.97 12.991 12.993 13.003 13.007 13.012 13.015 13.004 12.992 12
. 997 12
. 982 12
. 958 12
. 952 12.949 12 .94 12 .921 NO, PPM 24.45 24
.455 31.398 34
.443 35
. 272 35
. 373 35.46 35
. 396 35.633 35.597 35.637 35.496 35 .79 6 36
. 109 36
. 156 36
. 127 35.718 35.637 35.804 35
. 697 35.455 35
.482 35.562 36
. 065 35.886 35.886 35.812 35
. 873 36
. 128 36
. 165 36
.073 36
.04 35
. 793 35
. 871 35
. 647 35
. 702 35
. 549 35
. 376 35
. 151 35
. 181 34
. 953 35
. 209 35
. 005 35.248 35.258 35
. 301 35
. 51 35
. 667 35.542 35.367 35.499 35.547 34.289 30
. 813 30
. 639 30
. 96 31.015 31
. 063 31.127 

## co PPM 0.127 0
. 129 12.904 27.183 18.418 16
. 218 15 .764 15
. 915 15.429 14.409 14.315 14.616 14
.031 12
.097 11 .086 10.942 11.975 13.461 13.953 14.758 17.105 17.601 18 .189 16.0 19 15.454 15.714 15.708 15.844 14.927 14.58 14.423 14
. 343 15
. 949 15.96 17.066 18.854 21.377 23
. 35 25.873 26.879 28.259 25.257 24.967 25.01 24.118 23
. 857 24
. 731 24.558 24
. 892 28.009 25.414 25
. 595 29.34 115
.434 145.171

146.8 144
. 37 142.425 140
. 12 

### THC PPM -0.014 -0.Dl5 1.074 2
. 503 1.013 0
.737 0
. 631 0
. 599 0.555 0.5 0.559 0
. 532 0.434 0.384 0
. 287 0.273 0.34 0.281 0.422 0
. 563 0
. 687 0
. 591 0
. 809 0
. 657 0.548 0.549 0.592 0.544 0
.471 0.522 0
.421 0.413 0
. 571 0.588 0.666 0
.72 1.085 1.301 1.584 1.626 1.644 1.405 1.298 1.453 1.35 1
. 285 1
.411 1.448 1.419 1
. 879 1 .369 1.599 1.672 20
. 991 29
. 835 30.479 29 .27 9 28.46 1 27.835**~ ~** **N~** 00**~ N~**  00 Date Time % % PPM PPM % PPM PPM 1/ 30 / 2013 10 : 15:00 13.04 4
. 601 3
. 385 4
.003 12.946 3 1 .0 81 138
.731 1/ 30/ 2013 10 : 16 :00 13
.046 4
. 603 3
.419 4
.0 2 5 12
. 949 3 1
.419 13 7 .494 1/ 30/ 2013 10 : 17 :00 13
.058 4
. 612 3
. 391 3
. 954 12
. 962 31
. 677 138.22 3 1/30/2013 10:18:00 13.097 4.611 3. 2 9 4
.097 13
.003 31.494 141.094 1/30/2013 10 : 19:00 13.118 4
. 614 3
. 32 4.063 13.029 31
.473 139.47 1/ 30/ 2013 10 : 20:00 13.125 4
. 626 3. 343 4
.097 13.042 31
. 644 141.301 1/ 30 / 2013 10 : 21:00 13
. 138 4
. 629 3
. 38 3 4
.002 13
.062 31 .7 93 136
. 38 1/ 30/ 2013 10 : 22 :00 13.14 4
. 636 3 .2 26 3
. 94 7 13
.065 31 .7 46 134
. 307 1/30/ 2013 10 : 23 :00 13
. 14 3 4.639 3. 217 4
.082 13.081 31.634 139
. 179 1/30/2013 10 : 24:00 13.151 4.638 3.246 4.134 13.084 31.693 140.094 1/30/2013 10 : 25:00 13.16 4
. 637 3
. 328 4.175 13.088 31
.719 144
. 85 7 1/ 30 / 2013 10 : 26 :00 13
. 175 4
. 638 3
.403 4
. 305 13.112 31.541 147
. 861 1/ 30 / 2013 10 : 27 :00 13
. 173 4
. 645 3. 505 4
. 209 13.108 32
.039 143.43 3 1/ 30/ 2013 10 : 28 :00 13
. 186 4
. 64 3 3
. 367 3
. 9 0 6 13. 126 3 2. 27 132
.489 1/30/2013 10 : 29:00 13
. 19 2 4
. 646 3. 335 3.968 13
. 136 32
. 113 133.851 1/30/2013 10:30:00 13.204 4.643 3.368 4.003 13.146 3 1
. 908 137.934 1/ 30/2013 10 : 31 :00 13.204 4
. 645 3.308 4.183 13.147 3 1 .7 87 143
. 126 1/ 3 0/ 2013 10 : 32 :00 13.206 4
. 648 3
. 199 4
. 291 13.146 3 1.569 145
. 338 1/ 30 / 2013 10 : 33 :00 13.19 1 4
. 658 3 .2 68 4 .2 8 13
. 131 31
. 76 7 144
. 151 1 / 30 /2 013 10 : 34:00 13
. 191 4
. 657 3
.415 4
.04 13
. 129 32
. 202 138
. 771 1/30/2013 10 : 35:00 13.188 4.66 3
. 374 3.96 13.13 3 2.257 133
. 335 1/30/2013 10 : 36:00 13.198 4.655 3
. 372 3.964 13.133 32
.096 134
.093 1/ 30/ 2013 10 : 37 :00 6
.722 2
. 181 3
. 9 8 9 3
.081 5
. 806 28
. 859 107.4 0 1 1/ 30 /2 013 10 : 38 :00 0
. 147 0
. 129 4
. 751 0
. 36 0
.05 2 5.566 3
. 938 1 / 30 / 2

0 13 10 : 39 :00 0. 1 28 0
. 124 4
.74 7 0. 247 0
.027 25
. 314 0
. 162 1 / 30 / 2013 10 :40 :00 0
. 128 0.121 4
.744 0.25 1 0
.02 25
. 184 0
. 157 1/30/2013 10 :41:00 0.128 0.12 4
.744 0.246 0.019 25
.08 0.155 1/30/ 2013

### 10**42:001~0;;' ~11:';:5"""--;:O~** **1;;;18;;--':;4-:; 774--;;0;';** **2:::49;;-~0:;- 0;;'1;;;9~--:;274** **7:98;;-~0;;'.;;;15'-';1""** 1/ 30/2 013 10:43 :00 5 .5 4 2 3
. 153 2 .2 06 0
.01 2 6
. 128 11
. 395 0
.003 1/3 0/ 2013 1 0: 44 :00 10
.07 5.216 0

-0
. 309 10
.038 0
. 842 -0
. 239 1/ 30/ 2013 

### 10 :45 :001.-:1;;0;;, .0;,;89"......-;;5,;;.2;; 24;---""0 . ", 00

'"7,...,

-0
. 328 10.058 0
. 75 6 -0.236 1/30/2013 10 :46 :00 4.865 2.341

-0
.004 1.03 4
.006 0
. 68 31.881 1/30/2013 10 :47 :00 0
. 137 0
. 131 -0.009 4.332 0
.032 0.598 133
. 643 1/30/2 013 10 :48 :00 0
. 13 0
. 125 -0
.008 4.526 0
.016 0.529 1 136.515 

## 1 1/ 30/ 2013 10 :49 :00 4 .77 1 3
. 104 2
.47 5 4
. 521 1.977 6 .7 95 134
.76 1 / 3 0/ 2013 10 :50 :00 10 .073 5.22 2 4
.765 4.528 10
.009 24
. 275 135
.454 1/30/ 2013

## 10**51 001.....;1;;;0;;;** **.0 ;,92;;--;;5,;;.2;;2""1--4~** **7;,;64;;--..;4..;.5.;;26;;--;1;;;0;;;.0;;;63;;-....;;. 4;;;** **4~0,;4-.;;13:;;6;;, 4;;6"'8'1**  1/30/2013 10:52 :00 2
. 164 0.977 1.473 2.899 5
. 577 14
. 244 95.702 1/ 30/2013 10 : 53 :00 0
. 108 0
.098 -0
.007 0
. 113 0
.026 0
. 165 1.1 77 1/ 30/ 2013

### 10**54 001~0;;'** **;;;104;i;---;;0"; 0::;96;;--** **;;0 7:OOn.8;---;O;-:** **0:::4:'-~0:;-: 0;;'1~6,.....-;;0-;** **1-i;29;;-~0;;' 0;;;** **~3...,** 1/ 30/ 2013 10 : 55 :00 6
. 813 2
.809 1.585 1.036 5.45 10 .7 07 10
. 335 1/ 30/ 2013 10 : 56 :00 13 .099 4
. 641 3
. 3 3.58 5 13.018 31.902 110.428 1/30/2013 10 : 57:00 13.096 4.651 3
. 372 3.772 13.03 31
. 928 122
. 943 1/30/ 2013 10 : 58:00 13.104 4.65 3
. 338 3
.733 13.03 31.977 122
. 347 1/ 30/ 2013 10 : 59 :00 13.092 4
. 654 3
. 34 5 3
.721 13
.02 31. 904 121.108 1/ 30/ 2013 11 :00:00 13
. 11 2 4
. 644 3.2 86 3
. 8 2 1 13.041 31.677 123.508 1 / 30/2 013 11 :01:00 13.111 4
. 644 3.3 03 3.72 2 13.037 31
. 77 9 118
.43 1/ 30/ 201 3 11 :02 :00 13
. 1 0 8 4.644 3. 274 3
. 812 13
.027 3 1.705 121.99 1/30/2013 11 :03 :00 13
.088 4
. 65 3
. 319 3
. 728 13.006 31. 706 119
. 331 1/ 30/ 2013 11 :04 :00 13.091 4
. 646 3
. 3 2 3
.763 13
.007 31
.46 120
. 927 1/ 30 / 20 13 11 :05 :00 13.089 4 .647 3.37 1 3 .7 91 13
.001 3 1. 37 3 121
. 19 2 1 / 30/ 2013 11 :06 :00 13
.081 4
. 653 3
. 36 2 3 .7 45 12
. 99 3 1.476 120
. 681 1 / 30/ 20 13 11 :07:00 13.074 4
. 655 3 .48 3
. 88 7 12
. 977 31
. 524 120 .00 8 1/30/2013 11 :08:00 13.091 4
. 644 3
. 522 4
.083 12.991 31.399 123.032 1/30/2013 11 :09 :00 13.089 4
. 643 3. 514 3
. 961 12
. 987 31
. 628 118.207 1 / 30/2 013 11 : 10 :00 13
.092 4
. 643 3.4 77 3
. 854 12
. 988 31.801 116.526 1/ 30 / 2013 11 : 11 :00 13.088 4
. 646 3
. 5 3
. 90 2 12
. 983 3 1.798 118
. 13 3 1/ 3 0/2013 11 : 12 :00 13.089 4
. 644 3
.437 3
. 83 7 12
. 986 31.692 118.338 1/ 30 / 20 13 11 : 13 :00 13
.094 4
. 641 3
. 357 3
. 859 12
. 997 31.454 122
. 814 

### TH e PPM 27.37 6 26
. 955 27 .27 5 2 8
. 202 27 .3 97 28
.429 27. 102 26
.0 5 1 27
. 166 27.278 29
. 136 29. 833 28
. 6 7 2 5 .349 2 5. 355 26
. 934 28
. 59 29
. 146 28 .27 3 27
. 13 25
. 294 25.495 22 .0 3 0. 114 -0
.01

-0.01 -0.00 9

-0 .009 NOx bia s -0.01

-0
.01 -0 .009 02 / 00 2 bias -0.008 -0
.00 3

-0 .003 C O bia s

-0
.003 19
. 541 25 . 607 Span direct 25
. 348 25
. 339 25 .051 Zero d i rect 24
. 82 23
. 111 23
. 199 2 2. 488 21 .7 9 2 22
.74 6 21. 70 5 Start NH3 /RAT A Run 1 22
. 93 21
. 613 22
.083 2 2 .3 68 22
.422 21.728 23
. 1 5 3 2 1
. 646 20
. 969 21.505 2 1.107 22
. 80 7

### Date nme 1/30/2013 11:14:00 1/30/2013 11:15:00 1/30/2013 11:16:00 1/ 30/2013 11:17 :00 1/ 30 / 2013 11:18 :00 1/3 0/ 2013 11 : 19 :00 1/ 30 / 2013 11 : 20 :00 1/ 30/2013 11:21 :00 1/30/2013 11:22:00 1/30/2013 11:23:00 1/30/2013 11:24:00 1/30/2013 11 : 25:00 1 / 30/ 2013 11 : 26 :00 1 / 30 / 2013 11 : 27 :00 1 / 30 / 2013 11 : 28 :00 1/ 30/2013 11:29 :00 1/ 30/2013 11 : 30 :00 1/30/2013 11:31 :00 1/30/2013 11:32:00 1/30/2013 11:33 :00 1/30/2013 11:34:00 1/ 3 0/ 2013 11 : 35 :00 1/ 30 / 2013 11 : 36 :00 1/ 30/ 2013 11:37 :00 1/ 30/2013 11:38 :00 1/30/2013 11:39 :00 1/30/2013 11:40:00 1/30/2013 11:41 :00 1/30/2013 11:42 :00 1/ 30/ 2013 11 :43 :00 1/ 30/ 2013 11 :44 :00 1/ 30/ 2013 11 :45 :00 1/ 30/ 2013 11 :46 :00 1/ 30/2013 11 :47 :00 1/30/2013 11:48 :00 1/30/2013 11:49:00 1/30/2013 11:50 :00 1/ 30/ 2013 11:51 :00 1/ 30/ 2013 11 :52 :00 1/ 30/ 2013 11 : 53 :00 1/ 30/ 2013 11 :54 :00 1/ 30/2013 11:55 :00 1/30/2013 11:56 :00 1/30/2013 11:57 :00 1/30/2013 11:58 :00 1/ 30/2013 11:59 :00 1/ 30/ 2013 12:00 :00 1/ 30/ 2013 12 :01:00 1/ 30/ 2013 12 :02 :00 1/ 30/2013 12:03 :00 1/30/2013 12:04 :00 1/30/2013 12:05:00 1/30/2013 12:06:00 1/ 30/2013 12 :07:00 1/ 30/ 2013 12 :08:00 1/ 30 / 2013 12 :09 :00 1/ 30/ 2013 12 : 10 :00 1/ 30/2013 12:11 :00 1/ 30/2013 12 : 12 :00 

### 0 , % 13
. 106 13
. 102 13
.093 18
.07 13
. 137 13.094 13
.044 13
.088 13.087 13.088 13.087 13.087 13
.098 13.095 13.102 13.11 13.096 13
. 104 13.091 13
.087 13.071 13.061 13
.052 13.043 13
.017 13
.013 13.016 13
.008 15
.067 16
.054 13
.066 13.063 13.058 13
.051 13.061 13
.062 13.064 13.06 13
.058 13.051 13.033 13
.012 12
. 99 12.982 12
. 979 12
. 975 12
. 956 15.54 13
.008 12
. 921 12
. 915 12
. 922 12
. 919 12
. 909 12
. 907 12
. 898 12
. 905 12
. 891 12
. 892 

### CO, % 4.635 4.636 4.639 1.699 4
. 642 4
. 64 4
. 666 4.642 4.64 4.642 4.65 4
. 655 4
. 655 4
. 66 2 4
. 663 4.659 4.664 4.657 4.66 4.659 4
. 667 4
. 668 4.671 4.6 7 4.675 4.676 4.665 4.676 3.289 3
.082 4.659 4
. 664 4.666 4.668 4.66 4.661 4.657 4.66 4
. 658 4
. 656 4
. 656 4.658 4.667 4.668 4.662 4.661 4
. 666 3
.093 4
. 664 4.67 4.673 4.666 4.666 4.671 4.672 4
. 679 4
. 677 4.688 4.687 NO , 

### PPM 3
. 262 3.441 3
.491 1.127 3
. 354 3
. 163 3
. 372 3
.068 3
. 102 3
. 229 3
. 242 3
. 226 3
. 187 3
. 259 3
. 204 3
. 186 3
. 246 3
. 137 3
. 341 3
. 321 3
. 329 3
. 134 3
. 203 3
. 249 3
. 288 3
. 248 3.236 3
. 386 2. 457 1.857 3 .2 22 3
. 267 3
. 231 3
. 2 5 3 3.181 3.247 3
. 229 3
. 297 3
. 332 3
. 298 3
. 247 3.334 3.247 3.205 3
. 24 3
. 251 3 .2 34 2
.082 3
.065 3
.096 3.125 3
.057 2
. 957 2
. 976 3
. 139 3
. 177 3
. 16 3
. 356 3
. 105 

## co PPM 4
.022 4.033 3
. 688 1.933 2. 394 3
. 84 2.566 3.368 4.069 3.935 3.903 3
.402 3
. 15 3
. 134 3
.046 2
. 908 3.027 3.048 3.144 3
.003 2.972 2
.911 2
. 899 2
. 856 2.91 2.835 2.9 2.714 2.568 1.461 2
. 944 3
. 102 3
. 247 3
. 307 3
.078 3
.09 3
.098 3
. 12 3
. 173 3
. 115 3
. 209 3.172 3
.014 2.898 2
. 862 2
. 937 2
. 916 2
. 292 2.358 2
. 538 2.584 2.602 2
. 608 2
. 651 2
. 353 2
.048 2
. 174 2.166 2
. 153 

### 0 , % 12.998 12.995 12.993 12
. 991 12
. 979 12
. 985 12
. 944 12
. 988 12.994 12.993 12
. 991 12.983 12.994 12
. 994

13 13
.009 12
. 998 13.009 13.002 12.977 12.958 12
. 951 12
. 942 12
. 931 12
. 925 12
. 919 12.923 12.912 12
. 923 12
. 938 12
. 957 12
. 948 12.939 12
. 939 12.946 12
. 95 12
. 958 12
. 944 12
. 935 12
. 93 12
. 92 12.915 12.893 12.883 12.886 12
. 875 12
. 85 12
. 841 12
. 828 12
. 826 12.821 12.82 12
. 821 12
. 803 12
. 813 12
. 806 12
. 813 12
. 791 12
.797 NO, 

### PPM 31.196 31
. 364 31.744 31.478 32
. 334 31
.448 33
. 246 31
. 396 30.883 31.025 31
. 361 32
. 246 32
. 342 32
. 607 32
. 651 3 2. 636 32.503 32.296 32.366 32
. 592 32
. 674 32
. 705 3 2. 85 32
. 822 32
. 866 32.786 32.576 32.894 32.832 32
. 866 32 .7 81 32
.791 32
. 616 32
.492 32
.497 32.663 32
.713 32
. 871 32
. 913 32
. 902 32
.74 32
. 677 32.929 33.058 33.058 32
. 916 32
. 996 32
. 681 33
.051 33
. 256 33.096 33.066 32
. 658 32.787 32
.725 33
. 217 32
. 938 3 3
. 39 33.025 

### CO PPM 128.068 130.774 118.054 125.962 102.426 134.555 93
. 294 117
. 156 141.297 137.239 136.13 119
. 678 113.337 111.621 110.02 105.023 109
. 341 109.782 113.377 108
. 65 110
. 151 107.414 108
.428 108
.013 108
. 304 107.866 108.248 102
. 195 105.467 108
. 555 106
. 172 105.921 111.534 113.034 107.914 107.236 105.445

105
. 6 104.86 103
. 726 105.801 104.199 104.484 104.353 101.123 105
. 176 103
. 649 100
. 888 104
. 972 97.522 100.253 99.925 99
. 689 102
.499 99
.009 95
. 103 96
. 956 97
.448 96.209 

### THe PPM 24
. 119 25.41 21.614 24
. 304 16
. 593 28
. 154 14
. 74 21
. 573 28
. 124 26
. 823 27
. 151 22
.024 20. 433 20
.053 19
. 719 18
. 399 19.841 18.863 20.54 19
.059 20. 008 18
. 22 18
.771 18
.761 18
.458 18
.788 19.073 17.493 17
.734 18
.794 18
.454 18
.495 19
. 941 20
.484 19
.093 19
. 173 18
. 181 18
. 195 17
.421 17
. 625 18
. 613 17
. 612 17
.459 17.503 17
. 166 18
. 274 17
. 661 16
.703 18
. 37 4 16.402 16
. 88 17.318 17
. 257 17
. 559 16
. 809 15
. 904 15
. 943 16
. 294 15.988O 2 CO 2 NO K CO O 2 NO K Date Time % % PPM PPM % PPM 1/30/2013 12:13:00 12
. 897 4.682 3.212 2.204 12.789 33.008 1/30/2013 12:14:00 12.886 4.694 3.341 2.114 12.763 33.27 1/30/2013 12:15:00 12.886 4.691 3
. 154 2
. 139 12.769 32.928 1/ 30/2013 12:16:00 12
. 881 4
. 696 3 .2 87 2
.035 12 .7 61 33
. 51 1/ 30 / 2013 12:17 :00 12
. 877 4
. 696 3
. 311 2
. 127 12 .7 57 33.333 1/3 0/2013 12 : 18 :00 10
. 975 4.613 1.93 1.976 11
.058 19 .7 81 1/ 30/ 2013 12 : 19 :00 9
. 889 5.24 0 .00 6

-0
. 116 9
. 813 1.788 1/3 0/2013 12:20 :00 9
.067 4.661 0 .2 59 -0
. 337 9
. 802 1.491 

## co PPM 98.901 93.463 97
. 263 94 .0 82 95
. 644 81.79 3.93 -0.238 1/30/2013 12:21 :00 0.287 0
. 166 4
. 674 0.04 9
. 805 1.321 1/30/2013 12:22:00"1

## -0;.'::12~3""''''';0;;;.1:';4:;7-''';4.:;70;';9;'''''''''0::;.1:;9:''1--9;.;80;;5:'-'''';1;;.2**;;1;:'1""** -0
. 284 -0.243 1/30/2013 12:23 :00 0
. 124 0.142 2.385 1.407 4.265 12.347 1/30/2013 12:24 :00 0
. 101 0.138 0
.003 4
. 337 0.D35 25.013 1/3 0/ 2013 12 : 25 :00 0
.099 0.136 -0 .007 4
.494 0.01 25.029 1/30 /2 013 12 : 26 :00 4
. 995 2.914 -0
.003 3
. 156 0
.012 13.421 1/ 30/2013 12 : 27 :00 9
. 883 5.233 -0
.011 -0
. 16 0
.012 0
. 838 1/30/2013**12 :2** **00~:.;9 ;:96:::6:........:5:;;.2~4::.5** __**-O:::::: 0~13::....,**  -0.342 0
.013 0 .7 38 1/30/2013 12 : 29:oo L I....;:9:;:
.9:;:9_....:5:;;.2;,:5;..1
__ - ::::0::::

.0;.11;..J -0.344 0
.012 0 .693 1/30/2013 12:30:00 1.919 1.06 -0.009 -0.296 0.014 0
.457 1/30/2013 12:31:00 0
. 1 0.118

-0.008 -0.038 0.012 0.157 1/30/2013 12:32 :00 0
. 1 0.12 -0.016 0.026 0.012 0.137 -0.233 0
.049 0
.086 24.872 132.462 136
. 145 1 136.466 

## 1

115.002 4.981 

### 1 0.013 1 / 30/ 2013 12 : 33 :00 7
.027 3
. 979 2.43 1
.905 5
.053 10
.742 33.034 1/30/2013 12 : 34 :00 9
. 968 5.255 4
.731 4.452 9
. 937 24.089 134
. 3761 1/3 0/2013 12 : 35 :00 1
.406 0 .7 34 0
. 644 0
. 686 1.321 3.378 21.654 THe PPM 17.067 15
. 104 16
. 248 15
. 365 15
.426 15.539 36.496 40 .776 42
. 512 43.883 NOx bias @ stack , 02 bias @ inlet 44.686 45
. 131 45 . 59 7 NOx bias @ inlet ;CO bia s @ stack 45 .73 1 45
. 875 46 .277 46.744 CO bias inlet ;0 2/C02 bia s Stack 46.433 46.499 ITHe Mid 31.913

-0
.007 -0
.005 ITH e Zero 1
. 189 1 / 30/ 2013 12 : 36 :00 8
. 356 4.986 2.654 0
.015 8
. 344 2.349 0.162 0
. 149 1/30/2013 12:37 :00 9
.96 5
. 332 1.647 2.417 9
. 95 0.406 0.743 -0.145 1/30/2013 12:38:00 9.993 5.27 4.835 4.595 9
. 973 21.77 73.938 -0
.009 1/30/2013 12:39 :00 9.973 5.258 4.798 4.561 9.971 24.333 135.596 -0
.006 1/30/2013 12:40 :00 9
. 967 5.254 4.794 4.545 9
. 947 24.546 135.954

-0 .00 7 1/30/2013

## 12**41 00~1-=9::** **9.:::44;--;:.5.;::2;:.54.;....-.;.4 ;;,7;:.85.;....-.:;4;;.5.:;4:....-:,;9:"** **9~4---=2::4;.:.5,;7::-~13;;5;:; 9;;7;;2,....-** **0;** . .;;00;:.6,.,loire ct Span 1/30/2 013 12 :42 :00 6.984 3.544 3.741 4
. 349 8.915 24.126 133
. 542

-0 .007 1 /30/2 013 12 :43 :00 0
. 13 0
. 122

-0
.008 0
. 642 0
. 139 1
.089 24
. 912 -0.011 1/ 30 / 2013

## 12:44**:00 ~1** **~0;;; 1:,;02;--:;O:.:.1;22;..-.::-O;::** **.0 ;::1::..-0;** **:;05;:8;........;0::; 0.::2::;8:....-0;;.::::11::;9:........:-O;.::0.:,13;..--O;."0.::12;...,loirect**  Zero 1/30/2013 12:45 :00 4
.037 1.678 0.693 0
. 183 2.768 4
. 943 0.78 4
. 321 1/30/2013 12:46:00 12.873 4.706 3
. 102 2
. 134 12.747 33.361 73.769 14
. 291 1/30/2013 12:47:00 12.905 4.708 3.132 2.6 12.78 33
. 222 96.506 15.523 1/30/2013 12 :48:00 12.894 4.717 3
. 186 2.599 12.764 33.304 94.141 15.338 1/30/2013 12 :49:00 12
. 887 4.726 3
. 12 2.553 12.746 33
.028 91.142 14
.025 1/3 0/ 2013 12 :50 :00 12
. 891 4
.722 3
. 105 2.668 12.753 32.751 95.407 15
.423 1/3 0/ 2013 12 :51 :00 12 .8 89 4
.725 3 .0 64 2.503 12 .7 61 32.799 92
. 861 14
.737 1 / 30/ 2013 12 : 52 :00 12.887 4.726 3
. 11 2.726 12 .7 3 32
. 683 101.553 16.97 1/30/ 2013 12 :53 :00 12
. 886 4
.729 3.184 2.589 12 .7 43 33.03 95
. 292 15
. 618 1/ 30/2013 12 :54:00 12
. 889 4.726 3
.072 2.609 12.747 32.948 98.248 16.127 1/30/2013 12:55:00 12
. 893 4.728 3.082 2.645 12
. 732 33.054 98.302 15.83 1/30/2013 12:56:00 12.894 4.728 2.981 2.75 12.735 32.935 101.055 16.648 1/30/2013 12:57:00 12
. 891 4.737 3
. 109 2
. 684 12.729 33
. 379 98.366 16.058 1/ 30/2 013 12:58:00 12
. 893 4.736 3.159 2
.724 12
.734 33
. 204 99
. 627 16 .5 61 1/30/ 2013 12:59 :00 12
. 894 4 .7 4 3
. 199 2 .60 5 12 .72 8 33
. 612 96
. 334 16
. 147 1/30/2013 13:00 :00 12
. 892 4
.741 3
.027 2
. 618 12
. 726 33.395 93.849 14.592 1/30/2013 13:01 :00 12
. 869 4 .7 44 3
. 179 2.611 12
.729 33.423 94.006 15
.062 1/30/2013 13:02:00 12
. 867 4.742 3.024 2
. 673 12.731 33.267 97
. 682 16
.027 1/30/2013 13:03:00 12.862 4.749 3.146 2.817 12.725 33.18 104.783 17.924 1/30/2013 13:04:00 12.859 4.751 3
.058 2
. 556 12.725 33.764 94.044 15
. 362 1/30/2013 13:05 :00 12
. 865 4.75 2
. 977 2.602 12
. 73 33
.472 96.74 15
. 855 1/ 30/2013 13 :06 :00 12
. 852 4
.76 3
.042 2.605 12.725 33
. 832 94.515 14
. 632 1/3 0/ 2013 13:07 :00 12.848 4.764 2
. 948 2.479 12
.726 33
. 833 92
. 154 13 .9 96 1 / 30 /20 13 13 :08 :00 12
. 858 4
.759 2
. 962 2
. 63 12
. 731 33
.461 96 .258 15.49 1/ 30/2013 13 :09 :00 12
. 871 4
.756 2
. 965 2.534 12.754 33.66 91.166 14
. 691 1/ 30/2013 13 : 10 :00 12
. 878 4.755 2
. 901 2.534 12.756 33
.463 92
. 92 14
. 367 1/30/2013 13:11:00 12 .8 65 4.765 2.996 2.56 12.753 33.702 92.731 14
. 646 Start NH3/RATA Run 2Date Time 1/30/2013 13:12:00 1/30/2013 13:13:00 1/30/2013 13:14:00 1/30/2013 13:15 :00 1/30/2013 13: 16 :00 1/30/2013 13:17:00 1/30/2013 13:18:00 1/30/2013 13:19:00 1/30/2013 13:20:00 1/30/2013 13:21:00 1/30/2013 13:22:00 1/30/2013 13:23:00 1/30/2013 13 :2 4:00 1/30/2013 13:25:00 1/30/2013 13:26:00 1/30/2013 13:27:00 1/30/2013 13:28:00 1/30/2013 13:29:00 1/30/2013 13:30:00 1/30/2013 13:31:00 1/30/2013 13:32:00 1/30/2013 13:33:00 1/ 30/2013 13:34:00 1/30/2013 13:35:00 1/30/2013 13:36:00 1/30/2013 13:37:00 1/30/2013 13:38:00 1/30/2013 13:39:00 1/30/2013 13:40:00 1/30/2013 13:41:00 1/30/2013 13:42 :00 1/30/2013 13:43:00 1/30/2013 13:44:00 1/30/2013 13:45:00 1/30/2013 13:46:00 1/30/2013 13:47:00 1/30/2013 13:48:00 1/30/2013 13:49:00 1/30/2013 13:50 :00 1/ 30/2013 13:51 :00 1/30/2013 13:52:00 1/30/2013 13:53 :00 1/30/2013 13:54:00 1/30/2013 13:55:00 1/30/2013 13:56:00 1/30/2013 13:57:00 1/30/2013 13:58:00 1/30/2013 13:59:00 1/30/2013 14:00:00 1/30/2013 14:01:00 1/30/2013 14:02:00 1/30/2013 14:03:00 1/30/2013 14:04:00 1/30/2013 14:05:00 1/30/2013 14:06 :00 1/30/2013 14:07 :00 1/ 30/2013 14:08:00 1/30/2013 14:09:00 1/30/2013 14:10:00 

### 0, % 12.873 12.879 12.862 12
. 872 12.881 12
. 877 12 .8 68 12.868 12.863 12.871 12.885 12.886 12.882 12
. 868 12 .8 8 16
. 677 13.13 12.915 12.885 12.886 12.889 12
. 891 12
. 886 12
. 886 12
. 888 12
. 895 12
. 911 12.915 12
. 933 12.917 12 .923 12.921 12.925 12.918 12.928 16.213 13.322 13 .306 13.633 15
.063 15
. 99 14.969 14.009 13.798 13.802 13.798 13.794 13 .795 13.796 13
.78 13.768 13.753 13.75 13.754 13 .7 55 13.755 13
. 812 14
. 618 15.595 CO, % 4.763 4.762 4.775 4.772 4.77 4.775 4.782 4.784 4.787 4.785 4.78 4
.776 4.784 4.795 4.789 2.436 4.734 4.762 4.796 4.795 4.787 4.789 4.795 4 .7 98 4.794 4.792 4.783 4.784 4.774 4.783 4.783 4.785 4.782 4.789 4.783 2.832 4.544 4.552 4.355 3.487 2.948 3.572 4.142 4.268 4.262 4.269 4.275 4.277 4.275 4.281 4.284 4.289 4.293 4.287 4.286 4
. 284 4.247 3.757 3.176 NO, PPM 2.976 2.896 3.032 2.989 2
. 923 2.925 2
. 969 3 .00 1 3.089 2.995 2
. 925 3.113 2
. 967 2.975 2.984 1
. 603 2.844 3.011 3 .2 52 3.135 3
.089 3
. 16 3.134 3.124 3.044 3.082 3.059 3.088 3.014 3.144 2 .9 5 2.987 2.939 2.914 2.962 2.76



### 5 5 4
. 631 3
. 186 2.646 4.447

5 5 4.779



### 5 4.938 3
.992

5 5 3.795 3.934

5 

### 5 5 5 5 4.484 1.838 

## co PPM 2.529 2.642 2.486 2.645 2.548 2.663 2.1 2.227 2.242 2.142 2.218 2.232 2.292 2.111 2
. 213 1.739 2.292 3.217 2.847 2.83 2.943 2.679 2.982 2.775 2
.725 2.943 3.034 2.734 3.188 3.032 3 .03 1 2.837 3.068 2.931 3.089 1.51 -0.054 -0.065 -0.065 -0.022 0.009 -0.034 -0.066 -0.069 -0.064 -0.076 -0.077 -0 .07 3 -0 .052 -0.073 -0.074 -0.Q75 -0.087 -0.091 -o.Q78 -0 .09 6 -0.096 -o.Q78 0.Q28 

### 0, % 12.757 12.758 12.752 12.754 12.768 12 .77 5 12 .773 12.775 12.777 12.778 12.786 12 .7 9 12.803 12.797 12.803 12.808 12.82 12.815 12.771 12.777 12.789 12.802 12.79 12 .7 88 12.788 12.801 12.817 12.815 12.834 12
. 826 12
. 832 12.839 12.838 12.832 12.845 13.001 13.215 13.191 13.666 14 .656 15.085 14.232 13.405 13.253 13.279 13.263 13.248 13.247 13.251 13.249 13.249 13.247 13.246 13.26 13.245 13.266 13.358 14.163 14
. 92 NO, PPM 33.806 33.647 34.016 33.869 33.867 33.504 33
. 7 33.41 33.524 33.748 33.615 33.682 33.554 33
. 865 33 .6 26 33
. 92 33.719 33.737 34.849 34.627 34.659 34.718 34.478 34.723 34
. 655 34.261 34.203 34.436 33.68 34 .06 8 33.819 34.014 33.834 34.101 33.709 41.253 49
. 998 49
. 998 49.998 49
. 815 46.381 49.998 49.998 49.998 49.998 49 .9 98 49.998 49.998 45.241 49.998 34.265 43.544 49.998 49
. 998 49
. 998 49.998 49.998 45.508 49
. 593 

## co PPM 90.76 92.728 88.842 93.807 90.637 96.398 92.09 98.843 97.093 93.293 98.398 97.675 102.762 99.041 100.764 101.129 98.506 104.192 91.151 90.333 93.374 83.801 93.158 86.678 84.488 92.283 94.009 84.498 98.575 94.572 97.343 93.227 101.378 96.702 102.503 87.729 9.633 4.388 4.958 8.838 15.77 10.426 5.854 4.382 4.165 4.244 4.191 4.165 4.132 4.09 4.052 4.12 4.092 4.113 4.092 4.098 4.147 6.116 11.247 

### THC PPM 14.408 14.825 12.945

14 .6 14
.007 15.562 14.647 16.63 14.989 14.371 16.304 16.075 16.603 16
. 349 16.627 17.336 15.643 17.782 14.584 14.122 14.561 12.296 14
. 967 13.277 12.67 14.664 14.4 12.663 16
. 258 14.45 15
. 782 14.428 16.594 15.289 17.179 15
. 183 0.824 0.193 0
. 108 0.099 0.097 0.052 0.069 0.114 0
.048 0
. 12 0
.094 0.031 0.Q35 0
.077 0.122 0.113 0.091 0.036 0.039 0.003 -0.007

-0
.014 -0.013Date Time 1/30/2013 14 : 11:00 1/30/2013 14:12:00 1/30/2013 14:13:00 1/ 30/2013 14 : 14:00 1/ 30 / 2013 14 : 15 :00 1/ 30 / 2013 14:16:00 1/ 30/ 2013 14:17 :00 1/30/2013 14 : 18:00 1/30/2013 14:19:00 1/30/2013 14:20:00 1/30/2013 14:21:00 1/30/2013 14:22:00 1/30/2013 14:23 :00 1/ 30/2013 14:24 :00 1/30 / 2013 14 :25:00 1/30/2013 14:26:00 1/30/2013 14:27 :00 1/30/2013 14:28:00 1/30/2013 14:29:00 1/30/2013 14 :30:00 1/30/2013 14:31 :00 1/30/2013 14 : 32 :00 1/ 30/ 2013 14 : 33 :00 1/ 30/ 2013 14:34 :00 1/30/2013 14:35 :00 1/30/2013 14 :36:00 1/30/2013 14 : 37 :00 1/30/2013 14 :38:00 1/30/2013 14 :39:00 1/ 30/ 2013 14 :40 :00 1/30/ 2013 14 :41 :00 1 /30/2013 14 :42:00 1/30/2013 14 :43:00 1/30/2013 14 :44:00 1/30/2013 14:45 :00 1/30/2013 14 :46:00 1/30/2013 14:47:00 1/30/2013 14:48:00 1/30/2013 14 :49:00 1/30/2013 14 : 50 :00 1/30/2013 14:51:00 1/30/2013 14:52:00 1/30/2013 14:53:00 1/30/2013 14:54:00 1/30/2013 14:55 :00 1/30/2013 14:56 :00 1/ 30/2013 14 : 57 :00 1/30/2013 14 :58:00 1 /3 0/ 2013 14:59 :00 1/30/2013 15 :00:00 1/30/2013 15:01:00 1/30/2013 15:02 :00 1/30/2013 15 :03:00 1/30/2013 15 :04:00 1/30/2013 15 :05:00 1/30/2013 15 :06 :00 1/30/2013 15 :07 :00 1/30/2013 15 :08:00 1 /30/20 13 15:09 :00 

### 0, % 15.515 14.527 13.551 13.312 13
. 31 13
. 328 13
. 324 13
. 332 13.305 13.324 13.036 12.956 12
. 955 12
. 95 12
. 944 12.957 12.96 12.961 12.95 12.95 12
. 958 12.96 12
. 964 12
. 97 12.969 12.984 12.979 12
. 971 12
. 969 12.98 12
. 974 12
.973 12.969 17
. 286 20.618 20.632 20
. 639 18.859 13 .0 22 12
. 985 12
. 979 1 2.981 12.981 12.978 12
. 98 12
. 989 12
. 983 12
. 979 12
. 982 12
. 993 12.994 12.996 12
. 993 12
. 996 12
. 996 16
. 887 20
. 625 20.623 19
.048 

### CO, % 3.233 3.832 4.417 4.553 4.555 4
. 547 4.551 4.547 4.567 4.559 4.74 4 .79 4
.791 4
.795

4.8 4.795 4.797 4.795 4.806 4.809 4.806 4.806 4
. 806 4.803 4.805 4.798 4.804 4.81 4
. 813 4
. 807 4.812 4.815 4.82 2.205 0.299 0
. 29 0.289 1.393 4.797 4
. 812 4
. 819 4.819 4.818 4.822 4.822 4.816 4.823 4.823 4.823 4.817 4.817 4.816 4
. 819 4.816 4.816 2
.455 0
. 308 0.309 1.04 NO, PPM 2.761 1.547 4 .43 2.86 2.6C5 2.562 2.439 2.431 2.496 2.471 2.342 2.621 2
.763 2
.731 2
. 802 2
.79 2.849 2.775 2.83 2.868 2
.797 2
. 903 2
. 808 2.88 2
. 896 2
. 774 2.871 2
. 853 2
. 855 2
.787 2.849 2 .77 1 2
. 829 1.422 0.039 0.029 0.029 0.566 2.829 2
. 931 2.953 2.919 2.864 2.989 2
. 951 3
.051 3
.053 3
. 103 3.167 3.017 2.993 3.036 2
. 969 2.95 3.039 1
. 676 0
.029 0.027 0.021 

## co PPM -{).013 0.532 1.299 4.273 3
. 941 3
. 695 2.854 2.893 2.794 2.469 2.71 2.568 2.187 2
.443 2
. 205 2.318 1.985 2.063 1.951 2
.089 1.881 1.979 1.929 1.936 1.927 1.769 1.77 1.645 1.649 1
.796 1.684 1
. 668 1.656 1.042 0.198 0.166 0.163 0
. 247 1
.473 1
. 835 1.927 1.697 1.816 1.785 1.713 1.768 1.988 1.815 1.926 1.839 1.741 1.762 1.791 1.632 1.621 1
. 237 0
. 187 0.151 0.182 

### 0, % 14.82 13.892 13.057 12.896 12
. 883 12
. 895 12.888 12.911 12.868 12.873 12
. 895 12.88 12
. 885 12.882 12.872 12
. 89 12
. 881 12
. 894 12.869 12.873 12.873 12.888 12
. 881 12
. 882 12.887 12.915 12.903 12.887 12.893 12
. 903 12.888 12
. 883 12.885 12.88 12.882 12.883 12.874 12.872 12
. 887 12 .898 12.884 12.878 12.877 12.882 12.877 12
. 895 12
. 878 12
. 877 12
. 88 12
. 904 12.906 12.894 12.891 12.903 12.901 12
. 899 12
. 906 12
. 92 12.278 NO, PPM 43
.062 26.093 31.928 33.043 33
. 7 34
. 193 34
. 683 34
. 313 34.837 34.937 34.246 34.378 34
. 567 34
. 258 34
. 614 34
.473 34.715 34.444 34.653 34
. 81 34
. 64 34
.47 34.579 34.6C6 34.77 34.468 34.735 34.812 34.785 34
.494 34
. 852 34.813 34.932 34.995 35.017 35.012 35.066 35
. 103 34
. 857 34
. 612 34
. 814 34.995 34
. 805 34.927 35.139 34.839 34.931 34.986 35
.043 34.966 34.808 34.839 35.099 34
.782 34
. 995 34
. 992 35.022 34
.738 32.537 

## co PPM 14.218 5l.l71 64.53 143.529 127
. 951 116.359 87.616 91.226 88.547 72.603 86.546 90
. 918 78.833 89.338 80.619 85.71 70.621 72.43 71.963 74.991 68
. 522 75
.477 68 .7 43 65.114 64.683 60.818 60.686 58.213 58.864 62
.488 59.106 57.773 57.922 54.937 57.208 53.57 54.694 53.709 53 .487 60.309 63.811 55.375 57.066 55.592 54.355 53.057 58.171 53.845 56.125 55.121 55.775 54.248 54.214 56
. 66 53.572 55
. 185 53.064 55.692 57.411 

### THe PPM -0.001 2.872 6
. 836 28
.07 22
. 805 19
. 915 13.244 14
. 942 13.937 10
. 373 13
. 965 15
. 333 12
.054 14
.053 12
.059 14
. 246 10
.097 10 .521 10.735 11
. 895 9
. 369 11.402 9 .7 13 8
. 936 8.663 7.968 8.095 7.343 7.645 8 .242 7.514 7
.073 7.362 6
. 876 7.255 6.527 6.943 6.447 6
.457 7
. 703 8.915 6
.724 6.975 7.097 6.65 6.01 7
. 316 6
. 1 77 6.823 6
. 914 6.618 5
. 966 6.572 7.1 6
. 688 6.52 6.41 6
. 824 7.041**~ ~** **N~** 00**~ N~**  00**~C** Date Time % % PPM PPM % PPM PPM PPM 1/30/2013 15:10:00 10.036 5.36 0.004 -0.201 9.918 l.758 17.447 1.929 1/30/2013 15:11:00"1"':9::::.;'::964;';"-";5;';.3:::7;"7---;;'0;;'.0"'02:"'" -0.359 '-9:;;.:;;91;'7;--:1;';.0"8;;'6"" -0.306 -0.017 02/002 bias 1/30/2013 15:12:00 16.338 2.224 0.01 -0.213 3.684 14.266 0.053 0.027 1/30/2013 15:13:00 12.508 0.599 1.549 0
.086 0.044 24.937 0.008 -0.016 1/30/2013 15:14:00 0.154 0.243 4.753 0.176 0.027 24.897 -0.068 1/30/2013 15: 15 :00"1

## -0;;;.~12:';2~""'::0:;'.2;':4::--4;;':.=75;':9~-:0::';.1:;'9;;'7**--0;;;.;;:02,;6,.....~24;:..84~3-....:,-o::.;.0:::2:....,** -0.016 -0.017 NOx bias 1/30/2013 15:16:00 0.122 0.237 2.117 1.694 0 .026 10.892 37.806 -0.016 1/30/2013 15:17:00 0.109 0.237 -0.005 4.4 0.023 0.588 133.628 -0.012 1/30/2013 15:18:00 0.096 0.236 -0.003 4.48 0.023 0.492 1 134.928 

## 1 -0.012 CO bias 1/30/2013 15:19:00 8.023 4.462 3.087 4.465 6.784 15
. 357 120.254 1.337 1/30/2013 15:20 :00 9.962 5.376 4.774 4.483 9.916 24.314 131.986 6.634 1/30/2013 15 : 21:00
.. 1....;;9."9;:.63;--5;:.."37.;,7;--4'"
. .;,76;,9;--4'"
. .;.47:;;1;--;9;;.9;;.1;;9;-....;;2.;.4."3;;.33;--1;;3:,::5;.;.0:,::5"8.,1 6.217 Direct Span 1/30/2013 15:22:00 1.72 1.025 1.337 2.601 4.425 12.006 99.079 5.908 1/30/2013 15:23:00 0.097 0.22 -0.007 0.071 0.027 -0 .0 34 2.183 7.536 1/30/2013 15:24:00 L 

# I**_0~.0::;9;;:6;--;i0:.;.2::;2;;-~-;:.0.;;;0~13;--;i-0::;.00~1**__

## 0~.0;;:2;:;5~~-0~.0~6::;4_-:-~0.::;;06~4~ 1/30/2013 15:25:00 15.27 0.268 0.002 0.075 8.328 21.908 15.959 1/30/2013 15:26:00 20.671 0.28 -0.008 0.135 12.853 34.665 54.829 1/30/2013 15:27:00 20.664 0.291 0.002 0.142 12.876 34.328 60.801 1/30/2013 15:28:00 16.858 2.556 1.397 0
.446 12.867 34.775 59.342 1/30/2013 15:29:00 12
. 999 4.818 2.92 1.566 12.861 34.912 57.861 1/30/2013 15:30:00 12.985 4.829 2.916 1.626 12.859 34.99 55.125 1/30/2013 15:31:00 12.986 4.832 2.891 1.845 12.869 34.74 62.078 1/30/2013 15:32:00 12.986 4.834 2.998 1.911 12.871 34.753 64.065 1/30/2013 15:33:00 12.975 4.841 2.992 2.075 12.864 34
. 572 67.739 1/30/2013 15:34:00 12.974 4.845 3.099 1.969 12.857 35.123 63.355 1/30/2013 15:35:00 12.983 4.839 2.899 2.003 12.873 34.573 69.013 1/30/2013 15:36:00 12.971 4.847 2.909 2.048 12.858 35.013 67.871 1/30/2013 15:37:00 12.963 4.855 2.986 2.098 12.849 34.952 68.574 1/30/2013 15:38:00 12.973 4.85 2
. 936 1.769 12.854 35.348 62.83 1/30/2013 15:39:00 12.964 4.856 3.027 1.577 12.849 35.665 53.688 1/30/2013 15:40:00 12.964 4.857 2.915 1
. 823 12.849 35.207 57.744 1/30/2013 15:41:00 12.963 4.856 2.977 1.766 12
. 846 35.407 60.532 1/30/2013 15:42:00 12
. 957 4.862 3.024 1.994 12.837 35.155 65.095 1/30/2013 15:43:00 12.954 4.863 3.021 2.159 12
. 834 35.107 69.023 1/30/2013 15:44:00 12
. 962 4.858 2.946 2.365 12.856 34.594 70.946 1/30/2013 15:45:00 12.959 4.861 3.036 2.622 12.841 34.478 82.941 1/30/2013 15:46:00 12.962 4.859 3.01 2.617 12.854 34.567 80.973 1/30/2013 15:47 :00 12.952 4.863 3.046 2.681 12.841 34.536 84.374 1/30/2013 15:48 :00 12.965 4.855 3.047 2.586 12.861 34.555 81.331 1/30/2013 15:49:00 12.957 4.864 3.152 2.853 12.834 34.574 82.496 1/30/2013 15:50:00 12.969 4.852 3.121 2.835 12.858 34.68 82.876 1/30/2013 15:51:00 12.958 4.858 3.193 2.669 12.842 34.8 76.373 1/30/2013 15:52:00 12.978 4.841 3.071 2.766 12.86 34.566 82.194 1/30/2013 15:53:00 12.992 4.834 3.084 2.798 12.878 34.278 82.594 1/30/2013 15:54:00 12.98 4.843 3
. 101 2.85 12.868 34.439 86.852 1/30/2013 15:55:00 18.424 1.61 1.065 1.714 12.863 34.54 86.315 1/30/2013 15:56:00 13.595 4.497 2.601 1.517 12.878 34.499 83.912 1/30/2013 15:57:00 12
. 991 4.832 2.999 2.542 12.898 34.042 89.061 1/30/2013 15:58:00 12.988 4.834 3.088 2.775 12
. 897 33.928 95.149 1/30/2013 15:59:00 12.976 4.842 3.055 2.564 12.887 34.476 90
.059 1/30/2013 16:00:00 12.986 4.836 3.055 2.468 12.905 34.146 89.103 1/30/2013 16:01:00 12.996 4.83 2.93 2.558 12.911 34.107 91.678 1/30/2013 16:02:00 13.008 4.824 2.929 2.731 12.921 33.881 94.668 1/30/2013 16:03:00 13.009 4.82 2.994 2.738 12.921 33.836 96.194 1/30/2013 16:04:00 13.007 4.819 2
. 919 2.592 12.919 34.144 90.202 1/30/2013 16:05:00 13.024 4.806 2
. 892 2.771 12.925 33.759 96.4 1/30/2013 16:06:00 16
. 679 2
. 632 1.649 2.074 12.922 34.019 90.534 1/30/2013 16:07:00 14
. 233 4.109 2.285 1.556 12.921 33
. 935 96.934 1/30/2013 16 :08:00 13.003 4.813 2.86 2.455 12.922 33.971 94.896 6.751 Direct Zero 7.598 6.903 7.766 7.412 6.915 6.431 7.969 8.168 8.89 8.223 9.363 9.025 9
. 235 8.325 6.38 6.678 7.691 8.431 9.562 9.567 12.831 Start RATA Run 3 12.289 13.183 12.502 12.362 11.861 10.815 12.556 12.638 13.63 13.675 12.437 14
. 121 15.642 14.458 13.734 14.626 15.59 15.831 14.482 16.455 14.498 16.009 15.61O2 CO 2**NO~** CO Date Time % % PPM PPM 1/30/2013 16:09:00 13.001 4.815 2.846 2.511 1/30/2013 16:10 :00 13.01 4.804 2.862 2.563 1/30/2013 16:11:00 13 .009 4.806 2.855 2.281 1/30/2013 16:12:00 13.009 4.804 2.917 2.132 1/30/2013 16:13:00 12.991 4.816 2.948 2.088 1/30/2013 16:14:00 13.011 4.801 2.842 2.167 1/30/2013 16:15 :00 13.011 4.802 2.978 2
. 22 1/30/2013 16:16:00 13
.01 4.8 2.935 2.201 1/30/2013 16:17:00 14.901 3.667 2.265 1.995 1/30/2013 16:18:00 16.283 2.893 1.6 1.07 1/30/2013 16:19:00 13.031 4.783 2.778 2.516 1/30/2013 16 : 20:00 13.041 4.78 2.779 2.729 1/30/2013 16 :2 1:00 13.019 4.787 2
. 891 2
. 804 1/30/2013 16 : 22:00 13.017 4
.786 2.865 2.77 1/30/2013 16:23:00 13.019 4.785 2.86 2.792 1/30/2013 16:24:00 13.019 4.782 2.887 2.681 1/30/2013 16:25:00 13
.019 4.782 2.856 2.546 1/30/2013 16:26:00 13
.01 4.785 2.919 2.228 1/30/2013 16 :27: 00 13.01 4.784 2.94 2.367 1/30/2013 16:28:00 13.018 4
.779 2.911 2.339 1/30/2013 16:29:00 13.032 4.77 2.933 2.374 1/30/2013 16:30:00 13.019 4.775 2.847 2.499 1/30/2013 16:31:00 7
. 773 2.847 1
. 878 2.813 1/30/2013 16:32:00 0
. 14 0
. 203 0
.009 4.311 1/30/2013 16:33:00 0.124 0
. 194 -0.002 4.462 1/30/2013 16:34:00 4
. 842 2.722 0.003 3
. 353 1/30/2013

## 16:35:001'"!-9~.~99:;:;2:---;:5"=.3~0';;'1-"";;';';;0:';;'" -0
. 12 1/30/2013 16:36:00 4.528 2.432 2.44 -0 .2 24 1/30/2013 16 : 37:001'"!

### -0;;"**~12;';6"""--;:O~.1'i;9~6 --4:;-.:;:77;;1---;:O~.1;;3':;'8'**  1/30/2013 16:38:00 12
. 225 0.211 2
. 114 0
. 192 1/30/2013 16:39:00 20.745 0.223 0.021 0
. 179 1/30/2013 16:40:00 18.804 1.4 0.596 0.337 1/30/2013 16:41:00 13.047 4.749 2.766 2.433 1/30/2013 16 :42 :00 13.008 4.765 2.846 2.91 1/30/2013 16:43:00 13
.009 4.765 2
. 804 2.767 1/30/2013 16:44:00 13.005 4.768 2
. 852 2.894 1/30/2013 16:45:00 12.997 4.772 2.865 2.67 1/30/2013 16:46:00 12.986 4.78 2.982 2.308 1/30/2013 16 :47:00 12
. 988 4.777 2.984 2.337 1/30/2013 16 :48:00 13.008 4.764 2
. 915 2.24 1/30/2013 16:49:00 13
.007 4.765 2
. 929 2
. 311 1/30/2013 16:50:00 13 .00 8 4.76 2.95 2.367 1/30/2013 16:51:00 18.594 1.449 0
. 898 1.453 1/30/2013 16:52:00 17.451 2.186 1.131 0.844 1/30/2013 16:53:00 13.054 4.737 2
. 866 3.349 1/30/2013 16 :54:00 13
.031 4 .7 46 2
. 885 3.377 1/30/2013 16:55:00 13
.044 4.739 2
. 916 3
.447 1/30/2013 16:56:00 13.046 4.736 2
. 925 3
.715 1/30/2013 16:57:00 13.054 4.731 2.835 3.57 1/30/2013 16:58:00 13.069 4.719 2
. 935 4
. 149 1/30/2013 16:59:00 13.059 4.722 2
. 99 4.125 1/30/2013 17:00:00 13.058 4.721 2.921 4
.093 1/30/2013 17 :0 1:00 13.049 4.729 2
.782 3
.744 1/30/2013 17:02:00 13.037 4.733 2.766 3
.736 1/30/2013 17:03:00 13.012 4.743 2.93 3.358 1/30/2013 17:04:00 17.193 2.277 1.27 2.16 1/30/2013 17 :05:00 13.058 4.732 2
. 865 2.992 1/30/2013 17:06:00 13.011 4.739 2.872 3.533 1/30/2013 17:07:00 13.007 4.743 2.956 3.401 

### 0, % 12.921 12.923 12.925 12.939 12.922 12.926 12.925 12.927 12.922 12.921 12.953 12
. 955 12.943 12.947 12.951 12.961 12.955 12
. 958 12.954 12.949 12.97 12.954 8.02 0
.064 1.532 12.85 12.945 12.966 12
. 951 12 .965 12.968 12.956 12.946 12
. 928 12.934 12 .9 27 12
. 926 12
. 923 12
. 923 12
. 926 12 .926 12.931 12.927 12.937 12
. 936 12 .9 28 12.942 12.947 12
. 956 12
. 969 12 .9 61 12
. 958 12.949 12.937 12.922 12
. 934 12
. 924 12
. 923 12.92 NO, PPM 33.956 33.962 33
. 849 33.755 34.065 33.937 33
. 958 34
.071 34.134 34.175 33.781 33
. 68 33
.775 33
. 907 33.829 33
. 94 33
. 859 33
. 823 33
.708 33.902 33.704 33.793 23.428 1
. 266 2.888 32.443 33.236 33
.046 33
.462

33
. 5 33.447 33.552 33
. 702 33 .7 56 33 .7 53 33.927 33.727 34.237 33.932 33
. 992 33.795 33.759 33.725 33.607 33.587 33.828 33.435 33.376 33.344 32
. 64 32
. 946 32 .9 81 33.114 33.171 33.636 33.176 33
.418 33.489 33.741 CO PPM 95.791 96.947 95.012 97.188 97.184 97.335 98.204 95.769 94.563 96.756 97.252 100.191 102.061 99.441 100.544 97.583 100.076 98
. 218 103.379 102.722 103.781 104.082 106.659 132.844 135.686 114.291 104.831 106.918 107.257 102.342 103.691 105.309 102.515 104
. 91 101.068 101.921 100.765 100.31 101
. 365 98.258 100.04 102.93 103.989 104.861 106.99 102.214 103.617 112.398 106.719 119.524 116.993 116.35 111.465 116.323 105.621 113
. 615 112.486 111.499 106.975 

### THC PPM 16 .3 52 15
. 718 15 .601 16.126 16.031 15
. 696 16.152 15
.024 15.104 16.255 15
. 367 17 .02 5 17.519 16.876 16.489 16
. 151 16
. 691 16.429 17.655 17.831 18.049 17.638 16.99 0 .7 62 -0 .008 Co bias 13.057 18.173 02/C02 bias 18.688 18 .87 NOx bias 17
. 612 17.029 18.338 17
. 598 18.25 16
.426 17
. 746 16.605 17
. 133 17
.471 15.939 16.625 17.761 17.843 18.584 18
. 331 17.435 17.718 20.045 18
. 322 22.121 20 .6 22 21.034 19 .9 68 21.036 18
. 381 20
. 142 19
. 399 20.47 18
. 926**~ ~** **~** ro**~ ~**  Date Time % % PPM PPM % PPM 1/30/2013 17:08:00 13.007 4.742 3.006 3.481 12.917 33.408 1/30/2013 17:09:00 13.001 4.744 2.994 3.577 12.912 33.663 1/30/2013 17:10 :00 13.005 4.742 2.974 3.402 12
. 919 33.569 1/30/2013 17:11 :00 12
. 998 4
. 743 2.977 3.533 12
. 912 33.447 1/30/2013 17:12 :00 12.996 4.744 2.93 3.38 12.911 33
. 501 1 / 30/ 2013 17:13 :00 12
. 995 4 .7 42 2
. 848 3
.473 12
. 905 33.468 1 / 30/2013 17:14 :00 12
. 998 4.738 2.891 3
. 268 12
. 909 33
.499 1/30/2013 17:15:00 15.426 3.309 1.999 2.785 12
. 922 33 .20 1 1/30/2013 17:16:00 13
.024 4.722 2.972 3.985 12.923 33
.015 1/30/2013 17:17 :00 13.009 4.731 3.06 4.039 12.917 33.406 1/30/2013 17:18 :00 13.006 4.73 2.946 4.136 12.919 33.141 1/30/2013 17:19 :00 13.007 4.729 2
. 986 4
. 142 12.911 33.207 1/30/2013 17 : 20 :00 13
.007 4
. 726 3
.018 3
. 944 12.919 33.484 1/30/2013 17:21:00 13.011 4.721 3.124 4
. 169 12
. 915 33 .27 1/30/ 2013 17 : 22 :00 13
.003 4.727 3.195 4.291 12.902 33.538 1/30/2013 17:23 :00 13.008 4.72 3.072 4
. 348 12.919 33.2 1/30/2013 17:24:00 12
. 997 4.727 3.075 3.842 12.902 33
. 606 1/30/2013 17:25:00 13.01 4.717 3.004 3.822 12.912 33.347 1/30/2013 17:26:00 13.011 4.714 2.948 3.972 12.922 33.191 1/30/2013 17:27:00 10.117 4.827 1.107 1.838 12.911 33.361 1/30/2013

## 17:28:oo'"I..:9:::**::;99;,1:.....--,;5~.2:;;76;,.........,0~ 0;;;1;,;l--.**  -0.294 12.918 33
. 343 1/30/2013 17:29:00 4
.475 2.365 2.483 -0.222 12
. 904 33
. 55 1/30/2013 17 : 30 :00 '"1

## --::0.;,**1"3-....;;0~ 1:;;75;;-:.....4~** **.** 7,;;6"'1:.....--,;0;;,;.1;,:;5;;;1..., 7
. 103 20.528 1/30/2013 17:31:00 0
. 125 0.165 1.639 1
. 962 0.041 0.196 1/30/2013 17:32:00 0.1 0
. 161 0 .005 4.379 0.025 0
.091 1/30/2013 17:33:00 0.099 0.157 0.001 4.473 0.D25 0.043 1/30/2013 17:34:00 7.708 2.933 1.599 4.345 14.822 29.183 1/30/2013 17:35:00 12.965 4.702 3.016 3.936 18.777 6.64 1/30/2013 17:36:00 4.996 1.726 1.523 3.215 18
. 781 0
. 55 1 / 30/ 2013 17 : 37 :00 3 .957 1.717 0 .002 0.116 18
. 793 0.393 1 / 30/2 013 17 :3 8 :00 12 .93 9 4
. 695 -0.004 0.007 18
. 8 39.713 CO PPM 110.269 110.59 108.859 114.188 108.565 113.306 108.312 115.803 118.881 113.011 116.046 116.305 111.23 113.418 113.986 114
. 271 113.217 114.164 117.373 114.701 113
. 938 112.02 110
. 214 10.335 -0.057 -0.058 54.679 230.063 236
. 689 236.947 236.93 THC PPM 19.359 19
.011 18.323 20
. 913 18
.497 19
. 662 18 .77 6 20
. 395 21.815 19.586 19
. 975 20.322 19
. 816 20
. 232 20
. 745 20.608 19.21 20.207 21.827 20.103 20.397 02/C02 bias 19
. 973 22.352 NOx bias 21.433 18
. 999 20.485 CO bias;lnlet Cal Zero 20.926 18.896 21.335 20.074 22
. 222 1 / 30/2013 17:39 :00 12
. 961 4 .7 04

## L..~-0~.0'::'l:--_0:'.":00~6:----:1:;;8;.;.8~0::-1_-::4::::8'i**.2 ::::85:':-_2::'3~7:':.2;.;;1~6** ... 1 21.081 Stack NOx/ro Cal Zero 1/30/2013 17:40:00 12.956 4.71 3
. 641 1.752 12
. 988 30.899 237.154 19.33 1/30/2013 17:41 :00 12.955 4.708 4.776 5.58 9
.971 24.033 166.668 21.798 1/30/2013 17:42:00 16.94 2.202 4.777 9.426 9.97 24.332 135.249 20.025 1/30/2013 17:43:00 15.687 2.109

### L..4~.-::77'::5:--_9::' . .,:.48:::1:--.....,;:.9::;.9:::7:-.....;2';:4'::
. 3':'5

__

### 1~3~5,;;.9::'04-::-'1 21.431 5tack Oirect High, Inlet Direct Mid 1/30/2013 17:44 :00 9.972 5.248 3.929 9.399 9.929 8
.04 106.458 20.027 1/30/2013 17:45 :00 9 .9 66 5.257 2.572 5.281 9
. 919 0 .3 64 23
.714 1 /3 0/ 2013 

### 17 : 46 : 00'"1-'=9"'= .9"'6---=5"'=.2"57=--"'=2'=.5""4--':4""' .4"'=9'"1"" 9
. 919 0
. 263 4
. 88 1 / 30/2013 17 :47 :00 4.079 2.036 3.373 2.182 11 .7 35 16
. 984 26.603 1/30/2013

## 17**48:oo'"I...;,0,;; 1;,;3:....-0~.;;:16;;;2;-,**  4 .7 61 0.219 12
. 898 33 .254 102.654 1/30/2013 17:49:00 0.107 0.131 1.516 0.202 12.905 32
. 944 109.511 1/30/2013

## 17:50:00'"1-0~.0:::9;,;9.....,....;;0~.1::;247-0 0.018 0.201 12.911 32.929 108.365 1/30/2013 17:51:00 7.228 4.03 0.016 0.206 12
. 916 33.033 112.57 1/30/2013 17 :52 :00 9
. 972 5.246 0.017 0.207 12
. 917 32
. 836 108.049 1/30/2013 17 :53 :00 17
. 131 9
. 244 0.017 0
. 213 12
. 92 32
. 987 111
. 224 1/ 30 /2 013 17 :54 :00 18 .7 13 9.848 0
.019 0
. 215 12
. 911 32 .97 5 107
. 671 1/30/2013

## 17**55 001'"-:1'i8;:,** **8":72:--....;;9;.; 6~67,-,**  0
.062 0.21 12
. 922 32 .9 89 108.53 1/30/2013 17:56 :00 11.552 5.793 0
. 11 0.218 12
. 923 32.735 115.603 1/30/2013

## 17**57 oo'"I-:1;;:0'i.0~66;;-....;;5":.1i':347-0**  0.12 0.218 12
. 923 32.879 107.818 1/30/2013 17:58:00 9.702 5.14 0.157 0.228 12
. 923 32.986 110.738 1/30/2013 17:59:00 1.19 5
. 143 0.169 0.23 12.924 32.521 115.207 1/30/2013 17:59:20 7 .1 56 5
. 143 0
. 15 0
. 25 12.922 32
. 873 112
. 196 1/30/2013 17:59:30 9
. 268 5
. 143 0
. 156 0.204 12.923 33.011 108
. 967 1/ 30 / 2013 17:59 :40 7
. 902 5
. 143 0
. 157 0
. 235 12
. 998 32
. 58 107.544 1 / 30/2013 17 : 59 :50 1
. 349 5
. 143 0
. 163 0
. 237 13.09 30.828 110
. 241 1 / 30/2013 18 :00 :00 9
.788 5.144 0
. 169 0
. 242 13.168 30 .7 82 116
. 198 1/30/2013 18:00 : 10 18
. 134 5.144 0
. 156 0.26 13.273 29
. 109 116.926 1/30/2013 18:00:20 18 .72 8 5.145 0 .1 48 0.255 13
. 329 27.14 125.057 21
. 6 

### 21 .64 2 Stack M id; 02 /C 02 b ia s 20.552 19 .7 33 NOx bias 22.224 21.088 

### 02/C02 direct Zero 22.603 21.318 02/C02 Mid direct 22
. 885 20.872 20
. 964 Cal High 24.464 21.743 02/C02 Mid 22.86 24.124 23
. 15 22.572 21.452 21.536 25.366 29.272 26.027

### 0 , Date TIme % 1/ 30/ 2013 18 :00 : 30 18.841 1/30/2013 18 :00 :40 18
. 871 1/ 30/ 2013 18 :00 :50 18
. 881 1 /3 0/ 2013 18 :01 :00
... 1

## -:1~8,,:;**8:::9::-,** 1/ 30/2 013 18 :01 : 10 18.898 1/30/2013 18 :01 : 20 18.902 1/ 30/2013 18 :01 : 30 18.9 1/ 30 / 2013 18 :01 :40 17
. 124 1/ 30/ 2013 18 :01 :50 15.231 1/30/2013 18 :02:00 15.054 1/ 30/2013 18 :02 : 10 15
.019 1 / 30 / 2013 18 :02 : 201 15
.012 1/ 30 / 2013 18 :02 : 30 14
.413 1/30/2013 18 :02 :40 11.662 1/30/2013 18:02 :50 11.263 1/ 30/ 2013 18 :03 :00 11
. 186 1/ 30/ 2013 18 :03 : 10 11
. 178 1/30/2013 18:03 : 201 11.178 1/30/2013 18:03:30 11.177 1 / 30/ 2013 18 :03 :40 10
. 734 1 / 30/ 2013 18 :03 :50 9.542 1/30/2013 18 :04:00 9.352 1/30/2013 18:04:10'"1""9;;;.;;;33:;3'""' 1 / 30/ 2013 18 :04 : 20 8
. 881 1 / 30/ 2013 18 :04 : 30 7
. 641 1/ 30/ 2013 18 :04 :40 7
.491 1/30/2013 18:04:50 7.459 1/ 30/ 2013 18 :05 :00 

### r 

# l**-:7"'.4~58~** 1 / 30/ 2013 18 :05 : 10 7 .2 9 1/ 30/ 2013 18 :05 : 20 4.529 1/30/2013 18 :05 : 30 3
. 883 1/ 30/ 2013 18 :05 :40 3
. 804 1/ 30/2 013 18 :05 : 50
...

### 1_3::-**7~7::6** ..... 1/ 30/ 2013 18 :06 :00 4.701 1/30/2013 18 :06 : 10 9.245 1/ 30/2013 18 :06 : 20 9
. 921 1/ 30/ 2013 18 :06 : 30 10
.024 1 / 30/ 2013 18 :06 :40 10
.04 1/30/2013 18 :06 : 501 10
.054 1/30/2013 18 :07 :00 10
.046 1/ 30 / 2013 18 :07 : 10 9
.476 1/ 30/ 2013 18 :07 : 20 13.669 1/30/2013 18:07 : 30 14.777 1/30/2013 18 :07 :40 14
. 888 1/ 30 / 2013 18 :07: 50 14
. 915 1/ 30/ 2013 18 :08 :001 14
. 916 1/30/2013 18 :08 : 10 14.916 1/30/2013 18 :08 : 20 13
.002 1/ 30 / 2013 18 :08 : 30 11
. 329 1 / 30/ 2013 18 :08 :40 11.162 1/ 30/ 2013 18 :08 : 50 11.128 1/30/2013 18:09 :001 11
. 128 1/ 30/ 2013 18:09 : 10 11.125 1 /3 0/2013 18 :09 : 20 10.401 1/30/2013 18 :09 : 30 9
.412 1/30/2013 18:09 :40 9
. 326 1/ 30/2 013 18 :09 :50 9.318 1 / 30/20 13 18 : 10 :00 9
. 315 1/ 30/ 2013 18 : 10 : 10 9.307 

### CO , % 5.144 5.143 5.145 5
. 143 5.142 5.145 5.142 5
. 144 5
. 144 5.143 5
. 142 5
. 142 5
. 144 5.144 5
. 143 5
. 143 5
. 142 5.144 5.144 5
. 144 5
. 143 5
. 143 5
. 145 5
. 143 5.145 5.144 5
. 143 5
. 144 5.143 5
. 142 5
. 143 5
. 141 5
. 143 5
. 142 5.143 5
. 144 5
. 142 5
. 141 5
. 143 5
. 142 5
. 141 5
. 143 5.144 5
. 143 5
. 142 5
. 142 5
. 142 5
. 142 5
. 142 5
. 143 5
. 143 5.144 5
. 142 5
. 143 5.142 5.143 5
. 14 5
. 14 2 5
. 139 NO, PPM 0
. 144 0
. 158 0
. 172 0
. 178 0
. 185 0.181 0
. 175 0
. 182 0
. 191 0.179 0
. 179 0
. 163 0
. 169 0.177 0.181 0
. 176 0
. 154 0
. 152 0
. 157 0
. 173 0
. 154 0
. 149 0
. 143 0
. 139 0
. 128 0.13 0
. 118 0
. 128 0
. 139 0.156 0.145 0
. 118 0
. 117 0
. 116 0.107 0
. 107 0
. 118 0
. 102 0
. 104 0
. 109 0
. 119 0
. 113 0
. 116 0.106 0
. 103 0
. 121 0
. 115 0
. 111 0
. 103 0
. 11 0
. 109 0
.099 0
. 117 0
.097 0.109 0
. 142 0
. 131 0
. 12 0
. 142 

## co PPM 0
. 232 0
. 23 0
. 243 0
. 26 0
. 261 0
. 248 0
. 231 0
. 231 0
. 232 0
. 248 0
. 248 0
. 23 0
. 257 0
. 237 0
. 232 0
. 235 0
. 25 0
. 271 0
. 271 0
. 255 0
. 243 0.257 0.264 0 .2 99 0
. 268 0
. 241 0
. 236 0.253 0
. 264 0 .2 63 0.266 0 .2 64 0
. 261 0
. 252 0
. 248 0
. 285 0
. 274 0
. 281 0
. 277 0
. 265 0 .2 77 0
. 275 0.282 0.308 0
. 267 0
. 281 0
. 285 0.284 0. 289 0
. 299 0
. 296 0
. 315 0
. 29 0
. 299 0
. 285 0
. 301 0
. 302 0
. 304 0.275 

### 0 , % 13
.4 24 13.558 13
. 679 13. 7 8 7 13.896 14
.055 14
. 247 14
.439 14
. 659 14
. 904 15
. 292 15
. 816 16
. 299 16
. 273 16
. 272 16
. 289 16
. 29 7 16
. 312 16
. 308 16
. 298 16
. 319 16
. 323 16
. 331 16
. 346 16
. 321 16
. 337 16
. 345 16
. 346 16
. 331 16 .3 3 7 16.345 16
. 346 16
. 346 16
. 367 16.347 16
. 346 16
. 346 16 .3 46 16.346 16
. 346 16
. 346 16
. 346 16
. 346 16.346 16
. 346 16
. 346 16
. 346 16
. 346 16
. 34 6 16
. 346 16
. 346 16.345 16
. 346 16
. 343 16
. 345 16.342 16
. 33 7 16
. 341 16.33 2 NO , PPM 27
. 384 28
. 153 27
. 9 26
. 984 25
. 596 24
. 511 24
. 225 24
. 314 23
. 85 23.24 24
. 239 34
. 274 32
. 833 29
. 36 29
. 311 29
. 284 29
.095 28.983 28
. 699 28
.754 28
. 72 2 28
. 656 28
. 609 28
.461 28.43 4 28.491 28
. 394 28
. 388 28
. 35 6 28
. 37 28
. 334 28
. 318 28
. 255 28 .2 1 2 28
.078 28
. 113 2 8
. 139 28
. 176 28
. 134 28
.082 28
.081 28
.055 28.045 28
.036 28
.00 2

28 27.995 27
. 973 27. 94 27
. 931 27.919 27
. 891 27
. 871 27
. 849 27
. 856 27
. 852 27
. 829 27
. 8 0 2 27. 777 

### CO PPM 138.892 135.023 113.901 85.53 7 64
. 683 57.286 57
. 293 57 .6 85 56
.031 53.659 52.386 49
. 128 40
. 649 37.734 39.406 42
. 694 45.139 46.04 47.14 48.47 6 49
.053 49.512 50.083 50.392 51.281 51.726 52.171 52.314 52.465 52.754 52 .7 6 53
.058 53
.063 53.532 53.542 54
.05 54
. 141 54.29 54.288 54.289 54
.426 54
. 33 8 54.578 54
. 323 54
.43 2 54
.438 54
.741 54
.742 54
.74 2 54
.742 54.735 54.436 54
.775 55
.041 55.193 55.192 55.341 55
. 344 55.345 

### THC PPM 35.58 47.625 34
. 36 16
. 277 7
. 582 3
. 649 4
. 332 4
. 833 4
. 219 3.452 3
. 187 3
. 203 2
.737 0
. 873 1
. 147 1
. 106 0
.791 0
.772 0
. 857 0
. 976 1
. 106 1.088

1.1 1
.099 1
. 12 3 1.239 1.253 1
. 224 1.259 1.299 1.291 1.301 1
. 312 1.343 1.355 1
.416 1.397 1.404 1.4 1.353 1
. 366 1
. 357 1.322 1
. 345 1
. 363 1
. 384 1.403 1.454 1.479 1.464 1.533 1.524 1.464 1
.426 1.476 1.512 1.457 1.452 1.413 100%

80 %

60%

50%

4 0 %

20 %



### Mid

80%

60%

### 0, Date Time % 1/30/2013

### 18:1O:20L!_9~**~30~1,-,** 1/30/2013 18:10 : 30 9.061 1/30/2013 18:10 :40 7 .698 1/30/2013 18 : 10:50 7
.482 1/ 30/2013 18 : 11:00 7.441 1/ 30 / 2013 18 : 11 : 10 7 .4 32 1 / 30 /2 013

## 18:11**:20 "!-7:::** **""43~4;-'** 1/30/2013 18:11 : 30 6.8 1/30/2013 18:11 :40 4
. 212 1/30/2013 18:11:50 3
. 842 1/30/2013 18:12 :00 3.786 1/30/2013 18 : 12 :10 3
.774 1 / 30/2013 18 : 12 :20 3.774 1/ 30/ 2013 18 : 12 :30 3
.774 1/30/2013 18 : 12 :40 3 .776 1/30/2013

## 18**12 50"!-=-3** **~77::-:1"""** 1/30/2013 18:13 :00 5.128 1/30/2013 18:13 : 10 9.377 1/30/2013 18:13:20 9.913 1/30/2013 18:13:30 10.003 1/30/2013 18:13 :40 10
.018 1/ 30/2 013 18:13 :50! 10
.038 1/30/2013 18:14 :00 9.996 1/30/2013 18 : 14 : 10 12.917 1/30/2013 18:14 :20 14 .77 1 1/30/2013 18:14:30 14.918 1/30/2013 18:14:40 14.946 1/30/2013 18:14:50 14
. 962 1/30/2013 18:15:oo! 14 .965 1/30/2013 18:15 : 10 14 .05 1/30/2 013 18 : 15 :20 11.521 1/30/2013 18:15 :30 11.214 1/30/2013 18:15:40 11.167 1/30/2013 18:15:50 11.152 1/30/2013 18:16:00! 11.152 1/30/2013 18:16:10 10.967 1/30/2013 18:16:20 9
. 644 1/30/ 2013 18:16:30 9 .3 44 1/30/2013 18 : 16 :40 9
. 318 1/30/2013 18:16 :50 9 .308 1/30/2013 18:17 :00 9
. 299 1/30/2013 18:17:10 9.294 1/30/2013 18:17:20 9.293 1/30/2013 18:17:30 

## r !

## -:9:".2;;;94~ 1/30/2013 18 : 17 :40 8
. 868 1/3 0/2013 18:17 : 50 7.623 1/30/ 2013 18 : 18 :00 7.471 1/3 0/ 2013 18 : 18 : 10 7.437 1/30/2013 18 : 18 :20 7.433 1/30/2013 18:18 :30 "!-7:::.""43"'3;-' 1/30/2013 18:18:40 7.432 1/30/2013 18:18:50 7.433 1/30/2013 18:19 :00 7.432 1/30/ 2013 18 : 19 : 10 6
. 845 1/30/ 2013 18 : 19 : 20 4 .2 16 1 / 30 / 2013 18 : 19 : 30 3 .842 1/3 0/ 2013 18 : 19 :40 r !

## "';3:;;**7:::8~2'** 1/30/2013 18 : 19:50 4
.475 1/30/2013 18:20:00 9
. 261 

### CO, % 5.14 5
. 139 5.14 5.14 5
. 141 5
. 139 5.139 5.139 5.138 5.139 5.139 5.139 5.14 5 .13 8 5.137 5.139 5
. 137 5.136 5.138 5.138 5.139 5.137 5
. 138 5
. 136 5.135 5.135 5.135 5.132 5.132 5.132 5
. 132 5
. 132 5
. 131 5.131 5.132 5
. 13 5
. 131 5.131 5
. 129 5.132 5.132 5.13 5.126 5.126 5.128 5.127 5
. 126 5.127 5.126 5.123 5.122 5.124 5.122 5.123 5
. 121 5.122 5.124 5.121 5.121 NO, PPM 0.113 0.104 0.107 0.108 0
. 125 0.126 0.112 0.128 0
. 14 0.133 0.13 0
. 123 0.134 0.134 0.14 0
. 14 0.123 0.11 0.13 0.149 0.137 0.123 0.11 0.092 0.084 0.081 0.071 0.076 0.076 0.068 0.069 0
.073 0.074 0.078 0.076 0.076 0
.079 0.076 0
.073 0
.072 0.07 0.071 0.075 0.076 0.082 0
.067 0
.066 0
.064 0.07 0.059 0.061 0
.061 0
.059 0
.058 0
.056 0
.058 0
.07 0.077 0
.063 

## co PPM 0
. 297 0.276 0
. 283 0 .303 0
. 319 0
. 311 0 .2 85 0
. 285 0.282 0.301 0
. 309

0.3 0.29 0
. 289 0
. 277 0.279 0.296 0.308 0.315 0 .3 05 0.3 0 .2 97 0 .2 89 0 .3 02 0.323 0.326 0.297 0.303 0.302 0 .2 99 0.337 0.329 0
. 307 0.301 0.311 0
. 325 0.318 0 .30 6 0
. 326 0.308 0
. 318 0.325 0.283 0.289 0.331 0.323 0.31 0.323 0.317 0
. 316 0.312 0.338 0.334 0
. 341 0
. 324 0
. 322 0.297 0.303 0.344 

### 0, % 16
. 322 16.332 16.322 16.321 16.321 16
. 321 16.32 16.321 16.326 16.322 16.322 16 .3 22 16 .3 44 18.651 20.455 20.632 20.658 20.688 20.689 20.688 20.689 20.689 20.69 20.689 20.688 20.69 20.69 20.69 20.689 20.689 20.689 20.689 20.689 20.689 20.688 20.689 20
. 688 20.688 20.688 20
. 688 20.689 20
. 689 20.689 20.689 20
. 689 20
. 689 20.689 20.689 20.689 20.689 20.688 20.688 20
. 689 20.683 20.679 20.672 20.665 20
. 665 20
. 666 NO, PPM 27.773 27
.782 27.771 27.735 27.728 27.729 27 .72 5 27
. 722 27
.714 27
. 659 27.665 27
. 644 27.657 23.184 5 .74 6 1.478 1
. 193 1.074 0.989 0.922 0.869 0
. 827 0
. 81 0 .7 66 0 .73 5 0.706 0.675 0.648 0.633 0 .6 1 0.583 0.565 0.551 0.539 0.529 0.53 0 .5 17 0.487 0
.471 0
.471 0
.461 0
.444 0.433 0.417 0.42 0.4 0 .3 94 0
. 385 0.375 0
. 364 0.352 0.338 0 .3 37 0.329 0 .3 2 0
. 32 0
. 31 0
. 305 0
. 303 

## co PPM 55.493 55.493 55
. 638 55
. 637 55.636 55.795 55.791 56.087 55.936 55.792 55.941 55
. 943 55
. 946 56
. 318 GO
. 172 48.156 31.705 15.277 6.542 3.346 1.858 1.117 0.686 0.543 0.392 0.392 0.253 0
. 248 0
. 246 0 .3 88 0
. 248 0.393 0.39 0.387 0.241 0
. 392 0.245 0
. 242 0.241 0.242 0.242 0.243 0.241 0.242 0.245 0.241 0.245 0.246 0.242 0.236 0.236 0.236 0.237 0.236 0
. 24 0.239 0.24 0.242 0.241 

### THe PPM 1.408 1
.476 1.56 1
. 578 1.463 1
.495 1.513 1 .5 15 1.531 1.572 1.52 1.487 1.484 1
. 506 2.01 90
. 973 99.997 99
. 997 99
. 997 94
. 257 61
. 86 23.452 Mid 12.889 12.889 12.888 12.889 12
. 89 12.889 12 .88 9 1 2
. 89 12
. 889 12 .8 89 12
. 887 12.888 12.888 12
. 888 12.888 12
. 888 12 .8 88 12.888 12 .88 8 12.888 12.888 12.888 12.888 12
. 889 12
. 888 12
. 888 12 .88 8 12.887 12.887 12
. 888 12
. 888 12
. 88 7 12 .8 87 12
. 888 12.888 12.888 12.887 50%

40 %

20%

80%

60%

50%

40%

20%

### 0, CO, NO, CO 

### 0, NO, CO 

### THe Date Time % % PPM PPM % PPM PPM PPM 1/30/2013 18:20:10 10.055 5.122 0.065 0.343 20.664 0.29 0.241 12.887 1/30/2013 18:20:201 10.165 5.121 0.057 0.35 20.663 0.28 0.242 12.886 Mid 1/30/2013 18:20:30 10.189 5.122 0.061 0.328 20.664 0.275 0.237 12.887**~ ~** **N~** 00**~ ~**  00 THC PPM Date Time % % PPM PPM % PPM PPM 1/ 31 / 2013 7:58:00 13
. 924 0
. 508 0 0.36 20
. 257 -0
.021 1
. 17 2.669 2 .607 2
. 604 2
. 64 1/ 31 /2013 7 : 59 :00 0
. 368 0
.092 -0
.019 0.029 2.46 -0.128 0.645 1/3 1/ 2013 8 :00 :00 0
. 113 0
.077 -0
.016 -0
.022 0 .0 62 -0
. 141 -0
.026 1/3 1/2 013 8 :01 :00 0.109 0
.073 -0.015

-0.015 0
.048 -0
.086 -0
.026 1 / 31 / 2013 8 :02:00 0.108 0
.071 -0
.012 -0
.011 0
.036 0.055 -0
.03 1.319 N2/ NO Mode 73.686 1/3 1/2013 8 :03 :00 0
. 108 0.067 -0.021 -0.022 0.035 0.04 -0.031 1/31/2013 8 :04 :00

## rl-0::'.~1O~7~--;;0:'i**0';;647---~0.'i:0~17~--;;-0"'.0;::0~4-~0::'.0~3:;;5-~0~.0~5;;'7---'i:0.'i:0;;;31~** 1/31/2013 8 :05 :00 15.956 8.279 2.909 4
.741 10.411 2.847 64.422 61.957 N2/NO Mode ; 02/OO2/OO Cal Zero 1.42 1/31/2013 8:06 :00 18.963 9.625 4.821 9.367 18.829 4.869 232
. 191 0.614 1/31/2013 8:07:00**.....:1;;:8;;;.9:i:-75;---;;9:'i.6,,65;-1-4;:..8:;;1;,;6-4....,;9;.;.4~39~** 18.878 4.876 237.306 1/31/2013 8:08:00**L..;1;;:8;.:;.9;;81;-....,;9,;.;.6~6;;.2....1** 4.821 9.439 20.474 4.871 237.544 0.056 NO/NOx Mode -0
. 167 02/C02/OO Cal High 1/31/2013 8:09:00 18.52 9.417 4.814 9
.45 20.608 4.872 237.422 -0.18 1/31/2013 8:10:00 10
. 265 5
. 102 4.815 9.454 11
. 825 4
. 874 

# I 205.061 -0
. 181 NO/NOx Mode 1/31/2013 8:11:00 10.117 5.097 4.816 7.343 11
.053 4
. 869 87.309 -0.187 1/31/2013 8:12:00 10
. 109 5.095 4.829 4.478 11
.052 4
. 873 

# I 135.37 -0
.046 NO/ NO Mode 1/ 31 /20 13 8:13:00 10
. 104 5
.091 2.478 4
.457 11.16 2
. 63 136.057 -0
.002 02/C 02/CO Mi d 1/ 31 / 2013 8 : 14 :00 12.55 4
. 64 -0
.003 4.401 11
.075 0
.064 112 .873 -0.004 1/ 31 /20 13 8:15:00 13.236 4
.475 0
.002 4
.492 1
.475 0.069 28.193 -0
.007 N02/ NO Mode 1/3 1/ 2013 8:16:00 13.236 4.471 3.231 4
. 899 0
.056 3.386 0.737 -0 .009 1/ 31 /20 13 8 : 17 :00 13
. 226 4
.479 3
. 854 4.514 0.049 3.928 0.082 -0.009 N02/ NOx Mode @ 817 1/31 /20 13 8:18 :00 13.221 4.478 1.807 4
. 254 0.029 2.102 0.009 -0 .0 1 1 / 31/2013 8 : 19 :00 13.233 4.467 -0.008 4.534 0
.029 0.077 -0.001 -0.009 1/31/2013 8:20 :00 13.225 4.472 -0
.013 4.434 0.028 0.069 -0
.006 -0
.009 NOx/02Cal Zero 1/31/2013 8:21 :00 13.223 4.473 1/31/2013 8:22:00 13.218 4.474 1/31/2013 8 : 23:00 12.799 4.251 1/31/2013 8:24:00 12
. 852 4.414 1/31/2013 8 : 25:00 13
. 217 4.469 1/31/2013 8 :2 6:00 13 .2 11 4.472 1/31/2013 8 :27:00 13.206 4.477 1/31/2013 8 :2 8 :00 13
. 19 4
.486 1/ 31 / 2013 8 : 29 :00 13.202 4.481 1 / 31/2013 8 :3 0 :00 13.218 4.471 1 / 31 / 2013 8 : 31 :00 13 .2 3 4
.466 1 /3 1/2 013 8 : 32 :00 11
. 587 4
. 349 1/ 31 / 2013 8 : 33 :00 10
.067 5.079 1/ 31 /2 013 8:34:00 

# I 10.068 5.085 1 / 31 / 2013 8 : 35 :00 5
. 836 2.795 1/ 31 /2 013 8 : 36:00 0.14 1 0.082 1/31/2013 8 : 37:00 

# I 0.126 0.072 1/31 /2013 8 : 38:00 0
. 126 0.07 1/31/2013 8:39:00 0
. 118 0 .068 1/31/2013 8:40:00 0.101 0.067 1/31/2013 8:41 :00 4.39 1.693 1/31/2013 8:42 :00 13.141 4.468 1/31/2013 8:43 :00 13
. 186 4.47 1/31/2013 8 :44:00 13.183 4.479 1/3 1/2 013 8 :45 :00 13.195 4.476 1 / 31 / 2013 8 :46 :00 13.177 4.488 1/3 1/2 013 8 :47 :00 13
. 18 4.488 1/ 31 / 2013 8 :48 :00 13
. 191 4
.482 1/ 31 / 2013 8 :49 :00 13.187 4.486 1/ 31 / 2013 8 : 50 :00 13
. 191 4.483 1/31/2013 8:51:00 13.181 4.489 1/3 1/20 13 8 :52 :00 13.164 4.498 1/31/2013 8 :53 :00 13
. 161 4.5 1/31/2013 8:54 :00 17
. 665 1.889 1/31/2013 8:55 :00 13.231 4.494 2.966 4.245 4.782 3.872 4.782 3.666 4.788 3.59 3.231 3.652 2.56 3.601 2.542 3.681 3
.056 3
. 245 3
. 112 3 .2 91 3.098 3.439 3
. 11 4
. 286 2
. 175 2.777 -0 .001 -0.11 -0.007 -0.37 1.903

-0.281 4.769 0.137 4.783 0.198 1.51 2.137 -0.012 4.409 -0.012 4.484 0.951 4.199 2
. 986 2
.777 2.968 3
.013 3
.079 2
. 684 3
.049 2.775 3 .0 8 2.835 3.136 3.026

3
. 2 3
. 144 3.202 3.188 3
. 163 1.266 3
. 154 2.565 2.761 2.616 2.91 2
. 894 2.494 2.485 1.498 1.849 9.321 2.48 -0.04 -0.008 19
. 138 4.85 -0.021 -0.009 19.091 33.208 0
.071 -0
.01 19.39 48.937 0.06

-0.009 NOx/02 Cal H igh 12
. 251 22
. 504 0.022 -0.01 16
. 767 23.882 -0.002 -0.01 18
. 882 24
.479 0.021 -0
.011 NOx Mid 18.8 83 7
. 823 0.029 -0.011 02 Cal H ig h 11.201 0.227

-0
.053 -0
.011 10
.047 0
. 182 -0.056 -0
.011 02 Mid 4.522 0. 18 -0
.038 -0.011 3.547 0.269 1.83 -0
.012 

### ITHC Zero 9.961 0.212 1.636 8 .374 9 .9 71 0.204 -0.324 83.091 02 bias 4
. 941 10
.747 -0
. 287 84
. 567 0
.057 24.676 -0.04 84 .7 06 0
.032 24.704 -0.011 84.737 NOx bias 0
.03 8
. 623 46.602 84.445 0.026 0.183 135.372 84.47 0.026 0.161 

# I 135.972 

# I 84.458 CO bias 0.027 0
. 147 118.114 83.888 0.027 0
. 135 6.722 84.228 0.026 0.113 0.092 85
.037 0.026 0
. 126 0.091 85
.007 0
.026 0.1 2 6 0.088 84
. 807 2.222 3 .2 51 0.244 85
.008 

### ITHC High 5
.491 14
. 166 5
. 581 58.552 0.036 0
. 157 -0
.031 46
. 871 0
.026 0.136 -0
.02 46
. 63 0
.026 0.129 -0
.009 46
. 527 

### ITHC Mid 2
.465 0.13 0.029 38
.469 0
.031 0
. 134

-0
.058 25.219 0.027 0
. 116 -0.039 25
. 349 

### ITHC low 6
. 971 14
. 556 21.119 25.263

13 31
.498 97.914 20
. 687O2 CO 2**NO~** CO Date nme % % PPM PPM 1/ 31 / 2013 8:56:00 13.149 4.508 3
. 112 2
. 283 1/ 31 /2 013 8 :57 :00 13
. 14 4.513 3
. 156 2
. 253 1/ 31 / 2013 8:58 :00 13.147 4.51 3
.024 2
. 341 1/31/2013 8:59 :00 13
. 161 4.501 2
. 939 2.351 1/31/2013 9:00:00 13.161 4.503 2.972 2.446 1/31 / 2013 9:01 :00 13.16 4
. 504 3
.065 2
. 506 1/ 31 / 2013 9 :02 :00 13
. 15 4
. 51 3
.023 2
. 557 1 / 31 / 2013 9 :03 :00 13
. 156 4.508 2
. 926 2
. 556 1/31/2013 9:04 :00 13
. 157 4.507 2
. 98 2.55 1/31/2013 9:05:00 16.644 2.466 1.636 1.771 1/31/2013 9:06:00 13.213 4.513 3
.085 2
. 314 1/31 / 2013 9 :07 :00 13.134 4.523 3
.054 2
. 842 1/ 31/2013 9 :08:00 13
. 132 4
. 527 3
.001 2
.796 1/ 31 / 2013 9 :09:00 13
. 134 4.527 2
. 962 2
. 885 1/31/2013 9:10:00 13.135 4.526 3
.094 3.161 1/31/2013 9:11:00 13.133 4.527 3.037 3
. 112 1/31/2013 9 : 12:00 13.131 4.533 3
. 131 3
. 136 1 / 31 / 2013 9 : 13:00 13.114 4.545 3
. 205 3
.077 1/31 / 2013 9 : 14 :00 13.126 4.542 2
. 97 3
. 105 1/31/2013 9 : 15:00 13.131 4.54 2.974 3
. 28 1/31/2013 9 : 16:00 17.777 1.795 1.171 1.908 1/31/2013 9:17:00 13.249 4.536 2
. 987 2.462 1/31/2013 9 : 18 :00 13.128 4.548 2
. 985 3
. 257 1/31 / 2013 9 : 19 :00 13.108 4.558 3
.072 3
. 196 1/ 31 / 2013 9 : 20:00 13.096 4.569 3
.025 3
. 266 1/31/2013 9:21:00 13.056 4.591 3.243 3
.075 1/31/2013 9:22:00 13.059 4.592 3.202 3
. 104 1/31/2013 9 : 23 :00 13
.056 4.598 3
. 253 3
.004 1/31 / 2013 9 : 24 :00 13
.061 4.594 3
. 149 2.801 1/ 31 / 2013 9 : 25 :00 13.061 4.594 3
.05 2
. 93 1 / 31 / 2013 9 : 26 :00 13
.065 4.595 3
.031 3
.407 1/31/2013 9 : 27:00 7.715 2.545 1.877 3.677 1/31/2013 9:28:00 0.146 0.152 0
.001 4.393 1/31/2013 9 : 29 :00 0
. 122 0.146 -0,015 4.463 1/ 31/2013 9 : 30 :00 6.5 3.594 -0
.012 2.488 1/ 31 / 2013 9 : 31 :00 rl

## ~9;;'**;;:98;;3~---;5-::.1":7~5** --

_ ';;0

. ':':0::"11;' -{}
. 283 1/31/2013 9 : 32:00 3
. 862 1.918 2
. 813 -0.203 1/31/2013 9:33:00 '"I

## -0;;;**;::12;;3;-.....,;0.;:;.1~5;;.8 --4;::** **7;;:5;;;2~-"':0:::.1;::5::"'"** 1/31/2013 9:34:00 5
. 993 2.326 3
. 991 1
.083 1/ 31 / 2013 9 : 35 :00 13.073 4.574 2
. 977 4
. 149 1/ 31 / 2013 9 : 36 :00 13
. 105 4
. 576 2
. 972 4
. 347 1/ 31 / 2013 9 : 37:00 13
.092 4.589 3
.059 4
.057 1/31/2013 9:38:00 13.094 4.591 2
. 943 3.969 1/31/2013 9:39:00 13
. 103 4.592 3.263 4.404 1/31/2013 9:40:00 13
.084 4
. 598 3
. 124 4.48 1/ 31 / 2013 9 :41 :00 13.099 4
. 598 3
.084 4
. 39 1/ 31 / 2013 9 :42 :00 13
.09 4.602 3
. 176 4
. 227 1/31/2013 9 :43:00 13.089 4.604 3
. 204 4.366 1/31/2013 9:44:00 13.084 4.611 3
. 297 4.566 1/31/2013 9:45:00 15
. 255 3.242 2
. 367 3.895 1/31 / 2013 9 :46:00 18
. 646 1.511 0
. 678 0.776 1/ 31/2013 9 :47 : 00 13
.097 4.615 3
.053 3.512 1/ 31 / 2013 9:48:00 13.083 4.62 2
. 987 3
. 953 1/31/2013 9:49:00 13
.082 4.627 2.987 3.869 1/31/2013 9:50:00 13
.073 4.634 3.065 3.924 1/31/2013 9 : 51 :00 13
.081 4
. 635 2
. 953 4.007 1/ 31 / 2013 9 :52 :00 13
.077 4
. 638 2
. 887 3
.975 1/ 31 / 2013 9 : 53 :00 13
.058 4
. 648 3
.088 3
.76 1/31 / 2013 9:54 :00 13.08 4.64 2
. 993 3.968 

### 0 , % 13.012 13.006 13.023 13.031 13.034 13.038 13.026 13.032 13
.03 13.021 13.002 12
. 995 12
. 998 12
. 997 12.993 12.997 12.991 12
. 98 12
. 996 12.999 12
. 991 12.986 12
. 988 12
. 976 12
. 959 12
. 943 12.941 12
. 938 12
. 948 12
. 947 12
. 947 12.954 12
. 956 12
. 968 12
. 97 12
. 971 12
. 97 12.971 12
. 981 12
. 985 12
. 993 12.975 12.982 12.972 12
. 97 12
. 969 12
. 965 12
. 963 12.956 12
. 954 12
. 958 12
. 96 12
. 972 12
. 966 12.959 12
. 961 12
. 96 12
. 951 12
. 962 NO , PPM 31.944 32
. 309 32
. 165 32
.066 31.894 31.927 31.984 32
.002 31.847 32.303 32
. 631 32
. 636 3 2. 614 32
. 548 32
. 555 32
.453 32.574 32
. 669 32
. 344 32
.039 32
. 642 32.393 32
. 191 32
. 538 32
. 612 33.267 33.162 33
. 269 33
. 284 32
. 962 32
. 555 32.411 32.29 32
. 208 32.115 32
.005 32.179 32.02 31
. 649 31
. 595 31.48 31.918 31.743 31
. 8 31
. 929 31.812 3 1. 964 31
. 86 31
. 859 31
. 924 31.796 31
. 829 31.721 31.768 31
. 684 31
. 626 31
. 648 31
. 959 31.696 

## co PPM 99
. 181 94.353 99.788 99.539 102.767 106
. 121 109.258 108.335 109.846 104.818 99.362 100.334 99
. 974 102.143 104.432 103.05 104.609 104.572 107.131 115.415 108.616 108
. 876 114.346 111.421 113.825 102.674 100.824 98
. 771 96
. 832 99
. 398 111.686 114.197 119.572 120.D33 122
. 251 124
. 985 121.549 121.44 129.713

132
. 1 134
.913 127.946 124.905 129.546 127
. 576 128.512 124.424 127.123 131.455 126.375 128
. 872 131.254 133.151 130.428 133.245 134
.775 134
.072 128.899 134.578 

### THe PPM 18.527 17
. 106 18
. 559 18
. 703 19
.731 20
. 3 21.583 21.112 21.684 20.625 18.72 18
. 821 18
. 907 19
. 347 20.721 19
. 513 19
.436 19
. 332 20
. 251 2 3.04 21
. 63 21.174 22.591 21.773 22
. 586 18
. 815 17.837 17
. 341 16
. 993 17
.47 20
. 987 21.796 23.468 24.097 CO bias 24
. 354 25
. 322 02/ C02 bias 23
. 584 23 .927 NOx bias 26.67 27
. 655 28
. 593 25
. 909 24
. 168 26
. 603 26
.022 26
. 118 24
. 836 26.03 27.44 25
. 369 26
. 304 2 7
. 104 27
. 693 25
. 974 27.235 28
. 196 28
. 399 25
. 984 28
.404O2 CO 2 NO x CO Date Time % % PPM PPM 1/31/2013 9:55:00 13.063 4.65 3.134 3.927 1/31/2013 9:56:00 13.077 4
. 646 3.004 3.799 1/31/2013 9 :57 :00 13.458 4
. 378 2.853 3.788 1/ 31/2013 9 :58 :00 20.558 0
. 252 0
.068 1
. 112 1/ 31 / 2013 9 :59 :00 14
. 589 3
. 883 2
. 19 1
. 873 1/ 31/2013 10 :00 :00 13.064 4
. 655 2.851 3.466 1/31 / 2013 10 :01 :00 13.055 4
. 662 2
.772 3
.475 1/31/2013 10 :02:00 13
.039 4.672 2.867 3.467 1/31/2013 10:03:00 13
.032 4.681 2
. 839 2.652 1/31/2013 10:04:00 13.027 4
. 687 2.79 2.687 1/31/2013 10:05:00 13.03 4
. 688 2.848 2.925 1/31/2013 10:06:00 13.028 4.689 2.882 2 .77 2 1/ 31 / 2013 10 :07 :00 13 .0 32 4
. 691 2.867 2.964 1/ 31/2013 10 :08 :00 13.034 4
. 691 2
. 895 2
. 952 1/ 31/2013 10 :09 :00 13 .6 35 4
. 282 2.767 2.533 1/31 / 2013 10 : 10:00 20.509 0.32 1 0
.061 0 .7 31 1/31 /2 013 10 : 11:00 16
. 257 2.94 1.678 1.289 1/31/2013 10:12:00 13.05 4.698 3.006 3.673 1/31/2013 10:13:00 13
.042 4.704 2.973 3.924 1/31/2013 10 : 14:00 13.045 4.707 3.114 3.815 1/31/2013 10:15 :00 13
.056 4
.706 2
. 946 3.97 1/ 31/2013 10 : 16:00 13.053 4
.71 3.07 4
. 167 1/31 / 2013 10 : 17 :00 13.055 4
.713 3
.084 4
. 277 1/31 / 2013 10 : 18:00 13.057 4
.714 3 .0 57 3.949 1/ 31/2013 10 : 19:00 13
.046 4.721 3 .0 13 3
. 916 1/31/2013 10 : 20:00 13
.048 4.723 3
.01 3.816 1/31/2013 10:21:00 10.772 4.732 1.68 2
. 172 1/31/2013

## 10:22:001"'1"';9::i'.i97;";4~--;5"'.3:i:O"'7--_iO**:;:0~21:-1** -0.284 1/ 31/2013 10 :2 3 :00 8
. 987 4
.727 0 .2 58 -0
. 386 1/31/2013 10 :2 4 :00 0
. 22 9 0
. 268 4 .7 05 0.002 1/ 31 / 2013 10 : 25 :001"'1

## -0;;;**~12:;:1;-""';0';; .2** **;':;4;;'9 --4';';** **;':73:;:1~""';0';; 1:;;6;;'2""**  1/31 / 2013 10 : 26 :00 0
. 12 0
. 244 2 .3 1 7 1.401 1/ 31/2013 10:27 :00 0
.097 0.242 -0
.037 4
. 329 1/31/2013 10 : 28:00 0.095 0.241

-0
.041 4.44 1/31/2013 10:29:00 7.499 2.944 1.627 3.539 1/31/2013 10:30 :00 13.053 4.715 2.995 1.879 1/31/2013 10:31 :00 13.078 4
.718 2
. 967 1.598 1/ 31 / 2013 10:32 :00 13.083 4
.724 3
.015 1
. 854 1/ 31 / 2013 10 : 33 :00 13
.096 4 .724 2
. 955 1 .7 53 1/ 31/2013 10 : 34 :00 13.107 4
.722 2.921 1.624 1/ 31/2013 10 : 35 :00 13
.098 4.732 3.02 1.556 1/ 31/2013 10:36 :00 13
. 123 4.725 3 1.435 1/31/2013 10:37:00 13
. 117 4.731 3.108 1.62 1/31/2013 10:38 :00 13.125 4.73 2.957 1.498 1/31/2013 10:39 :00 13.119 4.735 3.047 1.635 1 / 31/2013 10:40 :00 13
. 124 4
.739 2
. 989 1.766 1/ 31 / 2013 10:41 :00 18 .3 73 1.602 1.022 0.945 1/31 / 2013 10 :42 :00 20
.487 0.5 0
.05 0
. 135 1/ 31/2013 10:43 :00 13
. 288 4.722 2 .72 3 0.999 1/31/2013 10:44 :00 13.135 4
.739 2.952 1
. 815 1/31/2013 10:45 :00 13.141 4.74 2.898 1.95 1/31/2013 10:46:00 13.141 4.742 2
.794 2.571 1/31/2013 10 :47:00 13.131 4.749 2
. 919 3.228 1/31/2013 10:48 :00 13
. 138 4.748 2.882 3.44 1 / 31/2013 1 0 :49 :00 13.145 4.746 2
. 822 3
.475 1/ 31 /2 013 10 : 50 :00 13
. 143 4
.748 2
. 938 3
. 527 1/3 1/ 2013 10 :51 :00 13
. 144 4 .7 49 2
. 919 3 .7 8 1 / 31 / 2013 10 : 52 :00 13.134 4
.755 3
.048 3.673 1/31/2013 10:53:00 13.138 4.757 2.977 3.454 

### 0 , 

### % 12.952 12.959 12.967 12
. 954 12
. 948 12 .946 12
. 946 12
. 946 12.944 12.943 12.94 12
. 925 12
. 926 12
. 943 12
. 946 12.942 12
. 928 12.916 12.926 12
. 929 12
. 933 12
. 933 12
. 941 12.938 12.929 12.922 12.927 12
. 93 12
. 934 1 2. 936 12
. 936 12.945 12.942 12.941 12.939 12.944 12
. 949 12
. 945 12
. 949 12
. 949 12
. 953 12
. 963 12.962 12.966 12
. 962 12
. 958 12
. 952 12
. 958 12
. 961 12.976 12.982 12
. 99 12
. 981 12
. 991 12
. 995 12
. 989 12
. 981 12
. 973 12
. 983 

### NO , PPM 31.823 31.814 31.712 31.951 32
. 151 32.246 32.15 32
.489 32.701 32
.456 32.412 32
. 517 32
.429 32
. 316 32
.472 32
. 51 32
. 637 32
. 599 32.449 32
.58 32
. 313 32
. 199 32.133 32
. 151 32
. 236 32.385 32.622 32.658 32
. 899 32 .99 3 33
. 114 33
.069 33.095 33.368 33.73 33
. 563 33
. 822 33
.412 33.805 33
.771 33
. 928 34
.013 33.789 33
. 793 33.697 33
. 584 33
. 929 34
.096 33 .7 48 33
. 329 33
. 289 32 .3 25 32
. 134 31.964 31.858 32.005 32
.011 32 .3 7 32.35 

## co PPM 132
. 994 130.564 132.239 131.345 125.515 125
. 954 125.576 124
.757 113.932 119.131 124
.722 123.821 124
. 836 126
. 273 121.869 120
. 343 118.741 119.525 123.859 120.15 124.012 124
. 868 128.647 124.947 125.453 124.189 113.902 108.858 101.823 95
. 106 90.984 87.517 87
. 82 80.19 70.732 70.104 60.772 69
.428 67
. 36 60.212 57.097 49.895 58.242 55.264 60.834 69.242 57
. 275 54.851 49.515 67.433 73.152 91.757 110.64 116
. 978 118
.058 118
. 641 119
. 274 112.812 110.44 

### THe PPM 26.775 26.544 27.108 27.498 24.203 24 .7 43 23.731 24
. 305 21.575 23.397 25.198 24.519 24.937 24.515 23
. 699 23.639 23.535 23.391 24.316 23.491 24.211 24 .208 26 .3 85 25.307 25.14 25
. 191 21.753 19.509 02/C02 bias 18
.433 17.051 15 .71 8 NOx bias 14.57 14
. 199 12.537 CO bias 10.823 10
. 808 8.598 10
. 502 10
. 278 8
. 613 7.618 6
. 169 8
.096 7.105 8.556 10.568 7.2 3 7.356 5 .63 9 .7 82 11
.477 15
.484 21.261 21.477 22
. 579 23.738 23
. 615 21.515 20.437O2 CO 2 NO x CO Date Time 

### % % PPM PPM 1/ 31 / 2013 10 : 54 :00 13.131 4
.764 2
.792 3
. 242 1 / 31 / 2013 10 : 55 :00 13.131 4
.766 2
. 818 3
.049 1 / 31 / 2013 10 : 56 :00 13.132 4
.764 2
. 857 2
. 966 1/31/2013 10 : 57:00 16.406 2
. 861 1.6 1.989 1/31/2013 10 : 58 :00 13.161 4.763 2.723 2.379 1/ 31 / 2013 10 :59 :00 13.138 4
.764 2. 722 2.651 1/ 31 / 2013 11 :00 :00 13.139 4
.762 2
.704 2
. 882 1/ 31 / 2013 11 :01 :00 13.131 4
.773 2
.797 2
.726 1/31 / 201 3 11 :02:00 13.134 4.771 2
.788 2.504 1/31/2013 11:03:00 13.136 4.77 2
. 666 2.363 1/31/2013 11:04:00 13
. 135 4.77 2.819 2.164 1/ 31 / 2013 11 :05:00 13.134 4.773 2
. 695 2
. 16 1/ 31 / 2 0 13 11 :06 :00 13
. 133 4
.776 2
. 862 2
.06 2 1/ 31 / 2013 11 :07 :00 13.1 2 1 4
.783 2.986 2.131 1/31/2013 11 :08:00 13
. 113 4.791 2. 875 1.933 1/31/2013 11:09:00 16.454 2.763 1
.703 2.169 1/31/2013 11:10:00 20
. 286 0.688 0
.098 0
. 288 1/ 31 / 2013 11:11 :00 13.239 4
.76 2
. 918 2
. 334 1/ 31 / 2013 11 : 12 :00 13.141 4
.773 2
. 941 3
. 226 1/31 / 2013 11 : 13:00 13.139 4.773 2
. 888 3
. 136 1/31/2013 11 : 14:00 13.134 4
.777 2
. 976 3
. 275 1/31/2013 11 : 15 :00 13.14 4.774 3.031 3
.407 1/ 31 / 2013 11 : 16 :00 13.133 4
.782 3
. 127 3
. 205 1/ 31 / 2013 11 : 17 :00 13.146 4
.773 2
. 974 3.516 1/ 31 /2 013 11 : 18 :00 13.155 4
.769 3
.022 3
. 391 1/31 / 2013 11:19:00 13
. 15 4.771 2
. 986 3
. 333 1/31/2013 11:20:00 13
. 15 4.773 3.035 3.267 1/31/2013 11:21:00 4
. 394 1.611 1.067 3.803 1/31 / 2013 11:22:00 0
. 1 2 4 0.292

-0
.029 4.393 1/ 31 /2 013 11 : 23 :00 0
. 12 0
. 287 -0.D35 4
.45 3 1/ 31 / 2013 11 : 24 :00 6
. 615 3
.766 -0
.032 2.476 1/31/2013 11:

## 25:001r-:1:';0:';**0'"31:--;;5';;.3~5;;'6** -- - "'0
.

"'0;;33:-' -0.31 1/31/2013 11:26:00 3
. 285 1.807 3
.034 -0.222 1/31/2013 11 : 27:001r-:';0":'
. 1'"2

## --;;0';;**2~96~-4'i' .** **7~1:-::5--;;0C;.1'"25;::-'** 1/ 31 / 2013 11 : 28 :00 0
. 109 0
. 274 1.879 0
.085 1/ 31 / 2013 11 : 29:001r-"0:;'
.0:::9:::4--;;0';;
. 2::=6:;"3

## ---~0**~0~32:--;;-0:-: 0~2~9"**  1/31/2013 11 : 30:00 8.113 4.521 3
. 228 1.85 1/31/2013 11 : 31:00 10.049 5.359 4
.736 4.374 1/31/2013 11 : 32 :00· .. 1...:,:;10,:.: 0;,;6;;.........:5,;:.'"36;;....-.;.4
. "74;;3:--"""'4;:;.4"'2.;.4-. 1/ 31 / 2013 11 : 33 :00 12
. 291 4
. 884 3
.423 4
.001 1 / 31 / 2013 11 : 34 :00 13.114 4
.786 2
. 922 3.605 1/ 31 / 2013 11 : 35 :00 13
. 125 4.782 2
. 86 3.485 1/31/2013 11 : 36:00 13.122 4.782 2
. 822 3.662 1/31/2013 11:37:00 13.117 4
.786 2.936 3
.783 1/31 / 2013 11:38 :00 13.121 4.784 3
.017 3
. 95 7 1/ 31 /2 013 11 : 39 :00 13.115 4.789 3
.094 3
. 992 1/ 31 / 2013 11:40 :00 13.115 4
.791 3
.09 3
. 951 1/31/2013 11 :41 :00 13
. 128 4.784 3
.008 3
. 676 1/31/2013 11:42:00 13.121 4.788 2.956 3.642 1/31/2013 11:43:00 13.116 4.79 2
. 988 3.569 1 / 31 / 2013 11 :44:00 18
. 281 1.724 1
.009 2
. 146 1/ 31 / 2013 11:45 :00 16
.095 3
. 136 1.655 1.407 1/ 31 / 2013 11 :46 :00 13.131 4.78 2
. 881 3
. 62 1/31/2013 11 :47:00 13.119 4.794 2
. 944 3.61 1/31/2013 11 :48:00 13.12 4.794 2
. 869 3.596 1/31 / 2013 11 :49 :00 13.112 4
.796 2
. 948 3
. 882 1/ 31 / 2013 11 :50 :00 13.108 4
.798 2
. 956 3
. 866 1/ 31 / 2013 11 : 51 :00 13.10 7 4
. 8 3
.02 4
.029 1/31/2013 11 : 52:00 13
.094 4.807 3
.034 3.599 

### 0, % 12
. 981 12
. 982 12
. 987 12.976 12
. 989 12
. 994 12
. 996 12
. 983 12
. 994 12
. 996 13.002 12
. 995 12
. 995 12
. 985 12.968 12.97 12.967 12
. 969 12
. 977 12.981 12.976 12.982 1 2. 96 12
. 979 12.988 12
. 991 12
. 984 12
. 991 12
. 989 1 2. 986 12
. 975 12
. 979 12.972 12
. 958 12
. 969 12
. 981 12
. 984 12.979 12
. 965 12
. 97 12.974 12.981 12.982 12.975 12
. 975 12
. 97 12.964 12.976 12.977 12
. 969 12
. 985 12
. 986 12.989 12.976 12
. 975 12
. 968 12
. 965 12
. 968 12
. 953 NO , PPM 32
. 391 32
. 383 32.494 32
. 52 32.353 32
. 241 32
.026 32
. 388 32
. 355 32.138 32.011 31
. 966 3 2. 114 32
. 183 32
.46 32
. 098 32
. 719 3 2. 743 32.548 32
.434 32
.425 32
. 603 32
. 897 32
. 505 32
. 289 32
.44 32
.425 32.459 32
. 35 2 3 2. 36 3 2
. 533 32.442 32
.427 32
. 928 32.45 32
. 2 0 9 32.372 3 2 .239 32
. 501 3 2
. 148 32
. 21 32.238 31
. 949 3 2. 065 32
.095 32
. 34 32
.404 32
. 202 32
. 161 32.468 31
. 97 32
. 194 32
. 215 32.495 32.472 32
. 329 32
.4 25 32
. 556 32
. 801 

## co PPM 110
. 928 109
. 835 107
. 266 105.603 107
. 977 107
. 204 116
. 261 111
. 56 109.53 110.24 113.125 110
. 974 112
.426 113
. 288 109
. 188 119.526 107
. 351 105.43 108
.742 109
.41 114.052 109.837 103
. 683 109
.482 112.854 115.663 114.65 114
.027 115
. 994 114
. 23 2 113.687 115.081 117.689 108
.039 116
. 288 118.581 118
. 877 120
.026 122.139 119.583 119
.099 117
.043 123
. 843 126.094 125.155 122.587 120
.446 120
. 131 120
. 189 120
. 816 125.312 123
. 246 121.513 119.002 116.785 121.442 119.191 123.173 111.824 

### THe PPM 2 1.004 20
.719 20
.066 19
. 621 19.556 19
. 686 22
. 63 21.226 20
. 682 20.394 21.465 21.218 22
. 23 21.632 20.148 23.752 19.892 18
. 666 19
. 899

20 21.763 20.632 18
. 234 19
. 717 21
. 248 22. 3 17 22.078 21.681 21.58 20 . 807 CO bias 21
. 186 21
. 976 02/C02 bias 22
. 346 18 . 636 NOx bias 21.9 7 3 22 . 559 D i rect Zero 23
. 142 22
. 142 24 . 163 Span Direct 23.567 22
. 94 22.475 23.528 25
. 207 24
. 912 24
.049 23
. 823 23.75 22.241 23.467 24
. 135 2 3
. 263 23
. 874 23.461 21.618 23
. 109 22
.492 24.556 20.672O z COz NO. CO Date Time % % PPM PPM 1/31/2013 11:53 :00 13.092 4.809 2.884 3.552 1/31/2013 11:54:00 13.082 4.814 2.844 3.489 1/31/2013 11:55:00 13 .0 77 4
. 818 2
. 931 3.514 1/ 31/2013 11:56:00 16.3 2 6 2.919 1.594 2.358 1/31/2013 11:57 :00 13.129 4
. 802 2.679 2.732 1/31/2013 11 :58 :00 13.083 4
. 813 2.772 3.279 1/ 31 / 2013 11 : 59 :00 13
.069 4
. 825 2
. 801 2.95 1/31 / 2013 12:00 :00 13 .0 76 4.82 2
.727 2
. 979 1/ 31/2013 12:01 :00 13
.058 4.828 2.902 2.563 1/31/2013 12:02:00 13.069 4.822 2.835 2.31 1/31/2013 12:03:00 13.051 4
. 831 2
. 923 2.11 1/31/2013 12:04 :00 13.056 4
. 828 2.804 2
. 371 1/31 / 2013 12:05 :00 13.056 4
. 829 2
. 868 2
. 323 1 /3 1/ 2013 12:06 :00 13.058 4
. 824 2.905 2.208 1/31/2013 12 :07 :00 17
.457 2
. 204 1
. 367 1
.491 1/3 1/ 2013 12:08 :00 20.76 0.364 ·0
.012 0
. 174 1/31/2013 12:09 :00 16
. 277 3.029 1.608 1.275 1/31/2013 12:10 :00 13.107 4.798 2.883 3.502 1/31/2013 12:11:00 13.094 4.806 2.884 3
. 388 1/31/2013 12:12:00 13
. 103 4.802 2.842 3.726 1/3 1/ 2013 12 : 13:00 13.104 4
. 804 3
.044 3.993 1/ 31 /2 013 12:14 :00 13.105 4
. 804 2.969 3
. 97 1/3 1/2 013 12 : 15 :00 13.103 4
. 806 2
. 999 4
.079 1/ 31 / 2013 12:16 :00 13
. 106 4.804 2
. 953 3 .7 06 1 / 31/2013 12:17:00 13.1 4
. 807 2.837 3.484 1/31/2013 12:18:00 13.104 4.807 2.977 3.136 1/31/2013 12:19:00 10,42 3.765 2.706 3.36 1/31/2013 12:20:00 0
. 168 0.322 ·0
.022 4.197 1/31/2013 12:21 :00 0 .12 0.311 ·0.033 4.43 1/31/2013 12:22 :00 7. 383 4
. 175 -0.03 2.007 1/31/2013 12 : 23 :00
.. '""'1;,;0::,;
.00:,;:2:,--::5.:; .3

"'8""3--
.""0"'

.0:,::3 7 .-. -0
. 354 1/31/2013 12 :24 :00 8 .605 4.597 0
.408 -0.387 1/3 1/2013 12:25 :00 0
. 181 0.332 4.704 0
.036 1/31 / 2013 12: 26 :oor"'

## -';;0-;**1'i2'---;O:-i.3~174**--::-4.'71;;9:---;O-;.1:i;6'2-' 1/31/2013 12:27:00 8
.728 3.487 3.602 1.425 1/31/2013 12:28 :00 13.032 4.822 2.879 3.227 1/ 31/2013 12:29:00 13 .047 4.826 2.948 3
. 287 1/ 31 / 2013 12:30:00 13.056 4.826 2.908 3.253 1 / 31 / 2013 12 :3 1 :00 13.056 4
. 828 2.89 3
. 181 1 / 31/2013 12:32 :00 13 .0 57 4
. 827 2.893 3
. 114 1 /3 1/2013 12:33 :00 13
.058 4.828 2
. 87 3
. 652 1/31/2013 12:34 :00 13.05 4
. 832 3.041 3.504 1/31/2013 12:35:00 13.062 4
. 826 3
.048 3.346 1/31/2013 12:36:00 13.064 4.826 3
.048 3.462 1/31/2013 12 : 37 :00 13.07 4.824 3.004 2.987 1/31/2013 12:38 :00 13 .07 4 4.823 2.932 3.122 1/3 1/ 2013 12 : 39 :00 13.069 4
. 826 2
. 95 3.622 1/ 31 / 2013 12 :40 :00 17 .4 26 2
. 171 1
.436 2.044 1/3 1/ 2013 12 :41 :00 16.443 2
. 985 1
.47 1 1
.097 1/ 31 / 2013 12 :42 :00 13.057 4
. 833 2
. 933 3.226 1/31/2013 12:43:00 13
.052 4.837 2.931 3.263 1/31/2013 12:44:00 13.045 4.84 2
. 959 3.145 1/31/2013 12 :45 :00 13
.047 4.842 3
.041 2.947 1 /3 1/2013 12 :46 :00 13
.063 4.832 2.803 3
. 18 1/31/2013 12 :47 :00 13
.054 4.837 2.92 3
. 186 1/ 31/2013 12 :48 :00 13
.055 4
. 835 2
. 845 3
. 174 1/ 31 / 2013 12 :49 :00 13.054 4
. 836 2 .7 86 3 .2 83 1/ 31/2013 12 : 50 :00 13
.062 4.83 2.806 3.38 1/31/2013 12:51 :00 16.429 2.749 1.716 2
. 579 

### 0 , % 12 .9 59 12.953 12.948 12
. 949 12 .9 63 12
. 957 12
. 944 12
. 945 12
. 945 12.952 12
. 936 12
. 943 12
. 939 12
. 945 12
. 945 12
. 944 12.944 12
. 947 12.945 12
. 954 12
. 945 12
. 945 12 .947 12
. 946 12
. 948 12.945 12
. 948 12
. 945 12
. 954 12
. 949 12
. 94 7 12
. 946 12
. 948 12
. 924 12
. 945 12.946 12
. 954 12 .94 8 12
. 952 12
. 952 12
. 954 12
. 945 12
. 948 12.953 12
. 958 12.956 12
. 961 12
. 955 12
. 955 12.953 12.95 12.949 12.945 12.965 12
. 956 12
. 959 12
. 956 12
. 963 12.943 NO, PPM 32.655 32
. 583 32 .72 3 32
. 563 3 2.2 48 32
. 226 32
. 679 32
. 739 32.829 32.705 33
. 198 32
. 761 32 .9 81 32
. 928 32
. 977 32
. 677 32
. 804 32.522 32
. 579 32
. 187 32
. 355 32 .2 66 3 2. 292 32
.412 32.593 32
. 852 32
. 557 32
. 693 32.749 32
. 611 32
. 548 32 .7 39 32 .7 68 33
. 143 33.004 32.821 32
. 613 32
. 693 32
. 871 32.763 32 .3 09 32
. 812 32
. 845 32.732 33
.057 32
. 539 32
. 632 32.734 32.485 32
. 375 32
. 682 32
. 705 32
. 872 32.341 32.508 32
.416 32
. 388 32
. 19 32
. 862 

## co PPM 114.384 117.281 117.105 116.082 119
. 959 124.63 117
. 2 116
. 117 112.413**~13.492** 107.471 112.684 113.298 111.926 109,078 111.652 114.708 116.513 114.756 121.07 123.923 122
. 914 123.361 121.746 117
. 124 112.036 112.944 117.904 108
. 191 113
.413 116
.099 112 .7 11 112.108 108.761 103.458 108.572 109
. 805 111.139 109
.037 107
.009 118.264 115
. 325 110.847 112.407 104.874 110.519 119.572 111.061 116
. 102 121.268 119
. 328 115.778 111.794 118
. 823 120
. 157 121.207 123 .3 22 124.852 119
.007 

### THe PPM 21.578 22.672 22.323 21.173 22.544 24.365 21.741 21.692 20.95 21.152 19
. 805 20
. 56 20
.714 20.898 20
.459 20
. 375 21.554 23.042 22.111 23
.075 24
. 256 23.323 24 .3 98 24.236 22.326 20
. 933 21.073 23
. 218 19.549 CO bias 20.643 22
. 31 02/C02 b i a s 2 1
. 63 7 20
. 594 21 . 191 NOx bias 18
. 147 19
. 587 19
. 603 19
. 864 19
. 106 18
. 708 22.425 20
. 8 19.703 20.04 18
. 622 19
. 565 21.966 19
. 833 20 .82 4 21
. 995 22
. 603 21
.494 20
.012 22
. 1 24 22.636 22
. 622 22.324 23 .2 16 22
. 305O2 CO 2 NO. CO Date Time % % 

### PPM PPM 1/31/2013 12:52:00 14.61 4.048 2.107 2.125 1/31/2013 12:53:00 13.032 4.846 2.921 3.606 1/31/2013 12:54 :00 13.034 4.846 2.942 3.504 1/31/2013 12 : 55 :00 13.032 4
. 849 3.073 3
. 262 1/31 / 2013 12 : 56 :00 13.033 4
. 847 2
. 944 3
.02 1/31/2013 12:57 :00 13
.046 4
. 839 3
.027 3
. 354 1/31 / 2013 12 : 58 :00 13.046 4.841 2.969 3
.771 1/31/2013 12 : 59 :00 13
.041 4
. 844 3.056 3.407 1/31/2013 13:00 :00 13
.035 4.848 2.92 3.533 1/31/2013 13:01:00 13.032 4.851 2.889 3.11 1/31/2013 13:02:00 13.028 4.857 2.896 3.123 1/31/2013 13:03:00 16
. 121 3.041 1
. 656 2
. 233 1 / 31/2013 13:04:00 13.05 4
. 859 2
. 872 2.378 1/ 31 / 2013 13 :05:00 13.014 4.867 2
. 804 2.695 1 / 31 / 2013 13:06 :00 13.023 4.866 2
. 793 2.753 1/31/2013 13:07:00 13.019 4.868 2.741 2
. 851 1/31/2013 13:08:00 13.026 4.866 2
. 676 3.2 1/31/2013 13:09:00 13
.028 4.865 2
. 831 2.897 1/31/2013 13:10:00 13.005 4.885 2
. 933 2.484 1/31/2013 13:11:00 13
.007 4.889 2
. 964 2.236 1/31/2013 13 : 12 :00 13
.006 4
. 889 2
. 972 2
. 332 1/31/2013 13 : 13 :00 13
.011 4
. 882 2
. 94 2.059 1/31/2013 13:14 :00 13.012 4.882 2
. 818 2
. 201 1/ 31 / 2013 13:15 :00 13.013 4.882 2
. 813 2
.091 1/31/2013 13:16 :00 11
. 339 4.785 2
.053 2.042 1/31/2013 13:17:00 9.987 5.425 -0.01 -0.252 1/31/2013 13:18 :00'"1""9;;;.;;;98,;7,.........;5-:.4"3::-1---"'0".0;,:;25,..., -0.388 1/31/2013 13:19:00 4.017 2.222 2.657 -0.219 1/31/2013 13 : 20 :00'"1

## ""0~.::-12~4-....;0".3;;:5::-6**--4::-.,;;72~4,.....~0~ 1::,:38~**  1/ 31/2013 13:21:00 0.118 0.348 2.587 1
. 262 1/31 / 2013 13 : 22 :00 0
. 118 0
. 345 -0.031 4
. 334 1/ 31 / 2013 13 :2 3 :00 0.095 0
. 342 -0,038 4
.434 1/31/2013 13:24:00 9.248 0.353 -0
.027 2.407 1/31/2013

## 13:25**001.....,0;;;.::-12;;;3-....;0" 3~1::-5** ---"'0
. ;'0'"37:--"";0':';.0;'5::-3-, 1/31/2013 13:26:00 6.136 3.592 2
. 332 1.174 1/31/2013 13:27:00 10.01 5.425 4.747 4.352 1/31/2013

## 13:28**001'--:1;;;0';; 0';'13;---;:5":.4;;;25~-4::'** **~74:':8"""--:4-: 4;;;3::-1-'**  1/31/2013 13 : 29 :00 18
.081 1
. 128 1.453 2
.714 1/31 / 2013 13:30 :00 20 .722 0.316

-0
.026 0.308 1/31/2013 13 : 31 :00 20.73 0,035 -0.026 0
. 163 1/31/2013 13 : 32 :00 20
.735 -0.006 -0
.028 0.131 1/31/2013 13:33 :00 20
.736 -0.006 -0.029 0
. 135 1/31/2013 13:34:00 20
.735 8.137 -0.029 0.127 1/31/2013 13:35:00 20.735 9.603 -0.026 0.136 1/31/2013 13:36 :00 20.741 9.613 -0
.032 0
. 132 1/ 31/2013 13:37:00 20.746 9.572 -0
.033 0
. 126 1/ 31/2013 13:38:00 20.746 9.537

-0
.036 0
. 121 1/31 / 2013 13 : 39 :00 20.746 9.505 -0.033 0
. 114 1/ 31/2013 13:40 :00 20.744 7.926 -0
.031 0
. 111 1/31/2013 13:41:00 20 .7 5 5.111 -0.033 0.112 1/31/2013 13:42:00 20.753 5.109 -0.029 0.13 1/31/2013 13:43:00 20.76 5.109 -0,028 0.124 1/31/2013 13 :44 :00 20
. 759 5.763 -0.034 0
. 102 1/31/2013 13:45 :00 20
.763
..... :,;9

. ,;;66:;;9:...., -0,038 0.115 1/31/2013 13 :46 :00 20.766 1-;.9.:,:.6;:,7,...... -0.039 0
. 108 1/31/2013 13 :47 :00 20
.77 6.247 -0
.037 0
. 107 1 /3 1/2013 13 :48 :00 20 .7 65**1-::-5'",08~5:-1** -0.032 0
. 113 1/31/2013 13 :49 :00 13.561 4.864 2.486 1.249 1/31/2013 13:50:00 13
.021 4.543 2.841 1.873 

### 0 , % 12.943 12.942 12.94 12
. 94 12
. 944 12
. 947 12.941 12
. 943 12.944 12.944 12.937 12.939 12.915 12
. 936 12
. 94 12.941 12
. 944 12.948 12
. 929 12
. 927 12
. 915 12.929 12
. 925 12
. 937 12.92 12.924 12.936 12.914 12.919 12
. 903 12.934 12.927 12.914 12.928 12.932 12.933 12
. 928 12
. 899 12 .9 15 12
. 906 12
. 927 12
. 938 12.922 12.907 12.918 12.922 12
. 904 12
. 901 12
. 871 12.885 12.89 12.899 12.896 12
. 888

12.9 12
. 898 12
. 895 12.89 12
. 888 NO, PPM 32
. 841 32.967 33
.093 33.35 33 .262 32
. 939 32
. 893 32
. 979 32
.792 33.008 33
. 207 32.903 33 .2 91 33
. 149 33
.075 32.892 32
. 63 32.638 33
. 212

33.1 33
. 134 33
.066 33
. 103 32
. 847 32.936 32.94 32.781 33.045 32.675 33.004 32.627 32
. 847 32
. 96 33.187 32.639 32.839 32
. 723 33
. 313 32
. 746 33
.022 33
.026 32
. 773 33
.076 33.279 33
. 362 33
. 215 33 .6 65 33
. 905 34
.424 33
. 822 33.647 33.508 33
.771 33
. 897 33.666 33 .7 65 33 .7 04 33
. 95 34
. 147 

## co PPM 117.361 114.642 112.627 107.448 102.424 107.213 115.862 104.867 113.164 106.441 104.398 106.624 105.995 102
.789 107.249 108.166 116.596 112.531 109.1 106.18 106.601 104.894 106.315 105.32 112.874 107.754 106.751 109.495 108.902 107
. 134 114
. 172 112.723 111.122 103.13 111.188 112.261 115.377 102.448 109
. 34 109.652 105.992 108.305 108.063 103.687 99.973 107.042 100.669 96.728 89.293 90.124 92.004 91.478 87.142 87
. 133 91.024 90 .7 91 94.335 92.218 86.149 THC PPM 21.224 20.39 19
. 792 19.045 17
. 839 19 .0 2 21.901 18
. 391 19
. 974 18.197 18.254 18
. 883 18 .7 69 18
.005 19
. 162 18.944 20.323 19.972 19.884 18
. 555 18
. 846 17 .79 3 18.356 18
.094 20.968 19.139 18.462 02/C02 bias 19
. 236 19 . 234 NOx bias 18
. 534 20
. 357 20 . 388 CO b ias 19
. 36 17 .577 Direct Zero 20.374 19.964 21 . 445 Direct Span 17.703 19.856 19
. 105 18
. 332 18 .975 C02 Cal Zero 19.442 17.812 16.975 18
.496 16
. 93 16
. 5 14
.493

14.5 14.252 14
. 995 13
. 267 13.76 14
. 81 C02 Cal High 14
. 867

15
.7 C02 Mid 15 .0 12 13.325**~ ~** **N~** 

# m**~ N~**  

# m Date Time % % PPM PPM % PPM PPM 1/31/2013 13:51:00 13.016 4.547 2.769 1.967 12.879 34.147 87.157 1/31/2013 13:52:00 13.013 4.548 2.828 1.972 12.886 34.017 89 .32 1 1/31/2013 13:53:00 13.016 4.549 2
. 821 2.004 12.89 34.22 87.036 1/31/2013 13:54:00 13.014 4.551 2.829 1.848 12.886 34.143 85.563 1/31/2013 13 : 55:00 13.012 4.551 2.78 1.83 12.885 34.387 81.383 1/31/2013 13:56:00 13.012 4.557 2
.758 1.796 12.884 34.302 80.254 1/31/2013 13:57:00 13.014 4.554 2.746 1.808 12.891 34.266 81.11 1/31/2013 13:58:00 13.021 4.551 2.674 1.972 12.899 33.795 87.379 1/31/2013 13:59:00 13.015 4.554 2.77 1.961 12.892 34.125 85.903 1/31/2013 14:00:00 13.028 4.54 2.769 1.844 12.951 33.78 81.344 1/31/2013 14:01:00 1.702 0.681 0.521 0.744 4.189 12.375 48.309 1/31/2013

### 14:02:00r-~0';;.09~6;.....~0:;;.0:::0:;,7_~-:;;0~.0~36;-.....::-0~.04~9 __

### 0~.;;.02;;8;.....~0~.3:::6;9__ 

### 0:;;'.;94;8:-, 1/31/2013 14:03

## :00LI....::0~.0.::.93=-_:::.0.~0:::.07:.........;-~0;::.0::3.:.7_~-~0;::.0::3:::.8**_...;0::;.:::.02;:2:..........:0:::..2~8:::9:.....--=-o:::..~2:;24:.J** 1/31/2013 14:04:00 7.197 3.763 2.656 1.572 5.198 9.519 11.157 1/31/2013 14:05:00 10.014 5.096 4.744 4.366 9.936 22.586 124.097 1/31/2013

## 14:06:oo"I"';1~0:;;.0:;2;'3**-..;5:;:.0;;9;;.7-....;4.;73;;9;.........:4;;;.4:;:2:::.8--9;;:.;;.93;:;9:.........;24~.3;4:;:9:......:.1;:3 4;'::.2:;;9;';'9"1**  1/31/2013 14:07:00 11.358 4.527 2.93 3.391 11.318 21.481 101.822 1/31/2013 14:08:oo
..... .::.9.:.::9::.82=--_...;5::;.;1
__**-~0;::.0~2:.4...** -0.018 9.921 1.915 17.03 1/31/2013 14:09:00LI....::;9.;:98::;:5:..........:5:;.:.1::;0.;.7
__

### -o.;:;.0;:,31~ -0.403 9.913 1.197 -0.416 1/31/2013 14: 10:00
.....**.::3.:.::9:::.07:....._~1.:::8:;87:....._.:;2.;7;13;:........;-o.;:;.:.2:.::3::.3 _~4;:.0:;:6:::7_~1.::3.;;7.:;88::....--=-0::;.~26;;:6;..,**  1/31/2013 14: 

### l1:oo L 

# I**....::O:..:.1~2_.....:0::;.0:::5:..._4:.;** .

### .:.72~9:..........:0:;;.1~1::.8__

### 0:::.::.044::...._.:;24::..9:::64::.........:-::.0.~1.:.;73::...J 1/31/2013 14:12:00 0.116 0.043 2.288 1.453 0.022 10.975 36.975 1/31/2013 14:13:00 0.108 0.04 -0.036 4.323 0.019 0.843 132.579 1/31/2013 14:14:00 0.092 0.04 -0.04 4.431 0.018 0.745 

## 1 134.402 

### 1 1/31/2013 14:15:00 9.759 3.382 1.829 2.549 8.903 18.03 107.891 1/31/2013 14:16:00 13.265 4.395 2.561 0.59 13.236 29.591 51.999 1/31/2013 14:17:00 13.274 4.403 2.822 0.513 13.228 30.016 50.046 1/31/2013 14:18:00 13.276 4
.406 2.65 0.514 13.228 30.44 46 .3 91 1/31/2013 14:19:00 13.288 4.403 2.589 0.471 13.245 30.587 44.649 1/31/2013 14:20:00 13.279 4.409 2.699 0.478 13.237 30.593 45.885 1/31/2013 14:21:00 13.274 4.416 2.827 0.518 13.241 30.648 48.88 1/31/2013 14:22:00 13.275 4.417 2.819 0.504 13.231 30.706 47.865 1/31/2013 14:23:00 13.275 4.422 2.846 0.464 13.226 31.014 45.962 1/31/2013 14:24:00 13.253 4.436 2.95 0.39 13.24 30.842 45.429 1/31/2013 14:25:00 13.256 1/31/2013 14:26:00 13.243 1/31/2013 14:27:00 13.268 1/31/2013 14:28:00 13.301 1/31/2013 14:29:00 13.292 1/31/2013 14:30:00 13.275 1/31/2013 14:31:00 13.273 1/31/2013 14:32:00 13.266 1/31/2013 14:33:00 15.976 1/31/2013 14:34:00 16.902 1/31/2013 14:35:00 13.321 1/31/2013 14:36:00 13.309 1/31/2013 14:37:00 13.308 1/31/2013 14:38:00 13.318 1/31/2013 14:39:00 13.313 1/31/2013 14:40:00 13.319 1/31/2013 14:41:00 13.297 1/31/2013 14:42:00 13.3 1/31/2013 14:43:00 13.307 1/31/2013 14:44:00 13.294 1/31/2013 14:45:00 13.299 1/31/2013 14:46:00 13.289 1/31/2013 14:47:00 13.267 1/31/2013 14:48:00 13.263 1/31/2013 14:49:00 13.265 4.436 2.748 0.371 13.24 30.992 45.342 4.444 3.002 0.343 13.247 31.006 44.584 4.433 2.701 0.339 13.272 30.279 46.107 4.414 2.765 0.472 13.295 29.912 55.232 4.422 2.748 0.442 13.284 29.958 54.945 4.438 2.941 0.375 13.251 30.698 48.523 4.438 2.678 0.335 13.269 30.424 46.197 4.443 2.903 0.352 13.234 30.662 47.113 2.766 1.997 0.322 13.24 30.625 47.311 2.419 1.269 0.211 13.249 30.501 46.582 4.413 2.754 0.635 13.235 30.635 47.908 4.42 2
.769 0.648 13.223 30.67 47.142 4.421 2.838 0.698 13.235 30.393 49.647 4.417 2.632 0.706 13.235 30.611 49.991 4.421 2.641 0.624 13.238 30.485 46.614 4.42 2.68 0.729 13.257 30.3 51.401 4.434 2.77 0.709 13.223 30.692 49
. 806 4.435 2.804 0.707 13.227 30.713 47.554 4.429 2.72 0.717 13.26 30.499 48.824 4.441 2.807 0.68 13.218 30.896 46.986 4
.438 2 .75 6 0.676 13.242 30.753 46.777 4.445 2.761 0
. 622 13.238 30
. 867 45.424 4.463 2.918 0.56 13.227 30.879 44.823 4.465 2.861 0.592 13.219 30.773 47.842 4.463 2.835 0.574 13.207 30.944 48.253 

### THe PPM 13.144 13.91 13.89 13.197 12.294 11.209 11.389 13.627 13.744 12.215 8.292 5.669 5.204 5.685 5.562 6.73 5.722 1.163 -0.02 -0.02 -0.021 -0.018 -0.Q15 -0.015 1.463 6.397 5 .9 57 5.201 4.864 4.973 5.845 5.594 4.959 4.919 5.082 4.806 4.67 7.181 6.807 5.862 4.919 4.881 4.761 4.903 5.403 4.943 5.756 5.751 4.975 5.928 5
. 663 5.184 5.425 4.993 5.Q38 4.818 4.615 5.389 5.537 Direct Zero
Span Direct

02/C02 bias NOx bias

CO bias**~ ~** **~** 

## ro**~ N~**  

## ro Date Time % % PPM PPM % PPM PPM 1/31/2013 14:5 0 :00 13 .2 72 4.459 2
.732 0.555 13
. 248 30
.725 46.027 1 / 31 / 2013 14 :51 :00 15
. 738 2
. 927 1
. 948 0.502 13
. 235 30
. 855 45
. 795 1/ 31 / 2013 14 : 52:00 13.751 4.27 2.514 0.336 13
. 27 30
. 613 45.495 1/31/2013 14:53:00 13.294 4.446 2
. 886 0.532 13
. 231 30
. 785 46.523 1/31/2013 14:54:00 13.299 4
.442 2.898 0.511 13.269 30.706 45.481 1/31/2013 14:55:00 13.306 4.436 3
. 195 0.525 13.282 30.49 47
. 183 1/ 31 / 2013 14:56 :00 13
. 307 4
.435 2
. 923 0.551 13
. 274 30
.72 48
. 821 1/ 31 / 2013 14 :57:00 13.302 4
.438 2
. 953 0
.498 13.266 30 .7 84 44
. 861 1 / 31 / 2013 14:58:00 13.304 4
.436 2 .846 0.539 13
. 276 30
. 654 47.165 1/31/2013 14 :59:00 13.31 4.432 2.877 0.512 13.285 30.66 46.003 1/31/2013 15 :00:00 13.306 4.435 2
. 906 0.516 13.29 30
.492 46
. 671 1 / 31 / 2013 15 :01 :00 13. 30 7 4.435 4
.427 0.491 13.281 30.554 45
. 909 1/ 31 / 2013 15 :02 :00 13.309 4
.435 5 0
.46 2 13
. 287 30
. 518 45
.025 1/ 31 / 2013 15 :03 :00 13.301 4.442 5 0.482 13.283 30.403 47.217 1/31/2013 15 :04 :00 13.3 4.446 4
.78 0.491 13.278 30
. 509 46
. 878 1/31/2013 15 :05:00 13.277 4.459 4.633 0.401 13.243 31.146 42.023 1/31/2013 15 :06:00 13.278 4.455 2. 327 0.415 13.26 30
. 963 41.422 1/ 31 / 2013 15 :07 :00 13 .2 76 4.456 2
.099 0
.43 7 13
. 242 31.006 42.115 1 / 31 / 2013 15 :08 :00 13.274 4
.459 2
. 191 0.425 13.212 31.118 41.332 1 / 31/2013 15 :09 :00 13
. 289 4.448 2
. 175 0.475 13.248 30
. 604 44
. 198 1/31/2013 15 : 10:00 13
. 287 4.448 2.021 0.588 13.257 30.17 50.633 1/31/2013 15 : 11:00 13
. 313 4.431 1.912 0
. 674 13.291 29.824 55.295 1/31/2013 15 : 12:00 13
. 258 4
.463 2
.062 0
. 52 13.247 31
.016 45.723 1/ 31 / 2013 15 : 13:00 13
. 357 4.404 1.798 1
. 219 13.314 28
. 219 90
. 907 1/ 31 / 2013 15 : 14 :00 13.299 4.443 1
.915 0
. 629 13.295 29
. 948 52
. 316 1/31/2013 15 : 15 :00 13.301 4
.446 1.909 0.628 13
. 271 30 .3 85 51.57 1/31/2013 15 : 16:00 13.305 4.443 1.962 0.681 13.269 29
. 608 57.438 1/31/2013 15 : 17:00 13.283 4
.461 2. 062 0.554 13.25 30
.747 47
. 221 1/ 31 / 2013 15 : 18 :00 13.295 4.454 2
.04 0
. 535 13.256 30
. 345 46
. 558 1/31 / 2013 15 : 19 :00 13.293 4
.457 2
.016 0.55 13 .2 6 30
.484 47
.03 6 1/ 31 / 2013 15 : 20: 00 13.2 77 4
.466 2. 1 0
. 5 07 13.242 30
. 805 43
.775 1/31 / 2013 15:21:00 13.279 4.467 2
. 125 0.505 13.247 30
. 664 44.014 1/31/2013 15 : 22:00 13.276 4.471 3
.417 0.517 13
. 224 30.752 45
. 618 1/ 31 / 2013 15 : 23 :00 13.284 4.47 5 0
.488 13
. 257 30
.487 46
.083 1/ 31 / 2013 15 : 24 :00 13.276 4
.478 4
. 815 0.489 13
. 231 30
. 78 45
. 811 1 / 31 / 2013 15 : 25 :00 13
. 29 4
.473 4
.717 0.515 13
. 251 30
.444 46
. 984 1/31 /2 013 15 : 26 :00 13.295 4.474 5 0.521 13.254 30
. 289 49.108 1/31/2013 1 5: 27:00 13. 287 4.479 5 0.528 13.24 30.544 48.328 1/31/2013 15 : 28 :00 13.301 4.475 5 0.517 13.267 3 0. 443 48.042 1/ 31 / 2013 15 : 29 :00 13 .2 98 4
.48 5 0.4 7 13.251 30
. 676 44.848 1 / 31 / 2013 15 : 30 :00 13
. 296 4
.479 5 0
.463 13
. 262 30 .47 1 44
. 911 1 / 31 / 2013 15 : 31 :00 13.291 4.484 5 0.513 13.269 30
. 182 48
. 563 1/31/2013 15 : 32 :00 13.301 4.479 5 0.57 13.291 29
. 95 51.811 1/31/2013 15 : 33 :00 13.292 4.483 5 0.521 13.249 30
.472 48.52 1/31 / 2013 15 : 34 :00 13.295 4.484 5 0
.488 13.278 30
. 238 46.993 1/ 31 / 2013 15 : 35 :00 13. 298 4
.482 5 0.497 13
. 275 30
. 206 47.468 1 / 31 / 2 0 13 15 : 36 :00 13
. 3 4.48 5 0.508 13.288 3 0. 071 48
. 936 1 / 31 / 2013 15 : 37 :00 13.278 4.496 5 0
.474 13.247 30
. 629 45.683 1/31/2013 15:38 :00 13 .2 91 4.484 5 0.455 13.277 30
. 287 45.683 1/31/2013 15 : 39 :00 13
. 279 4.489 5 0.476 13.26 30
.438 46.732 1 / 31 / 2013 1 5 :40 :00 13.281 4.49 5 0
.452 13.255 30
. 566 45.065 1/ 31 / 2013 15.41:00 13.29 4
.486 5 0.488 13
. 266 30
. 31 47
. 314 1 / 31 / 2013 15 :42 :00 13
. 296 4.484 5 0
.483 13.272 3 0. 317 47.577 1/31 / 2013 15 :43:00 13.233 4.483 5 0.494 13.271 30
. 279 48
.094 1/31/2013 15:44:00 0.742 0.357 1.574 0.177 4
. 221 12
. 805 36
. 639 1/31 / 2013 15 :45 :00 0
.093 0.089 0
.072 -0
.089 0
.028 0
. 285 1.056 1/ 31 /20 13 15 :46 :00 

## r 

# l**~0i:' 0:::;9;';2:---;;0-::** **0;i:87':--'::0':: 0~4'---:-0:':** **0':i6~5-~0i:' 0::;2;';2:---;;0;';** **.2 ~2** **':---o~ ;':2~25:-'**  1 / 31 / 2013 15 :47: 00 14
. 81 8
. 158 3
.493 4
.07 3 11
. 217 21.444 50
. 962 1 / 31 / 2013 15 :48 :00 18 .7 84 9
.796 4
. 753 9.297 18
.759 48
. 93 224
. 876 

### THe PPM 4
. 978 4
. 8 7 6 4
.72 4
. 93 4.534 4
. 837 5
. 656 4
. 69 5
. 105 4
. 696 5
.048 4 .7 6 2 4.58 7 5
. 125 4
. 837 3
. 885 3
.743 4
.03 3
. 949 4
.456 5.555 6
. 984 4
. 857 19
. 971 6
.056 6. 117 7
. 959 4
. 998 4
. 94 7 5
.04 5 4. 364 4.617 4.744 5
.096 4. 694 4
. 886

5. 7 5.412 5
. 19 4 .5 04 4. 364 4
. 938 5
. 867 5.346 4
. 961 5
.03 5
.416 4 .5 4 4
. 643 4
. 836 4
. 617 5
.064 5.078 5
. 15 4.75 4
.49 4.594 4
.463 4
. 907 Cal Ze ro

### 0, Date Time % 1/31/2013 15 :49:001 18
.794 1/31/2013 15 : 50:00 11.242 1/31/2013 15 : 51:001 10.036 1/31/2013 15 :52:00 10.036 1/31/2013 15 :53:00 9
. 986 1/31/2013 15 :5 4 :00 9 .976 1/31/2013 15 : 55:00 9
. 977 1/31/2013 15 :56:00 9
. 982 1/31/2013 15 :57:00 9
. 986 1/31/2013 15 :5 8 :00 9.985 1/31/2013 15 :59:00 9
. 987 1/31/2013 16:00 :00 9
. 999 1/31/2013 16:01:00 10.011 1/31/2013 16:02 :00 10 .011 1/31/2013 16:03 :00 10
.029 1/31/2013 16:04:00 10.036 1/31/2013 16:05:00 10.038 1/31/2013 16 :06:00 6.375 1/31/2013 16 :06:20 9.248 1 /31/2013 16:06:30 9.261 1/31/2013 16:06 :40 11
. 181 1 /31/2013 16:06 :50 14
. 656 1/31/2013 16 :07 :00 14
. 883 1/31/2013 16:07 : 10 14.916 1/31/2013 16 :07:20 1 14.935 1/31/2013 16 :07:30 14.121 1/31/2013 16 :07:40 11.452 1/31/2013 16 :07:50 11.172 1/31/2013 16 :08:00 11
. 131 1/31/2013 16 :08:10 11.124 1/31/2013 16 :08:20 11
. 124 1/31/2013 16:08:30 11.121 1/31/2013 16:08:40 11
. 259 1/31/2013 16 :08:50 12.857 1/31/2013 16 :09:00 14 .939 1/31/2013 16:09:10 15.106 1/31/2013 16:09:20 15.135 1/31/2013 16:09 :30 1 15
. 13 7 1/31/2013 16:09 :40 14.932 1/31/2013 16 :09:50 11.918 1/31/2013 16:10:00 11 .352 1/31/2013 16 :10:10 11 .286 1/31/2013 16:10 :201 11.271 1/31/2013 16 : 10 :30 11 .271 1/31/2013 16:10 :40 10.511 1/31/2013 16 :10:50 9.492 1/31/2013 16:11 :00 9.415 1/31/2013

## 16**:11:10 '"1-9::** **4';;04~'** 1/31/2013 16 :11:20 9.064 1/31/2013 16 :11:30 7.701 1/31/2013 16:11 :40 7.542 1/31/2013 16:11:50 7.526 1/31/2013

## 16:12:oo"I-7:;;.~50::;8~ 1/31/2013 16:12:10 6.581 1/31/2013 16 : 12 :20 4.104 1/31/2013 16 : 12 :30 3.856 1/ 31/2013 16:12:40 3.818 1/31/2013 

## 16 :12 :50'"1-3=- .=-81"'6"'" 1/31/2013 16:13:00 4.734 CO, % 9.799 5.83 5
. 198 7.668 9.672 5.492 5.127 5.141 5.142 5.143 5.141 5.14 5.14 5.141 5.141 5
. 14 5.138 5.136 5.134 5.133 5.133 5.132 5.13 5.133 5.131 5.13 5.129 5
. 128 5.13 S
. 12 7 5.129 5.13 5.129 5.129 5.129 5.129 5.127 5.127 5.125 5.128 5.13 5 .127 5.126 5.127 5.127 5.126 5
. 127 5.126 5.125 5.126 5.125 5.126 5.125 5.125 5
. 126 5.125 5.126 5.123 5.125 NO" CO O2 NO. CO THe PPM PPM % PPM PPM PPM

## L...4,;;.~75;;7,..........,;9,;;.3;;;5;;.3_...,1:;;8;;,.7.;,73:;-_4;;8;:,. 2;;5;,:1..J1 233.516 7.538 3.593 9.371 

## ,....;1;,;2".8;,;4,;;7_-:3;;:6-:.0;,:1",8., 219.429 5.684

### L..",2**~5;;39;-1-;;6.,"0:::16;-1-9~.",96~9:-......,;2~4;.;;.5~82,:-,** 137.502 4.476 2.518 4.393 9.965 24.467 134.064 3.632 2.443 4.401 9.926 24.449 134.045 3
. 633 0 .77 6 4
. 377 9.915 7
. 362 97
. 849 3
. 631 0
. 385 4.367 9.915 0.533 163 .969 3.634 0
. 309 4.348 9.911 0.45 235.579 3.637 0.285 4.31 9.896 0.403 1 239.936 

### 1 3.637 0.245 4.298 9.891 0.38 192.939 3.635 0.245 4.28 9.893 0.365 137.693 

### 1 3.632 0.226 4
. 266 9
. 9

0.2 4.252 9.912 0.189 4
. 22 9.915 0.192 4.207 9.915 0.182 4.191 9.915 0.167 4.167 9.915 0.154 4.152 9.914 0.161 4.142 9.915 0.15 4.147 9.916 0
. 153 4.134 9.915 0
. 1 43 4
. 136 9.914 0
. 14 4
. 125 9.915 0.144 4.133 9
. 915 0.14 4.1 9.915 0
. 141 4.124 9.915 0.156 4.142 9.915 0.169 4.123 9.915 0
. 154 4.088 9.916 0
. 158 4.086 9
. 915 0
. 148 4
.093 9
. 915 0.143 4.107 9
. 916 0
. 143 4.08 9.915 0
. 162 4.06 9.915 0.166 4.079 9.914 0.164 4.092 9.915 0.161 4.113 9.915 0.15 4
. 106 9.914 0
. 15 4
.082 9.915 0
. 145 4.079 9
. 915 0.16 4.089 9.915 0.155 4.057 9.915 0.145 4.062 9.915 0.151 4.08 9.915 0.16 4.094 9.915 0.156 4 .0 62 9.915 0
. 158 4.067 9
.914 0.163 4
.073 9.915 0
. 158 4
.02 9.916 0.158 4.022 9.916 0.158 4
.05 9.915 0.147 4 .0 47 9.916 0.141 4.042 9.916 0.143 4
.073 9.923 0
. 136 4.032 9.936 0
. 133 4
.014 9.941 0.132 4 .017 9.94 0.144 4
.011 9.94 0.141 4
.021 9.94 0.341 0
. 33 0.323 0.301 0.29 0
. 281 0.266 0.261 0.26 0.26 0.261 0.257 0
. 25 0.253 0
. 258 0.251 0.256 0.248 0 .249 0
. 269 0
. 256 0.258 0.288 0.25 0.24 0.231 0.234 0.229 0 .2 31 0.244 0.244 0.23 0.23 0.238 0.245 0.244 0.231 0.234 0.245 0.23 0.23 0.23 0.23 0
. 24 0.241 0.23 0.229 0.23 117.183 28.931 5.257 1.171 0.453 0.272 0.24 0.239 0.236 0.236 0.242 0.241 0.237 0.238 0.236 0.235 0.235 0.237 0.237 0 .2 35 0
. 237 0.238 0.241 0.126 0.205 0.246 0.129 0.208 0.123 0.086 0.204 0.123 0.202 0.24 0.124 0.089 0
.084 0.084 0.199 0.239 0.244 0.121 0.208 0.244 0.243 0.239 0.242 0.246 3.631 3
. 628 3.626 3.627 3.627 3.627 3.627 3.627 3.627 3.627 3
. 627 3
. 627 3
. 627 3.627 3.626 3.626 3.627 3.627 3.627 3
. 627 3
. 627 3.627 3.626 3.626 3.627 3.626 3
. 626 3
. 627 3
. 626 3.626 3.626 3.626 3.627 3.627 3.628 3 .6 27 3.627 3
. 628 3.628 3.628 3.629 3.627 3.628 3
. 628 3
. 628 3.628 3.627 3.628 Cal High Mid CO Mid C02 Cal High C02 Mid CO Cal High CO Mid

80%

80%

60%

50%

40%

20%

### 0 , Date Time % 1/31/2013 16:13 : 10 9
.487 1/31/2013 16:13 : 20 10
.083 1/31/2013 16 : 13 : 30 10
. 158 1/ 31/2013 16 : 13 :40 10
. 18 1/ 31 / 2013

## 16**13 501"'1-:1;:':0"i** **1~85~** 1/ 31 / 2013 16 : 14 :00 10
. 176 1/ 31 / 2013 16 : 14 : 10 13.406 1/ 31 / 2013 16 : 14 : 20 15
.044 1/31/2013 16 : 14 : 30 15.103 1/31/2013 16:14:40 15.049 1/31/2013 16:14:50 15
.049 1 / 31/2013 16:15:00 15
.057 1 / 31 / 2013 16 : 15:101 15
.058 1 / 31 / 2013 16 : 15 : 20 13.864 1/31 / 2013 16 : 15 : 30 11
.474 1 / 31 / 2013 16 : 15:40 11.258 1 / 31/2013 16:15:50 11
. 223 1/31/2013 16:16:001 11.214 1/31/2013 16:16:10 10.687 1/31/2013 16:16:20 9
.486 1 / 31/2013 16 : 16 : 30 9
. 365 1/ 31 / 2013 16 : 16 :40 L 

# I**~9 3;:.4~**  1 / 31 / 2013 16 : 16 : 50 8
. 256 1/ 31 / 2013 16 : 17 : 00 5.885 1 / 31/2013 16 : 17 : 10 5
. 67 1/31/2013 16:17 : 20 6
. 135 1/31/2013 16:17:30 7.342 1/31/2013 16:17 :401 7
.451 1 / 31/2013 16 : 17 :50 6
.455 1 / 31 / 2013 16 : 18 :00 4
.056 1 / 31 / 2013 16 : 18 : 10 3
. 82 7 1 / 31/2013 16 : 18 : 20 3
.797 1/31/2013 16 : 18 : 301 3
.794 1/31/2013 16:18 :40 4
. 973 1/31/2013 16:18:50 9.5 1/31/2013 16:19:00 9.998 1/31/2013 16 : 19:10 10
.067 1 / 31 / 2013 16:19:201 10.085 1 / 31 / 2013 16 : 19 : 30 10
.079 1/31/2013 16:19:40 12
. 527 1 / 31 / 2013 16 : 19 :50 14
. 883 1/31/2013 16:20:00 15.026 1/31/2013 16:20:10 15.052 1/31/2013 16 : 20:20 15.061 1/31/2013 16:20 : 30 15.06 1/ 31 / 2013 16 : 20 :401 15
.062 1/ 31 / 2013 16 : 20 : 50 14
. 905 1 / 31 / 2013 16 : 21 :00 11
. 92 1/ 31 / 2013 16 : 21 : 10 11
. 308 1/ 31/2013 16:21:20 11.236 1/31/2013 16:21 : 301 11.224 1/31/2013 16:21 :40 10
. 698 1/31/2013 16:21:50 9
. 504 1/ 31 / 2013 16:22 :00 9
. 372 1/ 31 / 2013 16 :22 : 10 9
. 36 1 / 31 / 2013 16:22 : 20 9
. 352 1/ 31 / 2013 16:22:30 9
. 342 1 / 31/2013 16:22 :40 9
. 34 1/31/2013 16:22:501"'1"""'9
. ';;33';9"'" 

### CO , % 5.123 5
. 126 5
. 122 5
. 121 5
. 123 5
. 123 5
. 122 5
. 122 5.121 5.12 5.119 5.12 5
. 12 5
. 12 5
. 119 5
. 118 5.117 5.117 5.115 5.115 5
. 116 5
. 115 5.114 5.114 5.112 5
. 113 5.115 5
. 112 5
. 11 5
. 112 5
. 111 5
. 111 5.11 5
. 109 5.107 5.108 5
. 107 5.108 5
. 107 5.112 5.109 5.107 5.106 5.106 5.105 5.104 5
. 103 5
. 104 5.103 5.103 5.105 5
. 104 5
. 104 5
. 102 5
. 103 5
. 102

5
. 1 5
. 1 5.101 NO, PPM 0.137 0
. 132 0
. 125 0
. 127 0
. 126 0
. 124 0
. 13 0
. 13 0
. 124 0
. 122 0
. 12 0
. 117 0
. 119 0
. 116 0
. 11 7 0
. 119 0
. 111 0
. 115 0.114 0
. 115 0
. 117 0
. 145 0
. 142 0
. 118 0
. 109 0.105 0
. 108 0.107 0
. 108 0
. 109

0
. 1 0
. 105

0
. 1 0.091 0
.091 0.092 0
.093 0
. 105 0
. 105 0
.095 0
.094 0
.097 0
.096 0
.09 0
.097 0
.085 0
.085 0
.094 0
.089 0
.086 0.084 0.086 0
.096 0
. 101 0
.092 0
.09 0.093 0
.093 0.088 

## co PPM 4
.01 4.019 4
.033 4
.01 4
.013 4
.02 3
. 989 3
. 983 3.987 3.996 4
.016 3.999 4
.014 4
.008 3
. 984 3
. 963 3.987 3.981 3.976 3.96 3.979 3
. 987 3
. 975 3
. 965 3.953 3
. 963 3.969 3
. 979 3
. 965 3
. 941 3
. 949 3
. 941 3
. 892 3
. 941 3.931 3
. 927 3
. 926 3
. 92 3
. 907 3
. 901 3
. 891 3
. 904 3.918 3.907 3.87 3.892 3
. 917 3
.873 3
. 871 3.871 3.883 3.889 3.889

3.9 3
. 888 3
. 876 3
.854 3
. 851 3
. 859 

### 0, % 9.94 9
. 939 9.941 9
. 94 9
.939 9
. 94 9
. 94 9
. 94 9.94 9.939 9
. 94 9
. 94 9
. 94 9
. 939 9
. 94 9
. 94 9
. 94 9.939 9
. 939 9
. 939 9
. 94 9
. 94 9
. 938 9
. 94 9.94 9
. 94 9
. 939 9
. 939 9
. 94 9
. 939 9
. 94 9
. 939 9
. 939 9.939 9
. 941 9.939 9
. 94 9
. 941 9
. 942 9
. 947 9
. 963 9.964 9.964 9.963 9.961 9.965 9
. 964 9
.964 9.965 9.965 9.966 9.965 9.965 9
. 965 9
. 965 9
. 965 9
. 965 9
. 965 9
. 965 NO , PPM 0.228 0.227 0
. 238 0
. 219 0
. 218 0 .2 24 0
. 216 0
. 218 0
. 215 0.224 0
. 221 0 .22 3 0
. 215 0
. 215 0
. 215 0.226 0
. 215 0
. 214 0
. 22 0
. 219 0
. 221 0
. 214 0
. 211 0.199 0
. 214 0.201 0
. 206 0
. 208 0
. 203 0 .1 99

0
. 2 0
. 228

0 .2 0
. 199 0
. 199 0
. 202 0
. 199 0
. 206 0
. 199 0
. 199 0
. 199 0
. 199

0.2 0
. 196 0
. 199 0
. 207 0
. 206 0
. 199 0
. 199 0
. 197

0.2 0
. 199 0
. 199 0
. 189 0
. 184 0
. 196 0. 188 0
. 189 0.199 

## co PPM 0.246 0.242 0.244 0
. 245 0
. 239 0
. 237 0
. 239 0
. 239 0.234 0.24 0
. 24 0.24 0
. 235 0
. 239 0
. 242 0
. 24 0
. 24 0.239 0.24 0.114 0
. 203 0
. 239 0
. 237 0
. 237 0
. 236 0.237 0.235 0.119 0
. 205 0
. 24 0
. 238 0
. 239 0
. 237 0.24 0.239 0.237 0.235 0.236 0.243 0.238 0.243 0.244 0.241 0.242 0.117 0.209 0
. 242 0.241 0.125 0.207 0.242 0.242 0
. 119 0
. 208 0
. 241 0
. 243 0.243 0.238 0.238 

### THe PPM 3.629 3.627 3.627 3
. 628 3
. 628 3
. 6 27 3
. 628 3
. 62 7 3.628 3.628 3.628 3
. 628 3
. 629 3
. 6 2 9 3
. 629 3.63 3.629 3.629 3.628 3
. 6 2 9 3
. 628 3
. 628 3
. 629 3.629 3
. 6 2 9 3.629 3
. 629 3
. 6 28 3
. 628 3
. 628 3
. 627 3.628 3
. 628 3.628 3
. 628 3
. 628 3
. 628 3
. 627 3
. 628 3
. 628 3
. 627 3
. 628 3
. 628 3
. 627 3
. 628 3
. 62 7 3
. 627 3
. 628 3
. 627 3
. 627 3
. 627 3
. 627 3
. 628 3
. 627 3
. 628 3
. 628 3
. 627 3
. 628 3.628 Mid

M i d 80%

60%

5 0%

40%

20 %

80 %

60%

50%

### 0, Date Time % 1/31/2013 16:23:00 9.341 1/31/2013 16:23:10 9.339 1/31/2013 16:23:20 9.338 1/31/2013 16:23:301"1

## ~9i:-**;'33;:'9~** 1/31/2013 16:23 :40 9
.098 1/31/2013 16:23 : 50 4
.79 1/31/2013 16:24:00 3
. 91 1/31/2013 16:24:10 3.819 1/31/2013 16:24:20 3.795 1/31/2013 16:24:301"1

## -3~.;;:79~4"" 1/31/2013 16:24:40 3.793 1/31/2013 16:24:50 5.685 1/31/2013 16:25 :00 9
. 661 1/31/2013 16:25 :1 0 10.024 1/31/2013 16:25:20 10
.064 1/31/2013 16 :25:30 8.694 1/31/2013 16:25:40 7.58 1/31/2013 16:25 :50 7.501 1/31/2013 16:26:00 7.48 1/31/2013

## 16:26:101"1-7:;".4':'7;';:9~ 1/31/2013 16:26 :20 7.736 1/31/2013 16:26 :3 0 9
.771 1/31/2013 16:26 :40 10
.065 1/31/2013 16:26:50 10
. 106 1/31/2013 16:27 :001 10.109 1/31/2013 16:27:10 10.093 1/31/2013 16:27:20 12.663 1/31/2013 16:27:30 14.89 1/31/2013 16:27:40 15.031 1/31/2013 16:27 :50 15 .053 1/31/2013 16:28 :001 15 .062 1/31/2013 16:28:10 14
.015 1/31/2013 16:28:20 11.514 1/31/2013 16:28 : 30 11.273 1/31/2013 16:28:40 11.233 1/31/2013 16:28:50 11.223 1/31/2013 16:29:00 11.222 1/31/2013 16:29:101 11.221 1/31/2013 16 : 29:20 10
. 744 1/31/2013 16:29:30 9.526 1/31/2013 16:29:40 9.372 1/31/2013 16:29:50 9.363 1/31/2013 16:30:001"1

## ~9i:-.'::35"i8~ 1/31/2013 16 :30:10 8.794 1/31/2013 16:30:20 7.61 1/31/2013 16:30:30 7.503 1/31/2013

### 16:30**401....,7'=' 4':'7:::9~**  1/31/2013 16:30 : 50 7.479 1/31/2013 16 :3 1:00 6.902 1/31/2013 16:31:10 4.188 1/31/2013 16:31:20 3.846 1/31/2013 16:31:30 3.803 1/31/2013 16:31:401 3.794 1/31/2013 16:31:50 5
. 848 1/31/2013 16:32:00 9 .7 1/31/2013 16:32 : 10 10
.038 1/31/2013 16:32:20 10 .0 88 1/31/2013 16:32:30 10.109 1/31/2013 16:32:40 10.109 

### CO, % 5.101 5.1 5.101 5.098 5.099 5.101 5.101 5.099 5.098 5.096 5.098 5.095 5.096 5.096 5.094 5.095 5.096 5.096 5.094 5.093 5.095 5.093 5.094 5.09 5
.089 5.09 5.09 5.092 5.09 5.087 5.088 5.089 5.088 5.087 5.087 5.087 5.085 5.085 5.085 5.086 5.083 5.084 5.083 5.083 5.083 5.08 5
.08 5.08 5.08 5.079 5.079 5
.081 5.079 5
.077 5.079 5.Q78 5
.078 5.076 5.079 

### NO , PPM 0
.082 0.082 0
.085 0.088 0
.085 0.Q78 0
.077 0.09 0
.095 0.081 0.081 0.Q78 0.078 0 .0 81 0
.081 0
.079 0.082 0.079 0.074 0.075 0.074 0 .0 7 0
.067 0.067 0
.072 0.082 0.073 0.073 0.071 0.07 0 .064 0 .07 1 0.079 0.07 0.069 0.065 0.066 0.077 0
.071 0.07 0.067 0.066 0.068 0.062 0.058 0
.065 0
.063 0
.071 0.067 0.085 0.083 0.069 0.061 0.064 0
.071 0.069 0.074 0.079 0.085 

## co PPM 3.881 3.884 3.872 3.866 3.855 3.849 3.841 3.851 3.847 3.859 3.833 3.847 3.842 3
. 815 3.806

3
. 8 3.808 3.822 3.836 3.82 3.801 3.814 3.803 3.796 3.766 3.788 3.809 3
.779 3
.795 3 .7 64 3 .772 3.774 3.778 3.799 3.788 3.768 3
.75 3.748 3 .7 54 3.731 3.75 3.741 3.726 3.745 3.751 3.766 3.725 3.715 3.724 3.74 3.722 3.738 3.751 3.737 3
.712 3
. 699 3.697 3.723 3.715 

### 0, % 9.966 9.966 9.964 9.965 9.965 9.965 9.966 9.965 9.964 9.964 9.965 9.965 9.965 9.965 9.965 9.966 9.972 9.982 9.988 9.989 9.987 9.988 9.99 9.986 9.987 9.986 9.982 9.988 9.988 9.986 9.988 9.99 9.991 9.99 9.989 9.991 9.99 9.99 9.991 9 .9 9 9.99 9.99 9.992 9.99 9.989 9.989 9.99 9.989 9.989 9
. 99 9.99 9.988 9.99 9.99 9.989 9
. 989 9.99 9.99 9.989 

### NO, PPM 0.194 0.184 0.196 0
. 203 0
. 185 0.194 0.19 0
. 184 0.184 0.185 0.185 0.198 0.186 0
. 197 0
. 184 0.186 0.185 0.19 0.187 0.184 0.184 0.184 0.184 0.184 0.185 0.191 0.184 0.184 0.185 0.184 0
. 184 0
. 185 0.184 0.189 0.193 0.169 0.19 0.187 0.181 0
. 169 0.169 0.169 0.176 0.177 0.184 0
. 194 0
. 183 0.169 0.17 0.173 0.184 0.177 0.169 0
. 172 0
. 169 0
. 169 0
. 169 0
. 162 0.169 

## co PPM 0.237 0.241 0.238 0.238 0.236 0.235 0.242 0.239 0.119 0.198 0.241 0.235 0.239 0.234 0
. 234 0.236 0.237 0.235 0.121 0.083 0.199 0.232 0.235 0.234 0.229 0.115 0.196 0.234 0.237 0.237 0.24 0.235 0.237 0.232 0.231 0.236 0.112 0.201 0.123 0.086 0.204 0.237 0.244 0.243 0.232 0.235 0.239 0.236 0.118 0.085 0.195 0.12 0.2 0.231 0.233 0
. 233 0.112 0.199 0.238 

### THe PPM 3.628 3.627 3.628 3
. 628 3.627 3
. 628 3.626 3.628 3.628 3.628 3.627 3.627 3
. 627 3
. 627 3
. 628 3.628 3.628 3.628 3.628 3
. 627 3.628 3
. 627 3.628 3.627 3.628 3.628 3.629 3
. 628 3.628 3
. 629 3
. 628 3.629 3.628 3.628 3.629 3.628 3
. 629 3.628 3
. 628 3
. 628 3.628 3.629 3.628 3.628 3
. 629 3
. 628 3
. 628 3.629 3.629 3.628 3.629 3.629 3
. 628 3
. 628 3
. 628 3 .629 3
. 628 3
. 628 3.627 Mid 40%

20%

40%



### 80%

60%

50%



### 40%

20%

### 0 , CO, NO, CO 

### 0, NO, CO 

### THe Date Time % % PPM PPM % PPM PPM PPM 1/31/2013 16 :32:50 10
. 111 5.077 0.109 3.692 9.99 0
. 169 0.119 3
. 627 1/31/2013 16 :33:00 10.11 5
. 0 75 0.12 3
. 695 9.99 0
. 169 0.082 3
. 627 1/31/2013 16:33 : 101 10.111 5
. 076 0.131 3.683 9.99 0.169 0
. 2 3
. 627 Mid 1/31/2013 16:33 :20 10.111 5
. 074 0.142 3.659 9.99 0.169 0
. 237 3
. 628 1/31/2013 16:34:00 10.111 5.07 0.183 3.671 10.003 0
. 172 0
. 237 3.628 1/31/2013 16:35:00 10
. 11 5
. 07 0
. 208 3
. 66 10
. 007 0
. 167 0
. 121 3.628**~ ~** **N~** 

### W**~ ~**  

### W**~C** Date Time % % PPM PPM % PPM PPM PPM 

### 2/1/2013 7:51:00 0.105 -0.1041 -0.0251 -0.023 0.0331 0.0531 -0.161 2.049 N2/NOx Mode 2/1/2013 7:52:00 0.104 -0.006 -0.022 -0.03 0.032...---::,;0',::;05:;, -0.164 1.942 2/1/2013 7:53:00 0.103 -0.011 -0.032 -0.026 0.032 0.045 -0.166 2.625 N2/NO Mode 2/1/2013 7:54:00 0.103 -0.015 2.935L..._-..::0:.;.0::;2:;.8_.,.;::0.::;0;:3201 2.89 -0.135 0.001 Cal Zero 2/1/2013 7:55:00 15.519 7.796 4.819 4.397 12.748 4.881 37.46 -0.009 2/1/2013 7:56:00 ...-...;1:;;:9..::.1:;;:17;,...._:;.9.'"'64,:.:3+-......;4;;:.8,,1:.:;2
..... --:.::,9.:;;:3:;.8_..::1;8.:;;:9;:55+-_,:4:;;.8;;:8
..... 2;;;3:;;:0,;;.

### 7~3;;!1f-_-;O.:;;:OO;;;l;JNO/NOX Mode;THC Zero 2/1/2013 7:57:00 19.142 9.661 4.814 9.447 18.965 4.885 242.805 7.574 Cal High 2/1/2013 7:58:00 11869 5889 4816 9455 12757 4886 238903 77.933 2/1/2013 7:59:00 79.903 NO/NO Mode 2/1/2013 8:00:00 80.087 Mid 2/1/2013 8:01:00 80.633 N02/NO Mode 2/1/2013 8:02:00 10.17 5.048 1.637 4.458 10.048 1.788 139.192 81.297 2/1/2013 8:03:00 10.168 5.046 r l-"::3'::.8:;:4';'81 4.474 10.0481 3.9221 139.31 81.638 N02/NOx Mode 2/1/2013 8:04:00 13.493 4.187 2.023 3.399 2.486 2.227 82.898 81.741 2/1/2013 8:05:00 14.051 3.988 -0.013 4.144 0.048 0.064 0.449 81.79 2/1/2013 8:06:00 14.071 3.9691 -0.0181 2.449 0.0271 0.0581 -0.051 83.499 NOx Cal Zero 2/1/2013 8:07:00 14.042 3.984 3.935 2.84 0.027 36.418 0.024 85.38 2/1/2013 8:08:00 14.098 3.945 4.793 2.872 0.027 48.845 0.051"1-"::8=-5.:::84;ITHC High 2/1/2013 8:09:00 14.054 3.968 r l--=4"::.7:::8;71 2.195 0.3081 48.7751 1.275 72.822 NOx Cal High 2/1/2013 8:10:00 14.069 3.955 3.294 3.373 0.026 22.754 0.07 47.253 2/1/2013 8:11:00 14.05 3.967 2.557 2.391 0.027 23.365 -0.002 47.124 2/1/2013 8:12:00 12.866 3.7441 r -':;2:';.5:;:4';'11 2.391 0.1561 24.4531 0.448 47.267 Mid 2/1/2013 8:13:00 0.345 0.019 0.597 3.99 0.038 5.841 101.418 47.534 2/1/2013 8:14:00 0.127 0.008 -0.023
.. 1-....;::4
. .::,45:;,1 0.025

# 0.198rl-1~3:.;9;.;.0:.;5:;.6--=4;;7.:::64::;3Iw bias;THC Mid 2/1/2013 8:15:00 1.219 0.672 -0.025 4.351 2.939 0.162 130.631 39.07 2/1/2013 8:16:00**...-~9..::.9:::68:::...._;:5.;05:;.:3:...........,-,.::0:;;.0:;,2** 

### 0.675 9.887 0.183 15.598 2/1/2013 8:17:00 

# I 10.041 5.079 -0.0271 -0.337: r l-..::9..::.9::;.05:,..........:0:;;.2:::0:;;,81 -0.4121 2/1/2013 8:18:00 L......:::: 6;.::.5:::13:::....-=-3
. .::.20;,;2:.....-.:0:::.8::1;:,J6 -0.322 5.299 10.234 -0.382 2/1/2013 8:19:00 0.143 0.039 2.525 0.025 0.043 24.567 -0.137 2/1/2013 8:20:00 "I 

### -..::0..::.1;23;;....-.::,0::..0:;.:3:.....-.::::2:;.5:;;:3-...::0..::.1::;2;.2--.::.0.::,0;:.26;,....-.::.24;;;.5:;;8:;5---..::0..::.0:;:5"'71 2/1/2013 8:21:00 0.123 0.031 2.529 0.123 0.026 24.584 -0.107 2/1/2013 8:22:00 0.122 0.031 2.523 0.119 0.025 24.601 -0.06 2/1/2013 8:23:00 0.122 0.034 2.523 0.115 0.025 24.58 -0.132 2/1/2013 8:24:00 10.08 3.3 2.763 1.224 10.485 25.265 71.95 2/1/2013 8:25:00 13.431 4.306 3.283 1.292 13.222 28.304 85.17 2/1/2013 8:26:00 13.474 4.292 2.787 2.09 13.27 26.811 137.763 2/1/2013 8:27:00 13.496 4.287 3.211 1.15 13.244 28.41 74.438 2/1/2013 8:28:00 13.478 4.304 2.936 1.831 13.268 27.684 122.314 2/1/2013 8:29:00 13.427 4.339 3.211 1.013 13.248 28.526 66.829 2/1/2013 8:30:00 13.422 4.346 2.937 1.638 13.264 28.2 112.971 2/1/2013 8:31:00 13.363 4.385 3.153 1.03 13.242 28.685 66.48 2/1/2013 8:32:00 13.377 4.38 3.072 1.272 13.251 28.835 81.47 2/1/2013 8:33:00 13.307 4.421 3.331 0.783 13.192 29.742 52.914 2/1/2013 8:34:00 13.333 4.412 3.022 0.88 13.227 29.277 58.348 2/1/2013 8:35:00 13.319 4.425 3.2 0.884 13.193 29.392 60.798 2/1/2013 8:36:00 8.145 2.676 3.555 0.742 13.195 29.574 55.742 2/1/2013 8:37:00 0.187 0.119 4.739 0.225 13.191 29.597 54.919 2/1/2013 8:38:00 rl-..,0:::.1:::6"'6--.::.0.:;:1;:12;,....-4;:..7;,;3"'9:..........;0:::.1:;;:5::;,71 13.195 29.74 53.301 2/1/2013 8:39:00 4.59 1.611 4.204 0.202 13.194 29.599 53.643 2/1/2013 8:40:00 13.268 4.428 3.021 0.676 13.197 29.588 54.524 2/1/2013 8:41:00 13.298 4.445 3.075 0.809 13.195 29.673 53.681 2/1/2013 8.42:00 13.307 4.45 3.073 0.776 13.197 29.615 53.796 2/1/2013 8:43:00 13.319 4.452 3.001 0.805 13.205 29.573 53.324 2/1/2013 8:44:00 13.314 4.459 3.026 0.805 13.195 29.623 53.162 2/1/2013 8:45:00 13.329 4.458 2.964 0.831 13.213 29.652 53.217 2/1/2013 8:46:00 13.336 4.457 2.986 0.745 13.227 29.698 50.782 2/1/2013 8:47:00 13.343 4.459 2.963 0.78 13.23 29.521 52.825 25.89 25.747102/c02 bias;THC Low 24.629 0.704 ·0.017 NOx bias 

### -0.017 -0.018 -0.017 19.967 15.512 35.268

10.37 30.106

8.296 27.77 10.075 15.203 6.624 8.045 8.676 7.172 7.154 6.772 NOx bias 

### 6.936 7.013 6.896 6.975 6.842 6.572 6.988 6.229

6.71Date Time 

### 2/1/2013 8 :48 :00 2/ 1/ 2013 8:49 :00 2/1/2013 8:50:00 2/1/2013 8:51:00 2/1/2013 8:52:00 2/1/2013 8 : 53 :00 2/1/2013 8:54 :00 2/1/2013 8 : 55 :00 2/1/2013 8 : 56 :00 2/1/2013 8:57:00 2/1/2013 8 :58:00 2/1/2013 8 :59 :00 2/ 1/2013 9 : 00 :00 2/1/2013 9:01:00 2/1/2013 9:02:00 2/1/2013 9:03:00 2/1/2013 9:04:00 2 / 1 / 2013 9 : 05:00 2/ 1/2013 9 :06 :00 2/1/2013 9:07:00 2/1/2013 9:08:00 2/1/2013 9:09:00 2/1/2013 9 : 10:00 2/1 / 2013 9 : 11 : 00 2/1/2013 9 : 12:00 2/1/2013 9 : 13:00 2/1/2013 9:14:00 2/1/2013 9 : 15 : 00 2/1/2013 9 : 16 : 00 2/ 1/2013 9:17:00 2/1/2013 9:18:00 2/1/2013 9:19:00 2/1/2013 9 : 20:00 2/1/2013 9 : 21:00 2 / 1/ 2013 9 : 22 : 00 2/1/2013 9:23 : 00 2/1/2013 9:24:00 2/1/2013 9:25:00 2/1/2013 9 : 26:00 2/1 / 2013 9 : 27 :00 2/ 1/ 2013 9 : 28 :00 2/1/2013 9:29 :00 2/1/2013 9:30:00 2/1/2013 9:31:00 2/1/2013 9 : 32:00 2/1 / 2013 9:33 :00 2/1/2013 9:34:00 2/1/2013 9:35:00 2/1/2013 9:36:00 2/1/2013 9:37:00 2/1 / 2013 9:38:00 2/ 1/ 2013 9 : 39 :00 2/1/2013 9:40:00 2/1/2013 9:41:00 2/1/2013 9:42:00 2/1/2013 9 : 43 : 00 2 / 1/2013 9 :44 : 00 2/1 / 2013 9 : 45 : 00 2/1/2013 9:46:00 

### 0, % 13.344 13
. 349 13.353 13
. 366 13.366

13
. 37 13.37 13
. 372

13
. 38 13.39 13.4 13
.404 13.403 13.411 13.418 13.413 13.413 13.425 13.429 13.432 13.437

13.43 13.432 13.438

13.45 13.437 13.445

13.45 13.476 13
.486 13.492 13.493 13
.494 13
.482 13.483 13
.478 13
.468 13
.471 16
.005 14 .3 1 6 13
.626 13
. 624 13
. 627 13.64 13.63 13.521 13
.492 13.497 13.467 13
.436 13
.427

13.43 13.43 13.427 13.428 17
. 212 14
.721 13.463 13.473 CO 2**NO~** CO % 

### PPM PPM 4.463 2
.947 0.792 4.466 3
.025 0 .72 4
.467 2
. 965 0.699 4.466 2
. 895 0.733 4.469 2.98 0.735

4
. 47 2
. 977 0.752 4.473 2
. 931 0 .76 4.476 2
.983 0 .7 37 4 .472 2
. 903 0.742 4.466 2.882 0.731 4.463 2.863 0.734 4
.462 2
.77 0.742 4
.463 2
.762 0 .7 83 4.462 2
.939 0
.784 4.458 2.978 0
.713 4
. 461 2.921 0.739 4.464 2.882 0.733 4
. 456 2
.785 0 .7 32 4.454 2.76 0
.755 4.448 2
. 858 0.781 4.448 2.845 0.735 4.452 2.838 0.739 4.453 2
. 831 0
. 748 4.451 2
. 847 0
. 765 4.449 2
. 84 0.773 4.455 2.888 0.73 4.453 2
.772 0
. 713 4.453 2.685 0
. 706 4.445 2
.716 0.718 4
.443 2
. 825 0.763 4.441 2.854 0.752 4.444 2.911 0.759 4.445 2.886 0
. 746 4.451 2
. 888 0
. 746 4
.454 2
. 924 0
. 683 4
.457 2.885 0
. 636 4.461 2.813 0
. 631 4
.461 2
. 816 0
. 64 3.015 1.919 0
. 538 3
.944 2.525 0
.429 4
. 359 2
.788 0
. 601 4
. 357 2
. 931 0
. 605 4.356 2
. 844 0.615 4.348 2
. 71 0
. 627 4. 351 2
.788 0
. 627 4
.419 2
.781 0
. 645 4.436 2
. 83 0
. 677 4.432 2
. 815 0
. 631 4.449 2.875 0
. 631 4
.462 2
. 883 0
. 642 4
.472 2.954 0
. 632 4
.471 2
. 914 0
. 621 4.468 2
. 866 0
. 622 4.471 2.838 0.623 4.471 2
.777 0
. 653 2
. 314 1
.441 0
. 527

3.69 2
. 313 0 .3 08 4.449 2.886 0.488 4.446 2
.941 0.507 13.236 29
. 638 13.237 29
. 851 13.247 29
.79 13.239 29
. 653 13.244 29
. 85

13.25 29
. 762 13
. 244 29
. 812 13.247 29
. 961 13.259 29
. 913 13.271 29.931 13.278 29
. 869 13.288 29
. 781 13.283 29.747 13.294 29
. 918 13 .2 95 29
. 924 13 .288 29
.997 13.289 30.097 13.299 30
.091 13.315 29.915 13.317 29
. 981 13.309 30.102 13.319 30
.036 13.319 29
. 968 13.324 29
. 999 13.329 30.002 13.318 30.25 13.336 30
. 237 13.334 30.261 13
. 339 30
. 113 13.343 29
.994 13
. 344 29.966 13.345 30.064 13
. 346 30.035 13.346 29.968 13
. 346 30.3 13
. 346 30
. 245 13.343 30.278 13.345 30
. 385 13.345 30.47 13
. 345 30
. 342 13.344 30
.466 13.345 30.584 13.345 30.37 13.342 30.393 13.341 30
. 379 13.344 30
. 225 13.344 30
. 216 13.344 30.28 13.345 30.347 13.342 30.353 13 .339 30
. 5 13.346 30
. 396 13.342 30
.462 13.343 30.297 13.344 30.268 13.345 30 .2 52 13.344 30
. 471 13.335 30
.455 13.344 30.472 

## co PPM 52
.007 48 .702 49.834 51
. 932 50.714 52.302 51
.585 51.182 51.242 50.373 50.927 51.431 53.761 51.624

49.46 51.265 50.552 50.409 51.275 51.813 51.435 51.386 51.429 51.869 52.164

49.41 49.472 48
. 573 49
. 668 52
.707 50.984 50.475 50.274 51.089 49.837 48.105

48.08 47.915 46 .054 47 .2 34 46
. 1 02 45 .44 1 47.557 46.574

47
. 29 48 .0 8 48.66 47.917 47 .85 4 47
. 533 48
. 207 47.962 46.927 48.268 49
. 052 49
. 322 47
. 902

47.93

46
. 5 

### THe PPM

6.581 5
. 662

5.9 6.477 6.368 6
. 863

6.53 6
. 536 6
. 395 6
. 249 6
. 195 6
. 276 6
. 656 6
. 526 5.978 6.431 6
. 283 6
. 296 6
.427 6.542 6
. 603 6.227 6 .2 21 6
. 504 6
. 678

6.1 5.687 5.83 6
.007 6.804 6 .2 93 6.219 6
.063 6
. 246 6
. 137 5.758 5
. 675 5
. 711 5
. 262 5
. 565 5
. 278 5.243 5.895 5.445 5.566 5 .7 18 5
. 738 5.623 5.741 5
.584 5
. 823 5.841 5.505 5.912

6.06 6.053 5
. 805

5.76 5.431**~ ~ ~**  

## ro**~ ~**  

## ro Date Time % % 

### PPM PPM % 

### PPM PPM 2/1/2013 9:47 :00 13.491 4.435 2.948 0
. 502 13.344 30.486 47.273 2/1/2013 9:48 :00 13.508 4.426 2.939 0.475 13.345 30.495 46.707 2/1/2013 9:49 :00 13
.497 4.428 2
. 867 0.495 13.342 30.497 47
.025 2/ 1/2013 9 : 50 :00 13
.449 4
.462 2.701 0.473 13
. 342 30
. 504 48
. 292 2 / 1/ 2013 9 : 51 :00 13
.421 4
.482 2
. 874 0
.409 13
. 344 30
.48 48
. 838 2 / 1/ 2013 9 : 52 :00 13.414 4
.485 2
. 79 0
.413 13.333 30
. 622 46
. 853 2 / 1/ 2013 9 : 53 :00 13.406 4.491 2.822 0.392 13.34 30
. 669 46
. 952 2/ 1/2013 9 : 54 :00 13
. 417 4.484 2.836 0.403 13.336 30.658 46.727 2/1/2013 9 : 55 :00 13
.424 4
.479 2
.922 0.413 13
. 345 30.534 46
. 855 2/1/2013 9:56:00 13.448 4.463 2.707 0.42 13
. 35 30.379 48.915 2/1/2013 9:57:00 13.429 4.475 2
. 859 0.416 13
. 339 30
. 558 48.111 2 / 1/2013 9:58:00 13.424 4.48 2
. 914 0
. 438 13.339 30
. 672 48.475 2/ 1/ 2013 9:59:00 13.422 4.484 2
.949 0
. 393 13.331 30
. 736 47.053 2/ 1/ 2013 10:00 :00 16
. 266 2
. 879 1
. 897 0
. 365 13.334 30
. 703 46
. 979 2 / 1/ 2013 10 :01:00 20
.764 0
. 239 0
.037 0
. 115 13.34 30
.467 49
. 599 2 / 1/ 2013 10 :02 :00 20
. 884 0
. 174 0
. 002 0.169 13.343 30.352 50.781 2 / 1/2013 10:03:00 20
. 895 0
. 169 0
. 007 0.247 13
. 343 30.474 49
. 863 2/1/2013 10:04:00 20.898 0.169 0
. 015 0.181 13.342 30.775 42.614 2/1/2013 10:05:00 20.899 0.167 0.016 0
. 136 13.342 30.471 44.147 2/ 1/2013 10 : 06 : 00 20
. 891 0.171 0
.004 0
. 127 13.341 30
. 294 47.462 2/ 1/ 2013 10 : 07 : 00 20
. 898 0
. 166

-0
.002 0
. 122 13.328 30
. 633 46
.049 2/ 1/ 2013 10 : 08 : 00 20
. 898 0.167 0
.012 0
. 113 13
. 334 30
. 677 42
. 664 2/ 1/ 2013 10 : 09 : 00 20
. 898 0
. 166 0
.008 0
. 109 13.326 30
. 34 49
. 571 2/ 1/ 2013 10:10:00 20
. 898 0
. 171

-0
.01 0
. 114 13
. 337 30
. 184 53
. 895 2/ 1/ 2013 10 : 11:00 20
. 89 0.177 -0
.003 0.12 13.34 30
. 187 52
. 19 2/1/2013 10:12 : 00 20.902 0.17 0 0.122 13.337 30.503 43.978 2/1/2013 10:13:00 20.911 0.168

-0.014 0
. 145 13.343 30.308 43.783 2/1/2013 10 : 14 : 00 20.911 0.172

-0.014 0
. 148 13.343 30
. 075 49
. 362 2/ 1/ 2013 10 : 15 :00 20
.906 0
. 174 -0.012 0
. 134 13.336 3 0.2 91 50
.485 2 / 1/2 013 10 : 16 :00 19
.965 0
. 182 0
. 195 0
. 179 13
. 34 30
. 365 45
. 645 2/ 1/ 2013 10 : 17 : 00 20
. 889 0
. 177 0
.07 8 0
. 192 13
. 323 30
. 341 46
. 986 2/ 1/ 2013 10 : 18 :00 14
.484 3.997 2
. 156 0
.494 13.327 30
. 203 52.113 2/ 1/2013 10 : 19 : 00 13
.489 4.479 2
.702 0
. 773 13
. 316 30
. 355 50
. 691 2/1/2013 10:20 : 00 13.492 4.48 2 .594 0.733 13
. 334 30.264 48.649 2/1/2013 10:21 : 00 13.493 4.483 2.575 0
. 698 13.331 30.276 47.543 2/1/2013 10:22 : 00 13
.477 4
.489 2.787 0.739 13
. 312 30.44 50.725 2/1/2013 10 : 23 :00 13
.475 4
.492 2
. 623 0.681 13
. 319 30
.499 46.56 7 2 / 1/ 2013 10 : 24 :00 13.478 4
.489 2. 598 0
. 667 13
. 3 22 30
. 284 47
.717 2 / 1/ 2013 10 : 25 :00 13.475 4
.488 2
. 665 0
.724 13
. 319 30
. 268 46
. 611 2 / 1/2013 10 : 26 :00 13
. 49 4
.479 2
. 649 0
. 707 13
. 319 30
. 13 47
. 98 2 2 / 1/ 2013 10 : 27 :00 13
.488 4
.481 2
.753 0
. 736 13.325 30
. 242 47.013 2 / 1/2013 10 : 28 :00 13
.49 4.481 2 .794 0.715 13.326 30
. 208 48.217 2/1/2013 10:29:00 13
.499 4.477 2
. 802 0.702 13.328 30
. 125 46
.092 2/1/2013 10:30:00 13
.487 4.482 2
. 795 0.695 13.329 30
. 159 46.179 2/ 1/ 2013 10:31:00 13
.479 4.488 2.739 0.637 13.315 30
.429 44
. 313 2/ 1/ 2013 10 : 32 : 00 13
.468 4
.499 2 .7 48 0
. 527 13.316 30
.452 40
. 961 2/ 1 / 2013 10 :3 3 : 00 13.47 3 4
.496 2 .7 67 0
. 601 13.318 30
. 25 46
. 279 2/ 1/ 2013 10 : 34 : 00 13
.469 4
.497 2
. 735 0
. 634 13.316 30
. 342 45
. 15 7 2/ 1/ 2013 10 : 35 :00 13.474 4.493 2
. 7 08 0.609 13
. 315 30
. 257 45
. 61 2/ 1/ 2013 10 : 36 : 00 13.059 4.287 2 .3 6 0.583 11.257 17
.017 36.147 2/1/2013 10:37 :00 10.128 5.235 -0
.006 -0.214 9
. 917 1.073 0.896 2/1/2013 10 :38: 00 r,""";"7,1 

### o;;'.1:----;5"'.

## 2:::4~5**-~.o::':. 0;;;1~8'**  . 0
. 367' r --:-:9
. -:-:9;;,17;-----;0;';.9::-1':1 7 ' -0.47 2 / 1/2013 10 : 39 :00 10.573 5
. 133 0
. 228

-0
. 348 4
. 61 12.806 0
. 312 2 / 1/ 2013 10 :40 :00 13.432 4
. 502 2
. 644 0
. 58 0
.053 24
. 868 0
.062 2/ 1/ 2013 10 :41 :00 8
.499 2
. 81 3
. 159 0
. 678 0
.034 24
. 854 -0
. 151 2 / 1/ 2013 10 :42 :00'",-"'0"
. 2"

2"'4

## --:::-0**=::18"'1:-.....;4~ .** **:;1;;2-~0,:,: 1:::7;;6** -....;,0
.

## ..;0"'25,;........:,**,;;4;;; 8"2.....;~** **0;;; 1;;;1.;4'**  2 / 1/ 2013 10 :43 :00 0
. 195 0
. 168 4
.405 0
. 244 0.Q28 14
. 601 20
. 95 2 / 1/ 2013 10:44 :00 0
. 175 0
. 164 0
.006 3.631 0
.023 0
.596 132
. 836 

### THC PPM 5
.77 5
. 576 5
.484 5
. 691 6
.084 5 .7 45 5
. 654 5. 598 5
.524 5
.981 5
.799 6
. 138

5
. 65 5
. 726 6
.501 6
.718 6
.539 4.245 4
.453 5
. 229 5
. 022 4
. 094 5
. 877 6
. 68 3 6
.096 4. 264 4.229 5
.447 5
. 89 2 4
. 9 17 5 .004 6
.014 5
. 607 5
.441

4.97 6
. 144 5
. 084 5
. 544 4
. 912 5
.0 6 8 4
.774 5 .2 69 4
. 714 5
. 027 4
. 591 3 .7 93 4
. 94 4
. 879 4
. 805 3. 768

-0
. 009 -0.019 02/C02 bias 

### 0
. 145

-0
.019 -0
.019 ·0 .019 NO x b ias 

### -0
. 018 -0
.013**~ ~** **N~** 

### W 0,**N~** 

### W Date Time % % PPM PPM % PPM PPM 

### 2/1/2013 10 :45 : 00 0
. 17 0
. 161 -0.02 61
.....

## _4~.~43~1 0.023 0.5171 138
. 5811 2/1/2013 10 :46 : 00 8.98 4
.763 3
. 621 4
.44 7.55 16
.578 135
. 155 2/1/2013 10:47:00 10
.064 5
. 255 4
.759 4
.446 9.968 24.502 138.205 2/1/2013 10:48:001"1-:1;.;0:':.0:::6::'5

## -~5.~2~58;--4:"'.**7;:5:-;;8.....,-:4~.4:':'5.,;.2 ---;:.9.'i:9~68;--.,;.24:"'.:=,51:-;8.....,,;,13;;8:':** **8;-;8~11** 2/1/2013 10:49 : 00 10
. 065 5.257 4
. 758 4
.448 9.968 24
. 52 138
. 647 2/1/2013 10 : 50 :0 0 1
. 371 0.616 0.935 2
. 328 2.937 10
. 558 81
.048 2/1/2013 10 : 51 :00 0
. 096 0.135 -0.028 0
. 004 0
. 024 0.155 0
.423 2/ 1/2 013

## 10**52 :00** **1"1-";0"; 0;;9~6---;:'0** **~1;:;34;--: -0** **.0 ;;;3;;:3---";0";** **.0 ;;:2';'3---;:'0.;;;0:';'24;--0~** **~12;;:7"""-;-0;;' 2:;o"'81**  2/1/2013 10:53:00 0.156 0.157 -0
. 029 0.497 1.525 5.717 3.519 2/1/2013 10 : 54:00 8
. 879 3.136 1.619 2.841 13.222 26
. 978 146
.066 2/1/2013 10 : 55:00 17
.478 1.961 1.315 1.465 13.285 27.493 172.625 2 / 1 /2 013 10:56:00 20. 743 0
. 249 0
.011 0 .2 35 13
. 271 28.03 153
. 822 2/ 1/ 2013 10 : 57 :00 20. 805 0.215

-0
.001 0
. 113 13
. 258 28
. 132 158
. 558 2/1 /2 013 10 :5 8 :00 20.812 0 .2 12

-0 .004 0
. 109 13
. 258 28
. 333 151.66 2/1/2013 10:59:00 20.797 0.22 -0.007 0
. 133 13.262 28.616 144.756 2/1/2013 11:00:00 20
.782 0
. 23 0.003 0
. 108 13.245 29
.028 126.426 2/1/2013 11 :01 : 00 20
. 549 0.227 -0.002 0
. 127 13.273 2 8
.914 124
. 859 2 /1/20 13 11 :02 :00 20
. 683 0
. 259 0
.026 0
. 158 13.292 29.29 105
. 533 2 /1/20 13 11 :03:00 19
. 888 0
. 33 0
.061 0.251 13.276 29.272 96 .09 2 2/1/2013 11 :04:00 16
. 876 2
. 616 1.291 0
. 537 13.275 29.404 90.405 2/1/2013 11:05:00 13
.44 4.505 2.544 1.696 13.311 28.948 103.931 2/1/2013 11 : 06:00 13.44 4
. 505 2.647 1 .7 3 13.308 28.739 107 .5 95 2 / 1/ 2013 11 : 07 : 00 13
.433 4
. 516 2.65 2
.014 13.3 29
. 032 115
. 202 2 / 1/ 2013 11 : 08 : 00 13.432 4
. 519 2 .7 54 1 .6 39 13
. 296 29.5 92
. 548 2/1 / 2013 11 : 09 : 00 13.44 4
. 512 2.678 1.341 13
. 326 29.445 74 .5 47 2/1/2013 11 : 10:00 13.45 4.51 2.549 1 .3 93 13.322 28.71 94.037 2/1/2013 11:11:00 13
.441 4.515 2
. 666 1
.715 13.315 29 .2 32 95
. 323 2/ 1/2013 11 : 12 :00 13.438 4.517 2.74 1
. 627 13 .2 97 28
. 867 101.647 2/1/2013 11 : 13 :00 13.445 4
. 513 2.738 1. 7 43 13
. 323 29.024 100.126 2/1/2013 11 : 14 :00 13.452 4.513 2
. 719 1
. 6 27 13.313 29.298 95
. 121 2/1/2013 11 : 15 :00 13
. 45 4.515 2.753 1.727 13.321 29 .2 2 98
. 681 2/1/2013 11:16:00 13.444 4.52 2
. 762 1.439 13
. 313 29
. 312 87.169 2/1/2013 11 : 17:00 13.437 4
. 524 2
.703 1.539 13.3 29 .06 1 99
.09 2 / 1/2 013 11 : 18:00 13.44 4.522 2
. 556 1.76 13.328 29
. 128 105.Q13 2 /1/20 13 11 : 19 :00 13.437 4.521 2.675 1
. 605 13
. 321 29
. 179 99
. 934 2/1 /20 13 11 : 20:00 13.438 4
. 521 2.731 1.488 13.318 29 .2 7 99
. 652 2/1/2013 11:21:00 14
. 263 3
. 954 2.553 1.57 13.32 28
. 731 110
. 723 2/1/2013 11:22:00 16
. 522 2.82 1.478 0.88 13.324 29
.076 113.878 2/1/2013 11 :23:0 0 13.423 4.531 2.767 1
. 518 13.326 29.051 101.824 2 / 1/ 2013 11 :2 4 : 00 13.425 4
.532 2.76 1.669 13.323 29
.085 107
.064 2 / 1 / 2013 11:25:00 13
.418 4
. 537 2.836 1
. 564 13.322 28
. 807 106.946 2/1/2013 11:26:00 13
.416 4
. 537 2.772 1
. 692 13.318 28
. 66 112.242 2/1/2013 11:27:00 13.41 4.543 2.861 1.909 13.324 28.553 126.77 2/1/2013 11 :2 8 : 00 13
.406 4.545 2.893 1
. 693 13
. 319 29.602 97
. 873 2/ 1/2 013 11 :29: 00 13
.405 4
. 547 2.868 1
. 159 13.311 29.828 78.667 2/1/2013 11 :3 0 :00 13
.404 4
. 545 2
. 842 1
.095 13.318 29
.477 7 8.114 2/1 / 2013 11 :3 1 :00 13.407 4
. 541 2.815 1.273 13.325 29
. 351 88
. 364 2/1/2013 11 :3 2:00 13
.418 4.534 2.751 1.317 13.323 29.425 92.317 2/1/2013 11 :3 3 : 00 13.409 4.541 2.917 1.17 13.319 29.804 67.984 2/1/2013 11 :3 4 :00 13.405 4.543 2.667 0.945 13.32 29.601 68.443 2/ 1/ 2013 11 : 35 :00 13.407 4
. 543 2.702 1
.005 13.318 29
. 464 70.408 2/1/2013 11 : 36 :00 13.412 4.543 2
. 667 1
.09 13
. 327 28.981 84.936 2/1/2013 11 : 37:00 13.413 4.543 2
. 734 1.152 13
. 33 29
. 358 78.027 2/1/2013 11 : 38:00 13.41 4.546 2
. 795 1.083 13.319 29.185 80.67 2/1/2013 11 : 39 :00 20
.024 0
. 603 0.425 0
. 544 13.311 29
. 216 89
. 168 2 / 1/ 2013 11 :40:00 14 .9 42 3 .7 57 1
. 923 0.803 13.313 29 .6 51 81.067 2 / 1 /20 13 11 : 41 : 00 13
.433 4.53 2.634 1.259 13.306 29 .7 47 71.586 2 / 1 /20 13 11 : 42 : 00 13.423 4
. 542 2
.771 1.103 13
. 315 29 .95 9 62 .7 51 

### THe PPM -0 .0 13 W bias 

### 6
. 928 16
. 31 35.366 Direct Span 

### 40
. 348

41.59 41.766 38.476 Direct Ze ro 

### 40.183 45
.906 44
. 195

37
.09 39
. 109 36
.433 34.061 28.217 30.311 24.159 21.354 18 .8 82 25.546 26.957

30.19 21.102 13.655 22
.019

20
. 86 24.023 23.144 21.555 22.929 18.653 23.474 24.077

23
. 17 23.815 27.971 29.842 23.389 25.849 26.343 28
. 279 33.989 21.071 16
.033

15
. 8 19.965 22.339 11.727 13.155 13.872 19
. 335 16.474 17
. 117 19
. 62 17 .7 4 14
. 101 10
. 544**~ ~** **N~** 

### W**~ ~**  

### W Date Time % % 

### PPM PPM % 

### PPM PPM 2/1/2013 11:43:00 13.428 4.537 2.672 1.039 13.318 29.643 66.384 2/1/2013 11:44:00 13.423 4.543 2.676 1.098 13.3 30.182 59.793 2/1/2013 11:45:00 13.422 4.546 2
. 609 0.949 13.316 30.139 55.33 2 /1/2013 11:46:00 13.428 4.539 2
. 512 0
.97 13.318 30.185 56.124 2 / 1/ 2013 11 :47:00 13.427 4.539 2
. 687 0
. 853 13.315 30
. 395 48.409 2/1/2013 11 :48:00 13
.43 4.539 2
. 646 0.848 13
. 318 30.291 48
. 56 2/1/2013 11:49:00 13.431 4.539 2
. 81 0.871 13.322 30
. 328 46.691 2/1/2013 11:50:00 13.434 4.541 2
. 704 0
. 821 13.309 30.457 45.08 2/1/2013 11:51:00 13.429 4.543 2
. 808 0.812 13.31 30.413 44.597 2/1/2013 11:52:00 13.428 4.547 2.76 0.761 13.315 30.586 42.47 2/1/2013 11:53:00 13.424 4.552 2.658 0.754 13.307 30.513 43.225 2 / 1/2013 11:54 : 00 13.417 4.561 2
. 651 0
. 662 13.315 30.621 39.274 2 /1/2013 11:55 :00 13.413 4.567 2
.707 0
. 507 13.309 30.764 33
. 251 2/1/2013 11 :56 : 00 13.411 4
.57 2 .7 36 0
. 522 13.305 30 .707 35
. 344 2/1/2013 11 :57 :00 13
. 407 4.571 2.667 0.497 13.315 30
. 649 34
. 69 2/1/2013 11 :58 : 00 14
. 571 3.798 2.308 0.444 13
. 297 30.906 30.496 2/1/2013 11 :59 : 00 18.044 1.961 0.905 0
. 103 13
. 285 31.216 25
. 652 2/1/2013 12:00 :00 13.407 4.571 2
. 635 0.135 13.294 31.017 22.081 2/1/2013 12:01:00 13.391 4.582 2
. 615 0.187 13.3 30.847 23.7 2/1/2013 12:02:00 13.392 4.587 2
. 573 0.23 13.308 30.822 25.729 2 / 1/2013 12:03:00 13.401 4.583 2
.548 0.217 13.3 31.002 23.716 2/1/2013 12:04 :00 13.381 4.595 2 .643 0
. 185 13 .2 93 31
. 122 21.546 2 / 1/2013 12 : 05:00 13.387 4.594 2 .6 71 0
. 16 13.292 31.162 20.933 2/1/2013 12:06:00 13.382 4.602 2.784 0.183 13
. 291 31.023 24.653 2/1/2013 12:07:00 13.36 4.615 2.848 0.125 13.27 31.403 21.163 2/1/2013 12:08:00 13.365 4.614 2.6 0.102 13.303 31.075 20.389 2/1/2013 12 : 09:00 13.378 4.61 2.622 0.129 13.287 31.133 21.551 2/1/2013 12:10:00 13.372 4.615 2
. 726 0
. 128 13.278 31.061 22.458 2 /1/2013 12 :11 : 00 13.384 4
. 605 2.733 0
. 171 13.294 31.108 21
. 938 2/1/2013 12 :12 :00 13.381 4 .6 08 2
. 862 0.145 13
. 277 31.323 19
.982 2 / 1

/ 2013 12 :13 : 00 13.391 4
. 6 2
. 618 0.158 13.3 31.034 20
. 528 2/1/2013 12 :14 : 00 13.394 4.602 2.576 0.153 13.297 31.069 20
. 7 2/1/2013 12:15 : 00 13.39 4.608 2
. 724 0
. 147 13
. 298 31.146 20.316 2/1/2013 12:16:00 12.997 4.405 2
. 275 0
. 194 10.901 13.98 18.766 2/1/2013 12: 17 :OO
.. !

## -:1:;;0.71::;15~--:5:;".3;;:1::-7--.0::'.0:;0';5! .0.192
.. !.....:7 9 .:;;9:;32:--:1:::.1"'2;2! 1.203 2/1/2013 12:18:00 9
. 974 5.232 0.007 -0.378 4.708 11.986 -0.324 2/1/2013 12 : 19 : 00 0.538 0.308 4.409 -0.024 0
. 052 24
. 97 -0.162 2/1/2013 12 : 20 : 00"!-";0"
. 1"9::-8-"';;0."'2':::46;--4;';
.

## 7,;;0;;;7,-.....;0".1;;;5.;.1-....;:,0:;;.~03;-~24;...;;;95;.;9,-.....;.0;;;.1::6:;3! 2 / 1

/2 013 12 :21 :00 0.193 0.239 4.143 0.323 0
. 026 12 .7 89 22.863 2/1/2013 12:22 :00 0
. 173 0.234 -0. 012 3
. 849 0.022 0.752 118.41 2/1/2013 12 : 23:00 0
. 168 0.231 · 0.Q25! 4.426! 0.022 0.663 124.871 2/1/2013 12:24:00 7
. 873 4.385 2.949 4.438 5.629 11
. 237 128.216 2/1/2013 12:25:00 10.048 5.34 4.745 4.437 10.196 18
. 086 130.491 2/1/2013 12:26:00
..

## !......;'-:1-:i0.':i0~6--5"'.;;.34:--4;.;**7;,,4;;:7,---:4.;,.4;;:3.;,,2!** 3
. 387 9.578 78
. 151 2 / 1/2013 12:27:00 6.632 3.459 3
. 525 4
. 122 0
. 033 0.65 136.832 2/1/2013 12 :28:00 0
. 107 0
. 202 -0.024 0
. 367 0
. 023 0.562! 137.709! 2/1/2 013 12 :29 :00 0
. 094 0 .2 -0
. 03 -0
. 029 0
. 022 0
. 513 137
. 992 2 / 1

/ 2013

## 12**30 00"!-";0";** **0:;:9';'4-~0 -:1;;;99;-""".0":** **0;;;3;;;6--.";0".0;;:2; 2!**  0
. 025 0
. 403 132
. 935 2 / 1/2013 12:31 :00 0.178 0
. 234 -0.024 1.117 0
. 022 0.126 19.789 2/1/2013 12:32:00 5.681 2.224 0.884 3.435 0.022 0.122 -0.212 2/1/2013 12:33:00 15.578 0.507 0.34 0.68"!-'::0";.0"'2::-3

## -"';;0.710~5;-""";.0::'.2:;1:;7! 2/1/2013 12:34:00 13
. 308 0.266 -0.02 0.389 8.24 17.559 45.347 2/1/2013 12:35:00 20
. 301 0.27

- 0
. 022 0.108 9.94 24
. 433 137.256 2 / 1

/2013 12 :36:00 2.46 0.235

-0
. 032 0
.038!"

## -";:9""**9~4';'1-~24';' 47.5;-';;1;'38';'.2;;;1:;2!**  2 /1/2013 12 :37 : 00 0.199 0.233

-0 .029 -0.002 11
. 561 24
. 126 108.912 2 / 1

/2013 12 :38 : 00 0
. 176 0.232

-0 .0 33 -0.001 13
. 289 29.92 30.7 2/1/2013 12:39:00 0
. 168 0.233 -0 .03 -0.012 13 .2 92 29.961 27.137 2/1/2013 12:40:00 0
. 167 0.233 -0.028 -0.008 13.292 30
. 151 29.546 

### THC PPM 12
.494 9
. 953 9.305 9
. 505 6
. 858 7.219 6
. 857 6.448 6
. 132 5.524 5
. 82 4.627 2 .7 52

3
. 5 3
. 314 2.396 1.393 0.826 1.135 1.326 1.137 0
. 71 0
. 57 1.462 0
. 672 0.634 0.827 

### 1 0.779 0 .5 18

0 .5 3 0.606 0.563 0.476 ·0.Q2 02/C02 bias

-0.02 -0
. 021

-0 .02 NOx bias



### -0
. 019 -0.015 -0
. 015 W bias 0
. 133 1.359 0 .493 Direct Span 

### -0 .0 15

-0 .0 14 Inlet CO bias 

### -0 .0 14 -0.014 Zero Direct 

### 0.571 0.911 0.919 Zero Direct 

### 0.909 1.005 1.101 Span Direct



### 0
. 9 1.267 0
. 95 1.745Date Time 

### 2/1/2013 12:41:00 2/1/2013 12:42:00 2/1/2013 12:43:00 2/ 1/2013 12:44 : 00 2/ 1/ 2013 12 :45 : 00 2/1 / 2013 12:46 : 00 2/1/2013 12 :47 :00 2/1/2013 12:48 : 00 2/1/2013 12:49:00 2/1/2013 12:50:00 2/1/2013 12:51 : 00 2/1/2013 12 : 52 :0 0 2/ 1/ 2013 12 : 53 :00 2/1/2013 12 : 54 :00 2/1/2013 12 : 55 :00 2/1/2013 12:56 : 00 2/1/2013 12:57:00 2/1/2013 12:58:00 2/1/2013 12:59 : 00 2/1/2013 13:00 :00 2 / 1/2013 13:01 :00 2/1/2013 13:02 :00 2/1/2013 13:03 :00 2/ 1/2013 13:04 :00 2/1/2013 13:05:00 2/1/2013 13:06 :00 2/1/2013 13:07 :00 2/1/2013 13:08:00 2/1/2013 13 :09 :00 2/1/2013 13 : 10 :00 2 / 1/ 2013 13 : 11 :00 2/1/2013 13 : 12 :0 0 2/1/2013 13:13 :00 2/1/2013 13:14:00 2/1/2013 13:15:00 2/1/2013 13:16:00 2/1/2013 13 : 17 :00 2/1/2013 13 : 18 :00 2/ 1/ 2013 13 : 19 :00 2 /1/2 013 13 : 20 :00 2 / 1/2013 13 : 21 :00 2/1/2013 13 :22: 00 2/1/2013 13:23:00 2/1/2013 13:24:00 2/1/2013 13 : 25:00 2/1/2013 13 : 26 : 00 2/ 1/ 2013 13 : 27:00 2/ 1/ 2013 13 : 28:00 2/1/2013 13 : 29:00 2/1/2013 13 : 30:00 2/1/2013 13:31:00 2/1/2013 13:32:00 2/1/2013 13:33:00 2/ 1/ 2013 13:34 :00 2/1/2013 13 : 35 :00 2/1 / 2013 13 : 36 :00 2/1/2013 13 : 37 :00 2/1/2013 13:38:00 2/1/2013 13:39 :00 

### 0 , % 

### 0
. 168 0
. 168 0
. 148 0.143 0.143 0.143 0.143 0.143 0
. 306 0.575 0.688 0.784 0
. 873 0
.957 0
.792 0.936 1.034 1.12 1.168 1.217 1.213 1
.005 1.039 1
.073 1.098 1.136 1
. 146 1
. 164 1
. 181 1 .2 01 1 .2 24

1.24 1 .2 66 1
. 298 1 .3 13 1
. 328 1
. 344 1.363

1.37 1.384 1.384 1
. 385 1.386 1.388 1.402 1.403 1
.412 1
. 389 1.352 1.302 1.255 1.211 1.152 1.032 1.009 0.528 0
. 282 0
. 334

0.08 CO 2 NO. CO % PPM PPM 

### 0.234

-0.031 0.002 0.234 -0.027 -0.01 0.235 -0.036 -0.01 0
. 235 -0.034 -0.003 0
. 236 -0.034 -0
.008 0
. 235 -0.031 -0
.013 0
. 236

-0
.036 -0.015 0.237

-0
.034

-0
.005 0.238

-0.032 -0.005 0.238 -0.035 -0.Q1 0.238 -0
.037 -0.023 0.238 -0.034 -0.02 0
. 239 -0.029

- 0
.01

0
. 24

- 0
.034

- 0
.018 0
. 241 -0.035 -0
.012 0
. 242 -0
.04 -0 .Q15 0.242 -0.04 -0.Q15 0.244 -0.039 -0.016 0.244 -0.036 -0.007 0.245 -0.036 -0.009 0.374 0.027 -0.039 0.523 0.124 -0.055 0
. 535 0.128 -0.Q7 0
. 546 0
. 136 -0.073 0.556 0.14 -0.067 0.569 0
. 149 -0.06 0.575 0.157 -0.077 0.581 0
. 158 -0.077 0.588 0.169 -0.0 66 0
. 594 0.176 -0. 074 0
. 602 0.176 -0.073

0.61 0.181 -0.067 0.62 0
. 204 -0.073 0.628 0.189 -0.081 0.635 0.188 -0.073 0.642 0
. 199

- 0
. 073 0
. 648 0
. 205 -0
. 073 0
. 655 0
. 203

- 0
. 085 0
. 659 0 .2 13

-0
. 084 0.662 0.212 -0.062 0.664 0 .2 1 -0.072 0.664 0.212 -0.072 0.667 0.219 -0.071 0.669 0
. 203 -0.068 0
. 672 0
. 212 -0.Q75 0.675 0.218 -0
.08 0
. 678 0
. 216 -0 .058 0
. 672 0.208 -0.064 0.664 0 .205 -0.073 0.647 0 .1 98 -0.062 0.632 0.188 -0.073 0.618 0
. 177 -0.064 0.601 0
. 161 -0.076 0
. 561 0.135 -0.061 0.554 0 .133 -0.07

0
. 39 0
.054 -0.059 0.319 -0 .005

-0
. 032 0.342 0
.008 -0.041 0.263

-0.02 -0.049 

### 0 , % 

### 13.282 13 .2 84

13 .29 13.283 13.286 13.265 13.272 13.273 13.264

13
. 26 13
. 274

13
. 26 13.258 13.253 13.249 13.247 13.244 13.266 13
. 257 13
. 248 13 .2 43 13
. 242 13
. 261 13.266

13.27 13.26 13.271 13.262 13.269 13.278

13.27 13.237

13
. 28 13.271 13.273 13.261 13.254 13
. 255 13.256

13.28 13 .2 64 13
. 264

13
. 27 13
. 276 13.278 13.265 13.289

13
. 28 13
. 281 13
. 282

13.29 13.289 13.286 13.282 13.279 13.281 13.282

13.27 4.02**NO~** CO PPM PPM 

### 30
. 381 28.247 30.407 25.479 30.388 25
. 708 30.465 25
. 35 30
. 521 26 .2 5 30
. 865 23
. 928 30 .7 89 23.788 30.622 25.66 30
. 903 24.949 30.979 22.606 30.872 22.99 3 0
. 948 23.319 31.045 23.152 31.036 23 .7 37 31 .0 66 23.175 31.062 22.786 31.141 22.617 30
.925 22.482 30.953 22.995 31.046 22.8

31.16 22.627 31
. 24 22
. 036 30.892 23
. 386 30.889 23.521 31.015 22.939

31.06 22.636 30.875 23.276 30.869 23
. 667 30.885 24
. 595 30.849 23.813 30.897 23.461 31.248 22.488 30.837 23
. 364 30
. 956 22.692 30
. 915 23.363 30.969 22
. 598 30.935 23 .3 9 30
. 905 23
.417 30
. 937 23
. 316 30 .7 84 23.984 30.943 23.269 31.047 22.459 30.996 22.382 30.932 22.652 30.892 23
. 323 30.936 23
.094

30
. 8 23 .021 30
.75 23.436 30.696 23.796 30
. 662 24.775 30.627 24.327 30.591 24.6 30.589 23
. 919 30
.772 23.676 30.775 23
. 514

30
. 67 24 .026 30.745 24.01 30.694 25
. 236 12.248 18
. 546 

### THe PPM



### 1.319 0.89 0
. 887 0
. 822

1.15 0
. 85 0.734 1.097 1.004 0.565 0
. 562 0.542 0.598 0
. 807 0.633 0.563 0
. 586 0
.415 0
.499 0
. 565 0
.488 0
. 524

0
. 69 0.701 0
. 548 0
.478 0
. 643 0
. 594

0 .92 0
. 597 0
. 567 0
. 388 0.529 0
.459 0
. 546 0.498 0.557 0.555 0
.463 0 .6 25 0.519 0.503 0.539 0
.42 0
. 517 0.575 0
.462

0
.52 0
. 588 0
. 758 0.645 0
. 676 0
. 613 0.523 0
. 574 0
. 604 0.597 0
. 854 1.289**~ ~** **N~** 

### W 0 ,**~** 

### W Date Time % % 

### PPM PPM % 

### PPM PPM 2/1/2013 13:40 :00 0.067 0.249

- 0
.039 -0.037 0.027 0
. 236 0.371 2/1/2013

## 13:41**00!r--::0;';:.0~67':--0';;.;:'24;';9:----: 0;;'** **0~3~4-- ;';:0;';:.0~31:---0';;."'02~2~--:0;;'.1~9::'5---;';:O:':.** **2~4~1!** 2 / 1/2013 13:42:00 7
.48 4.125 2
.91 1.669 5
. 859 12
. 673 19
. 848 2 / 1/ 2013 13 :43 :00 10
.036 5.399 4
.729 4
. 364 9
. 939 24
. 548 131.984 2 / 1/ 2013

## 13**44 oo!r--:1':::0;';:** **0~44:---5~.~40;::1~~4:" .** **7;':3:;:2---;4-:.4':;'38::--":9~ 9':':** **~"";;'2:'::4'"; 5";3-;;';1~3i:8** **";2::18!** 2/ 1/ 2013 13 :45 : 00 6
. 368 2
.782 2
. 189 3
.071 11
. 528 23 .7 06 102
. 634 2/ 1/ 2013 13 :46 :00 12
. 36 4
. 679 2
.099 0
. 312 9
. 954 5
. 69 18
. 338 2/ 1/ 2013 13 :4

## oo!r-"':'1;:;0**~04:-;3~"""';'5-:. 3';;:85;---;** **0;;' 0~1';;19!** **316!r-~9~ 9~175** --'1:-': .0:;';3';'1! -0.413 2/1/2013 13:48:00 10
.047 5.39 -0
.024 -0.395 10
. 648 5.104 0
.454 2/1/2013 13:49 : 00 11.597 5.034 1.14 -0
. 213 13
. 258 29
. 795 26
. 289 2/1/2013 13:50 : 00 1 2 .56 4.46 2
.447 0.195 3
. 516 26
. 346 15.941 2/ 1 /2 013 13:51 :00 0
. 401 0.342 4.59 7 0
.087 0
.046 24
. 945 0
.04 2 2 / 1/ 2013 13 :52 :00

## !r--::0**'";1':;'73:---0';; ~30:::5'-~4:;;** **. 7;;:1~1-""';;:i'0.~14':--0';;** **"'02;':2~-2~4:': 8~7:;:7---;';:0-:** **1-';78::'!** 2 / 1/ 2013 13 : 53 :00 0
. 166 0
. 298 4
. 72 0
. 148 0
.022 12.522 28
.964 2 / 1/ 2013 13 :54 :00 0
. 16 0
. 294 0
. 63 2
. 872 0
.021 0
. 732 132
.022 2/ 1 /2 013 13:55 :00 0
. 142 0
. 292 -0
.0 2 6! 4
. 385! 0
.02 0
. 643! 135
. 873! 2 / 1/2013 13:56 :00 0
. 14 2 0
. 29 -0
.032 4.4 6
.599 13
. 314 117.599 2/1/2013 13:57:00 9
. 674 3.638 1.9 27 2.357 13.241 30
. 06 29.213 2 / 1/2013 13 : 58:00 13
. 315 4.667 2
. 688 0.22 13
. 265 30
. 137 23.578 2/ 1/ 2013 13 : 59 :0 0 13
. 3 3 1 4
. 678 2
. 602 0
. 176 13.263 30
. 28 26
. 5 3 4 2/ 1/2 013 14 :00 :00 13.3 34 4.681 2
. 618 0
. 195 13.269 30
. 1 74 25
. 532 2/ 1/2 013 14 :01 :00 13 .3 5 4
. 677 2
. 589 0. 20 5 13.382 29. 597 25.495 2/ 1/ 2013 14 :02: 00 13.5 2 1 4.571 2
.072 0 .19 13. 7 33 2 6. 369 36
. 519 2/ 1/2 013 14 :03 :00 14
. 188 4.173 2
. 094 0
. 212 13.73 8 26.427 40
.596 2/ 1/ 2013 14 :04 :00 14
.458 4.027 1.75 2 0.316 13
.734 26 .718 38
. 895 2/1/2013 14 :05:00 14.464 4.024 1
. 654 0
. 305 13
. 734 26.793 38
. 323 2/1/2013 14:06 : 00 14
.453 4
. 032 1
. 575 0
. 305 13. 728 26
. 884 38
. 238 2 / 1/ 2013 14 :07 :00 14
.438 4
. 044 1
. 629 0
. 31 13 .7 47 26 .7 66 38
. 982 2 / 1/ 2013 14 :08 :00 14
. 446 4
. 041 1
. 55 7 0
. 315 13 .7 63 2 6
. 715 39
. 302 2/1 / 2013 14 :09 :00 1 4. 44 2 4
. 047 1
. 511 0
. 321 13 .7 46 2 6
. 921 38
. 996 2/ 1/ 2013 14 : 10 :00 14
.407 4
.068 1
. 576 0
. 297 13. 75 2 26
. 731 38 .7 96 2 / 1/ 20 13 14 : 11 :00 14
.424 4.06 1
.499 0
. 306 13
. 756 26.56 40
.469 2/ 1/ 2013 14:12 :00 14
.416 4.064 1
.487 0
. 317 13
. 741 26
. 817 39.398 2/1/2013 14:13 :00 14
. 396 4
. 075 1.736 0.293 13
.758 26.631 39.535 2/1/2013 14:14 :00 14.406 4
.073 1.69 7 0.311 13
.758 26
. 596 40.907 2 / 1/ 2013 14 : 15 :00 14.415 4
.0 7 9 1.67 0
. 318 13.734 26
. 935 39
. 391 2 / 1/ 20 13 14 : 16 :00 14
. 388 4
.098 1
. 801 0
. 293 1 3.7 33 26
. 953 39
.025 2/ 1/ 2013 14 : 17 :00 14 .3 68 4
. 11 1.844 0
. 285 13.723 27
. 216 37
. 853 2/ 1/ 2013 14 : 18 :00 14 .3 72 4
. 109 1.799 0
. 259 13 .7 38 26
. 964 38
. 309 2 / 1/ 2013 14 : 19 :00 14
. 395 4
. 099 1.68 0
. 303 13 .7 44 26
. 985 39
.072 2/ 1/ 2013 14 : 20 : 00 14
. 379 4
. 109 1
. 751 0.288 13
.7 37 27
. 115 38
. 18 2/ 1/2013 14 : 21:00 14
. 364 4.112 1.941 0.271 13.739 27
. 104 37
. 88 2 2/1/2013 14 : 22:00 14
. 373 4.106 1.949 0.274 13.756 26
. 95 38.289 2/ 1/2013 14 : 23 : 00 14
. 397 4.095 1.798 0
. 288 13.768 26
.752 39.693 2/ 1/ 2013 14 : 24 : 00 14
. 3 9 4 4
. 098 1
.759 0. 299 13. 7 61 26
.95 39
. 194 2 / 1/2 013 14 : 25 :00 14
. 38 3 4
. 104 1
. 854 0
. 284 13 .7 6 27. 018 38
. 333 2/1/2013 14 :2 6 :00 14
. 368 4
. 11 1
. 937 0. 251 13.768 26
. 8 7 5 3 9
. 191 2/ 1/ 2013 14 : 27:00 14
. 3 68 4.108 1. 909 0 .246 13.773 2 6. 8 47 39
.739 2/1 / 2013 14 : 28 : 00 14
. 3 6 3 4.113 1.918 0. 223 13.766 27
. 01 3 8
. 604 2/ 1 / 2013 14 : 29 : 00 14 .3 63 4.111 1
.995 0
. 214 13.776 26
.912 38.716 2/1/2013 14:30 : 00 14.372 4.101 1.866 0
. 222 13.766 27.001 38.914 2 / 1/2013 14 : 31 :00 14
. 366 4
. 103 2. 007 0
. 235 13
. 78 2 6.826 39
. 202 2 / 1/ 2013 14 : 32 :00 14
. 38 4.093 2
.048 0
. 274 13
. 773 2 6
. 865 40
. 37 2 / 1/ 2013 14 : 33 :00 14
. 371 4 .098 2.3 09 0
. 261 13
.784 2 6
. 862 39
.48 2/ 1/ 2013 14 : 34 :00 14
. 3 8 2 4. 08 7 1.847 0
. 244 13
. 77 3 27. 01 7 39 .2 34 2 / 1/ 2013 14 : 35 :00 1 4. 359 4
.09 7 2
. 148 0
. 247 13. 7 62 27
. 12 38
. 314 2 / 1/ 2013 14 : 36 :00 14
. 367 4
.088 2
. 346 0
. 247 13
. 771 26
. 977 39. 3 15 2/ 1/ 2013 14:37 :00 16.409 2
. 89 2 1.614 0
. 214 13
. 767 27
. 141 38.612 

### THC PPM



### 0 .66 7 0 . 577 Direct Zero 

### 0
. 575 0. 723 Span Direct 0. 554 S pan Di rect 

### 1.05 4

0
. 3

- 0
.0 2 3 0 2/C02 bia s

-0
.021 2
. 206 0.367

-0
.02 2 -0 .022 NO x bias



### -0
.021

-0
.017

-0
.017 CO bias 0
.022

0
.49 0
.452 1
.02 8 0
.785 0 .8 17 1.35 2 1
.47 9 1
. 31 2 1.195 1.162 1.372

1. 43 1
.468 1. 4 93 1.581 1.295 1.252 1
. 553 1
.438 1.393 1
. 335

1.3 1.4 5 6 1.239

1
. 32 1.341 1
.475 1 .3 86 1 .3 37 1.473 1.511 1.4 0 5 1.345 1.313 1.378 1
. 573 1
. 397 1.311 1
. 239

1
. 39 1
. 387Date Time 

### 2 / 1/ 2013 14 : 38 :00 2/1 / 2013 14 : 39 : 00 2/ 1/ 2013 14 : 40 :00 2/1/2013 14 :41 :00 2/1/2013 14 : 42 :00 2/1/2013 14 :43:00 2/ 1 / 2013 14 :44 :00 2/ 1/ 2013 14 : 45:00 2/1/2013 14 : 46:00 2/1/2013 14:47:00 2/1/2013 14 :48:00 2/1 / 2013 14 : 49:00 2/1 / 2013 14 : 50 :00 2 / 1/ 2013 14 :51 :00 2/1/2013 14:52:00 2/1/2013 14:53:00 2/1 / 2013 14 : 54 :00 2/ 1/ 2013 14 :55 :00 2/ 1/ 2013 1 4: 56 :00 2/1/2013 14:57 :00 2/1/2013 14:58:00 2/1/2013 14:59:00 2/1 / 2013 15 :00 :00 2/1/2013 15 :01 :00 2/ 1/ 2013 15 :02 :00 2/1/2013 15:03 :00 2/1/2013 15 :04:00 2/1/2013 15 : 05 :00 2 / 1/ 2013 15 :06 :00 2 / 1/ 2013 15 :07 :00 2/1 / 2013 15 :08 :00 2/1/2013 15:09 :00 2/1/2013 15:10 :00 2 / 1/ 2013 15 : 11 :00 2/1 / 2013 15 : 12 :00 2/ 1/2013 15 : 13 : 00 2/1/2013 15 : 14:00 2/1/2013 15:15 : 00 2/1/2013 15:16 :00 2 / 1/2013 15 : 17 :00 2/ 112013 15 : 18 :00 2/1/2013 15 : 19 : 00 2/1/2013 15 : 20:00 2/1/2013 15 : 21:00 2 / 1/ 2013 15 : 22 : 00 2/ 1 / 2013 15 : 23 : 00 2/ 1/ 2013 15 : 24 : 00 2/1/2013 15:25:00 2/1/2013 15 : 26:00 2/1 / 2013 15 : 27 : 00 2/ 1/ 2013 15 : 28 :00 2/ 1/ 2013 15 : 29 : 00 2/1/2013 15 : 30 : 00 2/1/2013 15 : 31:00 2/1/2013 15 : 32 : 00 2/1 / 2013 15 : 33 :00 2/ 1/ 2013 15 : 34 :00 2/ 1/ 2013 15 : 35 : 00 2/1/2013 15 : 36:00 

### 0 , % 

### 14.411

14
. 38 14
. 38 14
. 382 14
. 38 5 14
. 392 14.385 14
. 387 14
. 391 14
. 375 14
. 377 14
. 368 14
. 341 14
. 306 14
. 308 14
. 299 14
. 304 15
. 13 7 18
.098 14.346 14
. 343 14
. 336 14
. 344 14
. 344

14.35 14
. 345 14
. 342 14
. 349 14
. 345 14
. 344 14
. 345 14
. 348 14.342 14.34 2 14
. 348 14
. 349 14
. 344 14.346 14
. 345 14.455 20
. 379 15
. 877 14
. 399 14
. 398 14
. 391

14
. 39 14
. 392 14
. 398 14
.421 14
.434 14
.427

14.44 14
.427 14.437

14
. 44 14.462 14.452 14
.465 14.454 CO 2 NO x CO % 

### PPM PPM 4
. 071 2
. 283 0
. 304 4
.077 2
. 21 0
. 3 7 9 4.077 2
. 178 0.389 4.076 2 .227 0.387 4.076 2.201 0.392 4.072 2
. 127 0
. 386 4.074 2
. 166 0
. 386 4
.075 2.18 0
.4 4.072 2.155 0
.424 4.083 2.263 0.405 4.081 2
. 253 0
. 397 4.082 2
. 19 0
.41 7 4
.098 2
. 38 0
. 395 4
. 123 2
.492 0
. 329 4.119 2
.426 0
. 343 4.124 2.382 0
. 338 4
. 124 2
.437 0
. 328 3.597 2
. 161 0
. 328 1
. 951 0
. 819 0
. 166 4
. 086 2
. 318 0
.444 4
.094 2.309 0.418 4.102 2
. 395 0
. 398 4
.095 2
. 355 0
. 391 4
.096 2
. 309 0
. 391 4
.094 2
. 286 0.402 4
. 098 2.247 0.402 4
. 104 2
. 314 0.397 4
.093 2
. 259 0.403 4
. 101 2
. 256 0.422

4
. 1 2
. 27 0
.406 4
. 097 2
. 267 0
.405 4
. 097 2
. 236 0.392 4
. 106 2
.404 0
. 394 4
. 106 2
.47 0
. 3 7 9 4
. 099 2
. 219 0
.406 4
.096 2
.417 0
. 388 4.101 2.333 0.379

4.1 2
. 326 0
. 375 4
. 103 2
. 206 0
. 393 4
. 047 2
. 31 0
. 357 0.541 0
. 159 0
. 113 3.263 1.438 0
. 203 4.069 2.036 0
. 377 4.071 2.106 0
. 36 4.077 2
. 197 0
. 35 3 4
.075 2
. 127 0
. 367 4
.073 2
. 109 0
. 365

4.07 2.081 0
. 385 4.057 2.041 0
. 399 4.053 1
.976 0
.413 4
.057 2
.056 0
. 396

4
.05 2
.012 0
.418 4
.055 2
.072 0
. 408 4
.048 2.083 0
.4 4.043 1.937 0
. 385 4
.031 1.771 0
. 379 4
.037 1.883 0
. 383

4
. 03 1.856 0
. 385 4
.037 1.841 0
. 384 O2 NO x CO THC % PPM PPM PPM 

### 13.766 27
. 181 38
. 384 1
.421 13
. 765 27
. 174 38
. 359 1.402 13.763 27. 231 38
. 224 1.446 13.766 27.153 38.161 1
. 375

13.77 27.149 37
. 983 1
. 189 13.773 27
. 159 38
. 242 1
. 308 13
. 776 27
.08 38
. 126 1
. 369 13.777 27
.065 38
.494 1
. 366 13.775 27
. 113 38.466 1.311 13.763 27.286 37.651 1.181 13.769 27. 161 37.782 1
. 243

13.76 27
. 208 38
. 142 1
. 233 13
.746 27
. 345 37
. 251 1.058 13.761 27
. 22 37
.407 1.126 13
. 758 27.083 38.494 1.199 13.748 27.279 37
.513 1.27 13
.747 27
. 191 37.852 1
. 277 13.761 27
.064 38
. 333 1.22 13
. 738 27
. 154 38
. 248 1.271 13.738 27
. 292 37
. 668 1.258 13.738 27.321 37.237 1.17 13
. 731 27
. 398 36
.738 1.133 13
.738 27. 282 37
. 283 1.18 13.741 27
. 303 37
. 323 1.215 13.749 27
. 16 37
. 82 1.341 13.749 27
. 145 38
. 137 1.365 13
. 744 27
. 248 37.516 1
. 282 13.755 27
.084 38
.054 1.378 13
. 741 27
. 174 38
. 146 1
. 374 13.756 27
.05 7 38.464 1
. 394 13.763 27
.067 38
. 588 1
.439 13.744 27.262 38.266 1.278 13.738 27
. 389 36
. 944 1.119 13.747 27
. 242 37.471 1.259 13.757 27
.083 38
. 553 1
. 397 13.754 27
. 129 38.348 1.331 13.732 27.326 37.732 1.287 13.742 27
. 238 37.566 1.158 13.736 27 .3 95 37
. 278 1
. 108

13.73 27
. 553 36.444 1.042 13.739 27
. 38 36.422 1.149 13
.732 27
.421 37
. 242 1.12 13.727 27.555 35.902 0
.944 13.722 27
. 643 35
. 563 0.959 13
.733 27
. 532 35
.75 0
. 953 13
.734 27.582 35
. 904 1.089 13.747 27
. 51 36
.075 1.091 13.734 27.584 36
.084 1.144 13.756 27
. 373 36
. 662 1
. 175 13.738 27.533 36.441 1
. 105 13
. 748 27
.469 36
. 331 0
. 99 13.751 27
. 408 36
. 565 1
. 171 13
. 731 27. 576 36.39 1.236 13.747 27.493 36.357 1.176

13.76 27
. 385 36
. 692 1.163 13.749 27 .422 36
. 805 1
. 226 13.755 27
.465 36
. 29 1.044 13.757 27
. 354 37
.083 1.056 13.754 27.386 37.038 1.213**~ ~** **N~** 00**~ N~**  00 

### Date Time % % 

### PPM PPM % 

### PPM PPM 2/1/2013 15:37 :00 14
.449 4.039 1.875 0.389 13.762 27.327 37.305 2/1/2013 15:38:00 11.913 3.293 1.632 0.621 4.547 11 .392 65.329 2/1/2013 15:39:00 0.302 0
. 313

-0.02 3.884 0.05 1.064 133 .833 2/1/2013 15 :40:00 0
. 217 0.296 -0.026! 4.385! 0.034 0.927! 135.334! 2/1/2013 15 :4 1 :00 2.078 1 .389

-0
.035 4
. 129 6.134 0.864 101.253 2/1/2013 15:42

## :00**f"!--;l';;'0 .';;'03~2:-""';;~** **.';' 36~~** **0::-: .0~** **3;;'1!** 0. 136 f"!

## -9;;-**9;;';1~3-~0~ 8;-;1716!**  3.211 2/1/2013 15:43:00 7.117 3.768 1.201 -0.348 4 .839 11
. 589 -0.161 2/ 1/2013 15 :44:00 f"!

## -~O-;.**2~1::"2 --.;;.0.'i:30i:'7:----'4:-'.6:i:9:-;2:-.....:.;;0.;;.0~8** --;::-0
.

## .;;.04~1:-~24:-**.6~8;:;8----;0 :';.1~2i'15!**  2/1/2013 15 :45:00 0.175 0.279 2 .5 33 0.106 0.05 7.262 -0.116 2/1/2013 15 :46:00 0.093 0.252

- 0.032 -0.032 0.022 0.184 -0.216 2/1/2013 15:47 :00 f"!

### --;:0-;**.0:i;93i:--:;' 0.';'25;';1:-~-0~.0i:'3;;:5----;0~** **.04:::7 4** **--';;'0.';;'02;;'2:--~0;- 1;-;5";"1---~0:"'.**  2;";1:':!9! 2/1/2013 15:48:00 7
. 651 4.327 3.157 1
. 885 5.789 12.262 35.166 2/1/2013 15 :49:00
........;1:;;0;,:;
. 0:;,79=-_;;;5.;;;39=:9;.-_4;;.. 7;,;3;.;4_--:,.;4.:;;3;:,9

### _...;;;9.;;;95;;;6;.-...,;.24;;.**3~9;.;7_1;;;3:;;6;;.2:;;0~1** 2/1/ 2013 15 : 50 :00! 10.086 5.398 4 .7 42 4.427 9
. 966 24.424 138 .268 ! 2/1/2013 15 : 51 :00 6.208 2.448 3.99 2.745 12.214 23.476 99.129 2/1/2013 15:52 :00 14
. 342 4.003 1.969 0.504 13.758 26.875 40.157 2/1/2013 15 :53:00 14.398 4.051 1.95 0.453 13.763 26.944 39.292 2/1/2013 15:54:00 14
. 396 4.056 2
. 033 0.434 13
.75 27.261 37.89 2/1/2013 15:55:00 14
. 389 4 .062 2.236 0
. 392 13.764 27.057 38.359 2/1/2013 15:56:00 14
.407 4.054 1
. 935 0.412 13.761 27.094 38
. 81 2/1/2013 15:57:00 14
.4 4
. 06 2.165 0.418 13 .7 62 27.066 38.861 2/ 1 /2013 15:58:00 14
.412 4.056 2 .096 0.423 13 .7 66 27.021 39.447 2/1/2013 15 : 59:00 14.439 4.039 1
. 975 0.424 13.769 27
.032 39.615 2/1/2013 16 :00:00 14.466 4.025 2
. 009 0.431 13.785 27.007 39.743 2/1/2013 16:01:00 14.474 4.02 1.981 0.445 13.783 27.003 39.802 2/1/2013 16 :02:00 14.46 4.028 2.012 0.44 13.764 27.126 39.609 2/1/2013 16:03 : 00 14.452 4.03 2.038 0.441 13.765 27
. 127 39.775 2/1/2013 16 :04:00 14.453 4.027 2.074 0.437 13.764 27
. 344 38.172 2/1/2013 16:05 :00 14.473 4.017 2
.067 0
. 391 13.76 1 27.491 37.66 2/1/2013 16 :06 :00 14
.464 4.019 2
. 128 0
. 374 13.786 27
. 1 05 38.802 2/1/2013 16 :07 :00 14.501 4.003 1.96 0
. 396 13.764 27
. 347 39.089 2/1/2013 16 :08:00 14
.474 4.014 1.999 0.4 13.761 27.574 37.555 2/1/2013 16:09:00 14.462 4.018 2
.044 0.371 13.764 27.536 37.305 2/1/2013 16:10 :00 17.285 2.259 1.252 0.322 13.771 27.28 38.382 2/1/2013 16:11 :00 20.51 0.591 0.033 0.089 13.764 27
. 377 38.815 2/1/2013 16:12:00 14.508 4.036 2
. 397 0.242 13.764 27.631 37.436 2/1/2013 16 :13:00 14
. 364 4
. 068 2.428 0
. 336 13
. 764 27.674 36
. 426 2/1/2013 16:14:00 14
. 367 4
.068 2
. 253 0
. 345 13 .7 6 27
. 699 36.741 2 / 1/20 13 16 : 15 :00 14
. 356 4.074 2
. 373 0.343 13.764 27
. 547 36.977 2/1/2013 16:16:00 14
. 361 4.071 2.267 0.352 13.751 27
. 681 36.628 2/1/2013 16:17:00 14
. 349 4.079 2
. 331 0.342 13
. 742 27.711 36.509 2/1/2013 16 : 18:00 14
. 344 4.085 2.44 0.338 13
. 744 27.783 35.825 2/1/2013 16 : 19:00 14.345 4.08 2.395 0.348 13.743 27.776 35.943 2/1/2013 16:20:00 14
. 343 4.084 2
. 381 0.335 13.761 27.71 35.932 2/1/2013 16 :21:00 14 .353 4.072 2
. 343 0.353 13.765 27.458 36.674 2/1/2013 16 : 22 :00 14
. 353 4.077 2
. 306 0.365 13.765 27.344 37
. 616 2/1/2013 16 : 23 : 00 14
. 317 4.106 2
. 389 0
. 329 13.765 27
. 398 37.347 2/1/2013 16:24:00 14
. 319 4.103 2
.486 0
. 333 13 .77 1 27.403 37
. 194 2/1/2013 16 :25:00 14
. 326 4.099 2
. 373 0.338 13 .7 66 27.423 37.223 2/1/2013 16:26 :00 14.318 4.104 2.402 0.325 13.77 27.431 36.923 2/1/2013 16:27 :00 14.323 4.096 2
. 39 0.34 13.772 27.575 36.663 2/1/2013 16:28 :00 14.323 4
. 1 2.405 0.305 13.76 27.726 35.812 2/1/2013 16: 29:00 18
. 607 1.612 0.867 0.15 13.769 27.579 36
. 252 2/1/2013 16:30:00 14
. 388 4 .0 52 2
. 372 0.288 13.773 27
.415 37.309 2/1/2013 16:31 :00 14.38 4.052 2.285 0
. 366 13.775 27.506 37
. 211 2/1/2013 16 :32:00 14
. 374 4.055 2.285 0.364 13.765 27.613 36.521 2/1/2013 16:33 :00 14.36 4 .06 2.369 0.368 13.775 27.4 14 37.121 2/1/2013 16:34:00 14
. 376 4.052 2.311 0.393 13.791 27.353 37.75 

### THC PPM

1
. 237 0.87 -0.016 -0 . 016 CO bias 

### -0. 017 -0. 021 02/ C02 bias -0.021 -0.021 NOx bias 

### 0.271 1.221 1.257 Direct Zero 

### 1 .2 69 1. 241 1.218 Direct Span 

### 1.404 1.463

1.33 1.174 1
. 273 1.324 1
. 352 1
. 344 1
. 256 1.286 1
. 236 1 .299 1.332 1.236 1.197 1.227 1.301 1
. 142 1.156 1
. 155 1
. 335 1
. 139 1
. 168 1.129 1.223 1.193

1
.08 0.986 1.054 1.143 1.145 1.211 1.176 1.258 1.278 1.105 1
. 198 1
. 117 1
. 196 1
. 252 1 .2 51 1.014 1.115 1.218**~ ~** **~** 

# w 0 ,**N~** 

## W Oate Time % % 

### PPM PPM % 

### PPM PPM 2/1/2013 16 : 35 : 00 14.383 4.046 2.326 0.401 13.767 27.549 36.971 2/1/2013 16:36 : 00 14.367 4.053 2.394 0
. 387 13
.774 27.57 36.443 2/1/2013 16 : 37 :00 14.37 4
. 049 2
. 32 0
. 37 13 .8 04 27
. 334 37
.488 2/ 1/ 2013 16 : 38 :00 14
. 384 4.039 2
. 232 0
. 384 13 .8 09 27.239 38
.064 2/1/2013 16 : 39 : 00 14.4 4
.028 2
. 309 0.392 13.81 27.181 38
. 667 2/1/2013 16:40:00 14
.4 4.025 2.223 0.413 13.794 27.289 38.226 2/1/2013 16 :41 :00 14
. 385 4
.03 2
. 294 0
. 414 13. 7 83 27.383 37.818 2/ 1/ 2013 16 :42 : 00 14
. 37 4.04 2
. 31 0.4 13.773 27.448 37
. 199 2/ 1/ 2013 16 :43 : 00 14 .36 7 4.039 2
. 392 0
. 373 13
.793 27.282 37
. 9 2/1/2013 16 :44 : 00 14.379 4.031 2.266 0.409 13.765 27.506 37.329 2/1/2013 16 :45 : 00 14 .3 47 4
. 049 2
. 369 0.379 13.778 27.355 37.432 2/ 1/2013 16 :46 :00 14
. 369 4
.03 2
. 384 0
. 394 13 .777 27.355 37.657 2/1/ 2013 16 :47 :00 14.369 4.029 2
. 339 0.415 13.773 27.38 37
. 679 2/1/2013 16:48 : 00 14.365 4.03 2.333 0.388 13.771 27.505 37
.079 2/1/2013 16:49 :00 14.36 4.032 2.389 0
. 387 13.763 27.701 35.826 2/ 1/ 2013 16 : 50 :00 14 .3 47 4
. 041 2.473 0.371 13 .7 64 27.498 36.352 2/ 1/ 2013 16 : 51 :00 18
.975 1.241 0
. 789 0.246 13
.777 27.311 37.453 2/1/2013 16 : 52 : 00 15.199 3.677 1
. 614 0.239 13.803 27.2 38.168 2/1/2013 16:53 :00 14.453 3.973 1.906 0
.41 13
.796 27
. 219 38.444 2/1/2013 16 :54 :00 14.441 3
. 977 2
.006 0
.422 13 .7 64 27
.446 37
. 677 2/ 1/2013 16 : 55 :00 14.43 3.985 2
. 103 0.395 13.779 27
. 321 37
. 866 2/1/2013 16:56 :00 14
.435 3.981 2.071 0.4 13
.785 27
. 249 38
. 164 2/1/2013 16:57:00 14
. 44 3
. 978 2.008 0.407 13
.787 27.218 38.231 2/ 1/ 2013 16 :58 :00 14
.443 3
. 974 2
.084 0
.412 13.81 27
.052 39
. 247 2/ 1/2013 16 : 59 :00 14
.439 3.978 2
. 158 0
.422 13.785 27
. 163 38
. 876 2/1/2013 17 :00 :00 14
.444 3.974 2.177 0.41 13.799 27
. 17 38.407 2/1/2013 17:01 :00 14.479 3
. 953 2.164 0.428 13
. 803 27
.06 39 .2 6 2/ 1 / 2013 17 : 02 :00 14
.462 3
. 959 2
. 129 0
.444 13
.795 27.077 39
.083 2/1/2013 17 : 03 :00 14.471 3
. 952 2.106 0
.449 13.783 27
. 135 39
. 192 2/1/2013 17:04 :00 14
.463 3.951 2.131 0.456 13.771 27 .2 57 38.655 2/1/2013 17:05 :00 14
.456 3.953 2.035 0.446 13.765 27.437 37
. 7 2/1/2013 17:06 :00 l4.465 3
. 948 2
.002 0.413 13 .7 65 27.313 37 .8 5 2/1 /2 013 17 : 07: 00 14.484 3
. 936 1.936 0.411 13 .7 66 27
. 313 38
.072 2 / 1/2013 17:08 :00 14.481 3
. 936 1.945 0.402 13
.766 27.277 38
. 207 2/1/2013 17:09 :00 14.484 3.933 1.937 0.408 13.766 27.251 38.323 2/1/2013 17 : 10:00 14
.486 3
. 932 1.914 0
.417 13 .7 68 27
. 261 38
. 214 2/1/2013 17 : 11 :00 14
.451 3
. 945 2
.05 0.4 13 .7 66 27.303 38
. 34 2/1/2013 17 : 12 :00 14
.456 3
. 944 2
.072 0.399 13 .7 66 27.301 38
. 282 2/1/2013 17:13 :00 13.174 3.467 2.173 0.441 2.83 8.648 75.893 2/1/2013 17:14 :00 0
. 381 0.223 0
. 156 3.299 0
. 05 0
.987 138
. 384 2/1 /2 013 17 : 15 :00 0
. 199 0
. 198 -0
.011'-!

# -4~**3~8~3!** 0
.033 

# o 898! 138
.99! 2/1 / 2013 17:16 :00 0.203 0
. 193 -0.017 4.409 1.906 0
. 824 136.615 2/1/2013 17:17:00 2.868 1.768 -0.012 3.98 9.916 0.782 27.698 2/1/2013 17 : 18:00 10
.074 5.222 -0.013 0
. 221 9
. 965 0.729 -0
. 37 2/ 1/ 2013

## 17**19 00'-!--;l';;'0** **711;-:3;-"""';'5-; 2:':'44:;---;-0;-:** **00~8!** -0.355'-!

## -9;;-**9i;;6";'7-~0::-: 6;';7~5!**  -0
. 389 2/1/2013 17 : 20 :00 10.159 5
. 221

- 0.001

- 0.387 5
.473 14
. 622 3 .8 2 2/1/2013 17:21:00 3.069 0.932 3.697

- 0.048 0.048 24
. 679 0
. 792 2/1/2013 17 :2 2 : 00
.. !--=0-=
. 2"'05"....-0"".""19"'4,--4"'. 7"'1"'5--'.,,0.-=1""3--::.0
. "0"'25,--,2"'4-:
. 6"'8---""'0'"'
.0"'5,,,7! 2/ 1/ 2013 17 : 23 : 00 0
. 198 0
. 181 4
.739 0.162 8
.919 25
.773 11
.006 2/ 1/ 2013 17 :24 :00
..... --::..;0::;,
. ""1

### _~0::;..1",4:...........;0;;,.4,;:1:,;1_....;0;.;.0;;;2;,.7_....".1:,;
. 8:;;6:-.....;6;;,
. 2:,;0;;;6_...;2;,:2'=
.7.;:3.;,4 2/1/2013 17 : 25:00! 0.097 0.136 -0.018 -0.037 0.024 0
. 196 0.041 2/1/2013 17 : 26 : 00 7.099 3
. 898 2.698 1
. 364 5
.042 9.719 10
.431 2/ 1/2 013 17 : 27 : 00 10
. 107 5
. 251 4
.759 4
. 361 9
. 987 24
. 501 127
. 253 2/1/2013 17 : 28 :00"!

## ....;1:,;0;;;**1'"'14;--:;;5.~24~8:--4;;, .** **7;,;6:,;5-.....;~4.;.;;4~3 -~9** **:;,99:;;4,-...".24;;, 5:.;2;;;5-1:-:3:.;9;.;** **2;:;2;:,11** 2/1/2013 17:29 : 00 11.102 3.539 4.54 4.43 16.003 35
. 52 132
. 294 2/1/2013 17 : 30 : 00 14
. 359 3.845 2.601 5.258 18.876 44
. 25 50
. 633 2/1/2013 17 : 31 :00 14
. 382 3.866 2.528 7.847 18
. 88 8
. 849 17
. 292 2/1/2013 17 : 32 :00 14.425 3
. 905 2
. 534 8.882 18
. 88 29.509 13.498 

### TH( PPM



### 1.207 1.246 1.354 1.358 1.344 1.252 1.393

1 .2 5 1.305 1.196 1.327 1.292 1.333 1.294 1.042 1.229 1.186 1.391 1.408

1 .2 8 1.366 1.271 1.218 1.362

1
. 36 1.324

1
.48 1.325 1.376

1
. 3 1.255 1.225

1.25 1.251 1.366 1.259 1.241 1.389 0
. 802 -0.011

· 0 .01 CO bias 

### -0.011 -0.016 -0
.017 -0
.017 02/( 02 bias 0
. 118 -0.017

-0 .017 NO x bias 

### 0
. 347 1.406 1.147 Direct Zero 

### 1.173 1
. 187

1.07 Direct Span 

### 0.93 0
. 913 0
. 852 0
. 606**~ ~** **~** 

# w**~ ~**  

### Date T ime % % 

### PPM PPM % 

### PPM 2/1/2013 17 :33:00 14.458 3 .899 2.5 28 9
. 311 18.88 48.34 2/1/2013 17 :34:00 14.445

## 3.906r!--:2;:;.5:;:2:::.4--=9:.::.4,;.33;.........,,18~.;;:88;:1~-4:-::8,:;**3;;;5.,;,2!** 2/1/2013 17 : 35:00 14.477 3
. 893 2.157 9.418 18.8 15 .494 2/1/2013 17 : 36 :00 14.482 3.893 1 .992 9
. 356 18
.779 0.517 2/1/2013 17 :37:00 14.485 3 .892 1.98 9.308 18.778 0
. 438 2/1/2013 17:38 :00 14
.473 3.893 2.024 9.273 18 .779 0.411 2/1/2013 17 : 39 :00 14
.483 3.892 2.1 9.23 18
. 779 0.378 2/ 1/ 2013 17 : 40 :00 14
.477 3.892 2.171 9
. 182 18 .77 9 0
. 363! 2/1/2013 17 :41:00 14.502 3.878 2
. 063 9.131 18
. 779 0.351 2/1/2013 17 :42:00 14.51 3 .874 2.086 9.065 11
. 074 0.34 2/1/2013 17:43:00 14.5l4 3.87 2.122 9
.021 4
. 385 0
. 312 2/1/2013 17:44 :00 14.508 3
. 871 2
.088 8
. 977 4
. 504 0.304 2/1/2013 17 : 45 :00 14.519 3.864 2.04 8.942 4.505 0.292 2/1/2013 17:46 :00 14.514 3.864 1.978 8
. 896 4.505 0.29 2/1/2013 17 :47:00 14.493 3.872 2.142 8
. 853 4
. 506 0
. 282 2/1/2013 17 :48 :00 14.502 3 .869 2
. 168 8
. 807 4
. 505 0
. 285 2/ 1/2013 17 : 49 :00 14.51 3.866 2
. 169 8
. 759 4
. 505 0.267 2/1/2013 17 :50:00 14.515 3
. 861 2.178 8.717 4.506 0.268 2/1/2013 17 : 51:00 14
. 501 3.866 2.164 8.673 4
. 506 0 .2 59 2/1/2013 17 : 52 :00 14.5 3
. 865 2
. 168 8
. 629 4.506 0
. 262 2/1/2013 17 :53:00 14.512 3.855 2.093 8.579 4.506 0.255 2/1/2013 17:54:00 14.522 3.845 2.136 8.543 4.506 0.245 2/1/2013 17:55:00 14.524 3.84 2.288 8.495 4
. 506 0
. 234 2/1/2013 17:56 :00 14
. 53 3
. 832 2.112 8.464 4
. 506 0.235 2/1/2013 17:57 :00 14.525 3.831 2.04 8.423 4
. 507 0.235 2/1/2013 17:58 :00 14.527 3.827 2.019 8
. 366 4.507 0.231 2/1/2013 17:59 :00 14.519 3.831 2.188 8.333 4.507 0.235 2/1/2013 18 : 00 :00 14
. 519 3.825 2
. 104 8
. 291 4.523 0
. 23 2/ 1/2013 18 :01:00 14.53 3.816 2.027 8
. 242 4.531 0 .2 3 2/1/2013 18 :02:00 14.528 3.81 2.114 8.203 4.531 0.227 2/1/2013 18:03:00 14.544 3.797 1.989 8.156 4 .53 0.223 2/1/2013 18 : 04:00 14.545 3.795 2
.08 8
. 126 4.53 0.222 2/1/2013 18 : 05 :00 14.544 3
. 795 2.172 8
.094 4.546 0 .2 07 2/1/2013 18:06:00 14.537 3.799 2.196 8 .0 53 4.554 0.215 2/1/2013 18:07 :00 14.539 3.796 2.155 8.01 4.555 0.219 2/1/2013 18 :08:00 14
. 541 3.795 2
. 136 7
.966 4
. 554 0
. 233 2/1/2013 18 : 09 :00 14
. 53 3.8 2
. 188 7.925 4.565 0 .2 16 2/1/2013 18 : 10 :00 1 4.54 3.793 2.149 7.883 4.58 0.216 2/1/2013 18:11:00 14.529 3.798 2.185 7.852 4.579 0.216 2/1/2013 18 : 12:00 14
. 543 3.789 2.166 7.805 4.58 0
. 218 2/ 1/2013 18 : 13 :00 14
. 55 3.782 2.066 7
.77 4
. 58 0
. 215 2/1/2013 18:14 :00 14.551 3.779 2.014 7.726 4.593 0
. 215 2/1/2013 18:15 :00 14.552 3.776 2.002 7.672 4.604 0.213 2/1/2013 18 : 16:00 14.552 3.776 2.018 7.647 4
. 605 0.209 2/1/2013 18:17 :00 14
. 538 3
. 784 2.132 7
. 603 4
. 605 0
. 214 2/1/2013 18:18 :00 14.522 3.789 2.261 7.566 4.604 0
. 213 2/1/2013 18:19 :00 14.533 3.78 2.216 7.522 4.611 0.214 2/1/2013 18:20:00 10.773 4.336 1.165 7
.483 4.629 0
. 213 2/1/2013

## 18**:21:00 !r--:1':::0~** **1.;,,66;--5~ .~** **11~3!** 0.022 7.446 4
. 629 0 .2 18 2/1/2013 18:22 : 00 10
. 165 5 .12 0.012 7.408 4.629 0
. 206 2/1/2013 18:23:00 10.145 5.11 0.008 7.376 4.649 0.199 2/1/2013 18:24:00 1.763 0.572 3.685 7
. 355 4.654 0.201 2/1/2013 18 :25:00!..--=0::,.2;;:31 ;.....-:::,:0;;,
. 1! 4.754 7
. 304 4.654 0
. 198 2/1/2013 18 :26:00 0
. 164 0.063 4.759 7.268 4.666 0.202 2/1/2013

# 18:27**:00!..--= 0-:.0;:,99;.....-0;;** **.;;:03 ~2!**  4.775 7.24 4.679 0.19 2/1/2013 18:28:00 8.697 4.597 4
. 762 7
. 188 4.679 0
. 186 2/1/2013 18 : 29 :00!..--:1"0""
. 1",32"..........,5"
. "'11;,.,1! 2
. 917 7
. 152 4.679 0
. 189 2/1/2013 18:30 :00 16.571 8.538 2.155 7.118 4
. 691 0.165 W PPM 

### 13.653 14.801

11 .0 6 10 .27 4 36.681 229 .99 1 243
. 366 243
. 287! 192
. 146 41.634

7
.484 1 .7 07 0.762 0.557 0.546 0
. 545 0
. 547 0.549 0.524 0.509 0.424 0.422 0.399 0.396 0.398 0.402 0.404

0
.4 0.396 0.393 0.395 0.397 0.392 0.388 0.391 0.391

0
. 39 0.392

0.39 0.388 0.392 0.388 0.394 0.391 0.393 0.394 0.392 0
. 394 0
. 395 0.395 0.399

0
.4 0
. 379 0
. 306 0.245 0
. 246 0.248 0.248 

### THC PPM



### 0.329 0.329 NOx Mid, CO High, Inlet Direct High 

### 0
. 328 0.328 0.329 0.338 0.338 0.337 CO-In Direct Hi gh 

### 0.336

0.33 0.329 0
. 329 0
. 328 0 .329 0
. 329 0
. 328 0.328 0.328 0.329

0
. 33 0.329 0.329

0.33 0.33 0
. 33 0.33 0.33 0
. 33 0.329 0.329 0.329 0.329 0.328 0.328 0.329 0
. 329 0.329 0.329

0.33 0 .33 0.33 0.33 0.331 0.331 0.331 0
. 331 0.331 0.331 0 . 331 02 bias 0
. 331

0.33 0.331 0.331 Zero bias



### 0 .3 3 0.331 02/(02 Direct Zero 0.331 0
. 331 02/C02 Direct 

### 5pan 0.331

### 0, 

## co, Date Time % 

### % 2/1/2013

## 18**31:00IL.....:1:.:;9:.:.0~16;.._9~.;69;::J91** 2/1/2013 18:31:30 11.533 9.704 2/1/2013 18:31:40 3.961 9.709 2/1/2013 18:31:50 3.872 9
. 71 2/1/2013 18 : 32:00 3
. 828 9.704 2/1/2013 18:32:10 3
. 825 9.706 2/1/2013 18:32:20 3.814 9 .703 2/1/2013 18:32:30 3.8 9.704 2/1 /2 013 18:32:40 3.8 9.701 2/1/2013 18 : 32:50 3.807 9
. 699 2/1/2013 18:33 :00 10
. 657 9.7 2/1/2013 18 :33:10 14
. 606 9
. 699 2/1/2013 18:33:20 14 .97 9.698 2/1/2013 18:33:30 15.041 9.698 2/1/2013 18:33:40 15 .062 9.695 2/1/2013 18:33:501 15 .0661 9.694 2/1/2013 18:34 :00 14 .563 9 .69 4 2/1/2013 18:34:10 11
. 764 9.694 2/1/2013 18:34:20 11
. 319 9.694 2/1/2013 18:34 :30 11.256 9.689 2/1/2013 18:34:401 11
. 2351 9.689 2/1/2013 18:34 : 50 11.227 9.688 2/1/2013 18:35:00 11
. 226 9 .685 2/1/2013 18:35:10 10
. 264 9
. 683 2/1/2013 18:35:20 9.467 9.681 2/1/2013 18:35 : 30 9
. 394 9 .68 2/1/2013 18:35:40 9.37 9.677 2/1/2013

# 18:35:501"-9~**3;;:;6;;'91** 9.679 2/1/2013 18:36 :00 8.915 9.676 2/1/2013 18:36 :10 7.681 9.675 2/1/2013 18:36:20 7.529 9.671 2/1/2013

### 18:36:30.LI_-:7~.5;711 9.669 2/1/2013 18:36:40 6
.74 9.671 2/1/2013 18:36:50 4.208 9.669 2/1/2013 18:37:00 3.87 9
. 67 2/1/2013 18:37 : 10 3
. 825 9.668 2/1/2013 18:37:201 3
. 8011 9.666 2/1/2013 18:37:30 5.544 9.664 2/1/2013 18:37:40 9.544 9.661 2/1/2013 18 :37:50 10
.004 9.663 2/1/2013 18:38:00 10.082 9.661 2/1/2013 18:38:10 10
. 104 9.661 2/1/2013 18:38 : 201 10
. 1161 9.659 2/1/2013 18:38:30 10
. 181 9.657 2/1/2013 18:38 :40 13.46 9
. 655 2/1/2013 18:38:50 14.927 9.651 2/1/2013 18:39:00 15
.052 9.649 2/1/2013 18:39:10 15
. 078 9.645 2/1/2013 18:39:20 15.09 9.643 2/1/2013 18:39:30"1

# -1~5':;;.0;;'91 9.644 2/1/2013 18:39 :40 14.028 9.64 2/1 / 2013 18:39:50 11.588 9.638 2/1/2013 18:40:00 11.306 9.636 2/1/2013 18:40 : 10 11.255 9
. 634 2/1/2013 18:40:20 11.248 9.633 2/1/2013 18:40:301 11
. 2381 9.632 2/1/2013 18:40:40 10.727 9
. 627 2/1/2013 18:40:50 9.574 9.625 

### NO, 

### PPM

2.163 1
.452 0.09 0 .082 0
.052 0.054 0.057 0
.052

0.05 0.043 0 .042 0
.043 0
.045 0
.043 0
.043 0
.038 0.045 0.054 0.049 0.043 0
.047 0 .041 0
.037 0
.056 0.053 0
.042 0.042

0
.04 0.043 0.037 0
.045 0.059 0.072 0.067 0.076 0.083 0.192 0
. 299 0.217 0
. 167 0.156 0.162 0
. 127 0.108 0
.094 0.106 0.078

0.07 0
.067 0.063 0.059 0.063 0.058

0
.05 0.051 0.057 0.056 0
.062 

## co PPM

7.072 7
. 053 7.013 7.033 7.037 7.041

7
.01 7.002 6.992 6.976 7.002

6
. 98 6.995 6.972 6.969 6.958 6.948 6.965 6.939 6.944 6.939 6.897 6.922 6.911 6.902 6
. 905 6.906 6.891 6.866 6.877 6.876 6.869 6.881 6.851 6.844 6.843 6.812 6.839 6.823 6
. 844 6.817 6.813 6.808 6.794 6.781 6.813 6.786 6.771 6.771 6.735 6.741 6.756 6.763 6.749 6.732 6.723 6.702 6.705 

### 0, % 

### 4.703 4.704 4
.703 4 .703 4
.704 4.704 4
.704 4.704 4
.704 4
.704

4.72 4
.729 4 .728 4
.728 4.728 4.728 4
.728 4
. 728 4.728 4.729 4
.728 4 .729 4.728 4.728 4
. 729 4
.729 4.728 4
. 728 4 .728 4.728 4.728 4
. 739 4
.752 4.753 4 .7 53 4
.753 4 .753 4.753 4.753 4.753 4 .752 4.752 4.753 4.753 4 .7 52 4.752 4
.752 4.752 4.753 4
. 753 4.753 4.753 4.754 4
.753 4.753 4
.753 4.753 4.752 

### NO, 

### PPM 0.17 0.162 0.157 0.154 0
. 156 0.155 0.163 0.165 0.157 0.172 0.159 0.156 0.156 0.169 0.156 0.159 0
. 156 0.159 0.166 0.159 0.166 0.139 0.139

0.17 0.168 0.17 0.17 0
. 17 0.166 0.159 0.172

0.17 0
. 172

0.18 0.175 0
. 164

0
. 17 0.17 0.187 0.176 0.187 0.173

0.17 0.17 0.169 0.166 0
. 156 0.165 0
. 169 0.169 0.156 0.155 0.154 0
. 149 0.163 0.151 0.152 0.156 

## co PPM

0.206 0.232 0.246 0.251 0.249 0.248 0
. 146 0.201 0
. 249 0
. 248 0.246 0
. 141 0.197 0
. 245 0.248

0
. 25 0.145 0.199 0
. 143 0.091 0.193 0.248 0
. 246 0.249 0.253

0
. 25 0.248 0
. 143 0.094

0
. 2 0
. 25 0.246 0
. 244 0.248 0
. 254

0.25 0.249 0.351 0
. 396 0
.501 0.548 0.649 0.693 0.593 0.545 0
. 546 0
. 552 0.553 0.558 0
. 556 0.449 0.402

0.4 0
. 395 0 .397 0
. 398 0.293

0.35 

### TH( PPM

0.331 02/(02 Direct High 0.331 0.331 0.331 0.331 0.332 0
. 332 0.331 0.331 0.331 0.332

0.33 0.331

0.33 0.33 0
. 331

0 .33 0.331 0.331

0.33 0
. 331 0.331

0.33 0 .33 0.331

0
. 33 0.33 0.33 0.33 0.33 0.331 0
. 331 0.331 0.331 0.331 0.331 0
. 331 0.33 0.33 0.33 0.331

0.33 0.33 

### Mid 0.331 0.331 0 .33 1 0.331 0.331 0.332 0.3 31 0.331 0.331 0.332 0.332 0.331 0 .331 0.331 0.331 80%

60%



### 50%

40%

20%

80%



### 60%

### 0, Oate Time % 

### 2/1/2013 18:41 :00 9.408 2/1/2013 18:41:10 9.385 2/1/2013 18 :4 1 : 20I r

## -"i:9~**.3:':171** 2/1/2013 18:41 : 30 8.857 2/1/2013 18 :41:40 7.671 2/1/2013 1 8:41:50 7.53 2/1/2013 18:42 :00 7.51 2/1/2013 18:42:10 

### r 

# l**-7~.5~0:::t91** 2/1/2013 18:42 :20 6.738 2/1/2013 18:42:30 4.212 2/1/2013 18 : 42 :40 3.874 2/1/2013 18:42:50 3.823 2/ 1/2013 18 : 43:oo 

### r 

# l --";3:-;;
. 8"'0:':1 3 1 2/1/2013 18:43 : 10 4.181 2/1/2013 18 :43:20 8.922 2/1/2013 18:43 : 30 9.934 2/1/20 13 18:43 :40 10 .068 2/1/2013 18:43:501 1 0.0911 2/1/2013 18 :44:00 10.101 2/1/2013 18:44:10 11
. 91 2/1/2013 18:44:20 14 .7 58 2/1/2013 18 :44:30 15.005 2/1/2013 18:44 :40 15
. 04 2/1/2013 18:44 :50 

### r 

# l """""15;;; .0;;

5""31 2/1/2013 18:45:00 14.1 22 2/1/2013 18 :4 5 :10 11.599 2/1/2013 18:45 :20 11 .292 2/1/2013 18 :45:30 1 11.2361 2/1/2013 18 :45 :40 11
. 169 2/1/2013 18:45:50 9
. 834 2/1/2013 18:46:00 9.422 2/1/2013 18:46:10 9
. 374 2/1/2013 18 :46 :2 01 9
. 3691 2/1/2013 18:46:30 8.912 2/1/2013 18:46:40 7
. 675 2/1/2013 18:46 : 50 7.523 2/1/2013 18:47 :001 7.4991 2/1/2013 18:47 : 10 6
.488 2/ 1/2013 18:47:20 4.145 2/1/2013 18:47 : 30 3.861 2/1/2013 18:47 :40 3.82 2/1/2013 18 :47 :501.--:3:::.8"'0:;,21 2/1/2013 18:48:00 3.806 2/1/2013 18 :48:10 7.892 2/1/2013 18 :48:20 9.841 2/1/2013 18 :48:30 10.041 2/1/2013 1 8:48:40 10.087 2/1/2013 18:48 : 501 10 .09 11 

### CO , % 

### 9.625 9.626 9.622

9.62 9.616 9.612 9.613 9.607 9
. 607 9.604 9.603 9.599 9.595 9.592

9.59 9.588 9.588 9.586 9.581 9
. 579 9.576 9.574 9.571 9.568 9.565 9.563 9 .563 9.557 9.556 9.551 9.547 9.545 9
. 543 9.542 9.539 9.534 9
. 532 9.531 9.524 9.522 9.523 9.519 9.513 9.513 9.506 9
. 506 9.502 9.502 

### NO, PPM

0.065 0.054 0
.055

0
.05 0.043 0.041 0
. 046

0
.04 0.043 0.049 0.047 0.043 0.044 0
.045 0.044 0.059 0
.047 0.048 0.039 0.048 0.044 0.051 0.057

0.05 0.042 0.044 0.047 0.043 0.047 0.048 0.043 0.037 0
.044 0.044 0.052 0.039 0.044 0.038 0.039 0.037 0.039 0.043 0.048 0.D35 0
.038 0.043 0.034 0.036 

### CO PPM

6.713 6.699 6.717

6
. 69 6.703 6.699 6
. 677 6
. 669 6
. 673 6.658 6
. 673 6
. 64 2 6.599 6.623 6.666 6 .636 6.639 6.617 6.618 6 .5 77 6.587 6.591 6.589 6.622 6
. 605 6
. 586 6
. 558 6
. 539 6
.577

6.53 6
. 546 6
. 524 6
. 517 6.525 6.522 6
.496 6
. 526 6
.519 6.493 6.472 6.445 6.487 6.505 6
. 469 6.469 6.464 6.452 6.422 

### 0, % 4.755 4.774 4.777 4
.777 4
. 778 4.777 4.777 4.778 4 .778 4.778 4
. 777 4
. 777 4
. 778 4.777 4.777 4 .77 8 4.778 4.777 4.777 4 .777 4
. 778 4
. 778 4.777 4.777 4.778 4
. 777 4
. 777 4.777 4 .7 77 4.789 4.801 4
. 802 4
. 801 4
. 802 4.802 4.802 4
. 802 4
. 80 1

4.8 4.801

4.8 4
. 801 4.801 4.802 4
. 802 4.801 4.801 4
. 801 

### NO , PPM

0
. 155 0.151 0.153 0
. 143 0.154 0
. 147 0
. 147

0
. 14 0
. 146 0.161

0.14 0
. 14 0
. 14 0.14 0 .14 0
. 14 0
. 14 0.152 0.158 0
. 138

0.14 0.14 0.148

0
. 14 0 .1 42

0.14 0.147 0
. 147

0.14 0.14 0.14 0
. 134

0
. 14 0.14 0
. 152 0.143 0.151 0
. 141

0
. 14 0
. 14 0
. 14 0
. 14 0.138

0
. 13 0
. 141 0
. 138 0.124 0
. 131 

### CO PPM

0
. 395 0
. 291 0.349 0
. 396 0.399 0.398 0
. 398 0
. 287 0.344 0.289 0
. 244 0
. 246 0
. 243 0.239 0
. 244 0.244 0
. 244 0.245 0.245 0.245 0
. 247 0
. 244 0.249 0
. 247

0
. 25 0.248 0.243 0
. 248 0.247 0.247 0.244 0
. 25 0
. 251 0.243 0.246 0
. 245 0
. 244 0
. 242 0.239 0
. 241 0.236 0.243 0.241 0.247

0
. 25 0
. 244 0.242 0.245 

### THC PPM

0.331 0.331 0.331 0
. 331 0
. 329

0
. 33 0.33 0
. 33 0
. 33 0.331

0.33 0
. 33 0.33 0
. 331 0.331

0.33 0.329

0.33 Mid 

### 0.33 0
. 33 0
. 33 0.33 0.331 0.331

0
. 33 0.331 0
. 331 0
. 331 0.331 0.331 0.332 0 .331 0.331 0.331 0.331 0.331 0.331 0.331 0.333 0.333 0.333 0.332 0.332

0
. 33 0.33 0.33 0.331 0.33 Mid 50%



### 40%

20%

80%

60%

50%



### 40%

20%

## Appendix C.3 Ammonia Data 

## by SCAQMD Method 207.1

R0410673 C-7AMMONIA TEST RESULTS SUMMARY Client Gemma Parameter Locat ion CPV Sentinel Fuel Unit 2 Data By Test Number CPV**Sentine!~2· NH** **3-55-1** CPV**Sentine ~2** **NH3-56-2** Reference Temperature, F 60 60 Test Date 21112013 21112013 Test Method SCAQMD 207
. 1 SCAQMD 207
. 1 Samp le T rain 9-P&M 9-P&M Meter Calibration Factor 0 , 992 0 ,992 Stack Area (sq ft) 143.14 143 . 14 Samp le Time (Min) 60 60 Barometric Pressure {i n Hg}_ 29.69 29
.69 Start Time 14 ; 20 1 5 : 53 Stop T ime 15 : 35 17 :09 Meter Vo lume (act) 48 , 058 44 . 351 Meter Temperature (F) 80
. 7 78.4 Meter Pressure (iwg) 1 , 83 1 .60 liqu id Volume (ml) 99
. 3 96
. 0 Stack 02 (%) 14 , 38 14 , 36 Stack NOx (ppm) @ 15% 02 1 . 99 2
.05 Unit Load MW 55 56 F uel Flow Rate , hscfh 5,361 5 ,39 1 Standard Sample Volume (SCF) 45
. 700 42
. 332 Moisture Fraction 0.092 0.095 Stack F low Rate (dscfm, 60 of) 282,277 278,356 Stack Flow Rate (dscfm 70 of) nla nfa Gas Constant (ft- lbfllb-mo le-R) 1545
. 33 1545 .33 Standard Pressure (l bf/ft2) 2116
. 224 2116.224 Molecular We ight NH3 (I bllb-mole) 17 17 Specific Molar Vo l ume (ft3Itb -mole ) 379.50 379
. 50 Mass Conversion (lb/ug) 2.20E-09 2
. 20E-09 02 Correction Factor (%) 15 15 Mass NH3 (ug/sample) 669.90 769
.60 Mass NH3 (mg) 0
. 670 0.770 Mass N H 3 (Ib) 1.48 E-Q6 1 , 70E-06 P PM NH3 (flue gas) 0 , 7 0
. 9 PPM NH3 @ 02 Correction 0 , 7 O ,B Ib/hr 0.55 0,67 Ib/MMscf fuel 1 , 02 1 ,2 4
NH3 EQUATIONS ; ppm NH3 = (m ass NH3* Gas Const * Ref Temp * 106 )/(Sample vo l. • Press * MW) ppm NH3 @ 02 correct i on = ppm * (20.9-02 Corr)/(20.9-%02) NH3 natural gas AA, SP, SS, JM Averaae lim it

14.37 2.02

O.B 0 .73 5 0 .6 1 1
. 1310

## WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD CLIENT : 

## !';1\::;.tlN)

. " AMBIENT TEMPERATURE : 

# ,3- LOCATION: 

### S "" lAY 

## p'V- 5 

### ;;::cl'

## ?9.tc,;J'I/S~2 BAROMETRIC PRESSURE-:

## 2J~"--;.b-;"**'------ ---** **---** DATE : 

### '211/'3 ASSUMED MOISTURE: "\°1,, RUN NO :

## ~ - 2> S1'1"- -

## Alif~ 

## - 50-I PITOT TUBE COEFF, C
- p':



## tc'-:c 

## o-"

.**'\~~;;----- ---**  OPERATOR: '':>**~"'""** 

### PROBE ID NO/ MATERIAL : 

## ott oo'i? METER BOX NO : "\**~""-** 

### PROBE LENGTH:_.tc h_"

_ _ --,.,-

___ ____ _ M ETER t. H@: \.

### ~"'1 NOZZLE ID NO I 

### MATERIAL: 

# 1'1(+ METER Yd : 

## o. 

## '\otL NOZZLE DIAMETER: 

## rv(4 STACK AREA, FT' : 

# lin <l,,\ 

### FILTER NOITYPE : 

## -1'1-'-"','=-1'<'-------- --- TRAVERSE POINTS , MIN/POINT: 

# '12\I?- PRE·TEST LEAK RATE :: L.<j.&i?c; FM@ 

# t:;;: in

. Hg

. t. H =

## ~ X t. P : ./ /' POST·TEST LEAK RATE : : 

### L.O.cil? CFM@ I 

## '5 in

. Hg

. Probe Condition, pre/post testJ , · 

### PITOT LEAK CHECK · PRE: ,/**POST :~**  

### Silica Gel Expanded , YIN:**~** 

### CHAIN OF CUSTODY : SAMPLE CUSTODIAN-,"={>.

_ _ _ Filter Condition after Test Nt\" SAMPLER=')"'

...

### -,-,**~**

## __ Check Weight 

# Z SAMPLE CUSTODIAN 

### l'<AImp. 

### # Contents Post·Test· Pre·Test = Difference 

# .I-**\i\Jll ~<f**  '80(,

## l{"'-~=S2**-'- .7L** 

# __ _ ;;A 

# d , \ II; 

# Il'Zsoj 

# t:J/6 g-- (-.k3, 

# Z-=-
. _ 

# J. C

# ,...,?!:, 5f'3. '7 

# 5e>2-. 

# > , - - 

# .!1. S'G- 

# C/lc-, 'Y2ciJ, Jo

_ _ L..A - 1'0 c)



### Tota l:

_____________ _ Meter t. P t. H Stack Probe F i lte r Imp

. Out Meter T smp, o f 

### Vac uum 0, P

. static Point Time Volume, ft' in

. H , O in , H , O Temp , o f \, 

### Temp , o f 

### Temp , o f 

### Temp, o f 

### In Out in , Hg, 

### % in , H,O 

### 5 3 1'-12..'"**'12.V)~** 

### l yW O.\pl 

### ,/..:l:2-') 

# /'14 ()ItA- tJ t i'r 

## {,.'-t ",0., ' 77
. 1 

# ,<C.

. a**I~.,** 

### .. 2-L 2- I '{ 

### '2 '5"**~** 

### O , t..6 , 

## 1:;' -.l [ \ 1 1'-/;"0> 

### 2. 

## , ? : 1 ;,2. 

# -n.;l , \ CfVV ('fO**q~.">"--** 

### I I C)"S 1,).. 

# It '3 

### 1 ,\3"1**tI~b.712-** 

## I '-It< &.L"O 

# t , :, lib bJ.., 0-{**'I~** 

### h-, .' '2- 

## l'i't'f q 

## 0,'5'\ 

## '1'.2> 1 

## V-!'1'9 11 D


## . C",3 1l4> lire", 0 

## VttS'l.**~** 

## q

## 1/P/

# z. I 

## V
.ld., l15 

## ,,;3 \<;[-) 1**C\~1 812.-**  

## 1--Ie-O d "D 

## V'I I 'l l Gl ,3, 

## ,6i C,· .D 

## '2.- 1 <;0&

.**~** 

## ,p.rn "> .'70 \ ' '; i 1 

### '2 cf) 

## ·1.2.. l,b r't/rv(/ \ )1**~** 

## 'I'>'i.02.6 I 

## b
. 'O) 171 vJ ') \ 

### <;Zu 

## qS-q
. b 

# '2" L\ S**I~** 

### ,1 ) :-j 

### 1 1 '-f 

## i.:H**'32-"~** 

## ') <> 

### 1.. 

### i')7-> "**'6** 

### D "7'1 ' 

### \ 15'1'''' 1- 

### D 

## . "1 ", \>,**~"'O** 

### I ,),) 

## '172.1'1{; \ f) 

## . "6.' '1'1 

## '1**~** 

### \ 

# , AveraQe : I:> 

## \1<" Comments :

____________________________________________________________________________________________________________________ __



### Date of last revision 

### 1/25 /2 013 Page 

# .-L. of 

# 1- D8834049 Master Document 8torage\Forms\Datasheets\Field Datasheets

## s

.,;

fI


### vJ

# Della~ IW

_ _ _ 

## WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD CLIENT: 

# tJ,.P./Y""**/h-~** LOCATION ::1:/ 

# 4"1 - " < 

# d (C '" - 

# f .2.. DATE : 

### :J -- ) 

## 1:3 RUN NO: 

# 0 ' 

# :J.JS

- A ' 

# 9 3

- 5"0- · 

# '1' OPERATOR: 

## 6.5**METERBOX7N~0 :~** **Sn1 ~~** **~----** METER t. H@ : \

. 

### 3 'l Q METER Yd : 

## .---"-"" "-'-::Q '--

, "<1"'i" ')"

' --- STACK AREA , 

### FT2: 

## 143.1 '+ TRAVERSE POINT"'S",

## '"'M~'N';';/;:!-PO='N"'T:-**:** - 5 =/' (2

::- .• - t. H= /V!>: X t. P: Probe Condition , prelpost 

### test 

# v',./' Silica Gel Expanded, 

### YIN : 

# i\J Filter Condition after T

## est**-I N:-I:~2"-**  Check We i ght

_ __ -'/'-

_ _ ___ _ Meter 

### t. P Point Time 

### Volume, ft' in. H , O 

## ..4/ ' 1'5'> <, ,,\1 ;-:; 

## i1 i 4'**)**



### · 2 

### \ C, 

# oJ' 3 &v'&;? I 

## i003 2. &..,9vf) 

### ;:'1'1" 

## Ibo15 Q, 

## X'l ; 

# I, \ I**~>'IO** 

# t>/fJ.-" \ (,,{ J- 

# " n.ni +,..- to-"(; 

### "t 

## 1..- 

## IlIl 30.[g'l I 

### \ (, 2.'L A t> ! 

## "00 i'O rvC! \\"J,. l 

# 31i · D\1o \ 

## o Jb8 ?'? \ t,,'t '1'14 , "It, 

### '-\' '" C • 

## 5'\ 2.- 

### I b":>1 

## 3 /), "'S 

# 1 lu 'l f L.

. 

## e . tp'?> (i, vv 

## Ib'I'1 I 00"\ . \ 

## 2;;- \ t> , L,l2 

## 1 "''-**~** 

## \ 1o'5l\. rD 

## <to \\/;-- 

# I 

# 't "'0
. 5,\ '}.. 

### )b)'\ 

## ->: e ... o 1 

## nOli . ,**~** 

### , 1,,"1 

## !:rvP

_ 

## i1.D"! . 0 1"1/,2."'1 , 0 

## .1"1 Average:**~** 

### AMBIENT TEMPERATURE : 

# J**~** BAROMETRIC PRESSURE:--;2"" " -

d7

,, ' 

# "8---''=-

-- --- - ASSUMED MOISTURE: 

## '1 ' Ie> PITOT TUBE COEFF , 

### C
- P

: -+ O -'-"'

. q-=q -:- · - - - - - -- -- PROBE ID NO/ MATERIAL:

..**:ll§~ Q""o,-,g** **,,--** 

## _ _ _ _ _ _ _ _ PROBE LENGTH: 

## 6 ' NOZZLE ID 

### NO I M · :-: A-=T=E""R:-"A :;>" L-:

## ·~**"'7r. ,,** **----- --**  NOZZLE DIAMETER:_ --,'CI\'fI I

c- ,"'

_ _ _ ____ __ _ FILTER NOITYPE : 

### . <v/ h PRE-TEST LEAK RATE: : 

## La
. DO"/' CFM@ \ 

## <; in. Hg

. POST-TEST LEAK RATE: "-' 0.)'2 

### CFM @ I 

# i i n . Hg

. PITOT LEAK CHECK
- PRE: ......- POST. , __ CHAIN OF CUSTODY : SAMPLE CUSTODIAN, -=o, "' (),'---

__ SAMPLER , )""-

## SAMPLEC~U~S**D~IA~N ~A~A** **--** t.H Stack Probe Filter Imp

. Out in

. H , O Temp , O F Temp , O F Temp , O F 

### Temp, 

### O F \ . 8 

## """\'DC:> 

# A ;I? Iv/ rv 

# bo


# ... ""...,...

1'0 \ 

### " 'c)D I ,'b 

# ,,'1 ""2- 'l'OO '\9>.() 

### '1.0 "- I " 

### L{ 

# '1''', S") 'l'q. 

## 'b



# - n y**~** 

## l- 

# tt '1 '6'" ,,><= < Q,I

VO \ 

### "'6 \

, . I I I 

# ..

- - -

_ .- -- .- '--

-- 

### Imp. 

### # Contents Post-Test - Pre-Test = Difference

__ I 1:- 

# 3 --.!i. (P , I/'; 

### H

## '6,t~ 

# "7 t l 

# J**JO;(, l2fL116** **I,, !...** __ _



## _ _ '_'

_ 70(;, 

# Fe 

# 765
__ /"' "\-

# 6G**~ ~1** **,** 

# Y 6,5 €-'i

__ qb 

# (-'! '15<f3

_ _ I,**~** 

## it! R i ' ,(' 

### ' J-i'

-- 

### (00

Total:

_ _ _ _______ _ __ _ Meter Temp , O F 

### Vacuum 0 , P

. static In Out in

. Hg

. 

### % in

. H , O )10 

## 1& 

# <= 

# n · ) -r 2- , ,
'87 

## 1
. 4 6 ' n**~O** 

## 1 25 

# ,,0

'80 

# 1S 

# '>.0

-- 

### Comments:

____________________________________________________________________________________________________________________ __

Date of last revision 

### 1 / 25 / 2013 Page

__ of

_ _ DS834049 Master Document Storage\FormslDatasheetslField Datasheets

### AMMONIA ELECTRODE CALIBRATION CURVE "ample "oom NH , concentration log NH , concentration Electrode potential Temperature Temperature**(~g** 

### NH ,I ml as N) (mV) (C) 

### (C) 1 0.000 89.4 21 21 5 0.699 53.4 21 21 20 1
. 301 18 .6 21 21 100 2.000 -21.7 21 21 Ammonia Electrode Calibration Curve y = -55
. 7371x + 

### 90.6621 2105 12 013 R' = 0
. 9992 

## 100
. 0 

# ;;- 80
. 0

# Eo; 

## 60.0 

# ., .: .$ 0 

## 40.0 0.. 

# .. 20
. 0 "C 0**~** 

## 0
. 0 ti

# ~OO 

# .. jjj 

## -20.B( 

## 00 0.500 1.000 1.500 -40.0 

## - logarithm of the concentration of ammonia (l1g NH,I ml as N) slope y-intercept
Concentration**(~g** 

### NH,I ml as N) 1 5 20 100 Calculation: 

### -5 5 .7371 90.6621
Value LR line 1
. 0535 4
.6616 19
.6288 103 .7362 Regression Line : P=M"log(l1g of NH ,t ml as N)+B 

### Difference 0.0535 -0
. 3384 -0
. 3712 3.7362

Measured Concentration of Ammonia (C) in**~g** 

### 1 ml NH , as N: C=10 (P.BV M 

### where P = electrode potential , M= slope (must be -57±3) and B= intercept 

### % Difference 5
. 3522 -6
. 7684 -1
. 8562 3
. 7362

All standards were prepared in 0.04N H 2 

### S0 4 

### and allowed to equilibrate to room temperature
. 

## 2
. 00AMMONIA BY ION SELECT IV E ELECTRODE ANALYSIS CALCULATION Cl ienU Location : Sample Location : Distr ict Method : Sample Date: Ana lysis Date ; Analyst's Initials : Calibration Curve : 

### R' Sample GEMMA Sentinel Unit 2 50% SCAQMO 207
. 1 211/2013 2 1

5 / 2013 

### RF y= -55 .7 371 x+ 90
. 6621 0
. 9992 

### P Cone . mV )..19 NH3/ml as N 26 ug NH3I ml as N 9.9 repeal 26 ug NH 3Im l as N 10

1·NH 3S0% 63.4 repeal 1- NH3 50% 63.6 2-NH3 50 % 64
. 5 repeat 2- NH3 50% 65.4

spike 2-NH3 50% 17.2

repeat sp ik e 17.4 Reagent Blank 151 .0 repeat ReaQent Blank 151.4 F ield Blank 115.4 repeat Fie ld Blank 114.9

0 1 H20 Blank 135
.6 Repeal 01 H20 Blank 136
. 1 26 NH3/m l as N 10
. 1 repeal 26 ug NH3Iml as N 9
. 9
Notes: Measured Concentrat ion of Ammonia (e) in f.l9 NH3 1 ml as N C=10 1 P
-S)l M 

### P 

## =electrode potential ( mV) , M=slope and B =i ntercept 26
. 116 26
. 002
1 .3 50 1.339 1.290 1.243 20
. 797 20
. 626 0
. 063 0
. 061 0
. 360 0
. 367 0
. 156 0.153 27
. 667 26.116

Average Measured Ammon ia Concentration (Cavg) = (C1 + C2)/2 where C1, C2 results from duplicate analyses (Jl9 NH3/ml as N) Cavg**(~g** NH,/ml as NH3) 

### = Cavg**(~g** NH31 ml as N) ·17
. 03/14.01 J.1 9 NH 3 I sample = Cavg (J..Ig NH 3/ml as NH 3 ) .. TV Used 100 ml of samples and standards with 2 mllSA and constant st i rr ing rate. Solution turned blue and rema i ned blue with ISA. CavgasN

26
. 060

1.344 1.266 20 .7 12 0.0620 0
. 3636 0.1546 26
. 002

Maximum samp les {i nc l ud i ng blanks} between 28 ug/ml check standard is 5 samp les and a spike ana lyzed in dup li cate . TV C avg as NH3**g** NH,I (ml) sample NA 34 .1 09 NA

410 1
. 634 669.960 500 1
. 539 769.669 NA 25
. 177 NA NA 0
. 1 00 NA 350 0
.442 NA NA 0.166 NA NA 34
. 036 NA

### AMMONIA BY ION SELECT IVE ELEC T RODE ANALYSIS QUA LI TY CONTROL ClienV Location: Sample Location: District Method: Sample Date: Analysis Date: Analyst's I nitials:
Sample 28 ug NH3 1 

### ml as N repeat 28 uq NH3/ml as N
1-NH350% reo eat 1- NH3 50% 2 - NH3 50% repeat 2- NH3 50% spike 2-NH3 50% repeat so ike Reagent Blank reoeat Reaoent Blank Field Blank repeat Field Blank

01 H 2 

### 0 Blank Repeat 0 1 H 2

### 0 Blank

28 NH3/ml as N repeat 28 Uq NH3/ml as N
N otes: 

### GEMMA Sentinel Unit 2 50% SCAQMD 207.1 2/1/20 1 3 2/5/2013 

### RF



### % recovery
NA

NA NA 1 01
. 24

NA NA NA NA
spike: 100 ml sample + 2 m l (1000**~g** 

### NH31 ml as N) Matrix Spike Percent Recovery (%R) %R 

### = (C spike'O.104
- Csample'O. 102)/2 

### '100 Cspike = 

### average result of matrix spike**(~g** 

### NH,I ml as N) RPD % 0.41

0.83 3.72 0.83 1.65 -2.07 2.07 -0.83 RPA % 0.214

NA NA NA NA NA NA 0.008

Relative Percent Difference (RPD) 

### = (C1-C2)1 

### Cavg '100 (must be 5% or less) Relative Perce nt Accuracy (RPA) (must be 10% or l ess) RPA = 

### (Cavg-theoretical value of standa rd)1 theoretical value of standard' 100

# 88118/1**IW ....,uy** **., Ince~**  

## AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS Project # : District Method: SCAQMD 207.1 Sample Date : 

# 2/ i /13 Client/Location: 

# G £ M M,4 Calibration Date: 

## 2 

# ;913 Analysis Date : 

# 7./ 4 / 1 

## 3 Sample Location :

# .s..nL;~ t./ 

# u 2. Calibration Curve : 

## It'

# -~. 

# 7;/ X ./Y6.U Z I Analyst's Initials : 

# R l' Test#'s: 

# 5D% R' : 

# 0.9972.. ' Sample Electrode TV Cone. Cavg 

### fig NH,I Commentsl Temp/pH Potential (ml) fig NH,- (fig NH, sample

(mV) 

## N/ml - N 

## 1 mil Standard Check: Percent Recovery: 28**~g** 

### NH,Iml 

# '1 ' 7**2f·I/~** Repeat 28 

## /0·0 

# 2f.cxn. J./i'.oto 

# /- 1./1/, '.5'0% 

# fs·'/ 1350 0 

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- S/./'/n**~J.t**

## ~Ib 

## 1.]19 

# 13'/'1 

# t(7
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## /"-"21<::..**,~** 

# H ·s 2 - 

# N 

# IIrst.Plp I. '- 90 

# l/{eAed 2,-)/(/,-50% 

# 55·"1 SOD /

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# S;t'J.(L J'f."1 2 D

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# Rl.t,. I: 

# R.

# ~ I

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# P.1w. k' 

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# Iff 2&'.002..
, Notes : Total 

## volume of samples and standards used: 100 ml Volume of pH adjusting ISA used in ml: 2 ml Absorbing solution: 0
. 1 N H2S04 Calculations : Conc

. (fig NH, - N 

## 1 ml) 

## = 10 (P·B )IM 

### P = electrode potential, B = y·intercept and M = slope Cavg 

### = average result of duplicate analyses (fig NH, - N 1 

### ml) 

### = (C1+C2)/2 

### fig NH,I sample 

## = Cavg* 

### 17
. 03/14

. 01 

## * TV mg 

### 1 sample 

## = fig Isample .,. 1000 ppm NH, 

## = mg NH,Isample x 1Nmstd x 1/454000 

### x SV/17 

### x 10· 

# Del/ab..

--- - - DS834059 Date of last revision 12/5/2008 

### Master Document Storage\Forms\Datasheets\ Lab FormsAMMONIA TEST RESULTS SUMMARY Client Gemma Pa ra meter location CPV Sentin e l Fuel Unit 2 Data By Test Number CPV Sentlnel -2-NH3-80-1 CPV Sentine l-2- NH3-80-2 Reference Temperature , F 60 60 Test Date 21 1 12013 21112013 Test Method SCAQMD 207
. 1 SCAQMD 207
. 1 Sample Train 9·P&M 9·P&M Meter Calibration Factor 0
. 992 0
. 992 Stack Area (s q 

### ttl 143 .1 4 143.14 Sample Time (Min) 60 60 Barometr ic Pressure (in Hg) 29
.69 29.69 Start T ime 9 : 10 11:05 Stop Time 10 : 34 12 : 15 Meter Volume (act) 44 .244 48 . 914 Meter Temperature ( F) 78
. 8 82
. 7 Meter Pressure (iwg) 1
. 90 2.10 Liquid Volume (ml) 92.6 111.8 Stack 02 (%) 13 .4 7 13
. 32 Stack NOx (ppm) @ 15% 02 2
. 2 7 2
. 16 Unit load MW 80 80 Fuel F low Rate , hscfh 6 , 912 6 , 936 Standard Samp le Volume (SCF) 42
. 226 46 .36 9 Moisture Fraction 0
. 093 0.101 Sta ck Flow Rate (dscfm, 60 of) 306,797 301,392 Stack Flow Rate idscfm , 70 oFi nJa nJa Gas Constant (ft-Ibfllb-mole-R) 1545
. 33 1545
. 33 Standard Pressure (lbflft2) 2116
. 224 2116
. 224 Molecular We ight NH3 (Ibllb-mole) 17 17 Specific Mo lar Vo l ume (ft3/1b-mole) 379.50 379
. 50 Mass Conversion (I b/ug) 2
. 20E·09 2
. 20E · 09 02 Correction Factor (%) 15 1 5 Mass NH3 (ug/sam p le) 1029. 45 1217.46 Mass NH3 (m g ) 1
. 029 1 . 217 Mass NH3 (Ib) 2
.27E·06 2
. 68E - 06 PPM NH3 (flue gas) 1
. 2 1
. 3 PPM NH3 @ 02 Correction 1
. 0 1 , 0 I blhr 0 .9 9 1
. 05 Ib/MMscf fuel 1.43 1
. 51
NH3 EQUATIONS : ppm NH3 = (m ass NH 3" Gas Canst" Ref Temp .. 106 )/(Sample vol." Press" MW) ppm NH3 @02correction=ppm·(20.9-02 Corr)/(20.9-%02) NH 3 natural gas M, SP , 55 , JM**A\ler~ge** Limit

13.39 2
. 22

1
. 2 1.0 5 1.02 1
. 4698

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### Page

__ 

# 1
__ of

__ 

# 1
__ DS834049 Master Document StoragelFormslDatasheetslField Datasheets

### AMMONIA ELECTRODE CALIBRATION CURVE Mmple Koom 

### NH3 concentration log NH , concentration Electrode potential Temperature Temperature**(~g** 

### NH ,I ml as N) (mV) (C) (C) 1 0
. 000 89.4 21 21 5 0.699 53.4 21 21 20 1.301 18
.6 21 21 100 2.000 -21.7 21 21 Ammonia Electrode Cal ibration Curve y = 

### - 55 .737 1x + 

### 90
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05/2013 R' = 

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# " 20
. 0 

# " 0**~ ~**  

## 0
. 0 

# "

# ~O**O** " iii 

## -20.8 00 0.500 1
. 000 1
. 500 -40
. 0 logarithm of the concentration of ammonia**(~g** 

### NH, 1 

### ml as N) slope y-intercept


### Concentration**~g** 

### NH ,I ml as N) 1 5 20 100 Calculation: -55
. 7371 90
. 6621
Value LR line 1
. 0535 4
. 6616 19
. 6288 103
. 7362 Regression Line :**P=M'log(~g** 

### of NH , I ml as N)+B 

### Difference 0
. 0535 -0
. 3384 -0.37 1 2 3
. 7362

Measured Concentration of Ammonia (C) 

### i n**~g** 

### 1 

### ml NH , as N : C=10 IP- BVM where P = 

### electrode potential , M= slope (must be - 57±3) and B= intercept 

### % Difference 5 .3 522 -6
. 7684 -1
. 8562 3
. 7362

All standards w ere prepared in 0.04N H2 

### S0 4 

### and allowed to equil i brate to room temperature
. 

## 2. 00AMMON I A BY ION SELECTIVE ELECTRODE ANALYSIS CALCU LATION ClienV Location : Sample Locat ion: D istrict Method : Sample Date : Analysis Date : Analyst's In itials : Calibrat ion Curve : 

### R' Sample GEMMA Sentinel Unit 2 75 % SCAQMD 207
. 1 211 / 2013 2 1

5 / 2013 

### RF y= -55
. 7371 

### x+ 90.6621 0
. 9992 

### p Cone . mV 119 NH 3/ ml as N

Notes: Measured Concentrat ion of Ammon i a 

### (C) in "'9 NH3 ! ml as N C=10 (p- a)lM 

### P = electrode potential (mV) , M=slope and B=intercept Average Measured Ammonia Concentration (Cavg) = (C1 + C2)/2 where C1 , C2 results from duplicate analyses ("'9 NH 3Jml as N) Cav9 ("9 NH,/ml as NH3 ) 

### = Cav9 ( " 9 NH31 m l as N)' 17
. 03/14

. 01 ).19 NH 3 Jsample = Cavg (11 9 NH 3/ml as NH J ) * TV Used 100 ml of samples and standards with 2 m l lSA and constant stirring rale . Solution turned b l ue and rema i ned blue with ISA. C avg as N

Maximum samp les (including blanks) between 28 ug/ ml check standard is 5 samples and a spike analyzed in duplicate . 

### C avg as

### AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS QUALITY CONTROL ClienU Location : Sample Locat ion : D istrict Method : Sample Date : Analysis Date: Analyst's Initials :
Samp l e 28 ug NH3 

## 1 ml as N repeat 28 ug NH3/ml as N
1-NH375 % repeat 1- NH3 75 % 2-NH3 75 % repeat 2- NH3 75 % spike 2-NH3 75% repeat spike Reagent Blank repeat ReaQent Blank Field Blank repeat Field Blank DI H 2 

### 0 Blank Repeat DI H 2 

### 0 Blank

28 NH3/ml as N repeat 28 ug NH3/ml as N
Notes: 

### GEMMA Sentinel Unit 2 75 % SCAQMD 207
. 1 

### 2/1/2013 2/5/2013 RF

% recovery
NA

NA NA 98.83

NA NA NA NA
spike : 100 ml sample 

## + 2 ml (1000 f!g NH3 1 ml as N) Matrix Spike Percent Recovery (%R) %R 

## = (C spike*0.1 04 - Csample*0.1 

### 02)/2 *100 

### Cspike 

## = average result of matrix spike (f!g NH,I ml as N) RPD % -0.83

-1
. 24 -3.72 0.00 1
. 65 -2
. 07 2
. 07 0.00 RPA % 0
. 008

NA NA NA NA NA NA 0
. 007

Relative Percent 

### Difference (RPD) 

## = (C1-C2)1 Cavg *100 (must be 5% or less) Relative Percent Accuracy (RPA) (must be 10 % or less) RPA 

## = (Cavg-theoret i cal value of standard)1 theoretical value of standard 

## * 100

# 8ella~**N<Qt..ooIiIy .**  __"'" 

## AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS Project # : District Method: SCAQMD 207
. 1 Sample Date : 

# 2./ ( /13 Client/Location : 

# G £ M 

## fl'11t Calibrat i on Date : 

# 2lfll3 Ana l ysis Date : 

# zL5/ 13 Sample Location :

# .s:u,L"~t.{ U 

## 2.. Calibration Curve :

# IP-~**.** 7J,IK-,1 96

. 

## U 21 Analyst's Initials: 

# R l' Test #'s :

# 7~ 

# % R' : 

# 0
. 991'2... I 

### Sample Electrode TV 

## Cone . Cavg**g** 

### NH 31 Commentsl 

### Temp/pH Potential (ml)**~g** 

### NH 3 - (fig NH 3 sample

(mV) N Iml 

### - N I 

### ml) Sta n dard Check : Percent Reco very : 2 8**~g** 

### NH ,t m l 

# /0
./ 27.'OH Repeat 28 

# 9 , 'j 

## 2 

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## LI!>·tj1o 

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# 7<f%

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# f. Ot> 

## L 

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### Notes : Total volume of samples and standards used : 100 ml Volume of pH adjusting ISA used in ml : 2 ml Absorbing so l ution : 0. 1 N H 2S04 Ca lc ulat ions : Conc

.**~g** 

### NH 3- N 

### I m l) 

## = 10 (P · 8 )IM 

### P 

# = e l ectrode potentia l , B 

# = y-intercept and M 

# = slope Cavg = 

### average result of duplicate analyses**(~g** 

### NH 3 - N 

### I ml) = 

### (C 1

### +C2 )/ 2**~g** 

### NH 31 sample 

## = Cavg* 

### 1 7. 03 1 14
. 01 * TV mg 

### I sample 

## =**g** 

### I samp le .,. 1 000 ppm NH 3 

## = mg NH ,tsamp l e x 1 Nmstd x 

### 1 / 454000 x SV/1 7 x 1 0 · 

# D

e/ta t:..**--** 

### Date of last revision 

### 12 /

5

/2 008 D88 34059 Master Docume n t Storage l Fo rms l Data s heets l Lab FormsAMMONIA TEST RESULTS SUMMARY
CPV
60 60

1 /30/20 13 1/3012013 SCAQMD 207
. 1 SCAQMD 207
. 1 9 - P&M 9·P&M 0 . 992 0 . 992 143 . 1 4 143 . 14

60 60
12 : 17 15 : 05 49 . 350 47 . 820 75 . 9 67 . 5 1 . 80 2 . 00 118.4 116 . 0 12 . 98 12 . 97 2.49 2
. 25 103 103 47 . 521 46 . 802 0 . 104 0 . 103 339 , 745 344 , 040
Pressu re ( lbf/ft2) 211S . 224 2116 . 224 Molecular We ight NH3 (t bllb - mole) 17 17 Specific Molar Volume (ft3/1b-mole) 379
. 50 379
. 50 Mass Conversion (fb/ug) 2
. 20E·09 2
. 20E · 09 02 Correction Factor (%) 15 15 Mass NH3 (ug/sample) 1 801 . 55 2082
.66 Mass NH3 (mg) 1 . 802 2 . 083 NH 3(l b ) 3.97E-OS 4
. 59E·06

NH3 EQUATIONS: ppm NH3 = (mass NH3* Gas Const'" Ref Te mp ... 10S )/(Sa mple vol. ... Press' MW) ppm NH3 @02correction= ppm'" (20 . 9-02 Corr)/(20 . 9-%02) 12.98 2 . 37

2
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Commenffi:

____________________________________________________________________________________________________________ __



### Date of last revision 

### 1/25/2 013 Page

__ of

__ DS834049 Master Document StoragelFormslDatasheetslField Datasheets

### AMMONIA ELECTRODE CALIBRATION CURVE :sample Koom NH J 

### concentration 

### log NH3 concentration Electrode potential Temperat u re Temperature**(~g** 

### NH3 1 m l as N) (mV) (C) (C) 1 0.000 89.4 21 21 5 0.699 53.4 21 21 20 1
. 301 18.6 21 21 100 2.000 -21
. 7 21 2 1 Ammonia Electrode Calibration Curve y 

## =-55.7371x + 

### 90.6621 210512013 R' 

## =0.9992 

## 1 00
. 0 

## S- 80.0

# ~En; 

## 60.0 

# '" t: 

## 2 40.0 0 Q.


# ..**~** <l> 

## 20.0 

# " 0 

# - 

# - 0.0 

# "

# ~oo " iii 

## -20.&' 00 0.500 1.000 1.500 -40.0 logarithm of the c o ncentration of ammonia**(~g** 

### NH31 ml 

### as N) slope y-intercept


### Concentration**(~g** 

### NH 31 ml as N) 1 5 20 100 Calculation: -55.7371 90
.6621
Value LR line 1.0535 4
. 6616 19.6288 103.7362 Regression Line:**P=M'log(~g** 

### of NH,t m l as N)+B Difference 

### 0.0535 -0.3384 -0.3712 3.7362

Measured Concentration of Ammonia (C) in**~g** 

### 1 m l NH3 as N: C=1**(P·B~M** 

### where P = electrode potential, M= slope (must be -57±3) and B= intercept 

### % Difference 

### 5.3522

- 6.7684 -1.8562 3
. 7362

All standards were prepared in 0.04N H 2 

### S0 4 

### and allowed to equilibrate to room temperature. 

## 2. 00AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS CALCULAT I ON ClienV Location: Sa mple Locat ion: Distr ict Method: Sample Date: Analys is Date: Analyst's Initials: Calibration Curve: 

### R' Sample GEMMA Sentinel Unit 2 100% SCAQMD 207.1 2/1/ 2 013 2/5/2013 RF y= -55.7371 x+ 90.6621 0.9992 

### P Conc. mV**~g** NH3/ml as N 28 ug NH3 / ml as N 10.0 repeat 28 ug NH3/ml as N 10

1-NH3100% 59.0 repeat 1- NH3100% 59.4**2~NH3** 100% 60.8 repeat 2- NH3 100% 60.9

spike 2- NH3 100% 1 5.1

repeat spike 1 5.1 Reagent Blank 151.0**re~eat** Re a qent Blank 151.4

Field Blank 115 .4 repeat Field Blank 11 4 .9

DI H20 B lank 135.6 Repeat DI H20 Blank 136.1 28 NH3/m l as N 10.3 repeat 28 ug NH3Iml as N 10.2
N ote s : Measured Concentration of Ammonia 

### (C) in ).19 NH3! ml as N C= 1O(P-S )IM 

### P = electrode potential (mV) , M=slope and B=intercept 28.002 28
. 002
3.699 3.638 3.434 3.420 22
. 682 22.682 0.083 0.081 0
. 360 0.367 0.156 0. 1 53 27.657 27
. 772

Average Measured Ammonia Concentration (Cavg) = (C1 + C2)/2 where C1, C2 results from duplicate analyses ().lg NH3/ml as N) Cavg**(~g** NH,Iml as NH3) = Cavg**(~g** NH31 ml as N)· 17.03/14.01 ).lg NH31 sample = Cavg (I-'g NHiml as NH 3 ) * TV Used 1 00 ml of samples and standards with 2 mllSA and constant stirring rate. Solution turned blue a nd remained blue with ISA. CavgasN

28.002

3.668 3.427 22.682 0.0820 0.3636 0.1546 27.714

Maximum samples (including blanks) between 28 ug/ml check standard is 5 samp l es a nd a spike a nalyzed in duplica te . TV C avg as NH3 ).19 NH31 (ml) sample NA 34.038 NA

404 4.459 1801
. 548 500 4.165 2082.655 NA 27.572 NA NA 0.100 NA 350 0.442 NA NA 0
. 188 NA NA 33.688 NA

### AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS QUALITY CONTROL ClienV Location: Sample Location: 

### District Method: Sample Date: Analysis Date : Analyst's Initials:
Sample 28 ug NH31 ml as N repeat 28 ug NH3/ml as N
1-NH3100% repeat 1- NH3 100% 2-NH3 100% repeat 2- NH3 10 0% spike 2-NH3 100% repeat spike Reagent Blank repeat ReaQent Blank Field Blank repeat Field Blank

01 

### H 2 

### 0 

### Blank Repeat 01 

### H2 

### 0 Blank

28 NH3/ml as N repeat 28 ug NH3/ml as N
Notes: 

### GEMMA Sentinel Unit 2 100% SCAQMD 207.1 2/1/2013 2/5/2013 

### RF



### % recovery
NA

NA NA 100.47

NA NA NA NA
spike: 100 ml sample 

### + 2 ml (1000**~g** 

### NH31 m l as N) Matrix Spike Percent Recovery (%R) %R 

### = (C spike'0.104 - Csample'O. 102)/2 

### '100 Cspike = 

### average result of matrix spike**(~g** 

### NH,I ml as N) RPD % 0.00

1.65 0.41 0.00 1.65 -2 .07 2.07

- 0.41 RPA % 0.007

NA NA NA NA NA NA -1.020

Relat ive Percent Difference (RPD) = 

### (C1-C2)1 

### Cavg '100 (must be 5% or less) Relative Percent Accuracy (RPA) (must be 10% or less) RPA = 

### (Cavg-theoretical value of standard)1 theoretical value of standard' 100

## AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS Project # : D i strict Method: SCAQMD 207.1 Sample Date : 

# 21 1/13 

### Client/Location ' 

# G 

# £ M fI"!;4 Calibration Date ' 

# 2/5113 Analysis Date : 

# 7.15113 Sample Location

.

# .s..nt"~<.1 

# u Z. Calibration Curve : I/.:.-SS. 73,1 K-,I<j6.U 21 Analyst's Initials : 

# R"- Test#'s :_ -<-J",o-=o:....%'-!p",-

__ R2: O. 

# 7 91 2... I 

### Sample Electrode 

## TV Cone. Cavg fI9 NH31 

## Commentsl Temp/pH Potentia l (m l) fIg NH 3 - {fI9 NH 3 samp le

(mV) N/ml - N 1 

### mil Standard Check : Percent Recovery: 28**~g** 

### NH,iml 

# /6·0 U.6C>2.. Repeat 28 /{),C; 

## Zf.oo2..**~** 

# f.(jo2,**/-/JI/~ -Ivc>~~**  S"(·O 

## 3
. (.."}'1**~t** 

# I·NtI, -I(>O/r- 5'1. (I 

# L/o", 3**.f..~f-** 

# 3 

# · CoU· /,fc>I.S 

# Ill/'/' 2.. 

# T.:: 

# '2I>CC 2 - 

# IV 

# 11,- locI. 

# W·F ? 

# ·1 jJ.f 

# Re./Jed 2· 

# J/ fI, -I 

# oc!!, &0·9 

# SOD 3. «( 

## 20 

# 3 .1{2.1 2i!>f2
. C, 

# ,>I/.c: 2 

# T=.2I"cC"l". 

# 2.JlI/, -Ioo/. 15
. / 

# ntn Re Aet;{ 5P,'WL 

# / .$./ ZZ · Cf2. 2,2
.(;f2.. 

## D. UL/ 

# /60%

# Re:..~i R/r;..r.K 

# I S/
. O 

# 6.of? , 

# R**(..-j~G** C 

# R. IS 

# /S/,4**t).o~1** 

## D. 6**~'2.0** 

# Ft'elci 

# n.ic.v.. K 

## I{S. 

# L( 0,3(..0 

# IAII SolvilDrlS 

# l<<./lR&t Ff.? /11.[. " 0 , 3(,1 

# (')·3f,3? 

# LedecJ c..t iJl /../, is 

## f?1v.-. t 

## /'3,5. (, 6./5(, 

## 2. I 0 

### C 

# Re.;'Je.d IJII/ L 

# o.6/J< 

# !?I.-, ( 0./&1 f). 

# WIt 2. of 

# Nil

... /b.3 2 ':J. 

## t.S'l

# R.fl.;.€4/; 2N/J./, 

# 1°.1. 27. 

# Ttl. 

# 2t-. T I I.f Notes : Total volume of samples and standards used : 100 m l Volume of pH adjust in g ISA used in ml : 2 ml Absorbing solution : 0.1 N H2S04 Calculations : Conc. (fIg NH3 - N 1 

### ml) 

## = 10 (P,SlIM 

### P 

# =electrode potential

. B 

# = y-intercept and M 

# =slope Cavg 

# =average result of duplicate analyses (fIg NH3 - N 

## 1 m il 

# = {C1+C2)/2 fIg NH31 sample 

## = Cavg* 17
. 03/14 .0 1 * TV mg 

## 1 sample 

## = fIg Isample

... 1000 ppm NH3 

# = mg NH "Is ample x 1Nmstd x 1/454000 x SV/17 x 10 6 

# De/tab. 

# "'_

......... 

# ,- Date of last revision 12/5/2008 D8834059 Master Document StoragelFormslDatasheetslLab Forms

## Appendix C.4 SOx by 

## SCAQMD Method 307.91

R0410673 

## C-8

# De/ta**~** 

# ..

# _ ....... , 

### ...

# -

### Parameter

SOx 

### Units Ib/MMBtu Ib/MMscf grH2S/100se! Max Result 0.00003

0.034 0
. 013 Limit Rule 0.06 40 CFR 60 0.67 Rule 2011 0
.25 SCAQMD Permit 861.1Sentinel 2 Fuel A nalysis and Sulfur Cales Sulfur
Client Facility Unit Gemma CPV Sentinel 

### 2 CPV Se nti nel-2-Fuel-1 &2 HH V Fue l Sulfur Content, (BTU/ft3 MW MW ppm v @60F) (H2S) (S02) Result 0.20 1014.3 34
. 00 64
. 00 Limit

Reference gr/100 scI 

### = ppmv lue1 /10 ·6 x MW ( H2S)/SV x gr /lb x 100 Ib/ 10 ·6 set 

### = ppmv lu e1/1 0·6 x MW ( H2S)/SV x 10 ·6 Ib-S02lMMBtu = ppm**lue ~1**  0·6 x MW (S02)/SVlH H V x 10 ·6 (S pec ific Molar VoJ ume@

60F ) 379.5 gr /l b 7 ,00 0 gr-H2S/100 scI 0.013 0 , 25 SCAQMD

Perm it, B61.1 IbsH2S/MMsel

0.018 0 , 690
Rule 2011 IbS02/MMBtu

0.00003

0 .06
40 CFR 60

2/1412013

3 :3 7 PM

### Client 

### Facility Unit



### Load , MW

101.0 Gemma 

### CPV Sentinel 

### 2

Fue l Sulfur Content , ppm 1 

### 0 .20 Sentinel 2 Fuel Analysis and Sulfur Calcs SOx

CPV Sentinel-2-Fuel-1&2 

### Specific

Molar Volume Stack

(SV) , Flow Rate Fuel Flow dscf/lb- (Qsd19), Rate,

mol dscfm hscf /h 02 Ib/hr , S02 379.5 362 ,5 15 8319.3 13.13 0
. 02806 S02 Ib/hr = 

### (sulfur ppmv)/1 0'6 x (MW S02)/SV 

### x hscf/hr x 100 scf /hscf ppm S02 

### = Ib/hrx SV/MW x 1/Qsd19 x 

### 10'6160 Stack flow rate, fuel flow and 02 in conjuction with PM tests at 100% load condition ppmv@ ppmv 15% 02 0.008 0.006 S02 ,Ib/MMscfFuel 0.034



### 2/14/2013

3 : 44 PM

### Client Facility

Unit



## Carbons

1 2 2 3 3 4 4 4 4 4 4 4 5 5 6 Gemma CPV Sentinel 

### 2



## Compound Hydrogen Carbon Dioxide Carbon Monoxide Nitrogen OXVQen Methane Ethylene Ethane Propane Propylene Isobutane n - Butane 1-Butene Isobutylene t-2-Butene c-2-Butene 1,3-Butadiene Isopentane n-Pentane HexanesPlus Compound Total Reduced Sulfur FUEL F-FACTOR CALCULATIONS

CPV Sentinel-2-Fuel-1&2 

## 1 2 Average detect? MOLE 

## % detect? MOLE 

## % detect? 

# I MOLE 

## % < 

## 0 , 001 < 

## 0 , 001 < 

## 0 , 001 0 , 538 0 ,555 0 ,5 47 < 

## 0 , 001 < 

## 0 ,0 01 < 

## 0 , 001 4 , 778 2,475 3 , 627 0 ,037 0 , 015 0 , 026 89 , 675 91 , 836 90,756 < 

## 0 , 001 < 

## 0,001 < 

## 0 , 001 4
. 360 4,481 4,421 0,480 0,494 OA87 < 

## 0
. 001 < 

## 0.001 < 

## 0 , 001 0
. 034 0 , 036 0 ,035 0 , 057 0
. 058 0 , 058 < 

## 0
. 001 < 

## 0 , 001 < 

## 0 ,001 < 

## 0
. 001 < 

## 0 ,001 < 

## 0 , 001 < 

## 0
. 001 < 

## 0.001 < 

## 0.001 < 

## 0,001 < 

## 0
. 001 < 

## 0 , 001 < 

## 0
. 001 < 

## 0 , 001 < 

## 0 , 001 0 ,012 0 , 013 0 , 013 0 ,009 0 , 014 0
. 012 0 , 020 0 , 022 0 , 021 detect? ppm detect? ppm detect? ppm 0 , 2 0 , 2 0 , 20

## FUEL F-FACTOR CALCULATIONS C l ient Gemma Unit 

## 2 Facility CPV Sentinel CPV Sentinel-2-Fuel-1&2 SPECIES MW MOLE% MW*% HHV BTUlSCF 

## C 

## H 

## 0 CO 2 

## 44 0
. 547 24
. 05 0
. 07 0.00 0.17 CO 

## 28 0
. 001 0.03 3210 0.003 0.00 0
. 00 0
. 00 N 2 

## 28 3
. 627 101
. 59 0
. 00 000 000 O 2 

## 32 0
. 026 0.83 0.00 0.00 0
. 01 C 1 

## 16 90
. 756 1456.0 1012
. 0 91845 10.89 3
. 63 0.00 C 2 

## 30 4422 132.95 1773
. 0 78
. 39 106 0
. 27 000 C 3 

## 44 0488 21
. 52 2524
. 0 12
. 32 0
. 18 0
. 04 000 C4 

## 58 0.098 5.66 32710 3.19 0
. 05 0
. 01 0
. 00 C 

## s 72 0.024 1.73 3998
. 0 0
. 96 0
. 01 0.00 0
. 00 C 

## s + 

## 86 0
. 021 1
. 81 4743
. 0 1
. 00 0
. 02 000 0
. 00 Ave. / Total 100
. 01 1619
. 63 1014
. 30 12
. 20 3
. 95 0
. 00 Weight, % 

## 99.74 75
. 35 24
. 39 0
. 00

GasMW 16
. 20 Btu/set= 1014 @60F Btu/set= 1030 @68F Btu/lb.= 23,766 Ib.lscf= 0.0427 Fd"(60)= 8 , 456 (0 2 

## Based) Fd"(68)= 8 , 586 Fc"(60)= 1 , 002 CO 2 

## Based) Fc"(68)= 1 ,018
Calcula t ions: Fd"(68) = 10'6 * 

## [3

. 64 * 

## (H%) 

## + 1
. 53 * 

## (C%) 

## + 0.14 * 

## (N%) - 

## 046 * 

## (0%)]/ HHV , 

## Btu/lb Fd"(60) = Fd"(68) * 520 R / 528 R FC"(68) = 10'6 * 

## [0

. 321 * (C%)]/ HHV, 

## Btu/lb Fc"(60) = Fc"(68) * 520 R / 528 R N 000 0
. 00 1.02 0
. 00 0
. 00 000 0.00 0
. 00 0.00 0.00 0
. 00 0
. 00

### Sentinel 2 Fuel Analysis and Sulfur Cales F-Summary Client Facility Unit 

### Gemma CPV 

### Sentinel 2 CPV Sentinel-2 - Fuel-1&2 Gas MW 16.20 

### Btu/scf= 1 , 014 

### Btu/scf= 1 , 030 

### Btu/lb.= 23 , 766 

### Ib.lscf= 0
. 04268 

### Fd"(60)= 8,456 

### Fd"(68)= 8 , 586 

### Fc"(60)= 1 , 002 

### Fc"(68)= 1 , 018



## 2/14/2013 3:32 

## PM

## Parameter Method No. Method Title 

## Fixed Gases ASTM D1945/1946 Analysis of Natural Gas/Reformed Gas by Gas Chromatography HHV ASTM D3588 Calculating Heat Value, Compressibility Factor , and Relative Density of Gaseous Fuels Sulfur ASTM D5504/SCAQMD METHOD 307-91 Determination of Sulfur Compounds in Natural Gas and Gaseous Fuels by Gas Chromatography and ChemiluminescencelDetermination of Sulfur In A Gaseous Matrix

## Appendix C.5 ROG by Modified SCAQMD Method 25 . 3

R0410673 C-g

### Client/Location Gemma CPV Sentinel Unit 

### 2 Sample Location Sta c k Test No

. S- 2/STK
- R O G -50- 1A Date 2/ 1i 20 1 3 

### Test Method Modified SCAOMD 25.3 Sample Time (HH:MM) 1 : 15 Start Time 14:20 Stop Time 15 : 35 Stack O 2 

### (%) 14
. 38 Results Canister NMNEOC (ppm) 0 .79 ROG, ppm' 0 .7 9 ROG, ppm @15% O2 

### 0 .7 1 RPD 2
, 

### % 

# - 1) Includes bias correction of 1.086 2) Relative percent difference less than 20% 3) Samples were collected simultaneously as a pair Results at PQL level Reference Temp (F) 60 Data By AA , SP , SS , JM

S- 2/ST K-R OG
- 50 - 1 B Average 2/1/2013 

### Modified SCAOMD 25.3 1 : 15 14 :20 15 : 35 14
. 38
0
. 72 0
. 72 0
. 76 0.65 0
. 68



# - 4
. 6%

### Client/Location Gemma CPV Sentinel Unit 

## 2 Sample Location Stac k Test No. S- 2/ST K - ROG
- 15-1A Date 2/ 1 1 2 01 3 

### Test Method Modified SCAOMD 

## 25.3 Sample Time (HH:MM) 

## 124 Start Time 

## 9:10 Stop Time 

## 10:34 Stack O 2 

### (%) 

## 13.47 Results Canister NMNEOC (ppm) 

## 0
. 68 ROG, ppm' 

## 0.68 ROG, ppm@15%0 2 

## 0.54 RPD 2
, 

### %


# - 1) Includes bias correction of 1.086 2) Relative percent difference less than 20% 3) Samples were collected simultaneously as a pair Results at PQL level Reference Temp (F) 

## 60 Data By AA, SP, SS, JM

S-2/STK-ROG-75-1 B Average 2/1/2013 

### Modified SCAOMD 

## 25.3 1:24 9:10 10:34 13.47
0.70 0.70 0.69 0.56 0.55



# - 1.4%

### Client/Location Gemma CPV Sentinel Unit 2 Sample Location Stac k Test No. S -2 /STK-RO G
- 100 - 1A Date 1/30/2 0 13 

### Test Method Modified SCAQMD 25.3 Sample Time (HH:MM) 1 :09 Start Time 11 : 01 Stop Time 1210 Stack O 2 

### (%) 12
. 98 Results Canister NMNEOC (ppm) 1.01 ROG, ppm' 101 ROG, ppm@ 15% O2 

### 0
. 75 RPD 2
, 

### %

- 

### 1) Includes bias correction of 1.086 2) Relative percent difference less than 20% 3) Samples were collected simultaneously as a pair Run 2 at PQL level Reference Temp (F) 60 Data By AA, SP , SS, JM

S- 2/STK-ROG
- 100- 1 B Average

1/30/2013 

### Modified SCAQMD 25
. 3 1 :09 11 :01 12 : 10 12
. 98
0.62 0.62 0.82 0.46 0
. 61



# - 23
. 9%

## Client/Facility : Unit/Location: 

## SCAQMD METH O D 25.3 EVACUATED CANISTER SAMPLING DATA (],,;- rq /'{ 

## i T Date : 

# CJ-// / 

# 0**--~~ i~~,L-~** **--------------** (It!, 

## f Z

. 

## 'S f; , /'/ ; ,4- Performed By:

___ 

# 7.<..) '"--
______________ Probe Material

_________ "" "- >



## _ 5 '----

_______ Probe Length

__ 

# ---"'

6

=-______________ Connecting Tubing Material,

__ 

## -L:t-Ic... >A

______Connecting Tu b ing Length

__ ..::: lJ::......:4
______ _ 

## Barometric P ressu re

____ 

## ..:; 2. ..::."

.........,

· (o

=..

5-"

. '--

____ . Ambie nt Tempe rature
____ 

## l .!..."2 .::.;::.. b
______ _ Test No

. 

## s"-;2.
- s (I<.

.**~G-** 

### > , '

_

I e S - 2 ·· · s//-<; -R'ft;;:JiI- 

### 1:5 

## V iaii D 

# Nt\- __Alrt

## Canister 

## ID 

# '5 5 2--- 

# <-/5 

# '3 Time Vacuum Time Vacuu m Time Vacuu m Pre-Test Leak Start (01 2,/ /r:;2- C/ 

# 2'7 

# / Check 

# ;2'0 P re- T est Leak Stop 

# ; (/ j{ 

# '2 5 I,)] 

# V 

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# / Collect io n 

## b;,.l 

# ;;1.1" " 

# f**\~.'ZD** 

# \ Lj2-0 

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# I S i 

## --I. 

## '3, 

# ''I 2 

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## Collection P ost -Test Leak Start 

# " I(;./u 

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# i6:2c.J ,/ 

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/ 

## Line Rinse 

# ./ /" 

# /**~** 

# / Volume Comments:

__________________________________________________ _ 

# Dellaf).

... <>.oIdy ...... . . . .......... ... 

## Date of last revision 1 1/1 3/08 

## DS834043 Master Document StoragelFormslDatasheetslField Datasheets

## SCAQMD METHOD 25.3 EVACUATED CANISTER SAMPLING DATA ClientlFacility :

_ C::

_ :'1

_

O'

_

YlI

_ M

_ f'>.

_______ Oate: 

# :;:t[ \ \ 

# 13 S 0'J 'W' t:>J.-- 

### UnitlLocation : 

## U"-'I 'l. - 

### W I SWJifi''Y 

### Performed By:

__**s£'== ,--**  

## ______ _ Probe Material

___ 

## .:: S -'-

"'

______ Probe Length

# _----'-'**4s=---'~u ·**  '

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_

A-

____ Connecting Tubing Length,

__ N4

_'
___ _ 

### Barometric pressure--'= L=

1"'

. _

h

_ 1 .l.-

____ ,Ambient Temperature

__ 

## l '-

'1

'-

o ____ _ Test No.**S-;). 5\¥-'1>~** **i"** 

### <;'-2/s""-1 

## S .**~O<;rlb** 

### Vial 

## 10 t-l/(.>, 

## rJ IA 

# L Canister 

## 10 000 '3 

### 2-0 

## <7vO 

## sst) 

# I Time Vacuum Time Vacuum Time Vacjuum Pre-Test Leak Start OCZ06 

## 30" 

# DlDO 30'i Check Pre-Test Leak Stop**o~** tD 

## 3D 1\ 

# 01 1 

# 0 

# )0" Check Sample Start 4J 

# ){)V 

# '3()**~** 

### Collection 

# OliO 

# 6110 

# I 

# tJ U"\ 'J.l 

# 'J. S II

## C)~ 

# :n ;2 

# S" 

# I I**~<X1't~** 

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# " \. i OA. . w' I 

### , 

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# I Sample Stop 

# (03'-{ 

# LO lO3'1 

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## I{J...O(} I,) 

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## / d Uc) 

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## /')-./0 

# 10 /2../U 

# /0 

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# I Line Rinse 

# ;/ 

# /' / 

# /' 

# I Volume Comments : _________________________ _

Date of last revision 11/13/08 DS834043 Master Document Storage l Forms l DatasheetslField Datasheets

## SCAQMD METHOD 

## 25
. 3 EVACUATED CANISTER SAMPLING DATA Client/Facility :

# ivL~ <"--q < 

## Date : 

# (-,3 (). /3. Unit/Location :

# X 1/ 

# h,'.<,
.... . / IA " ,' j 

# i 2 Performed By:_.::: S:....:

5 =--

______ _ L'" 

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_ ______ Probe Length _""--" '0'---

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f'r

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# "J-y, 8 0 Ambient Temperature_.!.. 7

.:. o

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____ _ 

## Test No ,**.:5~** 

## J./('- a.'C_ " tO{)-,)f 

# 6,**~J6** '(1"

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## Vial 

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# S 11 

# «Joo 5.31 Time Vac u um Time Vacuum Time Vacuu m Pre - T est Leak Start

# IOf!)~ 

# set ' ).ti,3 

# t' Check 

# 1\0010 Pre-Test Leak Stop 

# 10 I (; 

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# NA- 

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## Comments :

_____ __________ _ ________ _ 

# Della;)..
Al< 0u0I. ........... . _ 

### Date of last revision 11 /13/08 DS834043 Master Document StoragelForms l DatasheetslField Datasheets 

# II

## SCAQMD METHOD 25.3 EVACUATED CANISTER SAMPLING DATA 

## Client/Facility :**tye~** /h-<<- 

## Date : 

# I - 3 /- 

## {-?, Unit/Location: 

# 6.e,zt (4/" 

# I U**i;)...** Performed By : --< ;[;z:.L£I --'--

_____ _ Probe Material

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## Connecting Tubing Length ' I

# Barometri**~essure** :H

. {.:( Ambient Temperature 

# /;
. S' / Test No, 

# \ .5

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# 5 - ;}./:'
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## Vial 

## 10 

# \ / Canister 

## 10 

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## 0

# 00 

# '"10 

# \ Time Vacuum Time VVacuum Time Vacuum Pre-Test Leak Sta\ 

## •• 

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## tJ?1t{J
_ .:J-.C( , J- 

### "j. 

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# ~'i}... 

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# d-1. }. " Sample Start

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# /«

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# vet Dellai1

...

# _-,- Date of last revision 11 /13 / 08 

## DS834043 Master Document StoragelForms l Datasheets lF ield Datasheets

# Atmospheric Analys i s & 

# Consulting, Inc.

CLIENT PROJECT NAME AAC PROJECT NO. REPORT DATE Delta Air Quality Services , Inc. Gemma, Sentinel Unit 2 130122 21712013 

## On February 5, 2013, Atmospheric Analysis & 

## Consulting, Inc. received six (6) Six-Liter Summa Canisters for TNMNEOC analysis by SCAQMD 25.3 Modified and Fixed Gases analysis by EPA 3C. Upon receipt the samples were assigned unique Laboratory ID numbers as follows: Client ID Lab No
. Initial 

## Pressure (mmHg) S2/ Stk-VOC-IOO-IA 130122-60797 453.1 S2/ Stk- VOC-I 00-1 B 130122-60798 4 79.1 S2/Stk- VOC-50-IA 130122-60799 376
. 9 S2/Stk-VOC-50-1B 130122-60800 416.0 S2/ Stk-VOC-75-IA 130122-60801 434.0 S2/ Stk-VOC-75-IB 130122-60802 421.4 Upon receipt at the laboratory, the initial vacuum was recorded and the canister was pres s urized to 900 mmHg using dry UHP Helium
. The PQL for this modified method was e stablished at 0.10 ppm V (as Propane) as dictated by the lowest point in the calibration curve. All results were detected below thi s level and therefore reported as <PQL. Canister numbers from the Chain of Custody did not match those on the sample ID tags for samples 60797-60802. The correct canister numbers were ascribed onto the original COC according to "Test # ." I certit'y that this data is technically accurate, complete and in compliance with the terms and conditions of th e contract. Release of the data contained in this hardcopy data package has been authorized by the Laboratory Director or his designee , as verified by the following signature.
. If you have any questions or require an explanation of your data result s, plea se contact the undersigned
. 

# 9/4. 

# b
J 

## Marcus

# Huep~**?** Laboratory Director
This report consists of 

# 41 pages.



# Page 1

1534 Eastman Ave., Ste

. A • Ven t ura , • CA 93003 

# @ www.aaclab.com. (805 ) 650 -1 642 • FAX (805) 650 - 1644

# ® lAce Atmospheric Analysis & 

### Consulting, Inc , 

# SAMPLE RECEIPT / LOG-IN REPORT AAC 

## Project 130122 Received By:
. 

### J. Zachman Sample Pro 

### ieet Desc 

### Clients ID Matrix Sampling Sampled 

### By Sample 

### # Receipt Date 

### Date/Time



### 215 1 2013 Delta Air Quality S2 1Stk

- VOC-I 00 Summa 

### 1 1 30 1 2013 Client 60797 1045 -IA Canister Gemma, Sentine l Unit 2 2 1512013 Delta Air Quality S2 1Stk- VOC-I 00 Summa 1 1 3012013 Client 60798 1045 -IB 

### Canister Gemma, Sentinel Unit 2 2 1512013 Delta Air Quality S2/ Stk-VOC-50- Summa 

### 2 1 1 1 2013 Client 60799 1045 IA 

### Cani ster Gemma , Sentinel Uni t 2 2 15 12013 Delta Air Quality S2 IStk-VOC-50- 

### Summa 2 1 11 2013 Client 60800 1045 IB 

### Cani ster Gemma, Sentinel Unit 2 21512013 Delta Air Qua lity S21Stk- VOC-75

- Summa 2 1 112013 Client 60801

1045 IA Ca nister 

### Gemma, Sentine l Unit 2 2 15 1 2013 Delta Air Quality S2 1Stk- VOC- 75

- Summa 21112013 Client 60802 1045 IB 

### Canister Gemma , Sentinel Unit 2

TURN AROUND TIME: Normal (I0day s)

Lab Due Date : 2112 1 2013 Total Samples: REMARKS: Client returned 7 

## x Summa canisters 

## + 7 

## x Flows. Canister numbers did not match from the COC to the sample 

### ID tags for sample s 60797-60802. The correct canister numbers were ascribed onto the orig inal COC according to TEST #.



# Page 2 Analysis Requested 

### SCAQMD 25.3M

SCAQMD 25.3M

SCAQMD 253M

SCAQMD 253M

SCAQMD 25.3M

SCAQMD 25.3M



### 6

### Client: Date : Delta A i r Quality 

### 2/

5

/ 2013

Canister # 

## 531 517 382 483 520 55 8 

# Atmospheric Analysis & 

# Consu lting, Inc

CANISTER PRESSURE LOG Proj e ct No .: 

## 1 3 0122

Samp l e # 

### In it i a l P ressure Fina l Pressure



## 60797 453
. 1 907.7 60798 479
. 1 908
.0 60799 376.9 908.6 60800 416
. 0 913
. 0 60801 434
.0 906 .7 60802 421.4 907
. 1

1



# Page 3

### ~07f7

### "07~ 

## &it) 

## 7'1' 

# to ()7oD 

## fl." rtr> ( 

# tof) 11":' 

# A l elF (30 I 

# t- 'l--
CHAIN OF CUSTODY CliENT : Sentinel

# r~Mt TEST DATE (S) : 1 13012013 2/1 / 2013 LOCATION : ______**~2**______________________________________________________________ _ SAMPLER(S): RM SAMPLE LOCATION :**~S~~~**________________________________________________________________ ___ PR OJ ECT MANAGER : 8F '<t Q) DATE DUE : 219/2013 OJ) oj TEST METHOD(S) : ______ --"S"'C"AQ"M=D.=2"'5

. "-3

____________________________________________________ ___ OUTSIDE LA8 REQUIRED? : -'Y"es"-

__________________________________________________________ _ COMPliANCE TEST?**~** Yes • 0 1130/2013**S21S~·VOC·1** 00-1A SCAQMD 25
. 3**Canister~** s-3; 1 RM 1 / 3012013**21 S~** **·V OC·** **1** 00-18 SCAQMD 25
.3 Can ister M9ia4 S", 1 RM 2/1 / 2013**S21S~·VOC·50·1A** SCAQMD 25
. 3**Canlster~** '3 2- 1 RM 2/1

/2013 S2IStk·VOC ·50·1 B SCAQMD 25
. 3 Canister #QQ866fI 

# ,. 1 RM 21112013 S21Slk·VOC·75·1A SCAQMD 25 .3 Canister #9Qi3&2**~-L** 0 1 RM 211/2013 S21S lk-VOC·75-1 8 SCAQMD 25.3**Can ster~**  

### .s-s-8 1 R M 

### n.**u~h** 

### ..

ala ampes eagent Keagent Lot #'S : I**~** ,-------------------"RE"'L-oEA=SE"'D"B"'y,----------
- -- ----,---**--~** ------**~---** "RECEIVED gy-- - -, --DATE/TIME

_ . m o m . - - - m ?.. - 70 / ' "

# ~**~-'J ~i4**  

# I 

# r9k:jg; 6**~~** 

# [777&ti7f:F¥kl!!
.**"/~;**

# ..**~** 

# I 1;:; /3**;:;~** 

# . Note : Canister #000403 and #000 4 11 WCIt: VU I Ut;:\j**It:;,~.** rlCdl3C UU I I UI Cl I IGIY'C . - <./

# A

# Results

Page 5

# Atmospheric Analysis & 

# Consulting, Inc.

CLIENT PROJECT NO. MATRIX UNITS



### Client 10 : Delta Air Quality Services, Inc. : 130122

Air : ppm C

Lab 10 

### # Tank Vol 

### Liters

as per 

# LABORATORY ANALYSIS REPORT

SCAQMD 

# 25.3 Modified Initial Pressure

mmHg(p;) 

### Return Pressure Final 

### Pressure

PQL:: 0.10 ppm 

### V Propane x 3.0 (carbon conversion) x Tank Dilution Factor x 1.086 (correction factor) 

# EPA3C PQL: 0 .1 

### % 

### An,lvte Client 10 Lab 10# 

### Oxygen CO S2/Stk-VOC-IOO-IA 130122-60797 13.0 <PQL S2IStk-VOC-IOO-I B**130122~0798** 12 .9 <PQL S2IStk-VOC-50-IA**130122~0799** 14
. 1 <PQL S2lStk- VOC-50-1 B 130122-60800 14
. 2 <PQL I S2IStk-VOC-75-IA 130122-60801 13.2 <PQL

S2IStk-VOC-75-IB 130122-60802 13
.2 <POL 

### Fixed Gases have been normalized to 100% on a dry 

### weight basis Tank Dil 

### Factor

CO2

5.9 6.1 5
. 3 5.2 6.1 6
.0 SAMPLING DATE : 01/30 , 02/0112013 RECEIVING DATE: 02/05/2013 ANALYSIS DATE : 0210612013 REPORT DATE : 0210712013

Total 

### NMNEOC' PQL

# ~d_~~ MarcusHuep!fe 7
. 

### Laboratory Director



### Page 6 1534 Eastman Ave., Ste. A • Ventura, • CA 93003 

# * (805) 650-1642 • FAX (805) 650-1644 • www.aaclab.com

# Method 25.3 Modified Calculation Summary Sheet TNMNEOC

- CTCA 

# x 

# DF Tank X 

# 3.0 x 

# 1.086
Where: 

## lNMNEOC = 

## Gaseous concentration of Source, ppmV (as Carbon) CTCA 

# = Average of analysis results from chromatograms, ppmv (as Propane) DFTank = 

## Dilution factor resulting from tank pressurization upon receipt 

## (PdP,) 3.0 = 

## Conversion of result (as Propane) to (as Carbon) Per method section 

# 4.11, the 

# fmal concentration includes a 

# 1.086 bias correction factor. Where: 

# Pr= Final canister pressure after pressurization for analysis ifrom Sample Receiving Data Sheet) 

# p, = 

## Return canister pressure upon sample receipt (from Sample Receiving Data Sheet)



## Page 7

# QA/QC 

# Summary

Page 8

# Atmospheric Analysis & 

# Consulting, Inc.

Quality Control/Quality Assurance R epor t


# I Date A nalyzed Analyst**Unit.~** 

### : 02/0612013 

### :ZG 

### : 0/0 I**~** 

### ODeniru!. Continuine: Calibration Verificatio n - SeA 

### AACID 

# I Analyte 

# I 0 , Spike Cone 5. 18 CCV 

### Result 5.0 4 % 

### Rcc-"" 97.4 5
. 3 

### 0, Concentra tion 

### NO MD 

### 25 .1 25.3 

## N, 14.4 

### 15.78 109.5 

## N, NO III-Labora tory Control Spike & Du licate - SCAQMD 25 .1,25 .3 

### AACID Analyte 

## N, Sa mple Con e 0.0 Spike C one 14.4 

### LCS Result 15
.2 La b Co ntrol 

### LCSD Result 14.6



### Standards 

### LeS % 

### Rec P 

### 105.3 

### LCSD % R ec" 101.4 

### % RPD· ... 3.8 IV-S ample & 

### Sample Duplieate

- SCAQMD 25.1,25.3 AACID Analyte 

## 0, S ampl e 6.3 SampleD up 6.3 130122-60797 Mean 6.3 

### %RPD 

### "'*" 0.5 V -Matrix Spike & Duplica te - SCA( 

### MD25.125
.3 AACID Analyte 

## N, SampleConc 19.7 Spi ke Co n e 9.2 MS Result 29.7 130122 -60797 MSD Remit 29.9 

### MS % 

### R ee""" 108.3 

### MSD % 

### Rec """" 110.0



### % 

### RPD 

### .** 1.5 VI -**Clos~ Continuin~**  Calibration Verification - SeA 

### AACID

CCV

• Must b e 85-115 % •• MUl1 be 7 5-1 2 5%

... Must be < 25 % ND - No t Detected 

### Analyte Spik e Cone 

### R es ult 0 / 0 Rec 11"

<,R,L '" less than Reporting Limit 

### 0, 5.18 4.82 93.0 CO, 0.0 10.3 10 .5 

### 10 .2 102.7 99.4 3.2 

## N

, 39.4 39.6 39.5 0.7 CO,

1.4 10. 3 12.1 

### 12.2 104.1 104.8 0.7 QMD 25 .1 25.3 

## N, 14.4 

### 15.2 105.4 

### CO, 10.3 

### 10.67 104.1 

# co, NO


### CH, 0.0 9.9 9.7 9.4 93.0 94 . 2 

### 3.9 CO, 2.8 2.9 2.8 2.6
Cu. 0.0 9.9 10.4 10.5 

### 104.9 105.5 

### 0.6 CO, 10.3 10.5 102.2 

### Instrument ID Calb Date TCD#1 04/13/2012 

### Reporting Limit: 0 . 1% 

### CH, CO 9.9 10.3 

### 10 .02 10.45 100.8 

### 10 1.0
Cu. 

# co NO NO
CO 0.0 10.3 10.2 

### 9.8 98.2 94.3 

### 4.0
Cu. CO 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0
C O 0.0 10.3 10.9 11.0 105.5 

### 106.3 0.8
Cu. CO 9 .9 10 .3 9.8 10.2 

### 98.6 99.0 

# 4/L4 Marcus Hueppe Laboratory Director Page 9 15 34 Eastman Ave ., Ste. A • Ve ntura, • CA 93003 www.aaclab.com • (805) 650 - 1642 • FAX ( 805 ) 650-1644

# Atmospheric Analysis & 

# Consulting, Inc.

SCAQMD Method 25.1,3 Quality COlltrol/Quality Assurallce Report



# I I Date Analyzed Analyst 02106 / 2013 : ZG
I Open"ng Carb afon Ver"ficafo Standard



## - I I 

### r I II I 

### n AA C II> 

### Analyte Concentration 

### O-CV NMNEOC 0.27 

### O-CV dp NMNEOC 0.27 

### O-CV tp NMNEOC 0.27


### "

- Method Blank AACID 

# I Analyt. 

# I Resul!

MB 

# I NMNEOC 

# I NO
III

- Matrix Snike & 

### DUDlic.t. Sample AACID 

### Analyte Concentration 

### 130102-60714 

# I NMNEOC 

## II 0.00


### IV - I DDm Backflush Standards MCID 

# I Analyt. 

# I Re sult Backflush 1 

### NMNEOC 0
. 884 

### Backflush 2 

### NMNEOC 0.950 

### Backflush 3 

### NMNEOC 1.023 Result 

### 0.262 0
.266 0.267

Spike 

### Added 

# I 54.35 

# I % Recovery .... 

### 81.3 87.4 94.1
V Bracketed CloSing Calibration Verification 

### Standards

- 

# I AACID 

# I C-CV Low C-CV High 

## * Must be 90-110% 

## ** Must be 80-120% 

## •• * Must be 75-125% **"'* 

### Must be < 

### 25% 

# "''''*.* Must be < 

### 10% Analyte 

### NMNEOC NMNEOC 

# I Conce ntrat io n 

# I Result 

### 0.27 0.261 2.72 2
. 82 % 

### Recovery" 96.4 97.9 98.3



### MS Result 

# I 43.66 

# I I

I % Recovery'" 

# I 96.0 103.8 

### MSD Result 43.81 

# I Instrument 10: FIO#4 Un its : PPMV Calibration Date:



### MS MSD 0/

8 

### Ree **'* 

### 0/0 Ree 

# It '"

80.3 

# I 80.6



### Laboratory Director 111012013

% RPD .. .... + 

# I 0.4



### Page 10 1534 Eastman Ave., Ste. A • Ventura, • CA 93003 www.aaclab.com • ( 805 ) 650 - 1642 • FAX (805 ) 650- 1 644 

# I

# Atmospheric Analysis & 

# Consulting, Inc.

SCAQMD Method 25.1,3 

### Quality Control/Quality Assurance Report Date Analyzed : 02106/2013 

### Analyst: : ZG


### I

. 

### RPD ' Sample Duplicate analysIs 

# I AAC !D 

# I Result 

# I Result**Du~** 

### 130102-60714 

## <PQL <PQL 130102-60715 

## <PQL <PQL 130122-60797 

## <PQL <PQL 130122-60798 

## <PQL <PQL 130122-60799 

## <PQL <PQL 130122-60800 

## <PQL <PQL 130122-60801 

## <PQL <PQL 1 30 122

- 60802 

## <PQL < PQL



# I Quali!1 Assurance Criteria



## Cone. (ppmv) %RPD 

### 1-3 <20 4-6 

### $15 7-12 < 12 13-30 <10 31-50 <5 S



# I Instrument !D: F!D #4 Units: PPMV Calibration Date: 111012013 

# I % RPD 

# I NA NA NA NA NA NA NA NA

Marcus Hueppe 

## Laboratory Director



## Page 11 1534 Eastman Ave
., Ste. A • Ventura, • CA 93003 

# @ www.aaclab.com. (805) 650-1642 • FAX ( 805 ) 650-1644

# Raw Data

Page 12
.600

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### Instrument = TeO 

### #1 Chrom Perfect Chromatogram Report



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## , 12 Time - Minutes 

# , 14 -<**~** 00 

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### ;;;

16 18 20 22

Raw File Name 

### = C:\CPDATA\lnst#01\2013\020613.0006_raw Date Taken (end ) 

### = 2/6/2013 9:29:25 AM Method F i le Name = C:\Cpmethods\lnst #01\2012\D1945-D1946-3C.MET Dilution Factor = 1 Calibration File Name = C:\Cpmethods\lnst # 01 \2012\D1945-D1946-3C-041312-standard

. CAL

Peak # Ret 

### T ime Name Amount Amt% Area Area % Type Width 1 7.03 Oxygen-MS5A 6.302 13.00 1 86350 12.448 BB 0.09 2 9.15 Nitroge n-MS5A 39.354 81.196 573552 82_684 SBB 0 .11 3 9.54 C02-Q bon d 2.812 5.803 33766 4
. 868 TBB 0.21 Total Area 

### = 69366 8 Total Height 

### = 99456.77 Total Amount 

### = 48.46832 

# "

Printed on 2/6/2013 9:29:56 AM 

# Page 13 P age 1 of 1C hrom Perfect Chroma tog r am Repo rt 1301 22 -607 97 dp
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0 2 4 6 8 10 12 14 16 18 20 22 24 Tim e - Minu t e s 

### Sample Na me ; 130122 - 60797 

### dp In str u ment = TCD #1 

### Raw Fi le Name; C:ICPDATAllnst#01120131020613

. 00 07,raw Date Ta ken (end ) ; 2/6 / 2013 

### 9 :49:02 AM M eth o d F i le Name ; C :I Cpmethods l lnst#01120 1 2 I D194 5-D1946-3C

. MET Dilutio n Fact or; 1 Ca l ib rat ion Fil e Na m e; C :I Cpme t hods l l ns t #0112012 I D194 5- D 1 946-3C-041312
- standa rd.CA L

Pe a k # Ret T ime Name Amount A m t % A r ea Area % 

### Type Widt h 1 7
. 03 Oxyge n -MS5A 6 ,332 12.960 86 766 12.4 1 1 BB 0
. 09 2 9
. 15**Nitrogen MS5A**  

### 39.640 81 .1 34 577714 82 , 634 SBB 0
. 11 

### 3 9 .54 C02
- Q bond 2
. 885 5
. 906 34641 4 , 955 TBB 0.20 Tot al A rea; 699 1 219 Tota l Height; 9979 0 .36 Tota l Amount = 48.8572



### -_ ._ --- --- -- --- - -- ------- --- -- - - -- Pri n t ed on 2/ 6/2013 

### 94 9: 25 AM 

# Page 14 Page 1 of 1Sample Name 

### = 130122-60798 Instrument = TeO #1 Raw File Name 

### = C:tCPDATAllnst#01t2013t020613.0010.raw Date Taken (end) = 2/6/201310:49:29 AM Method File Name 

# = C:tCpmethodstlnst #01 \2012tD1945-D1946-3C.MET Dilution Factor 

# = 1 Calibration File Name = C:tCpmethodstlnst #01\2012tD1945-D1946-3C-041312-standard.CAL

Peak # Ret. Time Name Amount Amt% Area Area 

### % Type Width 1 7.03 Oxygen-MS5A 6.916 12.947 94762 12.398 BB 0.09 2 9.15 Nitrogen-MS5A 43.327 81.112 631446 82.617 SBB 0.1·1 3 9
. 54 C02-Q bond 3.173 5.941 38100**985** TBB 0.20 Total Area 

### = 764307.6 Tota l Height 

### = 106587 Total Amount 

### = 53.41557

Printed on 2/6/201310:50:47 AM 

# Page 15 Page 1 of 1Chrom Perfect Chromatogram Report 130 122-60798 dp '00

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### = 2/6/2013 1 1: 08 : 12 AM Met h od File Name 

# =C : ICpmethods\lnst #01\2012\ D1945 - D1946-3C

. MET D i lut ion Factor 

# =1 Ca li bration F il e Name 

### = C :\ Cpmethods\ l nst #01 \2012 \ D1945 - D1946-3C-041312
- standard

. CAL Peak # Ret T ime Name Amount Am t% Area Area 

### % Type W idth 1 7
. 03 OXYgen-MS5A 6.498 12
. 904 89036 1 2
. 36 2 BB 0
. 09 2 9
. 15 N i t rogen-MS5A 40
. 74 6 80
. 91 7 593828 82.450 SBB 0
. 1 1 3 9
. 54 C02
- Q bond 3
. 112 6
. 180 37360 5
. 18 7 TBB 0
. 20 Total Area 

## =720224
. 1 Total Height 

## = 101784
. 8 Tota l Amount 

## =50
. 35493

Printed on 2/6/2013 11 : 13 : 05 AM 

# Page 16 Page 1 of 1SC(h I 

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# =C I Cp m ethodsl l nst #01\20 1 2ID1945 - D1946 - 3C

. MET Dilu ti on Factor 

# = 1 Cal i brat io n F i le Name 

### = C : I Cpmethodsllnst #01 \2012ID1945
- D1946 - 3C
- 04 1 312-standard

. CAL

Pe ak # Ret Time Name Amount Am t % Area A r ea 

### % Type W idth 1 7.0 3 Oxygen-MS5A 5
. 579 14
. 128 76448 1 3
. 523 BB 0.09 2 9
. 17 Nitrogen - MS5A 31
. 828 80.600 463869 82.055 SBB 0.10 3 9
. 56 C02
- Q bond 2082 5.2 7 3 24999 4.422 TBB 0.22 Total A r ea 

## =5653 1 6
. 3 Total Height 

## =85716.88 Total Amount 

## =39.4896 24

P r i n ted on 

### 2 1 6 / 2013 11 : 3048 AM 

# Page 17 Page 1 of 1Chrom Perfe c t Chromatogram Report 130 1 22-60799 dp
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### = C ;tCPDATAtJ nst#01t2013t020613
. 0013
. raw Date Taken (end ) 

### = 2/6/2013 11 :47 : 1 0 AM M e thod F il e Name = C :tCpmethods t lnst#0112012 t D1945-D1946 - 3C

. MET D i l u ti on Factor = 1 C a li b ra tion F il e Name 

### = C :tCpmethods t l ns t #0112012 t 01945 - 0 1 946-3C-041312- standard

. CA L Pea k 

### # R et. T ime 

### Name Amount Amt % 

### Area Area % Type Wi dih 1 7
. 03 Oxygen-MS5A 5

_ 512 14
. 169 7 5529 13
. 566 BB 0

_ 09 2 9
. 17 Nitroge n-MS5A 31.293 80.444 456068 81.915 SBB 0
. 10 3 9
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. 096 5
. 387 25159 4 .5 1 9 T BB 0

_ 23 T ota l Area 

### = 556756
. 8 Total He ight 

### = 84950
. 39 T otal Amount 

### = 38
. 90063



### -------- - -- -------- -------------------- Pnnted on 2/6/20 1 3 1147:42 AM 

# Page 18 P age 1 of 1Chrom Perfect Chromatogram Report
130122-60800
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. raw Date Taken (end) c 2/6/201312 :05 : 14 PM Method File Name c C :I Cpmethodsllnst #01\2012ID1945-D1946
- 3C

. MET Dilution Factor c 1 Ca li bration File Name c C: I Cpmethodsllnst #01 \2012ID1945-D1946-3C-041312-sta n dard

. CAL

Peak # Ret. T i me Name Amount Amt % Area Area 

### % Type Width 1 7.03 Oxygen-MS5A 6
. 106 14
.262 83668 13.648 

## BB 0.09 2 9
. 16 N i trogen-MS5A 34.537 80
. 672 503345 82
. 105 

## BV 0.1 1 3 9.55 C02
- Q bond 2
. 169 5
. 066 26039 4.247 

## VB 0.23 Tota l Area c 613053 Tota l Height c 91169.8 Tota l Amount c 42
. 8 1 182

Pri nted on 2/6/201312:2034 PM Page 1 of 1

# 600J

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### TeO #1 Chrom Perfect Chromatogram Report 130122-608001p



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. 0016
. raw D ate Ta ken (end) 

### = 21612013 12 : 37 : 39 PM Method Fi le Name 

# =C :I Cpmethodsllnst #0112012ID1945-D1946-3C.ME T D i l ution Factor 

# = 1 Cal i bration File Name = C:ICpmethodsl l nst #0112012 I D1945-D1946 - 3C-041312-standard

. CAL

Peak # Ret

. Time Name Amount Amt% Area A r ea % Type Width 1 7
. 04 Oxygen-MS5A 5
. 934 14
. 195 81319 13
. 590 BB 0
. 09 2 9 .1 7 Nitrogen-MS5A 33.622 80.420 490006 81.892 S B B 0

. 10 3 9.55 C02-Q bond 2 .2 51 5
. 385 2703 1 4
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. 23 T otal A rea 

### = 598355.5 Total H eight 

### = 89400
. 6 Tota l Amount 

### = 4 1.80766 24

Printed on 21612013 1 2 : 37:57 P M Page 1 of 1 

# Page 20 l>H

# ~~)13Chrom Perfect Chromatogram Report 130122-60801 dp
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# 500 1 ,

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### = 130122-60801 dp Instrument = TeD #1 Raw File Name 

### = C;ICPDATAllnst#01120131020613.0018.raw Date Taken (end) 

### = 2/6/20131:19:52 PM Method File Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C.MET Dilution Factor = 1 Calibration Fi le Name 

### = C:ICpmethodsllnst #0112012ID1945-D1946-3C-041312-standard.CAL Peak # Ret. T i me Name Amount Amt% Area Area % Type Width 1 7.03 Oxygen-MS5A 6.046 13 .179 82849 12.627 BB 0_09 2 9
. 16 Nitrogen-MS5A 37.023 80
. 700 539579 82.235 SBB 0.11 3 9
. 54 C02-Q bond 2
. 808 6.121 33715 5.138 TBB 0.21 Total Area 

# = 656143.1 Total Height 

# = 95167.28 Total Amount 

# = 45.87751

Printed on 2/6/2013 1 : 20: 18 PM Page 1 of 1 

# Page 21Chrom Perfect Chromatogram R e p ort 130122.00801 tp
600

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# 400j


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## =T C D # 1 Raw File N ame = C: I CPDATA\lnst#01 12013 1020613
. 0019.raw Da te T a ke n (end) 

### = 2/6/20 1 31:37: 1 6 PM Method File N ame = CICpmethodsllnst #0 1 12012ID19 4 5-D194 6-3C.M ET D ilution Facto r = 1 Calibration F ile Na me 

### = C:IC p methodsllnst #0 1 12012ID1945- D 194 6-3C-041 31 2- s t a ndard

. CAL

Peak # 

### Ret. Time N ame Amoun t Amt% Are a Area 

### % Type Width 1 7.03 Oxygen-MS5A 6
. 130 1 3 .2 07 84003 12.651 BB 0.09 2 9
. 16 N itrogen-MS5A 37
. 5 1 0 80
. 8 1 2 546667 82 .3 30 S BB 0 .1 1 3 9
. 54 C02-Q bond 2
. 776 5
. 981 33328 5
. 019 T B B 0.21 Total Area 

# = 663998
. 2 T ot al H e i ght 

# = 96125.48 T otal Amou n t 

### = 46 .4 1586

P r i nted on 2/6/20 1 3 1 :38:05 P M Pa ge 1 of 1 

# P a ge 22600

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Raw File Name = C :ICP DATA l lnst#01 12 013 1020613. 0020 .raw Date Taken (end) = 2/6/2013 2 : 01 :52 PM Method File Name 

### = C:ICpmethodsllnst #0112012ID1945·DI946·3C.MET D i lut ion Factor 

### = 1 Ca li bra tio n File Name = C :I Cpmethodsllnst #0112 012I D1 94 5- D1946-3C-041312-s tandard

. CAL

Peak 

### # Ret Time Name Amount Amt % Area Area 

### % Type W idth 1 7.03 Oxygen-MS5A 5.743 13
. 160 78692 12.606 BB 0
. 09 2 9
. 16 Nitrogen-MS5A 35.276 80
. 839 514114 82
. 358 SBB 0
. 11 3 9
. 54 C02-Q bond 2
. 618 6
. 000 31436 5
. 036 TBB 0.21 Total Area 

# = 624242.4 Total He ight 

# = 92045.65 Total Amount 

# = 43
. 637,08 14

Printed on 2/6/2013 2:02:19 PM Page 1 of 1 

# Page 23600

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. 0021.raw Date Taken (end ) 

### = 2/6/2013 2:18:22 PM Method File Name 

# = C :I Cpmethodsllnst #0112012 I D1945 -D19 46-3C

. MET D i l u t ion Fa ctor 

# =1 Calib ration File Name = C :I Cpmethodsllnst #0112012ID1945-D1946-3C -0 41312-slandard

. CAL

Peak # Re t. Time 

### Name Amount Amt% Area Area % Type Width 1 7.03 Oxygen-MS5A 5
. 832 13
. 176 799 18 12
. 621 BB 0
. 09 2 9
. 16 

### N i trogen-MS5A 35
. 781 80.836 521467 82.354 SBB 0.11 3 9
. 54 C02-Q bo nd 2 .650 5
. 988 31819 5.025 TBB 0:21 Tolal Area 

## =633204.3 Total He igh t 

## =92977.34 Total Amount 

## =44:26297 24

Pri nted on 2/6/2013 2 : 18:49 PM Page 1 of 1 

# Page 24Chrom Perfect Chromatogram Report**-----~---- ------** **-------~-------~---- -----**  130 122 -6079 7**1600 ,---------------~** **-------------------------------------------------------------.** 

### 1 4 00

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# = C :\Cpmethods\lnst #04\2013\Method25

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Peak # Ret . Time Name Amo u nt Amt % Area Area % Type Width 1 1. 88 Ca rbon Dioxide 1933.222 99
. 992 39723784 99.980 BB 0.48 2 6.27 NMNEOC 1 0.109 0.006 5822**0~0 5**  BB N 0.38 3 6.38 NMNEOC 2 

## + 0
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. 18 0 .\47 Total Area 

### = 3.973166E+07 Total Height 

### = 1058976 Total Amount 

### = 1933.369

P r inted on 2 / 6 / 2013 10 : 33 : 04 AM Page 1 of 1 

# Page 251600
1400
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### = C:ICpmethods l lnst #0412013IMethod25 .1 ,3Jow.m et Dilution Facto r 

### = 1 Calibration F i le Name 

### = C :I Cpmethods llnst # 0412013 I M25 .1 ,310w-01 1013
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### Ret. T i me Name Amount Amt % Area Area 

### % Type Width 1 1.93 Carbon 

### Dioxide 1966
. 198 99.992 40401380 99
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### = 1966.363

Printed on 2/6/201310:50:22 AM Page 1 of 1 

# Page 261600

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Raw File Name - C: \CPDATA\l nst#04\2 013\020613
. 0016.raw Date Taken (e nd ) - 2/6/2013 11 :03:54 AM Me thod File Na me 

# =C:\Cpmethods\lnst # 04\2 013\Me thod25 .1 ,3_tow . met D il ut ion Factor 

# = 1 Cal i bration F i le Name - C :\ Cpmeth ods\lnst #04\2013\M25

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. CAL Peak # Ret. T ime Name Amou n t Amt% Area Area 

### % Type Width 1 1
. 91 Carbon D ioxide 2005
. 571 99
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### o .c; i4 Tota l Area - 4
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. 645

Printed o n 2/6/201311:12:56AM P age 1 of 1 

# Page 271600 

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# = C:ICpmethodsllnst #04\2013IMethod25

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# =1 Calibrat ion File Name = C : ICpmethodsllnst #04\2013IM25

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Pe ak # Ret Time Name Amount Amt% Area Area 

### % Type Width 1 1.82 Carbon Diox ide 1996.489 99 .997 41023792 99.991 

## BB 0.49 2 5
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## BB 0.13 3 6.26 NMNEOC 2 .,0
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. 002 

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# = 4.102751 E+07 Total He ight 

# =1060476 Total Amount 

# =1996
. 559

Pr i nted on 2/6/2013 11 : 22 : 40 AM Page 1 of 1 

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### = C :\CPDATA\lnst#04\2013\020613.0022.raw Method File Name = C :\Cpmethods\lnst #04\2013\Method25.1 ,3

_ low.met Calibration File Name :: C:\Cpmethods\lnst #04\2013\M2S.1 ,3Iow-011013.CAL Date Taken (end) = 2/6/201312:57 : 10 PM D i l ution Factor = 1
Peak # 1 

### 2 Ret. Time Name 1.82 Carbon Dioxide 6.32 NMNEOC 1 T otal Area = 3
. 636246E+07

Printed on 2/6/2013 1 :01 :2 8 PM Amount 1769.601 0.014 Amt% 99.999

0.001 Total Height 

### = 1063320 Area 36361712 745 Area % 99.998

0.002 Type 

### SS SS Width 0.43 0.20 Total Amount = 1769.615

Page 1 of 1 

# Page 30

# '~**r** " 00 

## ! 1200
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### = 130122-60800 Instrument :;: FlO #4 Ch rom Perfect Chromatogram Report**~ ~**  i'U

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### = 2/6/20 13 1: 15:05 PM Method F i le Na me:;: C :\Cpmethods\ l nst #04\2013\Method2S . 1 ,3_low . met D i lutio n Factor = 1 Calib ra tion File Name 

### = C :\Cpmethods\ l ns t #04\2013 \M2 5
. 1.310w-011 013.CAL

Peak # 

### 1 2 Ret. T ime 1 .89 5.53 Name Carbon D ioxide NMNEOC 1 Total Area = 3.756472E+07

Printed on 2/612013 1 : 30 : 24 PM Amount 1828
. 043 0.040 Amt % 99.998

0
. 002 Total He igh t = 1 064896 Area 37562568 2148 Area 

### % 99.994

0.006 Type BB BB N Width 0,45 0 .1 2 Tota l Amount = 1828083

Page 1 of 1 

# Page 311600

1400

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Raw F i le Name < C :I CPDA TA l l ns t#04 1201 31 0206 13. 002 4. raw Date Taken (end ) < 2/6/20131 : 28 :1 7 PM Method File N ame = C: I Cpmethodsl l nst #0412013 I Method25

. 1 ,3_l ow . met Di l ut ion Factor < 1 Calibration File Name < C :I Cpmethods l lnst #04120 1 3 I M25

. 1, 3Iow-011 013.CA L

Peak# 

### 1 2 Ret. T ime Na me 1 .85 Carbon D ioxide 5
. 53 NMN E OC 1 Total Area < 3.70025 E +07

Printed on 2/6/20131 :30:3 1 PM Amount 1800
. 686 0
. 038 Amt% 99
. 998

0
. 002 Total H eight < 1057271 Area 37000440 2059 Area 

### % 99
. 994

0
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. 725

Page 1 o f 1 

# Page 321600

1400

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# 200**~**
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### #4 Chrom Perfect Chromatogram Report



## • c 

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. 0025
. ra w Date Taken (end) = 2/6/2013 2 : 30 : 10 PM Method File Name 

### = C :I Cpmethods l lnst #0412013IMethod25

. 1.3 Jow

. met Dilution Factor 

### = 1 Calibrat i on Fi l e Name = C : ICpmethodsl l nst #04120131M25

. 1
. 310w-0 1 1013
. CA L

Peak# 

### 1 2 Ret. T ime Name 1 .82 Carbon D ioxide 6.44 NM N EOC 1 Total Area 

### = 3.878849E+07

Printed on 2/6/2013 2:45 : 46 P M Amount 1887.675 0.01 1 Amt% 99
. 999

0.00 1 T otal Heigh t = 1061373 Area 38787880 606 Area 

### % 99
. 998 0.002 Type 

## B

B BB Width 0.47 0.16 Total Amo un t = 1887
. 686

P age 1 o f 1 

# Pag e 331600

14 00
1200
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# " 

# .. § 800 

# " : 0 0 600 

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### = C;ICPDATA l lnst#0412013 1020613.0026 .raw Date Taken (end) 

### = 2/6/20 13 2 : 43 : 32 PM Method File Name 

### = C:ICpmethodsllnst #0412 0 13 IMe thod25

. 1 , 3Jow

. met Di l ut i on Factor 

### = 1 Calibratio n F ile Name = C : ICp methodsll n st #0412013IM25.1 , 310w-01 1013.CAL

Peak 

### # 1 

### 2 Ret. T im e Nam e 1 . 8 3 Carbon D iox ide 6
. 34 NMNEOC 1 Tota l Area = 3
. 90983 E+ 07

Pri n ted on 2/6/20 13 2:45 : 52 PM Amount 1902
. 741 0.D16 Amt% 99.999

0
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### = 1063180 Area 39097468 835 Area % 99.998

0
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### = 19 02
. 757

Page 1 of 1 

# Page 341600
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# · ;;

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# ,.**~** 

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Raw F ile N ame = C :I CPDATA l lnst#04 12013 1020613
. 0027
. raw D a te Taken (e n d) 

### = 2/6/2013 2 : 57:07 P M Method File N ame 

### = C:ICpmethodsllns t# 0412013IMethod25 .1. 3Jow

. m et D i l ution Factor 

### = 1 Calib ration F i le N ame = C :I Cpmet h odsllnst #0412013IM25

. 1 , 310w-0 1 1013
. CAL

Peak # 

### 1 2 R et. Time Na me 1 .85 C a rbon D ioxi d e 6
. 32 N M NE OC 1 Tota l Area = 3
. 900964 E +07

P rinte d on 2/ 6 /20 1 3 3 : 1 3 .49 PM Amoun t 1 8 98.428 0
. 0 1 5 

### Amt% 99
. 999

0.001 T otal H eigh t = 1064 4 29 Area 390088 4 0 800 Area 

### % 99
. 998

0 .0 02 T ype 

### SS SS Width 0.47 0
. 1 9 Total A m ount 

### = 1898.443

Pag e 1 of 1 

# Page 35

# . "**~** 

# "**~** 0**~** 

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# . u 400 ;; 

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### FlO #4 Chrom Perfect Chromatogram Report



## • c 

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# . c 

## • 

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. 0 u 0 W N Z U 

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### = C;ICPDATAllnst#04120131020613.0028.raw Date Taken (end) = 2/6/2013 3:10:23 PM Method File Name 

# = C:ICpmethodsllns1 #04\20 1 3IMethod2S.1

. 3_lowmet Dilut i on Factor 

# = 1 Calibration F ile Name = C :I Cpmethodsllnst #04\2013IM25.1.310w-011 013
. CAL

Peak 

### # 

### 1 2 Ret. Time Name 

### 1.92 Ca rbon Dioxide 6.32 NMNEOC 1 Total Area = 3
. 900016E+07

Pr i nted on 2/6/2013 3 :1 3 : 55 PM 

### Amount 1897.969 0.014 

### Amt% 99
. 999

0 .0 01 Total Height 

### = 1064700 

### Area 38999400 758 

### Area % 99.998

0 .00 2 Type 

## BB BB Width 0.47 0. 18 Tota l Amount 

### = 1897.983

Page 1 of 1 

# Page 36

# Calibration Summary

Page 37

### SCAQMD Method 25.1 

### 125.3 Calibration Curve (GC/FID/TCA #4) ANALYTE: TNMNEOC (as Propane) Analysis Date: 1/1012013 Theoretical Retention time Response RPDfrom Std Theoretical Concentration initial result Concentration (ppmv) (min) Area (+1- 20%) Deviation (ppmv)

0
. 11 6
. 89 6436 0.11 6.84 6635 3
. 0 140
. 71 0
. 11 0
. 27 6.85 14293 0
. 27 6
. 86 14463 1
. 3 134
. 35 0.27 0
. 54 6
. 86 26743 0
.54 6
. 85 28478 6
.3 1226
.83 0.54 1
. 09 6
. 85 62346 1
.09 6
. 85 65692 5.2 2365.98 1
.09 2
.72 6
.84 167066 2
.72 6
. 85 158327 5.4 6179.41 2
.72 5
. 44 6
.84 282757 5.44 6
. 84 280611 0
.8 1517.45 5.44 AvgRT 6.85 RTWindow + /- 0 .20 

### min Calibration Verification Standards: CCV Retention Time 

### Result (ppm& 

### % 

### Rec" 2.5 ppmv 6
. 84 2
. 89 106
. 3 2.5 ppmvdp 6
.85 2.79 102
. 5 'M ust be +/- 10 % of Theoretical Concentration
Analyst ( Int itial & dale ): 

## Zl3 \ 

# I\0113 Lab Director ( In itial & date) : 

# tW

# ~**~7** Analyst: Response Area (mean)

6536 14388 27611 64019 162697 281684 Calb. Type R2 value: Intercept (B) Lin Const (M) 

### ZG Calculated Concentration (From Mean) 0.12 0
. 27 0
.52 1
. 19 3
. 04 5.26 

### Linear 0
. 9925

0
. 00 53584
.69 Recovery (+1-15 %)
112 99 95 110 112 97 Y:::MX+8 Must be> 0. 990 

### Included 00 f'") 

# '"**~** Po.

### 4
. E+05
3
.E+05
3
.E+05
2
. E+05

# ~ < 2
.E+05
1
. E+05
5.E+0
O

.E+O 

## TNMNEOC (as Propane) Plot



# V ,1 /

0
.00 1
.00 

# * .......**~** 

# /

2
.00 3
. 00 Concentration (ppmv) 

## /'

4
.00 y 

### = 

### 53584.691 1 X 

## R

2 = 

### 0
. 9925



# ./ 

# V·

5
.00 6
.00 0- M 

# '"**~** P-.

### Date: 0111012013 Analyst : 

## ZG Analvte : 

### Cone
. MOL #1 NMOC 

### 0
.05 0 0 .058

Analvte: Mean Std Dev N M O C 

### 0.051 0 .005 

## FlO MOL Study per SCAQMO 

## 25.1/25.3 Instrument : GCIFID 

### #4 Units : ppmV MOL#2 MOL #3 

## r.rot #4 MOL#5 MOL #6 MOL#7 

### 0
.0 50 0
.0 54 0 .04 3 0. 051 0. 05 6 0
.047 

### MOL
- Method Detection Limit Study per USEPA Gu i delines MOL MRL 

### 0,016 0.0 · 1 9 M OL (Method Detection Limit) (7 replicates) 

### = Stand a rd D eviation x 3
. 143 MRL (Minimu lll Reporting Limit) '"' MOL x 3.0 Is the sp i ked c o n centrati o n <: 10 times th e calculated MDL0 N
Defi n itio n : MDL- The min im um con centrat io n 

### of a s ubs tance th a t ca n be Identifie d , mea s ure d <I n d repo n ed witl! 

### a 99% 

### co nf idence int erval, tha t 

### the ana/yte concentr atio n 

### ;s grea ter than zero and is de t ennine d from the analysis of 

### a sam ple in 

### a g iven matrix containing the ana/yte. Definition: M RL**~** T he sm a lle st meas fJ.red concentra tio n of

### a subs tan ce ( hat can be relia bl y meas u red by u sing a give n an a lytica l m ethod. 

## o "<t OJ

## ~ p..

### Alt ern at i ve Supporting Cal c u l ations L OD ( Limi t of Det ection) -**S~'n arcl**  Of**li., ion**  x J.O L O a ( Limit o f Qu a nt i tati o n) = St;}I Ui i Ud Or ",i"l t i Qn X 10 .0 f;J] ea n Djl R ee • (Mean Res! T ru e**~lua}** y. 1001" ;;" Is the Mean % Re e betw ee n 80 % a nd 120 % 

# ? <£) I N
r::on c .JMD L**~** Concent ml l o n I M OL

### t8\ I s th e Conc.lMDL between 2 to 5? C!.J 1 N S i q n a l to Noise Ratio· (M eanIStdD ev) I s the signal to Noise Ratio between 2.5 and 

### 10"G1 N Defin it ion: LOD
- T /Je lowest conce ntration t ha t can b e determined to be s t atistica fly dif f erent from 

### a blank

. Defini tio n : 

### L OO**~** The co n ce n tratio n a bove wh ic h qua nt i ta tive res uff s call be o b tai n ed wi t h a specjf( c de gree of con fide nc e.
An.ly!e : POL 

# t= RL 

# rl N MO C 0
. 1 04 

### 0.104 

### Propo s ed PQL and RL Pr tlctical Ou an t i t il tio n Limit Is the PQL 2 to 5 tim es higher than the 

### LOQ ?(Y} f N R ep o rting Limit Is the RL equal to or greater than the POL

# (5) , N PQl ( P rac t i ca l Quantitation Limit) = E s tablish e d by the l aboratory bas ed on the abo \l e calculations RL ( Re porting Li m it):= Established by the la bo r atory based on the POL and/or method

. Definition: POL · T h e lowest leve l that can be r eliably ach ieved with in sp ecified limits of p recision a nd accuracy during routin e laborator y opera t ing co n ditio n s. In add ition, if qua tit ati

n g a t this level, the lowes t point of the calibra t ion cu r ve mus t be se t a t th is p o int. Comm e nts:
An

. lys! (sig n & d.te) : 

## 53 ' \ \ 0 \ 1 5 L. b Direc l ar (si g n & d ate): 

# I1!lP" 

# 47J -" 

# "'" .., bIl 

# '" Po<

## Appendix C

. G 

## PM 

## by SCAQMD Method 5.1

R0410673 C-10SCAQMD M ETH OD 5
. 1 PARTICU LATE TEST D A T A SUMM A RY ClientiLocatlon. Unit S am p l e Location T est No. Test Method Dale Start Time StopT!lne Sample Train Pitot Factor Meter cal Faclor Stack Area (sq h) Sample Time (Min) Bar Press (in Hg) Nozzle Diam (in) Stack Press (iwg) Slack Temp W) Vel Head (iwg) Stack. 02 (%) Stack C02 (%) Met8f Vol (ad) MetE)(Temp (F) MelE)( Press (iwg) L iquid Vol (mI) Sid Sample Vol (SCF) Mo i sture Fraction Stack Gas Mol WI Stack Gas Velocity (Nsec) Stack F/aoN Rate (wa cfm) Slack FloW Rate (dsctm) (soklnetrc Ra tio ( %) Facility Average Gas Flow (h sc1h ) .

. Faci Wty Average Gas Flow ( MMscfh )

.. Total Weight Gain. mg .. P a rt ic ul ate Em Issi ons Grain loading, gr/dsd..•.. Grain Loading C 3% 02.•... Grain Loading 1m 15% 02
. Grain Loa ding@ 12% C02

. .. Mass Em lss)o n s, Ib/ h r1
..................... .. Emission Rate. IblMMSCF 1) '1 IbIhr per Rule 475 PM Limit 2) 5
. 71 IblMMsdis stated In the permit as an emission factor Gemm.**Sen~nel** 

# , 5-2ISTK-PM·50-1

SCAOM05

. 1

21'/20'3

'4 : '4 18 : 25 '9-WCS

0.84 0
. 985 143
. 14 240 29.35 0
.234 '.90 784
.8 1
. 0467 14
.29 3
.80 157
. 850

76
. 1 1
. 16 258
. 1 148
. 438 0
. 075 28
. 34 89
. 52 768
. 849 292
.783 1 0 1 .21 

### ° r_ 0
. 537



# " 0
. 0002 0
. 0005 0
. 0001 0
. 0005 0.42 0 .78 Refe r ence Tem p (F). 60 F ue l Nat Gas D a l a B y SP

'90 78 4
. 8 1
. 0467 14
. 3 3
.8 157
. 85 7. , 1
. 16 258
.7 148.438 0.075 28
. 34 89
. 52 768.84 9 292.783 1 0 1. 21 5372
. 5 0.537 

# ,

# . •

0
. 0002 0
. 0005 0
. 0001 0
.0005 0
.42 0.78 Limits 0.01 0
. ' 

# " 5
. 71

Scnwlel U'"I 1**~O%** PM Summary 211912013 1 1 :33 AM14 :24 1 .3 1.10 1 .43 779 1.14 10 78 ! 1: '8 2.510 7.34 14:34 1
.0 1 . 10 1.10 780 1 10 79 989 .085 6.575 14:44 : 1.1 1.10 1 . 21 779 : 1 .049 10 80 14:54 : 1.1 1.10 1 .21 780 1.049 10 

### ao
15:29 15:39 10 79 6.74 15 :39 ; 15 : 49 10 79 7 5 6 .79 15:49 15:59 10 80 75 6.52 15 :59 16:09 10 79 75 6.34
16 : 33 16:43 S 5 : 0. 949 1 10 77 74 16:43 : 16:53 S 1 10 77 74 16 : 53 17:03 S 1 I 10 76 74 17:13 S 0.949 10 77 74
17:45**~** 10 

# . r 77 74 17 :55 1 10 78 73 18: .

05 10 78 73 18: 1 5 10 78 73

Page I

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### (' :n i'j' TRAVE 13SE POINTS , MIN/POINT : 

# Nt.),.- "H= 

# -*- X "P: 

# -:-7 Probe Condition , pre/post

## test~: ,/ Silica Gel Expanded, YI N:

__ . /:.' Filter Condition after T est 7 Check Weight

____ -''- Meter 

## " p Point Time 

### Volume

. ft3 in

. H , O 

## 'J () 1)'-' 

### 'I'i l " i¢O r"1**IQCD ~erage** **:** 

### AMBIENT TEMPERATURE : 

# e& BAROMETRIC PRESSURE- : 

# --,7-:';-1.*-0",------ ASSUMED MOISTURE::_--;;cnc'1f-/ ':.:.·

; ____ _ PITOT TUBE COEFF, Cp:

### o4~ 

# ( PROBE 10 NO/ MATERIAL: 

### tf-,!(., $1'i 

## pG 

# I :;, G Ss 

### PROBE LENGTH : 

# 7' , NOZZLE 10 NO/**MATE RIAL:** **-c:;--"':"' '-'** **S~**

### _ _____ _ NOZZLE DIAMETER: 

## o . • . 

# x

S 

### FILTER NOfTYPE: .50" - 17'" I PRE-TEST LEAK RATE : : 

### 40
. QO) CFM@ 15"" in

. Hg

. POST-TEST LEAK RATE: : "',}- CFM@ 

# tJlt in

. Hg

. PITOT LEAK CHECK
- PRE : ...- POST : 

## ,;ft C HAIN OF CUSTODY: SAMPLE CUSTOD IAN 

# !\f=
-- SAMPLER**~"** 

### SAMPLE CUSTODIAN 

# Ak"'"
"H Stack Probe Filter Imp

. Out in

. H , O Temp. O F Temp, O F Temp , O F Temp, O F



## r 

# , / 1 /1 ) 

## / / 1./
______ 

### 7 

## / 

# /I / 

# 1 1/ fl /\ 

# /\ I I / 

## IL 

## I .J ( If 

# , f' J 

# U/ \ 

### Imp

. 

### # Contents P ost- Test - Pre -Test 

### = Difference 

# 0]: I ·h' 

# ]8S
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# 750
. 0 3 

# .1)'1'\,

# ~33'1 

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# "'"

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### Total : _ ______ • __ _ Meter Temp

. O F 

### Vacuum 

## 0, P. static 

# I In Out in

. H g. 

### % in. H , O

I



### Comments:

____ ___ _________________________ _______________________ _



### Date of last revision 

### 1 125/2 013 Page

__ of

__ DS834049 Master Document Storagel Forms l Datasheetsl Field Datasheets

# DcllaJ1
PARTICULATE SCAQMD 5.1, WET IMPINGEMENT
Ga.""",
... 1/:rO/IJ Project 

### # ClienVLocation Sample Location Test 

### # Un;**~** 

### Water Blank 

### mg/ml Sample Date Analysis Date Analyst Initials 

## 5l 81.¥(· 

## P/II,-/ctrl MeCl, Blank 

### mg/ml 

## • Item Number
1. Glass Fiber Filter 

## :;'''5"- (Backup Filter) 

## ) 1(f' 2. Insol uble Solids Filter 

## 5S- 

# /790
3. Impingers and Probe Catches 

## 1l2(,jZ a. Water Fraction b. Organic Extraction 

# 1/2. c.(.. 125 ml MeCI2 (5 x 25 ml)



# Dellaf1 

# "' --- Date of last revision 11/13/08 Final Tare Gain Al iquot Net Gain Blank based Weight Weight Weight 

### Cor rection (mg/Sample) on Total

(g) (g) (mg) 

### (ml/ml) Volume (mg) 

## O.10'{O 

# o**.f{,~rl.** 

# G·U 0,0

-- -- --------- ----------------- 

# rJ. tb')]**D./~3{\** 

## 0 · 0 

# 0,0

--------------- -----------------



## 75"0 19.5('1£ 

## 2'1.S13S" 

## "l.o 

# :..--- Lj.o 

# 6 · 3**1~ 1~** **~81)**

## ~ "

. ,&'80 

# 15() 0.0 D·D 6
. 0 

# --- 75"0



## Total Particulate 

## =**_--' L(~**  

## ..:::D

____ __'m'_"g"_ 

## Method of Sample Prep/Notes

DS834012 Master Document StoragelFormslDatasheetslLab Forms

# DlJllai1.
PARTICULATE SCAQMD 5.1, WET IMPINGEMENT
Project 

### # ClienVLocation 

## C;"'M.:""'" Sample Location 

## Un; t. 1:. Water Blank mg/ml Sample Date Analysis Date Analyst Initials Test 

### # 5 

### 1:/#/(- P/II-/W-1.MeCI, Blank mg/ml • 

### Item Number


### 1. Glass Fiber Filter 

# g,- ( Backup Filter) 

# (7-(9 2. Inso lub le Solids Filter 

# S$- ir9( 3. Imp ingers and Probe Catches 

# 112(;.7 a. Water Fraction b

. Organic Extraction 

# I {7.,r,&" 125 ml MeCI2 

### (5 x 

### 25 ml)



### Date of last revision 11/13/08 Final Tare Gain Aliquot Net Gain Blank based Weight Weight Weight 

### Correction (mg/Sample) on Total

(g) (g) (mg) (mUml) Volume (mg) 

## O.lb 3'3 

# o.f('3f' 6,0

--------------- 

# 0.0 ------_.--- - -----


## 0
. ((,")0 

# 0./(;32.. 

# 6 , 0

--------------- 

# 0·0

------ -- ---------


### 1'1.(,002.. 

## 2'1 ·**~~I** 

## 2. \ 

# 110 

# 1/0 '2.. 

# I 

# 0 ,3
2ct.j(,t,2- 

## 2'1 · /('(.3 

# 0·0 

# JfJ2- 0 · 0 

# 0·0 

# 710

Total Particulate 

## = __ 

# 2_.-'I

____-'m"'9ilMethod of SamQle Prep/Notes

DS834012 Master Document StoragelFormslDatasheetslLab Forms

# D/Jlla~ PARTICULATE SCAQMD 5.1, WET IMPINGEMENT
Project 

### # Client/Location 

## C,""I'kM'" Sample Location UI); 

# r. Water Blank mg/ml Sample Date Analysis Date Ana lyst Initials 

# "Zf //.3 Test 

### # 5l /$0.1(- P/w"-Itx>-) MeCl, Blank mg/ml • 

### Item Number
1
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# 5S- (Backup Filter) 

# 113'7
2. Insoluble Solids F i lter 

# 5S- /7'{ 'I... 

### 3 . I mpingers and Probe Catches 

# tin) a . Water Fraction b

. Organic Extraction 

# {{ITo 125 ml MeCI2 (5 x 25 m l)



### Date of last revision 

### 11/13/08 Final Tare Gain A liquot Net Gain Blank based

## W~tt**W~tt** Weight 

### Cor rection (mg/Sample) on Total (mil) (ml/ml) Volume (mQ)

### O,\"I~ 

## 0./(,20 

# 0.0 D· O

---------- - --- ---._------ - --- 

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. lb'W O./(' ZO 

## 6,0 0 · 0 --------------. 

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# J55. :{b,f 

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Total Particulate 

## = 

# _-=='2:.. ' ''''c;.

____ ...:m.:..:....9 Method of Samp l e Prep/Notes

DS834012 Master Document StoragelFormslDatasheetslLab Forms

# 8811aJ1.
PARTICULATE SCAQMD 5.1, WET IMPINGEMENT
Project # Client/Location Sample Location Test# 

### 52161.1(- P/M,. 

## fl3 • Item Number
1
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## SS- (Backup Filter) 

# 17{j/ 2. Insoluble Solids Filter 

# 55'- 

# /1'6/ 3
. Impingers and Probe Catches 

# I [1.. 5 

# 'i a. Water Fraction b

. Organic Extraction

### 1(2,5~ 125 ml MeC I2 (5 x 25 ml) 

# DI**I{~** 0 

# 61CN\. K 

## /I]. (.0


# NoLC.! 1.... 

# 8l Vv\ 

### I< 1{2.(,\



# Deltal1 

# "'--. - Date of last revision 11/13/08 Water Blank 

### mglml MeCl, Blank 

### mglml Final Tare Weight

(Q) 

### Weight 

# Jg) 0.\{'1.6 

# 0./(''27- 

# O.u,;,3**,~** 

# ()

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## Z9.'io3J ).If

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## 'i<>j1


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### ~"rIl~Y 

## l.'i

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# :z.,.... HI 0.01>0</ 6. "'<>00 

### Gain Weight

(mol 

### 0 · 0 Sample Date Analysis Date Analyst Initials Aliquot Net Gain Correction (mg/Samp le)

(m l/ml) 

### 0·0



### ---------------- 

# 0·0

--- - ---------- 

## Q,O

(;.() 

# /92- 

# 19l 0-0 

## (;·0 

# !Jt /92-. 6 , 0



# o. {

# ~ 150 ZSO 

## 0 · 0

# ~ Blank based on Total Volume (mg)

---- - ------------

--------------



# o. {

0
. 0

Total Particulate 

## = 

## 6
. 0 mg**--------------~~** 

### Method of Sample Prep/Notes

DS834012 

### Master Document StoragelFormslDatasheetslLab Forms

### CPV SENTINEL UNIT 2 PARTICULATE TE ST STACK O2 • 

### CO 2 

### DATA Test 

### #: S -2/STK-PM-50
- 1 Date : 

### 2/1/2013 Tim e : 14:14 1 8 :25 L o ad: 55MW O 2 

### CO 2 

### Range 20 10 Cal Gas 9
. 98 4
. 96 Analyzer Zero 0.10 0
. 14 Analyzer Span 10
. 11 5 .2 5 P re-Bias Zero 0
.21 0
. 19 Pre - Bias S pan 10.11 5.24 Post-Bias Zero 0.23 0
. 10 Post-Bias Span 10
. 17 5
. 11 Average Bias Zero 0.22 0.15 Average Bias Sp a n 10.14 5.18 Pre-test zero bias 0.5% 0
. 6% Pre-test span bias 0
. 0% 0
. 0% Pos t-test zero bias 0.7% -0.4% Post-test span bias 0.3% -1.4% Zero D r ift 0. 1 % -0
. 9% Spa n Drift 0.3% -1.3% Test Results (fro m data l ogge r ave rag e) Av e ra g e 14.42 4. 0 1 Cal Corre ct ed 14. 29 3. 80

O 2 

### CO 2 

### Date Time % % 

### 2/1/ 2013 14:15:00 14.415 4.079 

### 2

/1/ 2013 14 : 16:00 14
. 388 4
. 098 

### 2/1 / 2013 14:17:00 14.368 4
. 11 

### 2/1/2013 14:18:00 14.372 4.109 

### 2/1/2013 14 : 19 : 00 14.395 4.099 

### 2/1/2013 14:20:00 14.379 4
. 109 

### 2/1 / 2013 14 :21 :00 14
. 364 4
. 112 

### 2/1/2013 14:22:00 14.373 4.106 

### 2/1/2013 14:23:00 14.397 4
. 095 

### 2/1/2013 14:24:00 14.394 4.098

### 2/ 1 / 2013 

## 14 :25 : 00 14
. 383 4
. 104 2/1/2013 

## 14:26 :00 14
. 368 4.11 2

/ 1/ 2013 

## 14 :27 :00 14
. 368 4
. 108 2/1/ 2013 

## 14:28 :00 14
. 363 4
. 113 2/1/2013 

## 14 :29 :00 14
. 363 4
. 111 2/1/ 2013 

## 14:30 : 00 14
. 372 4.101 2/1 / 2013 

## 14:31 : 00 14
. 366 4.103 2/1/ 2013 

## 14:32 :00 14
. 38 4.093 2

/ 1/ 2013 

## 14 :33 :00 14
. 371 4
.098 2/1/ 2013 

## 14 :34 : 00 14
. 382 4.087 2/1/2013 

## 14 :35 :00 14.359 4.097 2/1/2013 

## 14:36 :00 14
. 367 4
.088 2/1 / 2013 

## 14 :38 : 00 14.411 4
.071 2

/ 1/ 2013 

## 14 : 39 :00 14.38 4.077 2/1/ 2013 

## 14:40 :00 14
. 38 4.077 2/1/ 2013 

## 14:41:00 14
. 382 4.076 2/1/ 2013 

## 14:42 : 00 14
. 385 4.076 2/1/2013 

## 14:43 : 00 14
. 392 4
.072 2/1/ 2013 

## 14 :44 :00 14
. 385 4.074 2/1 / 2013 

## 14:45 : 00 14.387 4.075 2/1/ 2013 

## 14:46 : 00 14
. 391 4
.072 2/1/ 2013 

## 14:47 :00 14
. 375 4.083 2/1/2013 

## 14:48 :00 14
. 377 4.081 2/1/ 2013 

## 14:49 :00 14.368 4
. 082 2/ 1 / 2013 

## 14 : 50:00 14
. 341 4.098 2/1/ 2013 

## 14:51 :00 14.306 4
. 123 2/1/ 2013 

## 14 : 52:00 14
. 308 4.119 2

/ 1

/ 2013 

## 14 : 53 :00 14
.299 4
. 124 2

/ 1

/ 2013 

## 14 : 54:00 14
. 304 4.124 2

/ 1

/ 2013 

## 14 : 57 :00 14
. 346 4
.086 2

/ 1

/ 2013 

## 14 : 58:00 14.343 4
.094 2

/ 1

/ 2013 

## 14 : 59:00 14
. 336 4.102 2

/ 1/2013 

## 15 : 00:00 14
. 344 4
.095 2/1/2013 

## 15 : 01 :00 14.344 4
.096 2/1/ 2013 

## 15 : 02:00 14
. 35 4.094 2/1 / 2013 

## 15 :03 :00 14
. 345 4.098 2/ 1 / 2013 

## 15 :04:00 14
. 342 4.104 2/ 1 / 2013 

## 15:05:00 14
. 349 4.093 2/1/2013 

## 15:06:00 14
. 345 4 .1 01 2/1/ 2013 

## 15:07 :00 14
. 344 4.1 2

/ 1/ 2013 

## 15 :08 :00 14
. 345 4.097 2/1/ 2013 

## 15:09 :00 14
. 348 4
.097 2/1/20 1 3 

## 15 : 10 :00 14
. 342 4.106 2/1 / 2013 

## 15:1 1 :00 14
. 342 4. 1 06 2/1/ 2013 

## 15 : 12 : 00 14
. 348 4
.099 2

/ 1/ 2013 

## 15:13 : 00 14
. 349 4
. 096 2/1/ 2013 

## 15 : 14 :00 14
. 344 4.101 2/1/ 2013 

## 15 : 15 : 00 14
. 346 4.1 2/1/2013 

## 15:16 : 00 14
. 345 4
. 103 2/1/ 2013 

## 15 : 17 : 00 14.455 4
. 047 2/1/ 2013 

## 15 :20 : 00 14
. 399 4.069

### 2 / 1/2013 

## 15 :21 :00 14
. 398 4
.071 2

/ 1/2013 

## 1 5 :22 :00 14
. 391 4
.077 2/1/2013 

## 15 :23:00 14
. 39 4
.075 2/1/2013 

## 15:24 :00 14
. 392 4
.073 2

/ 1/ 2013 

## 15 :25 :00 14
. 398 4
. 07 2

/1/ 2013 

## 15 :26 :00 14.421 4
.057 2

/ 1/ 2013 

## 15 :27 :00 14.434 4
.053 2

/ 1/2013 

## 15 :28 : 00 14.427 4
.057 2

/ 1/ 20 1 3 

## 15 :29 :00 14.44 4
.05 2

/1/ 20 1 3 

## 15 :30 :00 14.427 4
.055 2

/ 1/ 20 1 3 

## 15 :31 :00 14.437 4
.048 2

/ 1

/ 2013 

## 15 :32 :00 14.44 4
.043 2

/1/ 20 1 3 

## 15 :33 : 00 14.462 4
.031 2

/ 1/ 2013 

## 15 : 34 :00 14.452 4
.037 2

/ 1/2013 

## 15 : 35 :00 14.465 4
.03 2/ 1 / 2013 

## 15 :36 : 00 14.454 4
.037 2

/ 1

/ 2013 

## 15 :37 :00 14.449 4
.039 2/1/2013 

## 15 : 52:00 14
. 342 4
.003 2

/1/ 2013 

## 15 : 53 :00 14
. 398 4
.051 2/1 / 2013 

## 15 : 54 : 00 14
. 396 4
.056 2/1 / 2013 

## 15 : 55:00 14 .3 89 4
. 062 2

/ 1/2013 

## 15 : 56 : 00 14.407 4
.054 2

/ 1

/ 2013 

## 15 : 57:00 14.4 4
.06 2

/ 1

/ 2013 

## 15 : 58 : 00 14.412 4
.056 2

/ 1

/ 2013 

## 15 : 59 :00 14.439 4
. 039 2

/1/ 2013 

## 16:00 :00 14
.466 4
.025 2

/ 1

/ 20 1 3 

## 16 :01 : 00 14.474 4
.02 2

/1/ 2013 

## 16:02 :00 14.46 4
. 028 2

/ 1/2013 

## 16 :03 :00 14.452 4
.03 2/1/2013 

## 16:04 : 00 14.453 4
.027 2/1/ 2013 

## 16 :05 : 00 14.473 4
.017 2

/ 1

/ 2013 

## 16:06 :00 14.464 4
.019 2/1/ 2013 

## 16 :07 : 00 14
. 501 4
.003 2/1/ 2013 

## 16:08 :00 14.474 4
.014 2/1/2013 

## 16:09 : 00 14.462 4
. 018 2/1/ 2013 

## 16:12 :00 14
. 508 4
.036 2/1 / 2013 

## 16 :1 3:00 14
. 364 4.068 2/1/ 2013 

## 16 : 14 :00 1 4. 367 4
.068 2/1/2013 

## 16 : 15 :00 14
. 356 4
.074 2/1/ 2013 

## 16 : 16:00 14
. 361 4
.071 2

/1/ 2013 

## 16 : 17:00 14
. 349 4
.079 2/1/ 2013 

## 16 : 18 :00 14
. 344 4
.085 2

/ 1/2013 

## 16 : 19:00 14
. 345 4
.08 2

/ 1/ 2013 

## 16 : 20:00 14
. 343 4
.084 2/1/2013 

## 16 :21 :00 14
. 353 4
.072 2/1 / 2013 

## 16 :22:00 14
. 353 4
.077 2

/ 1

/ 2013 

## 16 :23:00 14
. 317 4
. 106 2/ 1 / 2013 

## 16:24 : 00 14
. 319 4
. 103 2

/1/ 2013 

## 16:25 : 00 14
. 326 4
. 099 2/ 1 / 2013 

## 16:26 : 00 14
. 318 4
. 104 2/1/ 2013 

## 16 : 27 : 00 14
. 323 4
.09 6 2/1/ 2013 

## 16 :28 :00 14
. 323 4
. 1

### 2 /1/ 2013 

## 16 :30 :00 14.388 4
. 052 2/1/2013 

## 16 :31 :00 14
. 38 4
. 052 2/1/2013 

## 16:32:00 14.374 4
.055 2/1/2013 

## 16 :33:00 14 .3 6 4
.06 2/1/2013 

## 16 :34 :00 14.376 4
.052 2/1/2013 

## 16:35:00 14
. 383 4.046 2/1/2013 

## 16 :36 :00 14
. 367 4
.053 2/1/ 2013 

## 16 :37:00 14.37 4.049 2/1/2013 

## 16:38:00 14 .3 84 4
.039 2/1/2013 

## 16 :39 :00 14.4 4
.028 2/1/2013 

## 16 :4 0 :00 14.4 4
.025 2/1/2013 

## 16 :41 :00 14
. 385 4.03 2/1/2013 

## 16:42 :00 14.37 4.04 2/1/2013 

## 16:43:00 14
. 367 4
.039 2/1/ 2013 

## 16:44:00 14
. 379 4
.031 2/ 1 / 2013 

## 16:45 :00 14.347 4
.049 2

/1/2013 

## 16:46 : 00 14.369 4.03 2/1/2013 

## 16:47 : 00 14
. 369 4
.029 2/1/2013 

## 16 :48 :00 14
. 365 4.03 2

/1/2013 

## 16:49 : 00 14 .3 6 4
.032 2

/ 1/ 2013 

## 16:50:00 14.347 4.041 2/1/2013 

## 16:53 : 00 14.453 3
.973 2/1 / 2013 

## 16 :5 4 :00 14.441 3
.977 2/1 / 2013 

## 16 : 55 :00 14.43 3.985 2/1/2013 

## 16 : 56 : 00 14.435 3
.981 2

/1/ 2013 

## 16 : 57 :00 14
.44 3
.978 2/1/2013 

## 16 : 58:00 14.443 3
.974 2/1/2013 

## 16:59:00 14.439 3.978 2/1/2013 

## 17 :00 :00 14.444 3
.974 2/1/2013 

## 17 :01 :00 14.479 3
.953 2/1/2013 

## 17:02 :00 14.462 3.959 2/1/2013 

## 17 :03:00 14.471 3
.952 2/1/2013 

## 17 : 04:00 14.463 3 .9 51 2/1/2013 

## 17:05:00 14.456 3
. 953 2/1/2013 

## 17 :06:00 14.465 3
.948 2/1/2013 

## 17 : 07:00 14.484 3 .936 2/1 / 2013 

## 17:08:00 14 .4 81 3
.936 2/1/2013 

## 17 : 09 :00 14.484 3
.933 2/1/2013 

## 17 : 10:00 14.486 3.932 2/1/2013 

## 17 : 11 :00 14.451 3.945 2/1/2013 

## 17:12:00 14.456 3
.944 2/ 1/2013 

## 17:30 :00 14.359 3.845 2/1/2013 

## 17:31 :00 14
. 382 3.866 2/1/2013 

## 17 :32 :00 14.425 3
.905 2/1/2013 

## 17 : 33:00 14.458 3.899 2/1/2013 

## 17 :3 4 :00 14.445 3.906 2/1/2013 

## 17 : 35 :00 14.477 3
. 893 2

/1/ 2013 

## 17:36:00 14.482 3.893 2/1/2013 

## 17:37 :00 14.485 3
. 892 2/1/2013 

## 17:38:00 14
.473 3.893 2/1/2013 

## 17:39 :00 14.483 3.892

### 2/1/ 2013 

## 17:40 : 00 14.477 3
. 892 2/1/ 2013 

## 17 :41 : 00 14
. 502 3
. 878 2/1/ 2013 

## 17:42: 00 14
. 51 3
. 874 2/1/ 2013 

## 17 :43 : 00 14
. 514 3
. 87 2/1/2013 

## 17 :44 :00 14
. 508 3
. 871 2/1/ 20 1 3 

## 17:45 : 00 14
.519 3
. 864 2/1/ 2013 

## 17 :46 : 00 14
.514 3
. 864 2/1/2013 

## 17 :47 : 00 14.493 3
. 872 2/1/ 2013 

## 17 :48 :00 14
. 502 3
. 869 2/1/2013 

## 1 7 :49 :00 1 4
. 51 3
. 866 2/1/ 2013 

## 17 :50 :00 14.515 3
. 861 2

/ 1/ 2013 

## 17 :51 :00 14
. 501 3
. 866 2/1/ 2013 

## 17 : 52 : 00 14
.5 3
. 865 2/1/ 201 3 

## 17 : 53 : 00 14
.512 3
. 855 2/1/ 2013 

## 17 :54 : 00 14
. 522 3
. 845 2/1/ 2013 

## 17 :55 : 00 14
.524 3
. 84 2/1/ 2013 

## 17 :56 : 00 1 4
. 53 3
. 832 2/1/ 2013 

## 17 :57 : 00 14
.525 3
. 831 2/1/2013 

## 17 :58 : 00 14.527 3
. 827 2/1/ 2013 

## 17 : 59 :00 14
.519 3
. 831 2/1 / 2013 

## 18 : 00 : 00 14
.519 3
. 825 2/1/ 2013 

## 18 : 01 :00 14
. 53 3
. 816 2/1 / 2013 

## 18 : 02 :00 14
. 528 3
. 81 2

/ 1/2013 

## 1 8 :03 :00 14
. 544 3
.797 2/1 / 2013 

## 18 :04 : 00 14
.545 3
. 795 2

/ 1/ 2013 

## 18 :05 :00 14
.544 3
.795 2

/ 1/2013 

## 18 : 06 :00 14
. 537 3
.799 2

/ 1

/ 2013 

## 18 :07 :00 1 4
. 539 3
.796 2

/ 1

/ 2013 

## 18 : 08:00 14
. 541 3
.795 2

/ 1/20 1 3 

## 18 :09:00 14
. 53 3
. 8 2

/ 1

/ 2013 

## 18 : 10:00 14
.54 3
. 793 2/1 / 2013 

## 18:11 :00 14
.529 3
.798 2

/ 1/2013 

## 18 : 12:00 14
.543 3
.789 2

/ 1

/ 2013 

## 18:13 :00 14
.55 3
.782 2/1/ 2013 

## 18:14 :00 1 4
. 551 3.779 2

/ 1

/ 2013 

## 18:15 :00 14
. 552 3
.776 2/ 1 / 2013 

## 18:16:00 14
. 552 3
.776 2/ 1 / 2013 

## 18:17:00 14
. 538 3
.784

Average 

## 14.42 4
.01

### Test 

## # : Date : Time : Load : CPV SENTINEL UNIT 2 PARTICULATE TEST STACK O2 • 

### CO 2 

### DATA

S
-2/STK-PM
-75-1 2/1/2013 

### 8:11 13 : 22 80MW O 2 

### Range 20 Cal Gas 9
. 98 Ana lyzer Zero 0 .1 0 Anal yze r Span 10
. 1 9 Pre-B ia s Z ero 0
. 12 Pre - Bias Span 10
. 04 Post- Bias Zero 0
.20 Post- Bias Span 10
. 12 Average B ias Zero 0
. 16 Average Bias Span 10
. 08 P re -test z ero b ias 0
. 1 % P re -test span b i as -0
. 8 % Pos t-test zero bias 0
.5 % Post-test span b ias -0.4 % Zero Drift 0.4 % Span D rift 0.4 % CO 2 

### 10 4
. 96

- 0
. 02 5
. 05 0
. 03 5
. 08 0
.25 5
. 32 0
. 14 5
.20 0
.5 % 0
. 3 % 2
. 6 % 2
. 7 % 2 .2 % 2.4% T est R esults (from data l o gg e r av e rage) Average 13
. 43 4.4 9 Cal C o rrect ed 13.35 4.2 6

O 2 

### CO 2 

### Date Time % % 2/1/ 2013 

### 8 :25 : 00 1 3. 431 4
. 306 2/1/ 2013 

### 8:26 : 00 1 3. 474 4
.292 2/1/ 2013 

### 8:27:00 1 3 .496 4
.287 2/1/ 2013 

### 8 :28 : 00 13.478 4
. 304 2

/ 1

/ 2013 

### 8 : 29 : 00 13.427 4
. 339 2/ 1 / 201 3 

### 8 : 30 : 00 13.422 4
. 346 2/1/ 2013 

### 8 : 31 : 00 1 3.3 63 4
. 385 2/ 1 / 2013 

### 8 : 3 2: 00 13
. 377 4
. 38 2/1 / 2013 

### 8 : 33:00 1 3.307 4.421 2/1 / 20 1 3 

### 8 : 34 : 00 13
. 333 4 .412

### 2/1/2013 

## 8:35:00 13
. 319 4.425 2/1/2013 

## 8 :40:00 13
.268 4.428 2/1/2013 

## 8 :41 :00 13.298 4.445 2/1/ 2013 

## 8 :42 :00 13.307 4.45 2

/ 1/2013 

## 8 :43:00 13
. 319 4.452 2/1/ 2013 

## 8 :44 :00 13
. 314 4.459 2/1/2013 

## 8 :45:00 13
. 329 4.458 2/1/2013 

## 8 :46:00 13
. 336 4.457 2/1/ 2013 

## 8 :47:00 13
. 343 4.459 2/1/2013 

## 8 :48:00 13
. 344 4.463 2/1/2013 

## 8 :49:00 13
. 349 4.466 2/1/ 2013 

## 8 : 50:00 13
. 353 4.467 2/1/2013 

## 8 : 51 :00 13.366 4.466 2/1/2013 

## 8 : 52 :00 13
. 366 4.469 2/1/2013 

## 8 : 53:00 13.37 4
.47 2/1/ 2013 

## 8 : 54:00 13
. 37 4
.473 2/1/ 2013 

## 8 : 55 :00 13.372 4.476 2/1/2013 

## 8 : 56:00 13.38 4.472 2/1 / 2013 

## 8 : 57:00 13
. 39 4.466 2/1/2013 

## 8 : 58:00 13.4 4.463 2/1/ 2013 

## 8 : 59 :00 13.404 4.462 2

/ 1/2013 

## 9 : 00 :00 13.403 4.463 2/1/ 2013 

## 9:01 :00 13.411 4.462 2/1/2013 

## 9 : 02 :00 13.418 4.458 2/1/2013 

## 9 : 03:00 13.413 4.461 2/1/2013 

## 9 :04 :00 13.413 4.464 2/1/ 2013 

## 9 : 05:00 13.425 4.456 2/1 / 2013 

## 9 : 06:00 13.429 4.454 2/1/2013 

## 9:07:00 13.432 4.448 2/1/ 2013 

## 9 :08:00 13.437 4.448 2/1/2013 

## 9 :09 :00 13.43 4.452 2/1 / 2013 

## 9 : 10:00 13.432 4.453 2/1/2013 

## 9:11:00 13.438 4.451 2

/ 1/2013 

## 9:12:00 13.45 4.449 2/1/2013 

## 9:13:00 13
.437 4.455 2/1/2013 

## 9:14:00 13.445 4.453 2/1 / 2013 

## 9:15 :00 13.45 4.453 2/1/2013 

## 9:16 :00 13.476 4.445 2/1/2013 

## 9 : 17:00 13.486 4.443 2/1/2013 

## 9:18 : 00 13.492 4.441 2

/ 1

/ 2013 

## 9 : 19 : 00 13.493 4
.444 2

/ 1

/ 2013 

## 9 :20 :00 13.494 4.445 2

/ 1/ 2013 

## 9 :21 :00 13.482 4.451 2/1/2013 

## 9 : 22 :00 13.483 4.454 2/1 / 2013 

## 9 :23 : 00 13.478 4.457 2

/ 1

/ 2013 

## 9:24 : 00 13.468 4.461 2/1 / 2013 

## 9 :25 :00 13.471 4.461 2/1/ 2013 

## 9 :28 :00 13
. 626 4
. 359 2/1/ 2013 

## 9 :29 :00 13.624 4
. 357 2/ 1/2013 

## 9 :30:00 13
. 627 4
.356 2/1/ 2013 

## 9 : 31 :00 13
. 64 4
. 348 2/1/ 2013 

## 9 :32:00 13 .6 3 4
. 351

### 2/1/2013 

## 9 : 33 :00 13
. 521 4.419 2/1/2013 

## 9 : 34:00 13.492 4.436 2

/ 1/2013 

## 9:35 :00 13.497 4.432 2/1/2013 

## 9:36 :00 13.467 4.449 2/1 / 2013 

## 9 : 37 :00 13.436 4.462 2

/ 1/2013 

## 9 : 38 :00 13.427 4.472 2

/ 1

/ 2013 

## 9 : 39 :00 13.43 4.471 2/1/2013 

## 9 :40 :00 13.43 4.468 2

/ 1

/ 2013 

## 9:41 :00 13.427 4.471 2/1 / 2013 

## 9 :42: 00 13.428 4.471 2/1/2013 

## 9 :45 :00 13.463 4.449 2

/ 1

/ 2013 

## 9 :4 6 :00 13.473 4.446 2/1 / 2013 

## 9:47:00 13.491 4.435 2/1/2013 

## 9:48:00 13.508 4.426 2

/ 1

/ 2013 

## 9 :49 :00 13.497 4.428 2

/1/ 2013 

## 9 : 50 :00 13.449 4.462 2/1/2013 

## 9 : 51 : 00 13.421 4.482 2/1/2013 

## 9 : 52 : 00 13
.414 4.485 2

/ 1

/ 2013 

## 9 : 53 :00 13.406 4.491 2/1/2013 

## 9 : 54 : 00 13.417 4.484 2/1/2013 

## 9 : 55 :00 13.424 4.479 2/1/2013 

## 9 : 56 :00 13.448 4.463 2/1/2013 

## 9 : 57 : 00 13.429 4.475 2/1/2013 

## 9 : 58 :00 13.424 4.48 2/1/2013 

## 9:59:00 13.422 4.484 2/1/ 2013 

## 10:19:00 13.489 4.479 2/1/2013 

## 10 :20 : 00 13.492 4.48 2/1/2013 

## 10:21 :00 13.493 4.483 2/1/2013 

## 10:22:00 13.477 4.489 2/1/2013 

## 10:23:00 13.475 4.492 2/1/2013 

## 10:24:00 13.478 4.489 2/1/2013 

## 10:25 : 00 13.475 4.488 2

/ 1/2013 

## 10:26:00 13.49 4.479 2/1/2013 

## 10:27:00 13.488 4.481 2/1/2013 

## 10:28:00 13.49 4.481 2/1/2013 

## 10 : 29 :00 13.499 4.477 2/1/2013 

## 10:30:00 13.487 4.482 2/1 /2 013 

## 10 :3 1 : 00 13.479 4.488 2/1/2013 

## 10 :32: 00 13.468 4.499 2/1/2013 

## 10:33:00 13.473 4.496 2/1/ 2013 

## 10:34:00 13.469 4.497 2/1/ 2013 

## 10 : 35:00 13.474 4.493 2/1/2013 

## 10 : 36:00 13.059 4
. 287 2

/1/ 2013 

## 11 : 05 : 00 13.44 4
.505 2/1/2013 

## 11 :06 :00 13.44 4.505 2

/ 1/2013 

## 11 :07:00 13.433 4
.516 2

/ 1

/ 2013 

## 11 :08:00 13.432 4
.519 2/1/ 2013 

## 11 :09:00 13.44 4.512 2/1/2013 

## 11:10:00 13.45 4.51 2/1/2013 

## 11:11 : 00 13.441 4
. 515 2/1/2013 

## 11 : 12:00 13.438 4.517

### 2/1 / 2013 

## 11 : 13 : 00 13.445 4.513 2/1/2013 

## 11:14:00 13.452 4.513 2

/1/ 2013 

## 11:15 :00 13.45 4 .5 15 2/1/2013 

## 11:16:00 13.444 4.52 2/1/2013 

## 11:17 :00 13.437 4
.524 2

/1/ 2013 

## 11:18:00 13.44 4.522 2

/ 1

/ 2013 

## 11 :19: 00 13.437 4.521 2/1/2013 

## 11 :20:00 13.438 4.521 2

/ 1

/ 2013 

## 11 :23:00 13.423 4 .5 31 2/1/2013 11 

## :24:00 13.425 4.532 2/1/2013 

## 11 :25:00 13.418 4.537 2/1/2013 

## 11 :2 6 :00 13.416 4
. 537 2/1/2013 

## 11 :27 :00 13.41 4 .5 43 2/1/2013 

## 11 :28:00 13.406 4.545 2/1/ 2013 

## 11 :29:00 13.405 4
. 547 2/1/2013 

## 11 : 30 :00 13.404 4
. 545 2/1 / 2013 

## 11 :3 1 :00 13.407 4
. 541 2/1/2013 

## 11 :3 2 :00 13.418 4
. 534 2/1/2013 

## 11 :3 3 :00 13.409 4
. 541 2/1/2013 

## 11 :3 4 :00 13.405 4.543 2/1/2013 

## 11 :3 5 :00 13.407 4
. 543 2

/1/ 2013 

## 11 :36:00 13.412 4
. 543 2/1/2013 

## 11 :3 7:00 13.413 4
. 543 2

/ 1

/ 2013 

## 11 :3 8 :00 13.41 4 .5 46 2/1 / 2013 

## 11 :41 :00 13.433 4
. 53 2/1/2013 

## 11 :42 : 00 13.423 4.542 2/1/2013 

## 11 :4 3 :00 13.428 4
.537 2/1/20 13 

## 11 :44:00 13.423 4
.543 2/1 / 2013 

## 11 :45:00 13.422 4 .5 46 2/1/2013 

## 11 :46 :00 13
.428 4 .5 39 2/1/2013 

## 11:47 : 00 13
.427 4.539 2/1/2013 

## 11 :48 : 00 13.43 4
.539 2/1/2013 

## 11 :4 9:00 13.431 4
.539 2/1/2013 

## 11 :50 : 00 13.434 4
. 541 2/1/2013 

## 11 :51 :00 13.429 4.543 2/1/2013 

## 11 : 52 : 00 13.428 4
.547 2/1/ 2013 11 

## :53 : 00 13.424 4
.552 2/1/2013 

## 11 :54:00 13.417 4
.561 2/1/2013 

## 11 :55:00 13.413 4
. 567 2/1/2013 

## 11 : 56 : 00 13
.411 4
.57 2/1/2013 

## 11 : 57 : 00 13.407 4
. 571 2/1/2013 

## 12 : 00 : 00 13.407 4
. 571 2/1/2013 

## 12:01 : 00 13
. 391 4 .5 82 2

/ 1/ 2013 

## 12:02:00 13.392 4
.587 2/1/2013 

## 12:03 : 00 13.401 4.583 2

/ 1

/ 2013 

## 12:04 :00 13.381 4
. 595 2/1 / 2013 

## 12 : 05 : 00 13.387 4
. 594 2/1/2013 

## 12:06 :00 13
. 382 4
. 602 2/1/2013 

## 12 : 07:00 13
. 36 4
. 615 2/1/ 2013 

## 12:08 :00 13
. 365 4.614 2/1/2013 

## 12 :09 :00 13
. 378 4 .61

### 2/1/2013 

## 12:10:00 13.372 4.615 2/1/2013 

## 12:11:00 13
. 384 4.605 2/1/2013 

## 12:12:00 13.381 4.608 2/1/2013 

## 12:13:00 13.391 4.6 2/1/2013 

## 12 : 14:00 13.394 4.602 2/1/2013 

## 12:15:00 13.39 4.608

Average 

## 13.43 4.49

### Test 

## #: Date : Time: Load: CPV SENTINEL UNIT 2 PARTICULATE TEST STACK 

### 02. CO 

### 2 DATA

S-2/STK-PM-100-1 1/30/2013 

### 9 : 26 13 : 34 103MW O 2 

### Range 20 Cal Gas 9 .9 8 A n alyzer Zero 0
. 1 2 Anal yzer Span 10
. 10 Pre-Bias Zero 0
. 13 Pre-Bias Span 9
. 98 Post- B ias Zero 0
. 12 Post-B ias Span 9
. 96 Average Bias Zero 0
. 12 Average B ias Span 9.97 Pre -tes t zero bias 0 .1% Pre- test span bias -0
. 6 % Post-te st zero bias 0.0 % Post-test s pan bias - 0
. 7 % Zero Drift 0
. 0 % Span Drift -0
. 1 % CO 2 

### 10 4
. 96

-0
. 02 5
. 02 -0
.01 5
. 05 0 .2 4 5
.38 0
. 12 5
.21 0
. 2% 0
. 3% 2
. 6 % 3. 6 % 2
. 5% 3.3 % Test Results (from data logger average) Average 13.02 4
. 66 Cal Corrected 13
. 07 4
. 42

O 2 

### CO 2 

### Date T i me % % 1/30 / 201 3 

### 9 : 30 : 00 13 .1 04 4
.543 1/

30

/ 20 13 

### 9 : 31 : 00 13
. 103 4
.544 1 / 30/ 201 3 

### 9 : 32 : 00 13
. 106 4
.542 1 / 30

/ 2013 

### 9:33 : 00 13
. 103 4
.544 1/

30

/ 2013 

### 9 : 34:00 13
. 082 4
. 552 1/

30

/ 2013 

### 9 :3 5 : 00 13
. 082 4.554 1/

30 / 2013 

### 9 : 36 : 00 13.083 4
. 552 1/

30/ 20 13 

### 9 : 37 : 00 13.08 4
.555 1/

30

/ 2013 

### 9 : 38 : 00 1 3
. 073 4
.56 1 / 30

/ 2013 

### 9 : 39 : 00 1 3. 057 4. 568

### 1/ 30/2013 

## 9 :40:00 13
.061 4
.563 1 / 30 / 2013 

## 9 :41 :00 13
.057 4
.566 1/

30 / 2013 

## 9:42 :00 13
. 057 4
.566 1/30/2013 

## 9:43 :00 13
.057 4.565 1/

30 / 2013 

## 9 :44 :00 13.05 4
.571 1/

30 / 2013 

## 9 :45 :00 13
.054 4
. 567 1/

30

/ 2013 

## 9 :46 : 00 13.055 4.563 1/

30/2013 

## 9:47 :00 13
.048 4.565 1/

30 / 2013 

## 9 :48 : 00 13
. 056 4
.559 1/30 / 2013 

## 9:49 : 00 13
.04 4
. 565 1 / 30

/ 2013 

## 9:50 :00 13
.052 4
. 559 1/

30

/ 2013 

## 9 :51 : 00 13
.037 4
. 566 1/

30

/ 2013 

## 9:52:00 13
.037 4
. 566 1 / 30

/ 2013 

## 9:53 :00 13
.03 4
.568 1 / 30/2013 

## 9:54:00 13
.044 4
. 565 1 / 30

/ 2013 

## 9 : 55:00 13
.044 4
. 569 1/

30

/ 2013 

## 9 : 56 :00 13
.056 4
.567 1 / 30

/ 2013 

## 9 : 57 :00 13
.063 4
.571 1 / 30/2013 

## 9 : 58:00 13
.079 4
. 57 1/

30

/ 2013 

## 9 : 59 :00 13.077 4
.579 1/30 / 2013 

## 10 :00 : 00 13
. 1 4
.575 1 / 30

/ 2013 

## 10:01 :00 13
. 114 4.574 1 / 30/2013 

## 10 :02 :00 13
. 119 4
.577 1 / 30

/ 2013 

## 10 :03 : 00 13
. 126 4
. 58 1 / 30

/ 2013 

## 10:04 :00 13
. 139 4
. 576 1 / 30

/ 2013 

## 10:05 :00 13.133 4.578 1 / 30

/ 2013 

## 10:06 : 00 13
. 127 4
.578 1 / 30

/ 2013 

## 10 :07 :00 13
. 113 4
. 583 1 / 30

/ 2013 

## 10:08 :00 13
. 118 4
.576 1 / 30/2013 

## 10 :09 :00 13
.086 4
. 589 1 / 30

/ 2013 

## 10:10 :00 13
.06 4
. 6 1/

30

/ 2013 

## 10 : 11:00 13
.054 4
. 6 1 / 30

/ 2013 

## 10 : 12 :00 13
. 051 4
. 6 1 / 30/2013 

## 10:13 :00 13
.036 4
. 604 1 / 30

/ 2013 

## 10 : 14:00 13
.019 4
. 606 1 / 30

/ 2013 

## 10 : 15:00 13
.04 4
. 601 1 / 30/2013 

## 10:16:00 13
.046 4.603 1 / 30

/ 2013 

## 10 : 17 :00 13.058 4
. 612 1 / 30

/ 2013 

## 10:18 :00 13
. 097 4
. 611 1/

30/ 2013 

## 10 : 19 :00 13
. 118 4
. 614 1 / 30/2013 

## 10 :20:00 13
. 125 4
. 626 1 / 30

/ 2013 

## 10:21 :00 13
. 138 4
. 629 1 / 30

/ 2013 

## 10 :22:00 13
. 14 4
. 636 1 / 30

/ 2013 

## 10 :23 :00 13
. 143 4
. 639 1 / 30/2013 

## 10:24:00 13
. 151 4
. 638 1 / 30

/ 2013 

## 10:25:00 13
. 16 4
. 637 1 / 30

/ 2013 

## 10:26 :00 13
. 175 4.638 1 / 30

/ 2013 

## 10:27:00 13
. 173 4
. 645 1 / 30

/ 2013 

## 10:28 :00 13
. 186 4
. 643 1/

30

/ 2013 

## 10 : 29:00 13
. 192 4
. 646 1/30 / 2013 

## 10 :30 :00 13
.204 4
. 643 1 / 30

/ 2013 

## 10 :31 :00 13
.204 4
. 645 1/

30

/ 2013 

## 10:32 : 00 13
.206 4
. 648 1/3 0 / 2013 

## 10:33 : 00 13
. 191 4
. 658

### 1 / 30/2013 

## 10 :34 :00 13.191 4
. 657 1 / 30

/ 2013 

## 10:35:00 13
. 188 4
. 66 1/

30/ 2013 

## 10:36 : 00 13
. 198 4
. 655 1/

30/2013 

## 10 : 56 :00 13
.099 4
. 641 1/

30 / 2013 

## 10 : 57:00 13
.096 4
. 651 1/

30 / 2013 

## 10 : 58 :00 13.104 4
. 65 1/30/2013 

## 10 : 59:00 13
. 092 4
. 654 1/30 / 2013 

## 11 : 00 :00 13
. 112 4
. 644 1/30 / 2013 

## 11 : 01 :00 13
. 111 4
. 644 1/

30/2013 

## 11 :02 :00 13
. 108 4
. 644 1/

30 / 2013 

## 11 :03:00 13
. 088 4
. 65 1/

30 / 2013 

## 11 : 04 :00 13
.09 1 4
. 646 1/

30

/ 2013 

## 11 :05 :00 13
.089 4
. 647 1/

30/2013 

## 11 : 06:00 13.081 4.653 1/30/2013 

## 11 :07 :00 13
.074 4
. 655 1/

30

/ 2013 

## 1 1 :08 :00 13
.091 4
. 644 1/30 / 2013 

## 11 :09 : 00 13.089 4.643 1/30/2013 

## 11 :10 : 00 1 3.092 4
. 643 1/

30

/ 2013 

## 11 : 11 : 00 13.088 4
. 646 1/

30

/ 2013 

## 11 : 12 : 00 13
.089 4
. 644 1 / 30

/ 2013 

## 11:13 :00 13
.094 4
. 641 1/30/2013 

## 11:14:00 13.106 4.635 1/

30

/ 2013 

## 11:15 :00 13
. 102 4
. 636 1/

30

/ 2013 

## 11 : 16 :00 13
.093 4
. 639 1 / 30/ 2013 

## 11 : 18 :00 13
. 137 4 .642 1 / 30/ 2013 

## 11:19:00 13
.094 4
. 64 1/

30/ 2013 

## 11 :20 :00 13.044 4
. 666 1/30/2013 

## 11 :21 :00 13.088 4
. 642 1/

30 / 2013 

## 11 :22:00 13
.087 4
. 64 1/

30 / 2013 

## 11 :23 :00 13
.088 4
. 642 1/

30/2013 

## 11 :24 : 00 13
.087 4
. 65 1/

30/ 2013 

## 11 :25 :00 13
.087 4
. 655 1/

30 / 2013 

## 11 :26 :00 13
.098 4
. 655 1/

30 / 2013 

## 11 :27 :00 13.095 4
. 662 1/

30

/ 2013 

## 11 :28 :00 13.102 4.663 1/

30 / 2013 

## 11 :29 :00 13.11 4
. 659 1/

30 / 2013 

## 11 : 30:00 13
.096 4
. 664 1/

30 / 2013 

## 11 : 31 :00 13
. 104 4
. 657 1/30/2013 

## 11 : 32 :00 13
.091 4
. 66 1/

30

/ 2013 

## 11 : 33 :00 13
.087 4
. 659 1/30 / 2013 

## 11 : 34 :00 13
.071 4
. 667 1/

30

/ 2013 

## 11 : 35 : 00 13
.061 4.668 1/

30

/ 2013 

## 11 : 36 :00 13
.052 4
. 671 1/

30 / 2013 

## 11 :37 : 00 13
.043 4
. 67 1/

30/2013 

## 11 : 38 :00 13
.017 4
. 675 1/

30 / 2013 

## 11 : 39 : 00 13
.013 4.676 1/

30 / 2013 

## 11 :40 :00 13
.016 4
. 665 1/

30

/ 2013 

## 11 :41 :00 13.008 4
. 676 1/

30/2013 

## 11 :44 :00 13
.066 4.659 1/

30 / 2013 

## 11 :45:00 13
.063 4
. 664 1 /

30

/ 2013 

## 11 :46 : 00 13.058 4.666

### 1/ 30

/ 2013 

## 11 :47 :00 13
.051 4
. 668 1 / 30/ 2013 

## 11 :48:00 13.061 4
. 66 1/

30 / 2013 

## 11 :49 :00 13
.062 4
. 661 1/

30 / 2013 11 

## : 50 :00 13
.064 4.657 1/

30 / 2013 

## 11 : 51 :00 13
.06 4
. 66 1/

30 / 2013 11 

## : 52:00 13
.058 4.658 1/30 / 2013 11 

## : 53:00 13
.051 4
. 656 1/

30

/ 2013 11 

## : 54 :00 13
.033 4
. 656 1/

30 / 2013 11 

## : 55:00 13
.012 4.658 1/

30 / 2013 11 

## : 56:00 12
.99 4
. 667 1/

30

/ 2013 11 

## :57 :00 12
.982 4
. 668 1/

30 / 2013 11 

## : 58 :00 12
.979 4
. 662 1/

30

/ 2013 11 

## : 59 :00 12
. 975 4
. 661 1/

30 / 2013 

## 12 :00:00 12
.956 4
. 666 1 / 30

/ 2013 

## 12 : 02:00 13
.008 4.664 1/

30 / 2013 

## 12 :03 :00 12
. 921 4.67 1/

30

/ 2013 

## 12 :04 :00 12
.915 4
.673 1/30 / 2013 

## 12 : 05 :00 12
. 922 4
. 666 1 / 30

/ 2013 

## 12 : 06 :00 12
.919 4.666 1/

30

/ 2013 

## 12 :07 :00 12
. 909 4.671 1/

30

/ 2013 

## 12 :08 :00 12
.907 4
. 672 1/

30 / 2013 

## 12 : 09 : 00 12
. 898 4
. 679 1/

30

/ 2013 

## 12 : 10 : 00 12
.905 4
. 677 1130 / 2013 

## 12 : 11 :00 12
. 891 4.688 1 / 30/2013 

## 12 : 12 :00 12
. 892 4.687 1/

30 / 2013 

## 12 : 13 : 00 12
. 897 4.682 1/

30

/ 2013 

## 12 : 14 :00 12
. 886 4
. 694 1/

30

/ 2013 

## 12:15 :00 12
. 886 4.691 1/

30/ 2013 

## 12:16 :00 12
. 881 4.696 1 / 30

/ 2013 

## 12:17 : 00 12.877 4
. 696 1/30 / 2013 

## 12:46 :00 12
. 873 4
.706 1 / 30/2013 

## 1 2 :47 :00 12.905 4
.708 1 / 30

/ 2013 

## 12 :48 :00 12
. 894 4.717 1 / 30/2013 

## 12:49 :00 12.887 4.726 1 / 30

/ 2013 

## 12 : 50 :00 12
. 891 4
.722 1 / 30

/ 2013 

## 12 :51 :00 12
. 889 4
.725 1 / 30

/ 2013 

## 12 :52 :00 12
. 887 4
. 726 1 / 30

/ 2013 

## 12 :53 : 00 12
. 886 4.729 1 / 30/2013 

## 12 :54 :00 12
. 889 4
.726 1/

30

/ 2013 

## 12 : 55 :00 12
. 893 4.728 1/

30

/ 2013 

## 12 : 56 : 00 12
. 894 4
.728 1/

30

/ 2013 

## 12 : 57 : 00 12
. 891 4.737 1/

30

/ 2013 

## 12 : 58:00 12
. 893 4.736 1/30 / 2013 

## 12 : 59 : 00 12
. 894 4.74 1/

30

/ 2013 

## 13 : 00 :00 12
. 892 4
.741 1/

30

/ 2013 

## 13 : 01 :00 12
. 869 4
.744 1/

30

/ 2013 

## 13 : 02:00 12
. 867 4.742 1/

30

/ 2013 

## 13 :03 :00 12
. 862 4.749 1/30 / 2013 

## 13 : 04:00 12
. 859 4.751 1/

30 / 2013 

## 13 :05 :00 12
. 865 4.75 1/

30 / 2013 

## 13 :06 :00 12
. 852 4
. 76 1/

30

/ 2013 

## 13:07:00 12
. 848 4.764

### 1 / 30

/ 2013 

## 13 : 08 :00 12
. 858 4
.759 1/

30/2013 

## 13 :09 : 00 1 2
. 871 4
. 756 1/

30/ 2013 

## 13 : 10 : 00 12
. 878 4
.755 1/

30 / 2013 

## 13 : 1 1 :00 12
. 865 4
.765 1 / 30

/ 2013 

## 13 : 12 : 00 12
. 873 4
. 763 1/30 / 2013 

## 13 : 13 : 00 12
. 879 4
.762 1/

30 / 2013 

## 13 : 14 : 00 12
. 862 4.775 1/

30/2013 

## 13 : 15 : 00 12
. 872 4.772 1 / 30 / 2013 

## 13 : 16 : 00 12
. 881 4
. 77 1/

30 / 2013 

## 13 : 17 :00 12
. 877 4
.775 1/

30

/ 2013 

## 13 : 18 :00 12.868 4.782 1/

30 / 2013 

## 13 : 19 : 00 12
. 868 4
.784 1/

30 / 2013 

## 13 :20 : 00 1 2
. 863 4
.787 1/

30 / 2013 

## 13 :21 :00 12
. 871 4
. 785 1/

30/2013 

## 13 :22 : 00 12
. 885 4
. 78 1 / 30 / 2013 

## 13 : 23 :00 12
. 886 4.776 1 /30/ 2013 

## 13 : 24 : 00 1 2
. 882 4
.784 1/

30/ 2013 

## 13 :25 :00 1 2
. 868 4
.795 1/

30 / 2013 

## 13 : 26 : 00 12
. 88 4
.789 1/30 / 2013 

## 13 :2 9 :00 12
.915 4
.762 1/

30 / 2013 

## 13 :30 : 00 12
. 885 4
. 796 1/

30 / 2013 

## 13 :31 : 00 12
. 886 4
.795 1/

30 / 2013 

## 13 : 32 :00 12
. 889 4
.787 1/

30 / 2013 

## 13 :33 :00 12
. 891 4
.789 1 / 30/2013 

## 13 :34 :00 12.886 4.795

Average 

## 13
.02 4
. 66

### CPV SENTINEL UNIT 2 PARTICULATE TEST STACK O2 • 

### CO 2 

### DATA Test 

## #: S-2/STK-PM-100-2 Date: 1/30/2013 

### Time: 13 : 45 17:51 Load : 100 MW O 2 

### CO 2 

### Range 20 10 Cal Gas 9
. 98 4
. 96 Analyzer Zero 0.12 -0
. 02 Analyzer Span 10
. 10 5
. 02 Pre-Bias Zero 0
. 12 0.24 Pre-Bias Span 9
. 96 5
.38 Post-B ias Zero 0
. 13 0 .1 6 Post-B ias Span 9
. 96 5
.26 Average Bias Zero 0
. 13 0.20 Average Bias Span 9.96 5
.32 Pre-test zero bias 0
. 0 % 2
. 6% Pre-test span b ias -0
. 7 % 3
. 6% Post-test zero b ias 0
. 1 % 1
. 9 % Post-test span bias -0
. 7 % 2.4 % Zero Drift 0.0% -0.8% Span Drift 0.0 % -1.2% Test Results (from data logger average) Average 13
. 18 4
. 67 Cal Corrected 13
. 24 4.34

O 2 

### CO 2 

### Date Time % % 1/

30

/ 2013 

### 13:48 : 00 13
. 322 4.544 1/

30/2013 

### 13 : 49:00 13
. 306 4.552 1/

30

/ 2013 

### 13:50 : 00 13
. 633 4
. 355 1/30/2013 

### 13 : 51 :00 15.063 3.487 1/30/2013 

### 13 : 52:00 15.99 2
. 948 1/

30

/ 2013 

### 13 : 53 : 00 14
. 969 3.572 1/

30

/ 2013 

### 13 : 54 : 00 14.009 4
. 142 1/

30

/ 201 3 

### 13:55:00 13
. 798 4.268 1/30 / 20 1 3 

### 13 : 56:00 13
. 802 4
.262 1/

30

/ 2013 

### 13 : 57:00 13
. 798 4.269

### 1 / 30/2013 

## 13 :58:00 13
.794 4
.275 1/

30 / 2013 

## 13 :59 :00 13.795 4
.277 1 / 30 / 2013 

## 1 4 :00 :00 13
.796 4
.275 1/

30/2013 

## 14 :01 :00 13.78 4
.281 1/

30/2013 

## 14 :02 :00 13
.768 4
.284 1 / 30

/ 2013 

## 14 :03 :00 13
.753 4
.289 1/

30 / 2013 

## 14:04 :00 13.75 4.293 1/30/2013 

## 14 :05:00 13.754 4.287 1/

30 / 2013 

## 14:06 :00 13
.755 4.286 1/

30

/ 2013 

## 14:07 : 00 13
. 755 4
.284 1/

30 / 2013 

## 14 :08 :00 13
. 812 4
.247 1/

30

/ 2013 

## 14:09 : 00 14
. 618 3
.757 1/

30 / 2013 

## 14 : 10 :00 15
. 595 3.176 1/

30 / 2013 

## 14:11 : 00 15
.515 3
.233 1/30/2013 

## 14:12 :00 14
.527 3
. 832 1/

30/2013 

## 14:13 :00 13
. 551 4.417 1/

30

/ 2013 

## 14:14:00 13
. 312 4
. 553 1/

30 1 2013 

## 14:15:00 13
. 31 4
. 555 1130/2013 

## 14 : 16 :00 13
. 328 4
. 547 1/

30

/ 2013 

## 14 : 17 : 00 13
. 324 4
. 551 1 / 30 1 2013 

## 14 : 18:00 13
. 332 4
.547 1 / 30

/ 2013 

## 14 : 19 :00 13.305 4.567 1/30 / 2013 

## 14 :20:00 13
. 324 4
.559 1/

30 1 2013 

## 14 : 21 :00 13
.036 4
. 74 1 1

30 1 2013 14 :22 :00 12
. 956 4
. 79 1/30/2013 

## 14 : 23:00 12
.955 4
.791 1 / 30 1 2013 

## 14 :24 :00 12
.95 4.795 1/

30/2013 

## 14 :25 :00 12
.944 4
. 8 1/

30 / 2013 

## 14 :26 :00 12
. 957 4
. 795 1 1

30/2013 

## 14:27 : 00 12
.96 4
.797 1 1

30 1 2013 14:28 :00 12
.961 4
. 795 1 1

30 1 2013 14:29 :00 12
.95 4
. 806 1 1

30

/ 2013 

## 14:30 :00 12
. 95 4.809 1/

30/2013 

## 14:31 :00 12
.958 4
. 806 1/

30 1 2013 

## 14:32 : 00 12
.96 4
. 806 1 1

30 1 20 1 3 14:33 :00 12
.964 4
. 806 1/

30 1 2013 

## 14 :34 :00 12
.97 4
. 803 1/

30 / 2013 

## 14:35 :00 12
. 969 4
. 805 1 / 30 / 2013 

## 14:36:00 12
.984 4
.798 1 1

30 1 2013 14 :37 : 00 12
.979 4
. 804 113012013 14:38 :00 12.971 4.81 1/

30 1 2013 

## 14 :39 :00 12
. 969 4
. 813 1 1

30 1 2013 14:40 :00 12
.98 4
. 807 1 1

3012013 14:41 :00 12
. 974 4
. 812 1/

30/2013 

## 14:42 :00 12.973 4
. 815 1/

30

/ 2013 

## 14 :43 :00 12
.969 4
. 82 1/

30

/ 2013 

## 14:49 :00 13.022 4.797 1/

30 / 2013 

## 14 :50 :00 12
.985 4
. 812 1 1

30 1 2013 14 : 51 :00 12
.979 4
. 819 1/

30

/ 2013 

## 14:52 :00 12
.981 4
. 819 1 1

30/2013 

## 14:53 : 00 12
.981 4
. 818 1 1

30 1 2013 14:54:00 12
.978 4
. 822 1/

30 / 2013 

## 14 : 55 :00 12
.98 4
. 822

### 1/30/2013 

## 14 : 56 : 00 12
.989 4
. 816 1 / 30/2013 

## 14:57:00 12
.983 4
. 823 1/30/2013 

## 14:58:00 12.979 4.823 1/30/2013 

## 14 : 59:00 12.982 4.823 1/30/2013 

## 15 :00:00 12.993 4
. 817 1/

30/2013 

## 15:01 :00 12
. 994 4
. 817 1/30 / 2013 

## 15 :02:00 12.996 4
. 816 1/30 / 2013 

## 15:03 :00 12.993 4
. 819 1/30 / 2013 

## 15 :04 :00 12
.996 4
. 816 1/30/2013 

## 15 :05 :00 12.996 4.816 1/30/2013 

## 15:29:00 12
.999 4.818 1/

30/2013 

## 15 :30:00 12
.985 4.829 1/

30

/ 2013 

## 15 :31 : 00 12 .9 86 4.832 1/

30

/ 2013 

## 15 :32 :00 12.986 4.834 1/30 / 2013 

## 15:33:00 12.975 4.841 1/30/2013 

## 15:34 :00 12.974 4
. 845 1/30/2013 

## 15:35 :00 12
.983 4.839 1/30/2013 

## 15:36:00 12.971 4
. 847 1/30/2013 

## 15 :37:00 12
.963 4
. 855 1/

30/2013 

## 15:38:00 12.973 4
. 85 1/

30 / 2013 

## 15 :39:00 12
.964 4.856 1/30/2013 

## 15:40:00 12.964 4.857 1/3 0/2013 

## 15:41 : 00 12
. 963 4
. 856 1/30/2013 

## 15 :42 :00 12
.957 4
. 862 1 /30/2013 

## 15 :43:00 1 2
.954 4
. 863 1/30/2013 

## 15 :44:00 12
.962 4.858 1 / 30

/ 2013 

## 15:45 : 00 12
.959 4
. 861 1 / 30

/ 2013 

## 15:46:00 12
. 962 4
. 859 1/30/2013 

## 15:47:00 12
.952 4
. 863 1/30/2013 

## 15:48:00 12.965 4
. 855 1/30/2013 

## 15 :49:00 12 .9 57 4.864 1/30/2013 

## 15:50:00 12
. 969 4.852 1/30/2013 

## 15:51 :00 1 2
.958 4
. 858 1/3 0/2013 

## 15:52:00 12.978 4.841 1/30 / 2013 

## 15 : 53 : 00 12
.992 4
. 834 1/30 / 2013 

## 15:54 :00 12
.98 4.843 1/3 0/2013 

## 15:57:00 12.991 4.832 1/30/2013 

## 15:58 : 00 12.988 4.834 1/30/2013 

## 15 :59 :00 12
.976 4.842 1/30/2013 

## 16:00 : 00 12
.986 4.836 1/30/2013 

## 16:01 :00 12
.996 4
. 83 1/30/2013 

## 16 : 02:00 13.008 4
. 824 1/

30/ 2013 

## 16 :03 :00 13.009 4.82 1/30/2013 

## 16 :04:00 13
.007 4
. 819 1/

30/2013 

## 16 :05:00 13
.024 4
. 806 1/30/2013 

## 16 :08:00 13
. 003 4
. 813 1/30 / 2013 

## 16 :09:00 13.001 4
. 815 1 / 30

/ 2013 

## 16:10:00 13
.01 4
. 804 1/30 / 2013 

## 16:11:00 13
.009 4.806 1/30 / 2013 

## 16:12:00 13.009 4.804 1 /3 0/2013 

## 16 : 13:00 12 .9 91 4
. 816

### 1 / 30

/ 2013 

## 16 : 14 :00 13.011 4
. 801 1/30/2013 

## 16 : 15:00 13
.011 4
. 802 1/

30

/ 2013 

## 16 : 16 :00 13
.01 4
. 8 1/

30

/ 2013 

## 16:19 : 00 13
. 031 4
.783 1 / 30

/ 2013 

## 16 :20 :00 13
.041 4.78 1 / 30 / 2013 

## 16 :21 :00 13
. 019 4
.787 1/

30

/ 2013 

## 16:22 :00 13
.017 4
.786 1/30 / 2013 

## 16 : 23 :00 13
.019 4
.785 1/

30

/ 2013 

## 16 :24 : 00 13
.019 4.782 1 / 30/ 2013 

## 16:25:00 13.019 4.782 1/30 / 2013 

## 16:26 :00 13
. 01 4
.785 1/

30

/ 2013 

## 16 :27 : 00 13
. 01 4
.784 1/30 / 2013 

## 16:28 : 00 13
.018 4
.779 1 / 30/ 2013 

## 16:29:00 13.032 4
.77 1 / 30

/ 2013 

## 16:30 :00 13
.019 4.775 1 / 30

/ 2013 

## 16:41 :00 13
.047 4
.749 1 / 30

/ 2013 

## 16 :42 :00 13
.008 4
. 765 1 / 30/ 2013 

## 16 :43:00 13
.009 4
. 765 1/

30/ 2013 

## 16 :44:00 13
.005 4
. 768 1/

30/ 2013 

## 16:45:00 12
. 997 4
. 772 1/

30 / 2013 

## 16 :46 :00 12
. 986 4
.78 1/

30 / 2013 

## 16 :47 :00 12
.988 4.777 1/

30

/ 2013 

## 16:48 :00 13
.008 4
.764 1/30/2013 

## 16:49 : 00 13
.007 4.765 1/

30

/ 2013 

## 16 :50 : 00 13.008 4
.76 1 / 30

/ 2013 

## 16 : 53 : 00 13
.054 4.737 1 / 30

/ 2013 

## 16 : 54:00 13
.031 4
. 746 1/30/2013 

## 16 : 55 :00 13
.044 4.739 1/

30

/ 2013 

## 16:56 : 00 13
.046 4.736 1/

30

/ 2013 

## 16 : 57 :00 13
.054 4
.731 1 / 30

/ 2013 

## 16 : 58 :00 13
.069 4
. 719 1 / 30/ 2013 

## 16 : 59:00 13
.059 4.722 1/30/2013 

## 17:00 :00 13
.058 4
. 721 1/

30

/ 2013 

## 17:01 :00 13.049 4
.729 1/

30

/ 2013 

## 17 :02 : 00 13
.037 4
. 733 1 / 30

/ 2013 

## 17:03 :00 13
.012 4
.743 1 / 30

/ 2013 

## 17:05 : 00 13.058 4.732 1/

30

/ 2013 

## 17:06 : 00 13
.011 4
. 739 1/30 / 2013 

## 17 :07 : 00 13
.007 4
. 74 3 1 / 30

/ 2013 

## 17:08 :00 13
.007 4
. 742 1 / 30

/ 2013 

## 17:09 :00 13
.001 4.744 1/

30/2013 

## 17:10 :00 13.005 4
.742 1/

30

/ 2013 

## 17 : 11 : 00 12
.998 4.743 1/

30

/ 2013 

## 17:12 : 00 12
.996 4
. 744 1/

30

/ 2013 

## 17:13 : 00 12.995 4
.742 1/

30

/ 2013 

## 17:14 : 00 12.998 4.738 1/

30

/ 2013 

## 17 : 16 :00 13
.024 4
. 722 1/30 / 2013 

## 17 : 17 : 00 13
.009 4
.731 1/

30

/ 2013 

## 17:18 :00 13
.006 4
.73

### 1/3 0 / 2013 

## 17 : 19:00 13.007 4
.729 1/30/2013 

## 17 :20:00 13.007 4.726 1/30 / 2013 

## 17 :21 : 00 13
. 011 4.721 1/30/2013 

## 17:22:00 13
.003 4
. 727 1/30/2013 

## 17 :23:00 13.008 4
. 72 1 / 30

/ 2013 

## 17 :24 : 00 12.997 4
. 727 1/30 / 2013 

## 17 :25:00 13.01 4
.717 1 / 30 / 2013 

## 17 :26:00 13.011 4
.714

Average 

## 13
. 18 4.67

### Test 

## #: Dat e : Time : Load: CPV SENTINEL UNIT 2 PARTICULATE TEST STACK O 2 , 

### CO 2 

### DATA

S·2ISTK·PM·100·3 1 1

3112013

8:3 3 12:39 100 MW O 2 

### Range 20 Cal Gas 9
. 98 Ana lyzer Zero 0
. 11 Analyzer Span 10.10 Pre-Bias Zero 0
. 13 P re-Bias Span 10
. 07 Post-Bias Zero 0
. 12 Post-B i as Span 10
. 00 Average Bias Zero 0
. 12 Average Bias Spa n 1 0.04 P re -test zero bias 0
. 1 % P re-test span bias -0.2% Post-t est z ero bias 0.1 % Post-test span bias -0
. 5 % Zero D rift 0
. 0 % Span Dr ift - 0.3 % CO 2 

### 10 4
. 96 0
. 06 5
. 09 0.07 5
. 09 0 .3 1 5
. 38 0.19 5.23 0
. 1 % -0.1% 2
. 5 % 2
. 9 % 2.4% 3.0% T e st Re s ults (from data lo gge r ave rag e) Av e r a ge 13.11 4. 6 9 Cal Corre cte d 13
. 08 4.42

O 2 

### CO 2 

### Date Time % % 1 13112013 8:42 : 00 13
. 141 4.468 113112013 8 :43 : 00 13.186 4.47 1 13112013 8 : 44 : 00 13.183 4.479 1 13112013 8 : 45:00 13
. 195 4.476 113112013 8:46:00 13.177 4.488 113112013 8 :47 : 00 13
. 18 4.488 1 131 1 2013 8 :48:00 13
. 191 4.482 1 131 1 2013 8 : 49 : 00 13
. 187 4.486 113112013 8 : 50 : 00 13.191 4
. 483 1 131 12013 8:51 : 00 13
. 181 4.489

### 1/ 31 / 2013 

## 8 :52 :00 13
. 164 4.498 1/31 / 2013 

## 8 : 53:00 13.161 4
. 5 1/31 / 2013 

## 8 : 55:00 13
.231 4.494 1/31 / 2013 

## 8 :56:00 13.149 4
. 508 1 / 31 / 2013 

## 8 :57 :00 13
. 14 4
. 513 1/31 / 2013 

## 8 :58 :00 13
. 147 4
.51 1/

31 / 2013 

## 8:59 :00 13
. 161 4
. 501 1/

31/2013 

## 9:00 :00 13
. 161 4.503 1/

31 / 2013 

## 9:0 1: 00 13
. 16 4
.504 1/

31 / 2013 

## 9:02 :00 13.15 4.51 1/

31 / 2013 

## 9 :03 :00 13
. 156 4
. 508 1/

31 / 2013 

## 9 :04 :00 13
. 157 4
.507 1/31 / 2013 

## 9:06 :00 13
.213 4
.513 1/31/2013 

## 9 :07 :00 13
. 134 4
.523 1/

31 / 2013 

## 9:08 : 00 13
. 132 4
.527 1/

31 / 2013 

## 9:09 :00 13
. 134 4
.527 1/

31/2013 

## 9 : 10 : 00 13
. 135 4.526 1/

31 / 2013 

## 9 : 11 :00 13
. 133 4.527 1/

31 / 2013 

## 9 : 12 :00 13
. 131 4
.533 1/

31/2013 

## 9 : 13:00 13
. 114 4.545 1/

31 / 2013 

## 9 : 14 :00 13
. 126 4.542 1/

31 / 2013 

## 9 : 15:00 13
. 131 4
.54 1/

31 / 2013 

## 9 : 17:00 13.249 4
. 536 1/31 / 2013 

## 9 : 18 :00 13
. 128 4.548 1/

31/2013 

## 9 : 19:00 13.108 4
. 558 1/31 / 2013 

## 9 :20 :00 13
.096 4
. 569 1/

31 / 2013 

## 9 : 21 :00 13
.056 4
.591 1/31 / 2013 

## 9 : 22 :00 13.059 4
.592 1/

31 / 2013 

## 9:23:00 13.056 4
.598 1/

31 / 2013 

## 9 :24 :00 13
.061 4
. 594 1/

31/2013 

## 9 :25 :00 13
. 061 4.594 1/31 / 2013 

## 9:26 :00 13
. 065 4.595 1/

31 / 2013 

## 9 :35 : 00 13
.073 4
.574 1/31/2013 

## 9:36 : 00 13
. 105 4.576 1/

31 / 2013 

## 9:37 :00 13
.092 4
.589 1/

31 / 2013 

## 9 :38 : 00 13
. 094 4
. 591 1/31 / 20 1 3 

## 9:39 : 00 13
. 103 4
.592 1/31 / 2013 

## 9 :40 :00 13
. 084 4.598 1/

31 / 2013 

## 9:41 : 00 13.099 4
.598 1/31/2013 

## 9 :42 : 00 13
.09 4
. 602 1 / 31 / 2013 

## 9:43 :00 13
. 089 4
. 604 1/31 / 2013 

## 9:44:00 13
. 084 4
. 611 1 / 31 / 2013 

## 9 :47 : 00 13
. 097 4
. 615 1 / 31 / 2013 

## 9:48 :00 13
. 083 4
. 62 1/31 / 2013 

## 9 :49 : 00 13
. 082 4.627 1/31 / 2013 

## 9 :50 :00 13
.073 4
. 634 1 / 31 / 2013 

## 9 : 51 : 00 13
. 081 4
. 635 1/31 / 2013 

## 9 :52 :00 13
. 077 4
. 638 1/

31 / 2013 

## 9 : 53 :00 13.058 4
. 648

### 1/ 31 / 2013 

## 9 : 54 :00 13.08 4
. 64 1 / 31 / 2013 

## 9 : 55 :00 13
.063 4.65 1/31/2013 

## 9:56 :00 13
.077 4
. 646 1/

31 / 2013 

## 9 : 57:00 13.458 4
. 378 1/31 / 2013 

## 10:00 : 00 13
.064 4
. 655 1/

31 / 2013 

## 10 :01 :00 13
.055 4
. 662 1/

31 / 2013 

## 10 :02 :00 13
.039 4
. 672 1/

31 / 2013 

## 10 :03 :00 13
.032 4
. 681 1/31 / 2013 

## 10 :04 : 00 13
.027 4
. 687 1/

31 / 2013 

## 10 :05:00 13
. 03 4
. 688 1/31 / 2013 

## 10 :06:00 13
.028 4
. 689 1/31 / 2013 

## 10 :07 :00 13.032 4
. 691 1/

31 / 2013 

## 10 :08 :00 13
.034 4
. 691 1/31 / 2013 

## 10 :09:00 13
. 635 4
.282 1/

31 / 2013 

## 10:12 :00 13.05 4
. 698 1/

31 / 2013 

## 10 : 13 :00 13
.042 4.704 1/

31 / 2013 

## 10 : 14 :00 13
.045 4.707 1/

31 / 2013 

## 10:15 :00 13.056 4.706 1/

31 / 2013 

## 10:16 :00 13
.053 4
.71 1/

31 / 2013 

## 10:17 : 00 13
.055 4
. 713 1/

31 / 2013 

## 10:18 :00 13
.057 4.714 1/

31 / 2013 

## 10:19 :00 13
. 046 4.721 1/

31 / 2013 

## 10:20 :00 13
.048 4
.723 1/

31 / 2013 

## 10 :30 :00 13
.053 4
. 715 1/31 / 2013 

## 10 :31 :00 13.078 4
. 718 1/31 / 2013 

## 10:32:00 13
.083 4
. 724 1/

31 / 2013 

## 10 :33 : 00 13
.096 4
. 724 1 / 31 / 2013 

## 10 :34 :00 13
. 107 4
.722 1 / 31 / 2013 

## 10 :35 :00 13
.098 4.732 1 / 31 / 2013 

## 10 :36 :00 13
. 123 4.725 1/31 / 2013 

## 10 :37:00 13.117 4
.731 1/31 / 2013 

## 10 : 38 :00 13
. 125 4
. 73 1 / 31 / 2013 

## 10 :39 :00 13
. 119 4
.735 1 / 31 / 2013 

## 10 :40:00 13
. 124 4
.739 1 / 31 / 2013 

## 10 :43:00 13.288 4
.722 1 / 31 / 2013 

## 10 :44:00 13
. 135 4.739 1/31 / 2013 

## 10 :45 :00 13.141 4.74 1 / 31 / 2013 

## 10:46:00 13
. 141 4
.742 1/31 / 2013 

## 10 :47 :00 13
. 131 4.749 1/31 / 2013 

## 10 :48 :00 13.138 4
.748 1/31 / 2013 

## 10 :49:00 13
. 145 4
.746 1 / 31 / 2013 

## 10 : 50:00 13
. 143 4
. 748 1/31 / 2013 

## 10 : 51 :00 13
. 144 4
.749 1 /

31 / 2013 

## 10 : 52:00 13
. 134 4
.755 1/31 / 2013 

## 10 : 53:00 13.138 4
.757 1/31 / 2013 

## 10 : 54:00 13.131 4
.764 1/

31 / 2013 

## 10 : 55 :00 13
. 131 4
.766 1/

31 / 2013 

## 10 : 56:00 13
. 132 4
. 764 1 / 31 / 2013 

## 10 : 58 :00 13
. 161 4
.763

### 1/31 / 2013 

## 10 : 59 :00 13 , 138 4,764 1/31/2013 

## 11 :00:00 13 , 139 4,762 1/

31 / 2013 

## 11 :01 :00 13 , 131 4.773 1/31 / 2013 

## 11 :02 : 00 13,134 4.771 1/

31/2013 

## 11 :03:00 13
. 136 4.77 1/31 / 2013 

## 11 :04:00 13 , 135 4 ,77 1/31/2013 

## 11 :05:00 13.134 4.773 1/31 / 2013 

## 11 :06 :00 13 , 133 4 ,776 1/31 / 2013 

## 11 :07 :00 13
. 121 4,783 1/

31/2013 

## 11 :08 : 00 13 ,1 13 4,791 1/31/2013 

## 11 : 11:00 13.239 4.76 1/

31 / 2013 

## 11 : 12 :00 13
. 141 4
.773 1/31/2013 

## 11 : 13:00 13,139 4
.7 73 1/31/2013 

## 11 : 14 :00 13 , 134 4.777 1/31/2013 

## 11 : 15:00 13.14 4.774 1/31/2013 

## 11 : 16 : 00 13
. 133 4,782 1/31 / 2013 

## 11 : 17:00 13 , 146 4.773 1/31/2013 

## 11:18:00 13,155 4
.769 1/31 / 2013 

## 11 : 19:00 13 , 15 4,771 1/31/2013 

## 11 :20:00 13. 1 5 4,773 1/

31/2013 

## 11 :34 :00 13
. 114 4.786 1/31/2013 

## 11 : 35:00 13.125 4
.782 1/

31 / 2013 

## 11 :36:00 13,122 4.782 1/31/2013 

## 11 :37:00 13 , 117 4,786 1/31/2013 

## 11 :38:00 13 , 121 4
.784 1/31/2013 

## 11 :39:00 13 , 115 4.789 1/

31 / 2013 

## 11 :40:00 13 , 115 4.791 1/

31 /2 013 

## 11 :41 :00 13.128 4,784 1/31/2013 

## 11 :42:00 13,121 4.788 1/

31 / 2013 

## 11 :43 :00 13 , 1 1 6 4.79 1/

31 /2 013 

## 11 :46:00 13
. 131 4 ,78 1/

31 / 2013 

## 11 :47:00 13 , 119 4.794 1/31/2013 

## 11 :48:00 13.12 4.794 1/31 / 2013 

## 11 :49 : 00 13.112 4.796 1/31/2013 

## 11 :50:00 13
. 108 4 ,798 1/

31/2013 

## 11 : 51 :00 13 , 107 4
. 8 1/

31 /2 013 

## 11 :52:00 13,094 4.807 1/31/2013 

## 11 :53 :00 13
. 092 4,809 1/31/2013 

## 11 :54 : 00 13
. 082 4
. 814 1/31 / 2013 

## 11 :5 5 : 00 13
. 077 4 ,818 1 / 31 / 2013 

## 11 :57 :00 13 , 129 4 ,802 1/31/2013 

## 11 :58:00 13
.083 4,813 1/31 / 2013 

## 11 : 59 :00 13.069 4.825 1/31 / 2013 

## 12 : 00 :00 13.076 4
. 82 1/

31 / 2013 

## 12 :01 :00 13
. 058 4.828 1 / 31 / 2013 

## 12 : 02:00 13.069 4,822 1/31/2013 

## 12 : 03:00 13.051 4 , 831 1/31 / 2013 

## 12 :04:00 13 ,056 4.828 1/31/2013 

## 12 : 05:00 13
.056 4
. 829 1/

31 / 2013 

## 12:06:00 13 ,058 4,824

### 1/31/2013 

## 12 : 10:00 13
. 107 4.798 1/

31 / 2013 

## 12 : 11 : 00 13
.094 4
. 806 1/

31/2013 

## 12 : 12 : 00 13
. 103 4
. 802 1/

31 / 2013 

## 12 : 13 :00 13
. 104 4.804 1/

31 / 2013 

## 12 : 14 :00 13
. 105 4.804 1/

31 / 2013 

## 12 : 15 : 00 13
. 103 4.806 1/

31 / 2013 

## 12 : 16 :00 13
. 106 4
. 804 1 / 31/2013 

## 12 : 17 :00 13
. 1 4
. 807 1/

31 / 2013 

## 12 : 18 :00 13
. 104 4.807 1/

31 / 2013 

## 12 :28 :00 13.032 4.822 1/

31 / 2013 

## 12 :29 : 00 13
.047 4
. 826 1/

31/2013 

## 12 :30 : 00 13
.056 4
. 826 1/

31 / 2013 

## 12 :31 :00 13
.056 4.828 1/

31 / 2013 

## 12 :32 : 00 13
.057 4.827 1 / 31 / 2013 

## 12 :33 :00 13.058 4.828 1/

31 / 2013 

## 12 :34 : 00 13.05 4.832 1 / 31 / 2013 

## 12 :35 : 00 13
.062 4.826 1/

31 / 2013 

## 1 2: 3 6: 00 13
.064 4.826 1 / 31 / 2013 

## 12 :37:00 13
.07 4
. 824 1/

31 / 2013 

## 12 :38 : 00 13
.074 4.823 1 / 31 / 2013 

## 12 :39 :00 13.069 4.826

Av erage 

## 13.11 4.69

## APPENDIX D GENERAL EMISSIONS CALCULATIONS

R0410673 D-1 

# Delta /'). 

# ..

# __......

# -

## GENERAL EMISSION CALCULATIONS 1) Stack Gas Ve loc ity



## 2) A. Stack gas molecular weight, Ib/lb-mole MW dry 

## = 0.44 * %C0 2 

## + 

## 0.32 * %02 

## + 

## 0.28 * %N 2 MW wet 

## = MW dry 

## * 

## (1- B wo ) 

## + 18 * Bwo B. Absolute stack pressure, iwg Ps 

## = Pbar + Psg 

## 13.6 

# c. Stack gas velocity, ftlsec
Vs 

# = 2.9 * C p 

## * 

# -J IlP 

## * 

# Fs *
Moisture 

## A. Sample gas volume, dscf
V mstd 

# = 0.03342 * Vm 

## * (Pbar 

## +
B. Water vapor volume, scf 

# v = 0.0472 * V 

## * T ref

wstd Ie 

## 528 o R 

## 29
. 92 * 28.95 P, 

## * MW wet

IlH ) 

## * T ref 

## * Y d 

## 13.6 T m



# c. Moisture content, dimensionless 

## Bwo = 3) Stack gas volumetric flow rate 

## A. Actual stack gas volumetric flow rate, wacfm 

# Q = 

# v * 

## A * 

## 60 s s 

### B. Standard stack gas flow rate, dscfm

R0410673 D-2 

# De/lat6. "" 

### ....... "",,., -

## Q 

# = Q 

## * (1-B ) * Tre f

# ~ sd w o Ts 

## 29
. 92 4) Gaseous Mass Emission Rates , Ib/hr 

## M 

# = ppm * MW j 

## * Q Sd 

## * 60 SV * 

## 10 6 

## 5) 

## Emission Rates , Ib/MMBtu 

## Ib ppm*MW; *F * 20.9 MMBtu SV*10 6 

## 20.9 - %0 , 6) Emission Factor, Ib/MMSCF



## :-:-::-:-= 1 b

---:-= 

# = I b * 

## HHV MMSCF MMBtu VI

. Percent Iso kinetic 

## 17.32 x 

# T, 

# W m

sId ) 

## 528 0 R 1 = , 

## x --- (1- Bwa)O x V , x Ps x Dn T" f VII

. Particulate emissions a) Grain loading, gr/dscf 

## C = 0.01543 

## (M n N mSId) 

## b) Grain loading at 

## 12% CO" gr/dscf C 

## m • co, = C 

## (12/% CO , ) c) Grain loading at 

## 3% 0 " gr/dscf 

## C 3 %0 2 

## = 

## C * 

## 17
. 9/(20.9-%0 , ) d) Mass emissions , Ib/hr M 

## = C 

# x Qsd 

# x (60 min/hr)/(7000 gr/lb) e) Particulate emission factor

6 

## llb 2 0
.. 

## 9 lb l lO B tu 

# = ex x F x- --- 7000gr 20. 9 - % 0 ,

R0410673 D-3

### Nomenclature: 

## As B w o C 12 %C02 

## C 3%02 

## C 

# C

p 

### On 

## F 

## H HHV 

## I 

## M

n M; 

## MW 

## M

wi



# o**P** 

## P bar 

# P s P Sg 

### Q Q ws 

## QS d 

### SV 

# T

m T re f 

## T s Vs V'c 

# V

m Vmstd 

## V

wStd 

# Y

d



### R0410673 

## = stack area , 

## ft2 

## = flue gas moisture content , dimensionless 

# = particulate grain loading , gr/dscf corrected to 12% CO 2 

## = particulate grain loading , gr/dscf corrected to 3% CO 2 

## = particulate grain loading , gr/dscf 

## = pitot calibration factor , dimensionless 

## = nozzle diameter , in. 

## = fuel F-Factor , dscf/MMBtu 

## @ 0% O 2 

## = orifice differential pressure, iwg 

## = fuel higher heating value , Btu/SCF 

## = % isokinetics 

## = mass of collected particulate , mg 

# = mass emission rate of specie i , Ib/ hr 

# = molecular weight of flue gas , Ib/lb-mole 

## = molecular weight of specie i : 

## S02: 64 NO, : 

## 46 CO: 

## 28 HC : 

## 16 = sample time , min. 

## = average velocity head , iwg 

## =

## -J**~P)2** = barometric pressure , inches Hg 

## = stack absolute pressure, inches Hg 

## = stack static pressure , iwb 

## = wet stack flow rate at actual conditions , wacfm 

# =wet stack flow at standard conditions , wscfm 

## = dry standard stack flow rate , dscfm 

## =**s~ecific** 

### molar vo l ume of an ideal gas at standard conditions ,

ft lib-mole 

## = meter temperature , 

## o R = reference temperature , 

## O R = stack temperature , 

## O R = stack gas velocity , fUsec 

## = volume of liquid collected in impingers , ml 

# = uncorrected dry meter volume , dcf 

## = dry meter volume at standard conditions , dscf 

## = volume of water vapor at standard conditions , scf 

## = meter calibration coefficient

D- 4 

# Della /:"

.. .............. ,.....-

# ..

## APPENDIX E CHAIN OF CUSTODY

R0410673 E-1 

# De/la IJ. 

# ,,-

.......**~,** 

### ... --'CHAIN OF CUSTODY CLIENT : Sen tinel

# ~ TEST DATE (S): 1130/2013 211/2013 LOCATION : 2 SAMPLER(S): SS SAMPLE LOCAT ION: Stk PROJECT MANAGER: BF TEST METHOD(S): SCAQMDS

. 1 DATE DUE : 219/2013 OUTSIDE LAB REQUIRED? : No COMPLIANCE TEST? Yes .t 0 1130/2013 S2ISjk·PM·100·1 SCAQMD5

. 1 Probe Une Imp . 1 SS Water 1 1301 2013 S2fSt k· PM ·1 00 -' SCAQMD 5 . 1 5.1 Filter 1 SS 55mm 1/30/2 013 S2IStk·PM·100·2 SCAQMO 5 . 1 Probe Line 1m
. 1 SS Water 1/30/2013 S2IStk·PM-100·2 SCAQMD S

. 1 5.1 Filter 1 SS 55mm 113112013 S2IStk · PM·100 ·3 SCAQMD S

. 1 Probe , Line , 1m . 1 SS Water 1131/2013 S2lStk-PM-100-3 SCAQMD 5
. 1 5.1 Filter 1 SS 55mm 211/2013 S2IStk·PM·7S·1 SCAQMD S

. 1 Probe . Line, Imp . 1 SS Water 21112013 S2IStk·PM·7S·1 SCAQMDS.1 5 . 1 Filter 1 SS 55mm 21112013 S2IStk· PM·SO·1 SCAQMD S

. 1 Probe Line Imp. 1 SS Water 211/ 2013 S2IStk-PM-50-1 SCAQMDS

. 1 5 . 1 Filte r 1 SS 55mm 21 112013 S2IStk·PM·-FB SCAQMDS

. 1 Probe , Line . Imp. 1 SS Wate r 211/2013 S2IStk·PM 

### FB SCAQMDS

. 1 5 . 1 Fi lter 1 SS 5Smm 211/2013 S2IStk·PM·-RB SCAQMDS .1 Blank 1 SS Waler**~tal ~ampJes**  3 Rea 

### entl 

### water I I ea en t ot s: S 

### I 

# I**/?~j '**  

# Z?d**~~~~~** 

# I I**Di7TI~~** 

## '4

_**.,.....~** 

## )7/ b 

## 0

# I~**t:#p ~~**  

# - 

# IvY/emt;**!!.**CLIENT ; LOCATION ; SAMPLE LOCATION ; TEST METHOD(S); OUTSIDE LAB REQUIRED? ; 

## 71"i2oT'3
' 30

/ 2013 

### '3Oi2013

21172'013

1/201 Sentinel

# ~~ 2 SII< SCAQMD 207.1 No TIME 

## T TEST# i2lStk·NH 3-·FB Blank

S2ISII<-NH3-100-1 S2JStk-NH3·100-2**_S~Stk-NH~-?5-1**

- ,- - S2IStk·NH3·50-2 S2IStk-NH3- RB Blank S2IStk-NH3---RB Blank

'-

______ ...;R..:;e"'ag"e"'n':..;L"'o':.:#':.,:s"' I_ . _ _ _________ CHAIN OF CUSTODY TEST DATE (S) ; 1130 /2013 2/1120 1 3 SAMPLER(S) ; SS PROJECT MANAGER ; BF DATE DUE ; 219/2013 COMPLIANCE TEST? Yes Method SAMPLE I SCAQMD 207
. 1 Probe , lir SCAQMD 207
. 1 Probe line , SCAQMD 207 . 1 Probe nne SCAQMD 207.1 Probe line 

### be line IrTiPIi1gers 1 SS 0 . 1 N H2SO4 be , line . 1m 'n ers 1 SS 0
. 1 N H2SC SCAQMD 207
. 1 Probe line 1m In ers 1 SS 0.1 N HZSC SCAQMD 207 . 1 3110020/V9 1 SS 0.1 N H2SC 5CAQMD 207
. 1 3110020/Vl0 1 55 0
. 1 N H2SC

9


## J

# A-t /1 

## A/I

# ~EA15DBY /.

_ 

# d

___**DA;"ry~ ,..,** **EiiJ:f~!?!** 

# 6z'tb EITi 

# '1&n I • 

## 1 

# ,,= 1 

# 1--" 

# r- .. 1 -, (I

### -~

## ~

# A~!P**/301z..~** CHAIN OF CUSTODV CLIENT : Sentinel 

# CQ.owt TEST DATE(S) : 1130/2013 21 112013 LOCATION : 2 SAMPLER(S) : .:.:R"'M

___________ _ SAMPLE LOCATION : SII< PROJECT MANAGER : TEST METHOD ( S ): SCAQMD 25
. 3 DATE DUE : OUTSIDE LAB REQUIRED?' Yes 

### C7t7 1/30/2013 S2I 

# 1I<.,g ·1()()'1A _§C 2(,..

# v.'**'' .~"**  07" 1 130/2013 S2ISIk·VOC-1()().1B SCAQMD 25
.3 Can i sterj 

### IJ 

## 7'f 

## f 211 / 2013 S2ISII<·VOC-50·1A SCAQMD 25
. 3 Can i sterj 

### ..1! COMPLIANCE TEST? tJIII[ 

# -srr 0() 211 / 2013 S2ISII<.VOC-50·1B SCAQMD 25
. 3 Canlsterl 

## O!.../ 211 / 2013 S2ISII<· VOC-75-1A SCAQMD25

. 3 Canl

__ 

## --;::;;:O, ,.. ' 

# "0-**~** 21112013 S2ISIk· VOC

. 75-1B SCAQMD25

.3 Csn i

__**.r~** 1 RM



## .o1PJ

6

# ~"'iiit Reagent L({ 's :

, ' -- 

## ...l BF 21912013 Ves 

## v

# ~**~**

# l,zzj~)3**~;@** 

# I I 

# 2S!:i:'i jif I 

# Olii 6

# ~'" Note :**Can~t.r** #00<>403 and toQO.411 were voided

..... . Plea

.. do not analyze

. '

.. 

# -MFA

## APPENDIX F I NSTRUMENT STRIP CHARTS

R04106 7 3 F- 1 

# Delfa l1 ",o-.'- H ,_"

## APPENDIX G FACILITY PERMIT TO OPERATE CONDITION 029.1

R0410673 G-1

# De/ta**~** 

# ..**""",~** 

### ...........

# - ....

## SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 

## 21865 Copley Drtve, Diamond Bar, CA 91765


# FACILITY PERMIT TO OPERATE CPV SENTINEL LLC Section H Page: 35 Facility 10: 152707**R~inon#:** 0 Date: April IS. 2011



# SECTION H; PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE
The operator shall comply with the terms and conditions set forth below: The operator shall also install and maintain a device to continuously record the parameter being measured The measuring device or gauge shall be accurate to within plus or minus 5 percent. It shall be calibrated once every twelve months It shall be calibrated once every twelve months The pressure drop across the catalyst shall not exceed 12 inches water column [RULE 1303(a)(1)-BACT, 5-10-1996; RULE 1303(aXI)-BACT, 12-6-2002; RULE 1703(aX2)

- PSD-BACT, 10-7-1988; RULE 2005, 5-6-2005) [Devices subject to this condition: C4, CIO, C16, C22, C28, C34, C40, C46) D 12.5 The operator shall install and maintain a(n) non-resettable elapsed time meter to accurately indicate the elapsed operating time from the engine. [RULE 

## J 110.2,2-1-2008; RULE 1303(b)(2)-OlTset, 5-10-1996; RULE 1303(b)(2) -Offset, 12-6-2002; RULE 1470, 6-1-2007; RULE 2012, 5-6-2005) [Devices subject to this condition: D49) D29.1 The operator shall conduct source testes) for the pollutant(s) identified below. Pollutant(s) to Required Test Method(s) Averaging Time 

# I Test Location be tested NOX emissions District method 100.1 I hour Outlet of the SCR serving this equipment CO emissions District method 100.1 I hour 

# IOutlet of the SCR serving this equipment SOX emissions 

# I AQMD Laboratory Method 307-9\ Not Applicable 

# I Fuel sample VOC emissions 

# I District Method 25.3 I hour 

# IOutlet ofthe SCR serving this equipment

### SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 

### 21865 Copley Drive, Diamond Bar, CA 

### 91765



# FACILITY PERMIT TO OPERATE CPV SENTINEL LLC Section H Page : 36 Facilitv 10 : 152707 Revis ion #: 0 Date : April 15, 20J 1



## SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE
The operator shall comply with the terms and conditions set forth below: PM 10 emissions NH3 emissions 

# I District Method 5 

# I District method 207.1

and 5.3 or EPA method 17 4 hours 1 hour 

# IOutlet of the SCR serving this equipment 

# I

Outlet of the SCR serving this equipment

# ~- SOUTH COAST AIR QUALITY MANAGE.MENT DISTRICT 21865 Copley Drive, Diamond 

## Bar, CA 91765


# FACILITY PERMIT TO OPERATE CPV SENTINEL LLC Section H Facility lD : Revision II: Date : Page: 37 152707 

## o April IS. 20)1



## SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE
The operator shall comply with the terms and conditions set forth below: The test shall be conducted after AQMD approval of the source test protocol, but no later the later of 180 days after initial start-up or three hundred hours of operations after start-up. The AQMD shall be notified of the date and time of the test at least 10 days prior to the test The test shall be conducted to determine the oxygen levels in the exhaust. In addition, the tests shall measure the fuel flow rate (CFH), the flue gas flow rate, and the turbine generating output in MW
. The test shall be conducted in accordance with AQMD approved test protocol. The protocol shall be submitted to the AQMD engineer no later than 45 days before the proposed test date and shall be approved by the AQMD before the test commences. 

## The test protocol shall include the proposed operating conditions of the turbine during the tests, the identity of the testing lab, a statement from the testing lab certifying that it meets the criteria of Rule 304, and a description of all sampling and analytical procedures The test shall be conducted when this equipment is operating at maximum, average, and minimum loads_ For natural gas fired turbines only, VOC compliance shall be demonstrated as follows: a) Stack gas samples are extracted into final canister pressure between 400-500 mm Hg canisters are done with zero gas analyzed/certified total hydrocarbon as carbon, and c) Analysis of TO-l2 (with pre concentration) and temperature samples for analysis is not below 70 deg F
. Summa canisters maintaining a absolute, b) Pressurization of to contain less than 0.05 ppmv canisters are per EPA Method of canisters when extracting
The test shall be conducted for compliance verification of the BACT VOC 2.0 ppmv limit. The test results shall be 

## reported with two significant digits.

### SOUTH COAST AIR QUALllY MANAGEMENT DISTRICT 21865 Copley DrIve, DIamond Bar, CA 91765



# FACILITY PERMIT TO OPERATE CPV SENTINEL LLC Section H Facility ID: Revision Ii: Date: Page: 38 152707 

## o April 15, 201 1



## SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE
The operator shall comply with tbe terms and conditions set forth below: [RULE 1303(a)(1)-BACT, 5-10-1996; RULE 1303(aXl)-BACT, 12-6-2002; RULE 1303(b)(2)-Offset, 5-10-1996; RULE 1303(b)(2)-Offset, 12-6-2002; RULE 1703(a)(2)

- PSD-BACT, 10-7-1988; RULE 2005, 5-6-2005] [Devices subject to this condition: DI, 

## D7, 013, D19, D25, D31, 037, D43] D29.2 The operator shall conduct source testes) for the pollutant(s) identified below. Pollutant(s) to be tested NH3 emissions 

# IRequired Test Metbod(s) District method 207.1 and 5.3 or EPA method 17 Averaging Time I hour 

# I Test Location 

# IOutlet ofthe SCR

serving this equipment
The test shall be conducted and the results submitted to the District within 45 days after the test date. The AQMD shalI be notified of the date and time of the test at least 7 days prior to the test. The test shall be conducted at least quarterly during the first twelve months of operation and at least annually thereafter. The NOx concentration, as detennined by the CEMS, shall be simultaneously recorded during the ammonia slip test. If 

## the CEMS is inoperable, a test shall be conducted to determine the NOx emissions using District Method 100.1 measured oyer a 60 minute averaging time period. If the turbine is not in operation during one quarter, then no testing IS 

## required during that quarter The test shall be conducted to demonstrate compliance with the Rule 1303 BACT concentration limit [RULE 1303(a)(1)-BACT, 5-10-1996; RULE 1303(a)(I)-BACT, 12-6-2002] [Devices subject to this condition: Dl, D7, 013, D19, D25, D31, D37, D43]

## APPENDIX H CORRESPONDENCE AND TEST PLAN

R0410673 H-1

# Delta**~** "' 

## ...............

# _..

## Bob: Here is an answer to one of the issues for the CPY Sentinel te sting. From: Carey Willoughby [mailto:CWilloughby@aqmd.gov] 

## Sent: Wednesday, January 09, 2013 10:09 AM 

### To: Tom W

. Andrews 

## Subject: RE: 

# epy Sentinel 

# voe Tests 

## Mr. Andrews, Simultaneous duplicate samp lin g (s ix canister samples vs . nine sample canisters) for VOC is acceptab le to the SCAQMD. Sincerely, 

## Carey "'Wi{{oUEJfijjy 

## Air 

# Quaaty 'E11fJineer II SC.JI.Q:.M'D 21865 

## Coyfey 'Drive 'Diamoruf'.Bar, CA 91765 

## 'l'ef (909) 396-3006 :fax: (909) 396-2099 

# cwiC{OUO fi6

# y@aqmd:.IJOV

From: Tom W

. Andrews [mailto:TAndrews@sierraresearch.com] 

## Sent: Wednesday, January 09, 2013 9:39 AM 

### To: Carey Willoughby 

## Cc: W. Andrews, Tom 

## Subject: CPV Sentinel 

# voe Tests 

## Carey: Per our telecon this morning, for the VOC tests the test team would like to take duplicate simultaneous samples rather than triplicate samples in series at each ofthe three gas turbine loads. 

## In other words a total of six canister samples vs. nine canister samples. Could you please confirm this is acceptable to the SCAQMD. Thanks. 

## Tom Andrews

1801 

## J Street Sacramento, CA 95811 (916) 273-5139 

## (direct/voice) (916) 444-8373 

## ifax)

# SOURCE TEST PROTOCOL FOR INITIAL COMPLIANCE TESTING AT CPV SENTINEL ENERGY PROJECT UNITS 1 - 8
PREPARED FOR: GEMMA POWER SYSTEMS CALIFORNIA, INC. 2461 MAIN STREET GLASTONBURY, CONNECTICUT 06033 FOR SUBMITIAL TO : SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 21865 COPLEY DRIVE DIAMOND BAR, CALIFORNIA 91765-4178
PREPARED BY: DELTA AIR QUALITY SERVICES, INC

. 1845 N

. CASE ST

. ORANGE, CALIFORNIA 92865 714-279-6777 ROBERT 

## A. FINKEN DECEMBER 7,2012 DOCUMENT NUMBER: R0210458·R 1

# 8ellll~ Air Quality Services, Incorporated

## CONFIDENTIALITY STATEMENT

This information contained in this communication is intended exclusively for the individual or entity to which it is addressed. This communication may contain information that is proprietary, privileged or confidential or otherwise legally exempt from disclosure. If

## you are not the named addressee, you are not authorized to read, print, retain, copy, or disseminate this message or any part 

## of it.

R0210458-R1 ii 

# 1Je1/a/j.



# ..**--**

## CONTENTS SECTION 1 , 0 INTRODUCTION "'" ",.", "" ' " "" "" " "'" "'" """ ""'''' " " "

.. .. ""

.. , " "" ",,

.. '" ,,", "

... ""." 1 2
. 0 UNIT DESCRIPTION AND TEST CONDITIONS """ ''''''' ''' '''''' ''''' '' '''' ' ''''''''''' '' ''''''' 2 2,1 UNIT DESCRIPTION""" "

.. , """ "",,,,,,, '"''''',''' ".,,'

.. .... """.",

.. ,'" ",, " '" ,,, .. ,'''''' 2 2 ,2 TEST CONDITIONS ""

. "." ", '" ",,,,

.. ,,, .. ,,, ",, ' "",

.. , '" "

. ... "

.... ""

.. '"

.. ""

... " "

.. " " " 4 2 , 3 SAMPLE LOCATION" """,

... " "

.. " "

.. ' "

. " "

.. ,' "" "

.. '" "

.. ,," "

.. ,,, .. , " " .,, ' " ", ",

. .. , " " 5 3,0 TEST DESCRIPTION"." ""' " '' ''' ''''' ","',," "

.. ' "

. ""."'

.. " ""

.. " "

... '" "

.. "'

.. . " "

.. ,,'

.. " "" 7 3 , 1 O 2 • 

## CO 2 • 

## NO

# x AND CO """"""""."."""

.. ".""

.. ""."",,."""

.. ",,",,"

.. ,, .,, ",,""" " 8 3 ,2 NH3 BY SCAQMD METHOD 207,1 "" ."""""". " ."" ""

.. """"".".". "."""

.. """." 9 3 , 3 SOx BY SCAQMD METHOD 307,91 ".""""""""".".,,"."""

.. ""

.. " "

.. ,,.,, .. """'" 9 3.4 ROG BY MODIFIED SCAQMD METHOD 25
. 3"" ." " ""

.. ,,,,,,,,,.,, . ,,,, .. ,,. ,, .. ,,,,,,,,, 9 3
. 5 PM BY SCAQMD METHOD 5 , 1 """""'" ''''''''''' '''' '' '''''' ' '''''' '' ''''' '''' '''''''''''' ''''' 13 4,0 REPORTING """

.. .. ,' ,.. ",, " ," '

.. .. '"

.. .. "

... ". ", ,,"" ",, ' "'" "

.. " , '

.. "" "

.. ,,'

... " "

... " , ... "' ''' 15 APPENDICES A QUALITY ASSURANCE" "",,"

... ". , " ""

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.. . "" , '" " A-1 B TEST METHODS , "''' ' ''

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. .. "".,," B-1 C CALCULATIONS, '" "."".""" .,," .,, "' .,, '"

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# o FORMS " ' ''' ' ' "" "

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... . "" "."."., 0 - 1 E FACILITY PERMIT TO OPERATE CONDITION 029 , 1"""

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R021 0458-R 1 iii 

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# 1.0 INTRODUCTION Delta Air Quality Services , Inc. has been contracted by Gemma Power Systems California. Inc. (GEMMA) to perform the initial Permit to Operate Compliance Testing at the CPV Sentinel Energy Project Units 1, 2, 3, 4, 5 , 6, 7, and 8. Condition D29.1 of the Permit to Operate requires source tests within 180 days of initial startup. This document will serve as the test plan for the aforementioned tests. Tests will be performed at three load conditions to determine oxides of nitrogen (NO x ), carbon monoxide (CO), oxides of sulfur (SOx), reactive organic gases (ROG's), particulate matter (PM), and ammonia (NH3) emissions. Bob Finken will be the Senior Program Manager for Delta and can be reached at (714) 279-6777
. No conflict of interest, as defined in SCAQMD Rule 304, exists between Gemma or CPV Sentinel Energy Project and Delta. Section 2.0 of this document provides a description of the facilities and sample locations

. A description of the sampling strategy and test methods is provided in Section 3
. 0
. Section 4.0 outlines the final source test report format. A more detailed description of the test methods, calculations, and quality assurance procedures is provided in the Appendices.

R021 0458-R 1 1 

# /le/tat1
..

# _ .......

# -

# 2.0 UNIT DESCRIPTION AND TEST CONDITIONS
2 .1 UNIT DESCRIPTION CPV Sentinel Energy Project i s located at 62575 Powerline Road, Desert Hot Springs, California 92240. The facility consists of eight (8) identical generating units

. The CPV Sentinel Energy Project consists of eight (8) LMS100PA combustion turbines in simple cycle operation. The units are natural gas fired with a rated heat input of 891
. 7 MMBtu per hour at 72 degrees Fahrenheit. Each LMS100PA employs water injection and is equipped with a CO catalyst and Selective Catalytic Reduction (SCR) system for NOx 

## control. The LMS100PA is a General Electric (GE) combustion turbine with an intercooler located between the low pressure compressor (LPC) and high pressure compressor (HPC)

. Off engine combustion air to closed loop water intercooling is used for increased gas turbine thermal efficiency. Heat removed from the off-engine intercooler is circulated through a closed loop cooling system. Heat is rejected from the closed loop cooling system to an open loop cooling system via plate and frame heat exchangers

. The open loop system rejects heat via a mechanical draft counterflow cooling tower. The cooling tower is provided with drift elimination to comply with air emissions limits

. Figure 2-1 presents a block diagram of the units. Figure 2-2 shows a general arrangement of the major components.

R021045B-R1 

### 2 

# DeIIai1

...

# _--

## FIGURE 2-1 SIMPLIFIED PROCESS BLOCK DIAGRAM CPV 

## SENT I NEL ENERGY PROJECT COMBUSTION TURBINES

Simplified Process Flow Diagram


### Air Water Cooling Tower Air Water Heat

Closed Loop Exhaust to Atm

. Cooling

Air LMS100PA Exhaust CO Catalyst SCR 

## IWater Ammonia Natural Gas Fuel Demineralized 19% Aqueous



## R021 0458-R 1 

# Oe/lIl1

.. ..... .

# ...--- 3

## FIGURE 2-2 GENERAL ARRANGEMENT OF MAJOR COMPONENTS

;.u.o. . r ... ':rD-".

- Y' ....

.r.AoItII



# - . .. . .... .. .. .. . .... . . ... _ . .. . ... . . . .... . .lk9++=d.
_.... ..... .. .. .. .. .

A \ wr · ' • "'f t' '''T ·-4. B.UT

.... ;. t 

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## 2.2 TEST CONDITIONS 

## The permit requires that the tests will be performed at three operating conditions; 1) maximum, 2) average, and 3) minimum load

. Full load is nominally 100 megawatts and m i nimum load will be approximately 50 megawatts
. Since these will be the initial tests for the units and no long term average will have been established , average conditions will be approximated at 75% of capacity or approximately 75 megawatts.

R021 0458·R 1 4

## Unit operating data will be gathered during the tests by the facility from the CEMS DAS. These data will include, at a minimum :
• Fuel flow rate • Turbine generating output (MW) • Ammonia Flow • Exhaust Temperatures • Exhaust Flow Rates
2.3 SAMPLE LOCATION 

## There are four 6" test ports located at 90 degrees apart around the circumference of the 13'6" diameter stacks

. The ports are located 323" downstream (2.0 diameters) of the nearest flow disturbance (duct breeching) 84" upstream (0

. 5 diameters) of the nearest flow disturbance (silencers). The sampling location meets the minimum requirements of SCAQMD Method 2.1, being >2 diameters downstream and >0.5 diameters upstream of the nearest flow disturbances. Figure 2-3 presents the details of the sample location.
FIGURE 2-3 SAMPLE LOCATION DETAILS

Inside Diameter, in.

- 162 4-- 

### Stack Ex it 1080
. 0 in

. Si lencer Bottom 925 .9 in.


### Ports 841
. 6 in

. Platform 789
. 6 in

.

Base 01 

### Slack 518
. 5 in

.

Grade 0
. 0 in.



## R021 0458-R 1 

# T 84 Distance A, inches, 0 .5 Diameters 

# ! Sample ports 

# T
323 Distance B t inches, 2.0 Diameters

+_...;E::;x:;::hauSI 

### Flow 4


### Elevation View



## 5 90 

### ft
.

66 II.



# o fl
.



# Delta,1. 

# --.--Sample 

### Po int

2 3 4 5 6 7 8 9 10 11 

## Prior to performing the tests, gaseous stratification will be investigated with a 12 point traverse as described in 40 CFR 75, and the presence of cyclonic flow will be checked using the techniques described in SCAQMD Method 2. If stratification is less than 10% or less than 1 ppm, all future gaseous concentration measurements will be made from a single point. If stratification is greater than 10% and greater than 1 ppm , all future concentration measurements will be performed using a multi-point traverse (3-point short line, 3-point long line , or 12-points (using 40 CFR Part 75 criteria))

. A 16 - point cyclonic flow traverse will be performed with an S-type pitot tube

. If the average 

## yaw angle is less than 10 degrees , the location will be deemed acceptable for Method 2
. 1 velocity measurements. Table 2-1 illustrates the location of sample traverse pOints. TABLE 2-1 SAMPLE POINT LAYOUT
PM (24 pts
. ) Flow Disturbance (16 pts
. ) Strat.lNH3 (12 Pts

. ) 3 pI. Long Line CEMS 3 pI. Short Line CEMS % 

### of in . 

### % 

### of I n . 

### % of in. % of i n. % of 

### Diameter from Wa ll 

### D iameter from Wall D iameter from Wall 

### Diameter from Wall 

### Diameter

2
. 1 3.4 3.2 5
. 2 4
.4 7.1 16
. 7 27.1 N/A 6.7 10
. 9 10.5 17
. 0 14
. 6 23
. 7 50 81.0 N/A 11
. 8 19
. 1 19.4 31.4 29
. 6 48.0 17
. 7 28.7 32
. 3 52
. 3 25 40.5 67
. 7 109
. 7 35
. 6 57.7 80.6 130.6 64.4 104.3 89.5 145.0 75 121
. 5 82
. 3 133
. 3 86.4 140
. 0 93.3 151.1



## Prior to performing the tests, gaseous stratification will be investigated with a 12 point traverse as described in 40 CFR 75, and the presence of cyclonic flow will be checked using the techniques described in SCAQMD Method 2.1. If stratification is less than 10% or less than 1 ppm, all future gaseous concentration measurements will be made from a single point. If stratification is greater than 10% and greater than 1 ppm, all future concentration measurements will be performed using a multi-point traverse (3-point short line, 3-point long line, or 12-points (using 40 CFR Part 75 criteria»

. A 16-point cyclonic flow traverse will be performed with an S-type pitot tube

. If the average 

## yaw angle is less than 10 degrees, the location will be deemed acceptable for Method 2.1 velocity measurements.
R0210458 - R1 6 

# llella;}. "' 

## ......

# _- in . from Wall 15
. 7 47
. 2

# 3.0 TEST DESCRIPTION Table 

## 3-1 summarizes the test methods and techniques which will be used as the reference methods. The test matrix has been developed to meet the requirements of Section 

## 29
. 1 of the facility Permit (Application Number 

## 472137) dated April 

## 15, 2011
. The permitted emission limits are summarized in Table 

## 3-2. The following sections describe each method in further detail. Flue gas Oxygen and Carbon Dioxide concentration will be measured in conjunction with all tests using SCAQMD Method 

## 100.1
. The flue gas flow rate will be measured in conjunction with each particulate test. This measured flue gas flow rate in each duct will be used for all emission rate calculations of NO x , CO, NH 3 , 

## ROG's and SOx. 

## TABLE 3-1 TEST MATRIX Parameter Method 50% Load 75% Load 100% Load Test Duration NOx SCAQMD 100
. 1 1 run 1 run 1 run 60 minutes 

## 02 /C0 2 SCAQMD 100
. 1 With each run CO SCAQMD 100
. 1 1 run 1 run 1 run 60 minutes NH3 SCAQMD 207
. 1 2 runs 2 runs 2 runs 60 minutes S02 SCAQMD 307.91 2 samples N/A PM EPA 201NSCAQMD 5
. 1 1 run 1 run 1 run 240 minutes ROG Modified SCAQMD 25.3 3 runs 3 runs 3 runs - 60 minutes(1) 1) 

## ROG tests will be nominally 

## 60 minutes

. Flow controllers will be setup for 

## 60 minutes

. The test will be performed unlil the canister vacuum reaches approximately 

## 10 "Hg

. Actual test time may be less than or more than 

## 60 minutes per sample

.



## R021 0458 - R 1 

## 7 

# De/Ia/'). »

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## TABLE 3-2 CPV SENTINEL ENERGY PROJECT PERMIITED EMISSION LIMITS Parameter Units ppm@15%0 2 ppm @ 15% O 2 Ibs/MMscf 

# co ppm @15%0 2 

## NHa ppm@ 15% O 2 gr/dscf @ 3% O 2 Particulate gr/dscf @ 12% CO 2 Ib/hr Ibs/MMscf (Ib/hr equivalent) Ib/MMBtu Ibs/MMscf 

### SOx ROG's ppm@ 15% O 2 (1) The 12
.26 IbslMMscf is a RECLAIM emission factor, not a limij

. (2) This is stated in the permit as an emission factor

. 

## 3.1 O2 • 

## CO 2 • 

## NOx 

## AND CO Limit 2
. 5 15 12.26(1) 

## 4 5 0.Q1 0
. 1 11 5.71(2 ) (5.0) 0
. 06 0
. 69 2
. 0 Rule 1703(a)(2) 40 CFR 60 2012 1703(a)(2) 1303(a)(1 ) 475 409 475

40 CFR 60 Rule 2011 1303(a)(1)



## O2 , 

## CO 2 , 

## NO x 

## and CO concentrations will be measured using SCAQMD Method 100
. 1
. These measurements will be made with one of Delta's mobile emission measurement laboratories

. The system consists of a stainless steel or glass probe, heated Teflon line, moisture removal system , sample pump, sample filter, unheated Teflon line, and individual component analyzers. The measured concentrations are averaged over each sampling period, then corrected for system bias and analyzer drift

. All quality assurance procedures required by SCAQMD Method 100.1 will be performed including pre- and post-test Calibration Error, Sample System Bias and Analyzer Drift

. The sampling will be performed using a 12-point traverse at each test condition (or a single point if previous testing demonstrates the absence of significant stratification (less than 10% or less than 1 ppm)

. At the full load condition, the compliance test may be performed concurrently with the Relative Accuracy Test Audit (RATA)

. In this case, data from the RATA may be used to demonstrate compliance with the NOx 

## and CO emission limits. NOx 

## concentrations will be measured on a 0-5 ppm range . CO concentrations will be measured on a 0- 10 ppm range. CO 2 

## concentrations will be measured on a 0-10% range . O 2 

## concentrations will be measured on a 0-20% range. The measured concentrations are averaged over each sampling period, then corrected

R021 0458 - R 1 

## 8 

# DeltalJ..

... .... ..**...-.~-**

## for system bias and analyzer drift. The drift and bias corrected result will then be used to calculate NO, emissions in units of ppm, ppm corrected to 15% O2 , 

## pounds per hour, pounds per m i llion Btu, and pounds per m i llion standard cubic feet of natural gas. 3
. 2 N H 3 BY SCAQMD M ET HOD 

## 207.1 Duplicate flue gas samples will be collected non-isokinetically at each test condition using a SCAQMD Method 207
. 1
. A 12-point traverse will be performed during each NH3 slip test unless previous tests demonstrate the absence of sign ificant NO, stratification , then single point sampling will be performed

. The sample gas is drawn through a glass probe , Teflon sample line , two impingers each containing approximately 100 ml of 0
. 1 N H 2 

## S0 4 , 

## an empty impinger, an impinger containing silica gel, and a dry gas meter. The optional nozzle and filter will not be used since the units are natural gas fired. The contents of the probe, sample line and the f i rst three impingers are recovered and analyzed by SCAQMD Method 207
. 1 for ammonia concentration using the Ion Specific Electrode technique

. One reagent blank sample and one field blank sample will be analyzed

. Ammonia slip will be reported in units of ppm, corrected to 15% O2 . 

## The tests will be performed over a period of at least 60 minutes

. 3.3 SOx BY SCAQ M D METHOD 

## 307.9 1 Oxides of sulfur will be measured using SCAQMD Method 307-91
. Two fuel samples will be collected in a Tedlar bag and sen t to Say bolt Laboratory for Sulfur analysis as total reduced sulfur as H2 

## S

. 3
. 4 ROG BY M ODIFIED SCAQMD METHOD 

## 25.3 Sampling and analyses are performed using Modified SCAQMD Method 25
. 3 procedures. The sample apparatus and analyses are provided by Atmospheric Analysis and Consulting (AAC) in Ventura California

. At each test condition , triplicate flue gas samples are extracted sequentially from four points (one per port) in the stack through pre-cleaned (high temperature conditioned) stainless steel probes connected to an out-of-stack flow controller, into stainless steel Summa polished canisters

. The flow controller i s set to fill the evacuated canister to a pressure of -400 mm Hg over a period of a period of one hour

. Modifications to the Method 25.3 sampling procedures suggested or accepted by SCAQMD are :
• Elimination of the in-stack filter • Elimination of the water vial portion of the 25
. 5 equipment • The final pressure in the Summa Canisters is ma i nta i ned at between 400 and 500 mm HG (10 - 14 in. Hg) absolute.

R021 0458-R 1 9 

# Dell8!'3.

..

# _--

## Figure 3-1 presents a schematic drawing of the sample apparatus.
FIGURE 

## 3-1 MODIFIED SCAQMD M ETHOD 

## 25.3 SAMPLING APPARATUS



## Filter Probe

Flow Controller

The samples are analyzed for NMNEOC (Non-Methane Non-Ethane Organic Compounds, i.e

. Reactive Organic Compounds ROG) using modified SCAQMD Method 25
. 3 TCA procedures. Analysis consists of a fore-flush and back-flush of a gas chromatography (GC) column , followed by an oxidizer, a methanizer, and a flame ionization detector (FlO)

. The GC separates the NMNEOC from other constituents of the sample (methane, ethane, CO 2 , 

## H 2 

## 0, O2 , 

## N2 , 

## etc
. ). The oxidizer converts the NMNEOC to carbon dioxide

. The methanizer converts the resulting CO 2 

## to methane

. The methane content is detected by the FlO as ppmcarbon

.

R021 0458-R 1 10

## Modifications suggested by SCAQMD to the Method 25.3 analytical procedures approved for MC under the LAP are: • Pressurization of the canisters to 900 mm Hg with Ultra High Purity (UHP) helium analyzed/certified to contain less than 0.05 ppmv of total hydrocarbons as carbon • Analyzing only the Summa canister fraction of the normal 25.3 sample. No water vial used in sampling, no water vial analysis. • Utilization of a larger (-2 ml) sampling loop • Development of a custom low level (0.1 - 5.0 ppmV propane) calibration curve • Performance of a Minimum Detection Limit (MOL) study • Determination of a Practical Quantitation Limit (PQl) from the MOL study Results are reported in parts per million by volume as carbon to 2 significant digits, corrected to 15% O 2 

## using the O2 

## from the canister analysis. The average of the results for the duplicate samples is compared to the Emission Standard for determination of the compliance status. Note: The following message was received on November 9, 2012 and the content was incorporated into this protocol; 

## From: Roy Olivares [mailto:ROlivares@aqmd.gov] Sent: Friday, November 09, 2012 10:19 AM To: Mark McDaniels Subject: Revised 

# voe testing, condition D29.1
Mark
The current 

# voe section of 

## D29.1 is the following For natural gas fired turbines only, 

# voe compliance shall be demonstrated as 

## follows: a) 

## Stack gas samples are 

## extracted into Summa canisters maintaining a 

## final canister pressure between 400-500 mm 

## Hg absolute, b) Pressurization of 

## canisters are done 

## with zero 

## gas analyzed/certified to contain less than 0.05 ppmv total hydrocarbon as 

## carbon, and c) 

## Analysis of 

## canisters are per 

## EPA Method TO-12 (with pre concentration)and temperature of 

## canisters when extracting samples for analysis is not below 70 deg F. The use of 

## this alternative method for 

# voe compliance determination does not mean that it is more accurate 

## than AQMD Method 25.3, 

## nor does it mean that it may be used in lieu of

R0210458·R1 

# Deltab.

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# _-

........... 11

## AQMD Method 25.3 

## without prior approval except for the determination of 

## compliance with the VOC BACT level of 

## 2.0 ppmv calculated as carbon 

## for natural 

## gas fired turbines.
Mike Garibay from source testing has proposed the following VOC testing For natural gas fired turbines only, VOC compliance shall be demonstrated as follows an 

## alternative to AQMD Method 25
. 3 

## for 

## the purpose of 

## demonstrating compliance with BACT as determined 

## by CARB and 

## AQMD, may 

## be the following : a) 

## Triplicate S stack gas samples are 

## extracted directly into Summa canisters, maintaining a 

## final canister pressure between 

## 400-500 mm 

## Hg absolute, b) Pressurization of 

## the Summa canisters are 

## is done 

## wi th zero gas analyzed/certified 

## to containing less than 0.05 ppmv total hydrocarbons as carbon, and 

## c) Analysis of 

## Summa canisters are 

## is per unmodified EPA Method TO

- 12 (with preconcentration) or 

## the canister analysis portion of 

## AQMD Method 25.3 

## wi th a 

## minimum detection limit of 

## 0.3 ppmvC or 

## less and 

## reported to two significant figures, and 

## (d) The temperature of 

## the Summa canisters when extracting samples for analysis is not 

## to be below 70 degrees Fahrenheit. The use of 

## this alternative method for VOC compliance determination does not mean 

## that i t is more accurate than 

## unmodified AQMD Method 25.3, 

## nor does it mean 

## that it may 

## be used in 

## lieu of 

## AQMD Method 25.3 

## without prior approval, except for 

## the determination of 

## compliance with the VOC BACT level of 

## 2.0 ppmv VOC calculated as carbon set by CARE for 

## natural gas fired turbines. please have the 

# voc te s ting portion of the source test protocol address the above changes roy Roy Olivares Air Quality Engineer II 

## Energy and 

## Public Service Team 

## South Coast Air Quality Management 

## District 21865 Copley Drive Diamond 

## Bar , CA 91765 909

- 396-2208

R0210458 · R1 12

## 3.5 PM BY SCAQMD METHOD 

## 5.1 Particulate matter will be measured using EPA Method 201A in conjunction with SCAQMD Method 5.1. SCAQMD Method 5.1 is cited as the Table in Condition D29.1 lists District Method 5. District Method 5 .1 measures total particulate

. This total particulate measurement could include material >10 microns. Use of the cyclone as in 201A will prevent overstating of PM 10 

## emissions if all of the PM emiss i ons from these units are not PM 1o • 

## A single test will be performed at each of the three conditions; 100%, 75%, and 50% load conditions. Flue gas is drawn through a stainless steel nozzle, glass or stainless steel probe , unheated Teflon line followed by four impingers. Impingers #1 and #2 contain approximately 100 ml of deionized water, impinger #3 is empty, and impinger 

## #4 contains silica gel. A backup filter is placed between impingers #3 and 

## #4. The sample will be collected isokinetically (90 - 110%) using a 24-point traverse at the exhaust stack location

. Each point will be sampled for 10 minutes resulting in a 240 minute sample time per test. Figure 3-3 presents a diagram of the sampling system.

R021 0458-R 1 

## 13 

# 8e/laJ1. 

# "---Temperature

# ~- Pitot Tube



## s- Type Pitot 

### Tube

# ~ FIGURE 3-3 SCAQMD METHOD 5.1 SAMPLE SYSTEM

Manometer


## Orifice Connecting Tubing



## Dry 

## Gas

Meter Filter Temperature 

### Sensor

Empty 

### Vacuum Gauge



## The sample is recovered in two fractions: 1) nozzle, probe, connecting line and impinger rinse (01 

## water) and 2) backup filter. Filter weight gain and water solution weight gain are each determined gravimetrically.

R0210458-R1 14 

# De/fat.. 

# ""---

# 4.0 REPORTING Following the test. a report will be generated which documents the results of the tests
. The report will be prepared using the following basic outline: I. Title page A. Report Title B. Prepared For: C

. For Submittal To: D. Prepared By : E

. Date F. Report Number II. Review Page 

## A. Signatures of person who prepared the report and signature of person who reviewed the report II I. Table of Contents IV

. Introduction and Summary A. Identifies the client. source , reason for the test, test date(s), test personnel , client/source personnel B

. Presents a summary of the test results C

. Outlines the organization of remainder of the report. V. Unit Description 

## A. Process description B

. Control equipment description C. Sample location(s) description D

. Unit operating condition(s) during the test VI. Test Description 

## A. Test methods, replicates, duration, calculations VII. Test Results and Evaluation 

## A. Re-states the results of the test B

. Results tables with more detail on individual test runs and supporting data C. Evaluation of the test results and data validity VII I. Appendices 

## A. Test Data

R021 0458-R 1 15 

# De//a11 

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## 1
. Data Sheets/Stripcharts 2
. Laboratory Data 3. Quality Assurance Data B. Process data 1. Unit and control equipment operat i ng data C. Calculations D. Quality Assurance Program Summary

R021 0458 - R 1 

## 1 6 

# 1Ie//a!1
........

# _-

## APPENDIX A QUALITY ASSURANCE

R021 0458-R 1 

## A-1 

# Deltal1 

# "'-. --

## QUALITY ASSURANCE PROGRA M SUMMARY 

## Delta Air Quality Services, Inc

. is committed to providing emission related data which is complete, precise, accurate, representative, and comparable. Delta ' s quality assurance program and procedures are designed to ensure that the data meet or exceed the requirements of each test method for each of these items

. The quality assurance program consists of the following items :
• Assignment of an Internal QA Officer • Development and use of an internal QA Manual • Personnel training • Equipment maintenance and calibration • Knowledge of current test methods • Chain-of
- custody • QA reviews of test programs Assignment of an Internal QA Officer : Delta has assigned an internal QA Officer who is responsible for administering all aspects of the QA 

## program. Internal Quality Assurance Manual: Delta has prepared a QA Manual according to the guidelines issued by EPA. The manual documents and formalizes all of Delta's QA efforts

. The manual is a " living" document which is revised as Delta adds capabil ities and procedures

. The QA manual provides details on the items provided in this summary. Personnel Training : Personnel training is essential to the production of h i gh quality test results

. Delta's training programs include:
• A requirement for all technical personnel to read and understand the test methods performed • A requirement for all technical personnel to read and understand the Delta QA manual • In-house training • Quality Assurance meetings • Attendance at EPA sponsored training courses • Maintenance of training records

. Equipment Maintenance and Calibration: All laboratory and field equipment used as a part of Delta's emission measurement programs is maintained according to manufacturer's recommendations

. A summary of the major equipment maintenance schedules is summarized in Table A-1

. In addition to routine maintenance, calibrations are performed on all sampling equ i pment according to the procedures outlined in the applicable test method

. The calibration intervals and techniques for major equ i pment components i s summarized in Table A-2

. Knowledge of Current Test Methods : Delta maintains current copies of EPA, ARB , and SCAQMD Source Test Manuals and Rules and Regulations. De lta personnel coordinate , attend , and present pape rs at emission test i ng related conferences. Delta personnel maintain memberships in the Ai r and Waste Management Association and Source

R0210458-R1 

## A-2 

# De /

tab. 

# ----

## Evaluation Society

. Delta personnel continually work with i ndustry and regulatory agencies in monitoring and developing new methods and rules

. Chain-of-Custody : Delta maintains chain-of-custody documentation on all data sheets and samples

. Samples are stored in a locked area accessible only to Delta source test personnel. Data sheets are kept in the custody of the originator , program manager , or in locked storage unt i l return to Delta's office. Upon return to the office , copies are made and stored in a locking file. The original data sheets are used for report preparation and any additions are initialed and dated

. QA Reviews : Every Delta report is reviewed by someone sepa rate from the report author. The reviewer i s selected based on knowledge of the test methods used and the source tested

. Periodic field, laboratory , and report reviews are performed by the QA Officer

. Test plans are reviewed to ensure proper test methods are selected and reports are reviewed to ensure that the methods were followed and any deviations from the methods are justifi ed and documented

.

R02 1 0458-R1 A - 3 

# 861f11b..
...............

# -

## TABLE A-1 EQUIPMENT MAINTENANCE SCHEDULE Equipment Pumps

Flow Meters
Sampling Instruments Acceptance Limits 1. Absence of leaks 2
. Ability to draw manufacturers required vacuum and fiow 1
. Free mechanical

movement
1. Absence of

malfunction 2. Proper response to zero, span gas Integrated sampling 1. Absence of leaks tanks Mobile van sampling 1
. Absence of leaks system

Sampling lines

R0210458-R1 1
. Sample degradation less than 2%

A-4 Frequency of Service Every 500 hours of operation or 6 months, whichever is less
Every 500 hours of operation or 

### 6 months, whichever is less As recommended by manufacturer Methods of Service 1. Visual inspection 2. Clean 

### 3
. Replace parts 4. Leak check
1
. Visual inspection 2. Clean 

### 3
. Calibrate As recommended by manufacturer
Depends on nature of 1. Steam clean use 

## 2. Leak check Depends on nature of 1. Change filters use 2. Change gas dryer 

### 3
. Leak check 4
. Check for system contamination After each test series 1
. Blow dry, inert gas through line unt i l dry

.



# Delta/j.

.. .....**~--**

## TABLE A-2 MAJOR SAMPLING EQUIPMENT CALIBRATION REQUIREMENTS Sampling Equipment Calibration Frequency Calibration Procedure Acceptable Calibration Criteria Continuous Analyzers Before and after each 3-point calibration error < 2% of analyzer range test day test Continuous Analyzers Before and after each 2-point samp l e system < 5% of analyzer range test run bias check Continuous Analyzers After each test run 2-point analyzer drift < 3% of analyzer range d etermination CEMS System Beginning of each d ay leak check < 1 in

. Hg decrease in 5 min

. at> 20 in

. Hg Continuous Analyzers Daily 3-point linearity < 1 % of analyzer range NO, Ana l yzer Daily N02 -> NO converter > 90% efficiency S-type pitot tube Semi-annually Dimensional calibration Meet dimensional criter i a of Method 2 S
-type pitot tube Annually Wind t u nnel calibrat i on Defined in Method 2
S
-type p itot tube Prior to each project Visual inspection Meet dimensional criteria of Method 2 Differential Pressure Semi-annually Correction factor based +/- 5% Gauges (except for on 5-point compar i son to manometers) standard Differential Pressure Bi-monthly 3-point comparison to +/-5% Gauges (except for standard, no correction manometers) factor Manometer Semi-annually Clean and replace fluid Barometer Semi-annually Adjusted to mercury-in - +/
- 0
. 1 inches Hg glass or National Weather Service Station Dry gas meter Semi-annually Calibration check at 4 +/-2% flow rates using a NIST

traceable stand a rd Dry gas meter Bi-monthly Calibration check at 2 +/- 2% of semi - annual flow rates using a NIST factor

traceab l e standard Dry gas meter orifice Annually 4-point calibration for l1H@ Temperature sensors Semi-annually 3-point calibration vs. +/- 1.5% NIST traceable standard

R0210458-Rl A-5

## APPENDIXB TEST METHODS

R021 04S8-R 1 B-1 

# 1161111'1


# ..

# _--

## SCAQMD METHOD 100.1 CALIBRATION SEQUENCE AND CALCULATIONS DEFINITIONS: 

## 1) Analyzer Calibration:

2) Calibration Error:

3) Analyzer Linearity:

4) Sample System Bias:

R0210458-R1 

## Zero and span gas(es) are introduced directly to the analyzer

. Adjustments are made to the analyzer zero and upscale readings, as necessary to match the certified concentrations of the calibration gas. Zero, mid (40-60% of full scale), and high (80-100% of full scale) calibration gases are introduced directly to the analyzer and the analyzer response to each gas is recorded (without adjustment to the analyzer). The 

## Calibration Error (difference between the analyzer response to the calibration gas and the certified concentration of the calibration gas) must not exceed ±2% of the analyzer full scale for any of the three gases. Analyzer linearity is defined as the difference between an analyzer response to the mid range gas and the predicted analyzer response to the mid range gas based on the analyzer response to the zero and high range gas. The 

## Analyzer Linearity test is required on a semi-annual basis and must not exceed ±1 % 

## of the analyzer range. It 

## should be noted that this linearity requirement is more stringent than the best available calibration standards (+/-2%) for the low CO and NO, concentrations expected during this test program. For this reason, an analyzer linearity of less than 2% will be considered as acceptable for this program.
The 

## sample system bias test involves introducing zero and one upscale (mid or high) calibration gas to the entire sampling system and recording the analyzer response. The 

## analyzer response to the calibration gas after it has passed through the entire sample system is compared to the analyzer response to same the calibration gas injected directly to the analyzer. The 

## test is used to determine the effect which the sample system has on the species of interest and correct the measured values for any effect which the system has. The 

## sample system bias is required to be less than ±5% of the analyzer range for both the zero and upscale gas.

B-2

# Del/a~ 

# "---

## PROCEDURES AND CALCULATIONS : Figu re 1 presents a f l ow chart for the SCAQMD Method 100
. 1 calibration sequence. All calibrations are documented as one-minute averages from the reference method Data Acquisition System

. Following assembly of the system, analyze r warm up t ime, and a successful leak check of the sample system , the ca l ibration/test sequence presented in Figure 1 can begin. An Analyzer Calibration is performed as necessary by adjusting the zero and span settings of the analyzer. These calibrat i ons are not necessarily recorded on the chart recorder. Calibration Error is then determined at three levels for each range (which is expected to be used) of each analyzer

. Th i s check is performed, at a minimum , once at the beginning and once at the end of each test day. The calibration error must not exceed ±2% of the full range of the analyzer as determined by the following equat i on : Calibrat i on Error Analyzer Response- Cal. Gas Value 

# * 100% Analyzer Range The data from the Calibration Error test can be used to determine Analyzer Linearity

. The analyzer response to the mid gas is predicted using l i nea r regress i on and the analyzer response to the zero and high calibration gas and the zero and high calibration gas values. The analyzer linearity must be demonstrated on a semi-annual basis us i ng the following equation : Analyzer Linearity 

# = where : Analyzer Response - Predicted Response Ana lyzer Range * 100%

Respons e to High Gas - Respons e to Zero Gas Pred icted Response :;: .. M id Gas Value + Response to Zero Gas 

### H igh Gas Value 

## The Sample System Bias test is performed before and after each test run and must not exceed ±5% of the analyzer range fo r both the zero and upscale span gas . The system bias is calcu l ated using the following equation : Response to System Bias - Response to Analyzer Cal Sample System Bi as = 

## * 100% Analyzer Range

R021 0458 - R 1 B-3 

# /lell8l:1

.. .....**~--**

## where : Response to Analyzer Cal = 

## The analyzer response to the last time the same calibration gas was introduced directly to the analyzer (this may be the pre-test calibration error value or a more recent analyzer calibration adjustment) Zero and Calibration Drift are calculated for each test run based on the analyzer response during the pre - and post-test sample system bias test. Zero and upscale drift must not exceed ±3% of the analyzer range . I ·f 

## Post- Test System Bias Resonse - Pre - Test System Bias Response Ana yzer Dn t 

# = • 100% Analyzer Range The pre- and post-test analyzer response during the sample system bias test are used to correct the raw test average for any sample system bias and analyzer drift

. The drift/bias corrected data are the actual reported concentrations and are used for subsequent calculations (mass emission rates , Ib/MMBtu , corrections to 3% or 15% O2 , etc.). The drift/bias corrections is performed using the following equation : 

# c-c c = o. 

## C

c 

## C
_ C ma m 0 

## where: Cc 

## = Drift/bias corrected concentration 

# C 

# = Raw Test Average C m 

## = Average of pre- and post-test response to sample system bias span Co 

## = Average of pre- and post-test to sample system bias zero C ma 

# = Span gas value ADDITIONAL QUALITY ASSURANCE CHECKS : SCAQMD Method 100.1 specifies the allowed analyzer interferences for each analyzer type. No interference checks are required for O2 or NO, analyzers. Interference tolerances are given for CO, CO2 , and S02 analyzers

. The analyzers used by Delta are certified by the manufacturers to have interference responses which meet the requirements of Method 100.1. SCAQMD has published a draft method for determining the efficiency of a N0 2 to NO converter. This test will be performed once on the day of the test. The converter efficiency must be 90% or greater
.

R021045B-R1 8-4 

# De/tab. "'-.

# .......

# -

## Analyzer Cal Cal No Error < 2% No Yes /Yes

System No 

## System IBias < 5% Problem? Yes Don't Know Strat i fied No Lo cation? Yes Multi-Point Single Point T e st Test 

# !

. System No Bias < 5% Yes Cal No Drift < 3% Yes Note: AQMD policy allows multiple 

## Another No Analyzer Cal test runs to be validated by one set of pre- and post-test sample system 

## Test? (if necessary) bias tests as long as the bias 

# ! checks are performed w it hin 2 hours 

## Yes of the previous bias check. 

## No No Analyzer Cal Cal? Error < 2% Yes 

# ! Yes No Yes System 

# [ Finish 

# ) Bias < 5% 

# t-
FIGURE 1: SCAQMD METHOD 100.1 CALIBRATION AND TEST SEQUENCE

R021 0458 - R 1 8-5 

# Delfal'1 

# ..

# _ .........

# -Temperature S Probe

# ~

Pltot Tube



# / S-Type Pitot Tube



## R021 0458-R 1 Manometer



### Orifice Connecting Teflon TUbing



### Temperature



## Dry Gas

Meter Filter Temperature



### Valve



## SCAQMD METHOD 5.1 SAMPLING TRAIN

8-6

## Filter Probe

Flow Controller



## MODIFIED SCAQMD METHOD 25.3 SAMPLING APPARATUS

R021 0458-R 1 

## 8-7 

# 1le1/a!1.
....... 

# -.-

## APPENDIX C CALCULATIONS

R021 0458-R 1 C-1 

# IJeltal1 

# ""---

## GENERAL EMISSION CALCULATIONS 

## 1) Stack Gas Velocity A. Stack gas molecular weight, Ibllb-mole 

# MW dry 

# = 0.44 

## * 

# %C0 2 

# + 

# 0.32 * 

# %0 2 

# + 

# 0.28 * 

# %N 2 

# MW 

# wet 

# = MW dry 

# * (1-Bwo) + 

## 18 

# * Bwo B

. Absolute stack pressure, iwg 

## Ps 

# = Pbar + Psg 

# 13.6 

# c. Stack gas velocity, ftIsec 

# Vs 

# = 2.9 * 

# C p 

## * .J!).p 

# *.JT: * 2) Moisture A. Sample gas volume, dscf 

# V

mstd 

# = 0.03342 * 

# Vm * 

# (P bar 

## + B

. Water vapor volume, scf 

# v = 

# 0.0472 * V. 

# * 

# T ref wstd Ie 

# 528 oR 29.92 * 

# 28.95 P

s * 

# MW 

# wet



# c . Moisture content, dimensionless

3) Stack gas volumetric flow rate 

## A. Actual stack gas volumetric flow rate, wacfm Q 

# = V * 

# A * 

# 60 s s 

# B

. Standard stack gas flow rate, dscfm

R021 0458-R 1 C-2 

# 8e//a/1

..

# _--

## Q 

# = Q 

# * 

# (1- B ) * 

# T,er * 

# P s sd we Ts 

# 29
. 92 4) Gaseous Mass Emission Rates. Ib/hr M 

# = ppm * MIJII; * Q Sd • 

## 60 

## SV 

# * 10 6 

## 5) Emission Rates. Ib/MMBtu 

# Ib
_ ppm * MIJII; * F * 

# 20
. 9 MMBtu - SV*10 6 

# 20.9-%0, 6) Emission Factor. Ib/MMSCF 

# Ib Ib *HHV MMSCF MMBtu VI. Percent Isokinetic 

# 17.32 x 

# T, (Vm 

# std) 528 e 

# R 

# /- x----

- (1- Bwo)O 

# x V, x Ps x Dn' T,..! VII. Particulate emissions a) Grain loading, 

## gr/dscf C 

# = 0
.01543 (M,/Vm SId) 

## b) Grain loading at 

# 12% CO" 

## gr/dscf C 12 % 

## co, 

# = C 

## (121% CO,) c) Grain loading at 

# 3% 0" gr/dscf 

## C 3 % 0' 

# = C 

# * 17.9/(20.9-%0,) d) Mass emissions, Ib/hr M 

# = C x Qsd x (60 

## min/hr)/(7000 gr/lb) e) Particulate emission factor

6 

# lIb 20
..9 lb / 10 

# Btu 

# = ex 7000gr x F x 20.9
_ % 

# 0,

R021 0458-R 1 C-3

## Nomenclature : 

## As Bwo 

## C 12 %C02 

## C 3 %02 

## C 

# C

p 

## On 

## F H HHV 

## I 

## Mn MI 

## MW 

## Mwi



# o L\P 

## P bar 

# Ps Psg 

# a Ows Osd 

## SV 

# Tm Tret 

# T, Vs Vic Vm Vm'td 

## V WStd 

# Y

d



## R021 0458-R 1 

## = stack area , 

## ft2 = flue gas moisture content , dimensionless 

# = particulate grain loading, gr/dscf corrected to 12% CO 2 

## = particulate grain loading, gr/dscf corrected to 3% CO 2 

# =

particulate grain loading, gr/dscf 

## = pitot calibration factor, dimensionless 

# =

nozzle diameter, in. 

## = fuel F-Factor, dscf/MMBtu 

## @ 0% O 2 

# = orifice differential pressure , iwg 

# = fuel higher heating value, Btu/SCF 

## = % isokinetics 

# =

mass of collected particulate, mg 

## = mass emission rate of specie i, Ib/hr 

## = molecular weight of flue gas, Ib/lb-mole 

## = molecular weight of specie i : 

## S02: 64 NO x : 

## 46 CO: 

## 28 HC: 

## 16 = sample time, min. 

# =average velocity head, iwg 

# = (,hp)2 

# = barometric pressure, inches Hg 

## = stack absolute pressure, inches Hg 

# =

stack static pressure, iwb 

# =

wet stack flow rate at actual conditions, wacfm 

## = wet stack flow at standard conditions, wscfm 

# =

dry standard stack flow rate, dscfm 

## =**s~ecific** 

## molar volume of an ideal gas at standard conditions,



## ft lib-mole 

# = meter temperature, 

## OR = reference temperature, 

## OR 

# =

stack temperature, 

## OR 

# =

stack gas velocity,

. ft/sec 

## = volume of liquid collected in impingers, ml 

# =

uncorrected dry meter volume, dcf 

## = dry meter volume at standard conditions, dscf 

# =

volume of water vapor at standard conditions , scf 

## = meter calibration coefficient

C-4 

# De/Ia/:). '"'---"

## APPENDIX D FORMS

R0210458 · Rl D·l 

# 1Ie1/a!:1**---**

# South Coast Air Quality Management District 21865 Copley Drive, Diamond Bar, CA 91765-4178 (909) 

### 396-2000 ' www .aqmd.gov

Mr. Robert A. 

### Finken Delta Air Quality Services , Inc. 1845 N. Case Street Orange, CA 92865 Subject: LAP Approval Notice Reference 

### # 96LA 1220 Dear Mr . Finken : January 11,2012

We completed our review of the renewal application you submitted for approval under the South Coast Air Quality Management District's Laboratory Approval Program (AQMD LAP). We are pleased to inform you that your finn is approved for the perio' d beginning January 31 , 2012, and ending January 31, 2013 for the following methods: SCAQMD Methods 1-4 SCAQMDMethod 100.1 SCAQMD Methods 25.1 and 25.3 (Sampling) SCAQMD Methods 5.1, 5.2, 5.3, and 6.1 SCAQMD Rule 1420

- (Lead) 

### Ambient Sampling USEPA CTM-030 and ASTM 06522-00 Thank you for participating in the SCAQMD LAP. Your cooperation helps us to achieve the goal of the LAP: 

### to maintain high standards of quality in the sampling and analysis 

### of source emissions. You may 

### direct any questions or information to LAP Coordinator, Glenn Kasai. He may be reached by telephone at (909) 396

-2271, by facsimilie at (909) 396

- 2099, or via e-mail at gkasai@aqmd.gov
.

RE:GK/gk 

### cc: Mike Garibay 

### Glenn Kasa.i 12011 I LapRenewal.doc



## R021 0458-R 1

# s~~~er y 

# &

___ ;I Ru Eden, Senior Manager Laboratory Services & 

### Source Test Engineering



### D-2 

# Ilellal1

.. ................ 

# -

### ::0 

### o 

# '"**~**

### ~ 01 0> 

## ;'0**~**



## o 

## W



# II. 

# iI !i;:a

# !~ State of California 

# Air Resources Board Approved Independent Contractor 

# Delta 

# Air Quality 

# Services, Incorporated
This is to certify

. Ilia!the compa,ny listed EibQve 'hasbeen approved by the Air 

# ResoutceS' Board to ' conduct eompnance testing pursuant to titliH.7,: c'alifornia · Code : pf 

## RegutatIDns', section 

## 91207 until

## Ju~30**2013',.fc)r** those 

# test**methods ~sted**  below: 

## ARB S
... re<: 

### Test

## Meth~.; 1,2,3,
.4,5,
. 6,'8, 17, 20 / 501 

### 106'«;0; 

## cO:;. NO" 

### 0" SO,)

# (}L~/f_~ Alberto

## AY~1.. Ph.D., M

. S

. E

. 

### Chief, Monnoring and Laboratory DMsion;:0 

### a N**~** 

### a .". 

### en (l) 

# , ;:0**~**



# a


# ...**~**



# IS.

# ~ State of California 

# Air Resou r ces Boa r d Approved Independent Contractor 

# Delta Air Quality**Seni ~**  

# Incorporated This is to certifyiHat the cOi)1pany liste<)

# ~bovehas been approved by the Air Resolll;Ces : B6ard to ' condtictcorrip'!iance testing pursuant to titfEi J 1?: ; ; CallforruaCod!'fPf Ril9U1ations ; section 91207 until June30 ; 2013 ; ' for those- test
.niethOds : i1sted below :**.~'** 

## . . 

# , . ' 

# . , .**~ ~,**  '.**,~ "** 
• I 

### Visible · Emlw.oD.s E valuation U.S.

### EPATestMethods**2~lA (1991**  .....

### ~I, 202.(1991 version)



## . if
Alberto Ayala.?f>.D

. • M

. S

. E. 

### Chief . Monitoring and LaboratOlY Division

## STATEMENT OF NO CONFLICT OF INTEREST AS AN INDEPENDENT TESTING LABORATORY (To be completed by authorized source testing firm representative and included in source test report) 

## The following facility and equipment were tested by my source testing firm, and are the subjects of this Statement: Facility ID: .,.-,.-____ ='4;::6"'5:;::3=.6

__________________ _ Date(s) Tested:

_____ T:::e::;s::-t'=P,..la""n::--:-:::--_-=---:---:-

__________ _ Facility Name: :-____**-:=C7P7-V::::S'7e=7n!!t!!:in!:'e'7'""E~n:!!:e!.lrg:I.JvL!...P!.lro~i"'ec!<lt'--** 

## __________ _ Equipment Address: 911 Bixby Drive City of Industry , California 91748 Equipment Tested:

___ -:;U'-';n"-;its=''''',**2~',.:3",-,**

## =4,-:'**5::a,-,!6~,**

## .f:7!-" &7:'8-=,--:--:-:;

________ _ Dev i ce 10, 

## AlN, P/N:

___ ""DC!1""**D~7!..1,..!:D!..l1,"3** 

## ... ,**~D~19~'L..!D~2.,5",-,**

## .>1.3.!.J1 ,...,3!,!7

.... ,**~&~4~2** 

## ________ _ I state , as its legally authorized representative , that the source testing firm of: Source Tes t Firm: Delta Air Quality Services

. Inc. Bus i ness Address : .,!,1**",84",5,-",N~ .**  

## C=as"'e:.;S,..t"'re"'e"'t

__________________ _ Orange, California 92865-4234 i s an " Independent Testing Laboratory" as defined in District Rule 304(k): For the purposes of this Rule, when an independent testing laboratory is used for the purposes of establishing compliance w ith Di strict rules or to obtain 

## a District permit to operate, it must meet all of the following criteria:

(1) The testing laboratory shall have no financial interest in the company or facility being tested

. or in the parent company or any subsidiary thereof- (2) The company or facility being tested, orparent company or any subsidiary thereof, shall have no financial interest in the testing laboratory ; 

### (3) Any company or facility responsible for the emission ofsignificant quantities of pollutants to the atmosphere, or parent company or any subsidiary thereof shall have no financial interest in the testing lab'lratory ; and (4) The testing laboratory shall not be in partnership with, own or be owned by , in part or in full , the contractor who has provided or installed equipment (basic or control) , or monitoring systems, or is providing maintenance for installed equipment or moni t oring systems, for the company being tested 

## Furthermore, I state that any contracts or agreements entered into by my source test i ng firm and the fac i lity referenced above, or its designated contractor(s) , either verbal or written , are not contingent upon the outcome of the source testing , or the source testing i nformation provided to the SCAQMD

.._______ , Signature:

# L,t-**{~j** 

# J 1->..

Bob F inken (Name) President (Title) FORM ST- 1 10 : stevfor l. doc (Revised 

## 11/18/98)

R0210458-R1 0-5 Date:

___ 

## -'-"2='-17'-'1".20"-'",,2'--

___ _ 714 - 279-6777 

## 121712012 (Phone) (Date)



# 811/ 18/1 

# '"'- - -

## APPENDIX E FACILITY PERMIT TO OPERATE CONDITION 029.1

R038842-R1 E-1 

# DIlIfa!1


# ---

## SOUTH COAST AIR QUALITY 

## MANAGEMENT DISTRICT 

## 21865 Copley Drive. Diamond Bar. CA 91 765


# FACILITY PERMIT TO OPERATE CPV SENTINEL LLC Section H Page : 35 Facilitv 10 : 152101**R~ision# :**  0 Date: April 1S,20ll



# SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE
The operator shall comply w ith the terms and conditions set forth below: The operator shall also install and maintain a device to continuously record the parameter being measured The measuring device or gauge shall be accurate to within p lus or minus 

## 5 percent. It shall be calibrated once every twelve months It shall be calibrated once every twelve months The pressure drop across the catalyst shall not exceed 12 inches water column [RULE 1303(a)(1)-BACT, 5-10-1996; RULE 1303(aXI)-BACT, 12-6-2002; RULE 1703(aX2)

- PSD-BACT, 10-7-1988; RULE 1005, 5-6-1005) [Devices subject to this condition : C4, CIO, C16, C22, C28, C34, C40, C46) 012
. 5 The operator shall install and maintain a(n) non-resettable elapsed time meter to accurately indicate the elapsed operating time from the engine
. [RULE 1110.2,2-1-2008; RULE 1303(b)(2)-Offset, 5-10-1996; RULE 1303(bX2) -Offset, 12-6

- 2002; RULE 1470,6-1-2007; RULE 1012, S-6-100S) [Devices subject 

## to this condition : 049) D29
. 1 The operator shall conduct source testes) for the pollutant(s) identified below. Pollutant(s) 

## to 

# I Required Test Methodes) 

# I Averaging Time 

# I Test Location be tested NOX emissions Distr ict method 100.1 1 hour Outlet ofthe SCR serving this equipment CO emissions 

# I District method 100.1 

# I I hour 

# I Outlet of the SCR serving this equipment SOX emissions 

# I AQMD Laboratory Method 307-91 

# I Not Applicable 

# I Fue l sample 

# voe emissions 

# I District Method 25.3 

# I 1 hour 

# IOutlet ofthe SCR serving this equipment

## SOllTH COAST AIR QUALITY MANAGEMENT DISTRICT 21865 Copley Drlve. Diamond Bar

. CA 91 765



# FACILITY PERMIT TO OPERATE CPV SENTINEL LLC SeClion H Facility 10 : 

### Revision ' : Date : Page : 36 IS2707 

## o April 15.2011



# SECTIONH: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE
The operator shall comply with the terms and conditions set forth below: PM 

## I0 

# I District Method 

## 5 emissions NH3 emissions 

# I District method 207.1 and 5.3 or EPA method 17 

# I 4 hours 

# II hour 

# IOutlet of the SCR serving this equipment 

# I

Outlet of the SCR serving this equipment

# •**~i~** 

### • .**l~~ L**  

### SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 21865 

## Copley Drive, Diamond Bar, CA 91 765


# FACILITY PERMIT TO OPERATE CPV SENTINEL LLC Section H Page: 37 FacilitY 10: 152707 Revision II: 0 Date : April IS
. 2011



# SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE
The operator shall comply with the terms and conditions set forth below: The test shall be conducted after AQMD approval of the source test protocol, but no later the later of 180 days after initial start-up or three hundred hours of operations after start-up. The AQMD shall be notified of the date and time of the test at least 10 days prior to the test 

## The test shall be conducted to detennine the oxygen levels in the exhaust. In addition, the tests shall measure the fuel flow rate (CFH), the flue gas flow rate, and the turbine generating output in MW. The test shall be conducted in accordance with AQMD approved test protocol. The protocol shall be 

## submitted to the AQMD engineer no later than 45 days before the proposed test date and shall be approved by the AQMD before the test commences. 

## The test protocol shall include the proposed operating conditions of the turbine during the tests, the identity of the testing lab, a statement from the testing lab certifYing that it meets the criteria of Rule 304, and a description of all sampling and analytical procedures The test shall be conducted when this equipment is operating at maximum, average, and minimum loads
. For natural gas fired turbines only, VOC compliance shall be demonstrated as follows: a) Stack gas samples are extracted into Summa canisters maintaining a final canister pressure between 400-500 mm Hg absolute, b) Pressurization of canisters are done with zero gas analyzed/certified to contain less than 0
. 05 ppmv total hydrocarbon as carbon. and c) Analysis of canisters are per EPA Method TO-12 (with pre concentration) and temperature of canisters when extracting samples for analysis is not below 70 deg F. The test shall be conducted for compliance verification of the BACT VOC 2.0 ppmv limit. The test results shall be 

## reported with two sil\llificant dip;its.

## SOlITH COAST AIR QUALITY MANAGEMENT DISTRlcr 21865 Copley Drive, Diamond Bar, CA 91 765



# FACILI TY PERMIT TO OPERATE CPV SENTINEL LLC SectiDn H Page ; 31 Facility ID: 152707 Revision II: 0 o.tc : AprillS,2011



# SECTION H : PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE
The operator shall comply with tbe terms and conditions set forth below: [RULE 1303(a)(1)-BACT, 5-10-1996; RULE 1303(aXI)-BACT, 12-6-2002; RULE 1303(b)(Z}-Oft'aet, 5-10-1996; RULE 1303(b)(2}-Offset, 12-6-2002 ; RULE 1703(a)(2)- PSD-BACT, 10-7-1988; RULE 2005, 5-6-2005] [Devices subject to this condition: 01, 07, 013, 019, 025, 031, 

## 037, 043] 029.2 The operator shall conduct source testes) for the pollutant(s) identified below. Pollutant(s) to be tested NH3 emissions 

# I Required Test Method(s) 

# I District method 207.1

and 5.3 or EPA method 17 

# I Averaging Time 11 hour 

# I Test Location 

# I

Outlet ofthe SCR serving this equipment
The test shall 

## he conducted and the results submitted to the District within 45 days after the test date
. The AQMD shall be notified of the date and time of the test at least 7 days prior to the test. The test shall be conducted at least quarterly during the first twelve months of operation and at least annually thereafter. The NOx concentration, as determined by the CEMS, shall be simultaneously recorded during the ammonia slip test . 

## If the CEMS is inoperable, a test shall be conducted to determine the NOx emissions using District Method 100.1 measured over a 60 minute averaging time period. If the turbine is not in operation during one quarter, then no testing is required during that quarter The test shall be conducted to demonstrate compliance with the Rule 1303 BACT concentration limit [RULE 1303(a)( 1 }-BACT, 5-10-1996; RULE 1303(aXI}-BACT, 12-6-2002] [Devices subject to this condition: Dl, 07, 013, 019, 025, D31, 

## 037, 043]

# END OF DOCUMENT