March 11, 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 4 

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 4 at the CPV Sentinel Energy Project. Testing was conducted in accordance 

with Condition of Certification AQ-7 and Section H, Condition D29.3 of the facility's 

Title V Permit. 

Should you have any questions or require additional information related to this submittal, 

please contact me at (916) 444-6666. 

Sincerely, 

-r--c:--- ~ P"L ____ ____ 

Tom Andrews 

Senior Engineer 

cc: Roy Olivares, SCAQMD 

Craig Hoffinan, 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 4 

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 I ROBERT A. FINKEN 

MARCH 7, 2013 

REPORT NUMBER: R0410688 

Air 

/Jella 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. 

R041 0688 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. 

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. 

~ Lf (,! J I Date ----------~ ~~ ,~------------

R0410688 

Robert A. Finken 

President 

iii 
CONTENTS 

SECTION 

1.0 INTRODUCTION AND SUMMARy ........................................................................... 1 

2.0 UNIT DESCRIPTION AND TEST CONDITIONS ........... ................. ................. ......... 3 

2.1 UNIT DESCRIPTION ....................................................... ................................ 3 

2.2 TEST CONDITIONS ............. ................. ........ ................................................... 5 

2.3 SAMPLE LOCATION ............................. .......................... .................. ............... 6 

3.0 TEST DESCRIPTION ...................................................... ...... ............. ...................... 9 

3.1 O2• CO2 , NOx 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 4 Stratification Test .......................................... ...... ........ B-3 

B.1.2 Sentinel Unit 4 Ammonia, ROG, and NOx/CO Testing .......... .............. B-4 

B.1.3 Sentinel Unit 4 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 

R041 0688 iv 
D GENERAL EMISSIONS CALCULATIONS ...................... " .................................... D-1 

E CHAIN OF CUSTODY ............................................................................. .............. E-1 

F INSTRUMENT STRIP CHARTS ........................... ... ..................... ............... ........ .. F-1 

G FACILITY PERMIT TO OPERATE CONDITION D29.1 ............. ............................ G-1 

H CORRESPONDENCE AND TEST PLAN .. .... ...... .................................................. H-1 

R041 0688 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 029.1 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 4. 

Tests were performed at three load conditions to determine oxides of nitrogen 

(NOx), carbon monoxide (CO), oxides of sulfur (SOx), reactive organic gases (ROG), 

particulate matter (PM), and ammonia (NH3) 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 February 11-12, 2013. The Delta test crew consisted 

of Ali Aleshaiker, Ray Madrigal, Shannon Scrugham, and Justin Miller. 

The fuel sampling was repeated on February 22, 2013. There was insufficient 

sample in the original samples to complete the anaysis. 

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. 

R0410688 1 
TABLE 1-1 

CPV SENTINEL ENERGY PROJECT 

UNIT4 

STACK TEST RESULTS SUMMARY 

Parameter Units 100% 75% 50% Limit Rule 

ppm@ 15%0, 2.26 2.18 2.01 2.5 1703(a)(2) 

NO, ppm @ 15% 0, 2.26 2.18 2.01 15 40 CFR 60 

Ib/MMscf 8.97 842 8.29 12.26(1) 2012 

CO ppm@ 15% 0, 1.80 1.03 0.35 4 1703(a)(2) 

NH3 ppm@ 15% 0, 1.9 0.92 0.83 5 1303(a)(1) 

gr/dscf @ 3% 0, 0.0033 0.0010 0.0018 0.01 475 

Particulate gr/dsc! @ 12% CO, 0.0039 0.0011 0.0022 0.1 409 

Ib/hr 4.38 1.12 142 11 475 

PM1I)/PM'5 Ib/MMscf 4.95 1.60 2.65 5.71(') 

SO/3) Ib/MM8tu 0.00002 0.06 40 CFR 60 

gr H,S/1 00 sci 0.009 0.25(4) SCAQMD Permit 

Condition 861 .1 

ROGs ppm @ 15% 0, 0.58 0.56 0.55 2.0 1303(a)(1 ) 

(1) The 12.261b/MMscf 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/100 scf sulfur content limit is based on annual average of monthly sample results. 

R0410688 2 
2.0 UNIT DESCRIPTION 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 LMS 1 DOPA 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. 

R041 0688 3 
FIGURE 2-1 

SIMPLIFIED PROCESS BLOCK DIAGRAM 

CPV SENTINEL ENERGY PROJECT COMBUSTION TURBINES 

Simplified Process Flow Diagram 

Air 

Water 

Air 

Cooling Tower 

Closed Loop 

Cooling 

LMS100PA 

Water 

Natural Gas Fuel Demineralized 

R041 0688 

Air 

Water 

Heat 

Exhaust to Atm. 

Exhaust CO Catalyst SCR -

Ammonia 

19% Aqueous 

4 
FIGURE 2·2 

GENERAL ARRANGEMENT OF MAJOR COMPONENTS 

C I to ,. J, 

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 0688 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 5,354 6,974 8,845 

Turbine Generating Output (MW) 55.0 80.5 106.5 

Ammonia Flow, Ib/hr 105.0 112.3 110.0 

Exhaust Temperature, ' F 769 752 786 

Exhaust Flow Rates, kscfh 14,959 18,145 21 ,154 

Notes: Data from facility DAS except exhaust gas temperature where PM test data was used. 

Data collected during PM test intervals 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. 

R0410688 6 
Stack Exit 1080,0 in. 

Silencer Bottom 925.9 in. 

Ports 841 .6 in. 

Platform 789.6 in. 

Base of Stack 518.5 in. 

Grade 0.0 in. 

FIGURE 2-3 

SAMPLE LOCATION DETAILS 

Inside Diameter, in . 

--+- 162 +--

I 

84 Distance A, inches, 0.5 Diameters 

! Sam pie ports 

T 

323 Distance B, inches , 2.0 Diameters 

1 

.._--,E",x""haust Flow 

Elevation View 

90 ft. 

66 ft. 

Oft 

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 0.9' 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. 

R0410688 7 
TABLE 2-2 

12-POINT STRATIFICATION CHECK RESULTS 

GEMMA POWER SYSTEMS 

CPV SENTINEL UNIT 4 

0, CO, NO, CO 

Port Point % % ppm ppm 

South 3 13.18 4.56 3.14 1.50 

South 2 13.18 4.56 3.02 1.89 

South 1 13.13 4.59 3.03 1.84 

East 3 13.15 4.58 3.15 2.03 

East 2 13.19 4.55 3.01 2.75 

East 1 13.19 4.56 2.76 2.51 

West 3 13.19 4.55 3.28 3.11 

West 2 13.19 4.56 3.30 2.98 

West 1 13.18 4.56 3.28 2.81 

North 3 13.20 4.54 3.32 3.01 

North 2 13.22 4.53 3.43 2.72 

North 1 13.21 4.54 3.50 2.83 

Average 13.2 4.6 3.2 2.5 

Maximum 13.2 4.6 3.5 3.1 

Minimum 13.1 4.5 2.8 1.5 

Maximum Difference from Average 0.1 0.0 0.4 1.0 

Max Difference (% of average) 0.4% 0.7% 13.4% 40.0% 

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.) Strat.lNH3, NO;.;, and CO 

Compliance (12 Pts.) 

Sample % of in. % 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 80.6 130.6 95.6 154.9 

7 64.4 104.3 

8 75 121.5 

9 82.3 133.3 

10 86.4 140.0 

11 93.3 151 .1 

12 97.9 158.6 

R0410688 8 
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, NH3, ROGs and SOx. 

TABLE 3-1 

TEST MATRIX 

SENTINEL UNIT 4 

Parameter Method 50% Load 75% Load 100% Load Test Duration 

NOx SCAOMD 100.1 2 runs' 2 runs* 2 runs"" 60 minutes 

02/C02 SCAOMD 100.1 With each run 

CO SCAOMD 100.1 2 runs' 2 runs' 2 runs' 60 minutes 

NH3 SCAOMD 207.1 2 runs 2 runs 2 runs 60 minutes 

S02 SCAOMD 307.91 Fuel Sample, 2 Samples N/A 

PM SCAOMD 5.1 1 run 1 run 1 run 240 minutes 

ROG Modified SCAOMD 25.3 1 pair 1 pair 1 pair - 60 minutes(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 approximately 10 "Hg. Actual test time may be less than or 

more than 60 minutes per sample . 

• Additional runs performed compared to test plan. 

R041 0688 9 
TABLE 3-2 

CPV SENTINEL ENERGY PROJECT 

PERMITTED EMISSION LIMITS 

Parameter Units 

ppm@ 15%02 

NO, ppm @ 15% O2 

Ib/MMscf 

co ppm @ 15% O2 

NH3 ppm @ 15% O2 

gr/dscf @ 3% O2 

Particulate gr/dscf @ 12% CO2 

Ib/hr 

PMlO/PM2.5 Ib/MMscf 

SO, Ib/MM8tu 

gr H2S/100 scf 

ROGs ppm @ 15% O2 

(1) The 12.261b/MMscf is a RECLAIM emission factor, not a limit. 

(2) This is stated in the permit as an emission factor. 

Limit 

2.5 

15 

12.2611 ) 

4 

5 

0.01 

0.1 

11 

5.71 12) 

0.06 

0.2513) 

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 H2S/1 00 scf sulfur content limit is based on annual average of monthly sample results. 

3,1 O2• CO2• NOx AND CO 

O2, CO2 , 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. 

For some test runs, 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. 

R0410688 10 jJe!!i!A 
NO, concentrations were measured on a 0-5 ppm range. CO concentrations 

were measured on a 0-10 ppm range . CO2 concentrations were measured on a 0-10% 

range . O2 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% O2, 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 SCAQMD Method 207.1. A 12-point traverse was performed during each NH3 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 H2S04 , 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 SCAQMD Method 207.1 for 

ammonia concentration using the Ion Selective Electrode technique. One reagent blank 

sample, one DI water sample, and one field blank sample was analyzed. 

Ammonia slip is reported in units of ppm, corrected to 15% O2. 

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 SCAQMD Method 307-91 . Two fuel 

samples were collected in Tedlar bags and sent to Saybolt Laboratory for sulfur analysis 

as total reduced sulfur as H2S. 

3.4 ROG BY MODIFIED 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 (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. 

R041 0688 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 

Filter Probe 

Flow Controller 

R041 0688 12 
The samples are analyzed for NMNEOC (Non-Methane Non-Ethane Organic 

Compounds, i.e. Reactive Organic Compounds ROG) using modified SCAOMD 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 (FID). The GC separates the NMNEOC from other constituents of the 

sample (methane, ethane, CO2, H20, O2, N2, etc.). The oxidizer converts the NMNEOC 

to carbon dioxide. The methanizer converts the resulting CO2 to methane. The methane 

content is detected by the FID as ppmc.,bon. 

Modifications suggested by SCAOMD 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 (MDL) study 

• Determination of a Practical Ouantitation Limit (POL) from the MDL study 

Results are reported in parts per million by volume as carbon to 2 significant 

digits, corrected to 15% O2 using the O2 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 SCAOMD concerning the application of the modified 

SCAOMD Method 25.3 to permit condition D29.1 are located in the test plan in Appendix 

H. 

R041 0688 13 
3.5 PM BY SCAQMD METHOD 5.1 

Particulate matter was measured using 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 prevents overstating of PM10 emissions if all 

of the PM emissions from these units are not PM,o. It was assumed for reporting 

purposes that the SCAQMD Method 5.1 total PM results will be used to determine PM 10 

compliance. 

A single test was 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 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 

per test. 

Figure 3-3 presents a diagram of the sampling system. 

R041 0688 14 
Temperature 

Sensor Probe 

~ PitotTube 

/ 

S·Type P~otTube 

R041 0688 

FIGURE 3-3 

SCAQMD METHOD 5.1 SAMPLE SYSTEM 

Manometer 

Orifice 

Connecting 

Teflon Tubing Filter Temperature 

: _________ impinge~ _ ~_en~or 

Temperature 

Sensors 

Dry Gas 

Meter 

15 

Water 

, ------ ----- --~ 

Empty Silica 

Gel 

Vacuum 

Line 

Vacuum 

Gauge 
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 (NH3), and RaG -100% load 

PM results - 100% load 

NO" CO, NH3, and RaG - 75% load 

PM results - 75% load 

NO" CO, NH3, and RaG - 50% load 

PM results - 50% load 

SO, results 

Additional test runs were performed for some parameters to ensure that sufficient 

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. 

R041 0688 16 
TABLE 4-1 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 4 

NO., CO, NH3, AND ROG 

100% LOAD 

FEBRUARY 11, 2013 

Test Number Run 1 Run 2 Average Limit 

Condition 106 MW 107 MW 

Test Date 2/11/2013 2/11/2013 

Start Time 10:06 11 :40 

Stop Time 11: 19 12:54 

Fuel Flow, hscfh 8,830 8,854 

Stack Flow Rate, dscfm 383,018 357,556 

Stack 0, (%) 13.29 13.15 13.22 

Stack NO, (ppm) @ 15% 0, 2.34 2.18 2.26 2.5 

Stack NO, (lb/MMscf) 9.52 8.42 8.97 12.261') 

Stack CO (ppm) @ 15% 0, 2.08 1.52 1.80 4 

Moisture Fraction (%) 0.105 0.085 

PPM NH3 (flue gas) 245 2.50 248 

PPM NH3 @ 15% 0, 1.90 1.91 1.90 5 

Ib/hr NH3 2.52 240 2.46 

Ib/MMscf fuel NH3 2.85 2.72 2,79 

Stack ROGI1 ), ppm @ 15% 0, 0.58 0.58 2.0 

1) Collected as a simultaneous pair. 

2) The 12.26 Ib/MMscf is a RECLAIM emission factor, not a limit. 

R0410688 17 
TABLE 4-2 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 4 

Test Number 

Condition 

Test Date 

Start Time 

Stop Time 

Fuel Flow, hscfh 

Stack Flow Rate, dscfm 

Stack O2, % 

Stack CO2 , % 

Moisture Fraction, % 

Grain Loading, gr/dscf 

Grain Loading @ 3% O2 

Grain Loading @ 15% O2 

Grain Loading @ 12% CO2 

Mass Emissions, Ib/hr 

Emission Rate, Ib/MMscf 

PM -100% LOAD 

FEBRUARY 11, 2013 

S-4/STK-PM-100-1 

107 MW 

2/11/2013 

8:41 

12:55 

8,845 

350,311 

12.99 

4.44 

0.099 

Particulate Emissions 

0.0015 

0.0033 

0.0011 

0.0039 

4.38 

4.95 

(1) 11 bl/hr PM limit from SCAQMD Rule 475. 

(2) This is stated in the permit as an emission factor. 

R0410688 18 

Average 

0.0015 

0.0033 

0.0011 

0.0039 

4.38 

4.95 

Limit 

0.01 

0.1 

5.71(2) 
TABLE 4-3 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 4 

NO., CO, NH3, AND ROG 

75% LOAD 

FEBRUARY 11, 2013 

Test Number Run 1 Run 2 Average Limit 

Condition 81 MW 80MW 

Test Date 2/11/2013 2/11/2013 

Start Time 15:45 17:10 

Stop Time 16:52 18:19 

Fuel Flow, hscfh 7,018 6,961 

Stack Flow Rate, dscfm 304,102 311 ,648 

Stack 0, (%) 13.81 13.80 13.81 

Stack NO, (ppm) @ 15% 0, 2.07 2.30 2.18 2.5 

Stack NO, (lb/MMscf) 7.84 9.01 8.42 12.261') 

Stack CO (ppm) @ 15% 0, 1.02 1.03 1.03 4 

Moisture Fraction (%) 0.094 0.073 

PPM NH3 (fiue gas) 1.22 0.98 1.10 

PPM NH3 @ 15% 0, 1.02 0.81 0.92 5 

Ib/hr NH3 1.00 0.82 0.91 

Ib/MMscf fuel NH3 1.42 1.18 1.30 

Stack ROG(1), ppm @ 15% 0, 0.56 0.56 2.0 

1) Collected as a simultaneous pair. 

2) The 12.26 Ib/MMscf is a RECLAIM emission factor. not a limit. 

R041 0688 19 
TABLE 4-4 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 4 

PM -75% LOAD 

FEBRUARY 11, 2013 

Test Number S-4/STK-PM-75-1 Average Limit 

Condition 81 MW 

Test Date 2/11/2013 

Start Time 14:48 

Stop Time 18:56 

Fuel Flow, hscfh 6,974 

Stack Flow Rate, dscfm 336,734 

Stack 0" % 13.83 

Stack CO" % 4.05 

Moisture Fraction, % 0.092 

Particulate Emissions 

Grain Loading, gr/dscf 0.0004 0.0004 

Grain Loading @ 3% 0, 0.0010 0.0010 0.01 

Grain Loading @ 15% 0, 0.0003 0.0003 

Grain Loading @ 12% CO, 0.0011 0.0011 0.1 

Mass Emissions, Ib/hr 1.12 1.12 11(1) 

Emission Rate, Ib/MMscf 1.60 1.60 5.71(') 

(1) 11 bl/hr PM limit from SCAQMD Rule 475. 

(2) This is stated in the permit as an emission factor. 

R0410688 20 !!.tlla!:" 
TABLE 4-5 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 4 

NO., CO, NH3, AND ROG 

50% LOAD 

FEBRUARY 12, 2013 

Test Number Run 1 Run 2 Average Lim it 

Condition 55 MW 55MW 

Test Date 2/12/2013 2/12/2013 

Start Time 11 :58 13:30 

Stop Time 13:07 14:39 

Fuel Flow, hscfh 5,337 5,341 

Stack Flow Rate, dscfm 270,908 267,286 

Stack O2 (%) 14.27 14.26 14.26 

Stack NOx (ppm) @ 15% O2 2.16 1.86 2.01 2.5 

Stack NOx (lb/MMSCF) 8.97 7.61 8.29 12.26(2) 

Stack CO (ppm) @ 15% O2 0.32 0.38 0.35 4 

Moisture Fraction (%) 0.086 0.082 

PPM NH3 (flue gas) 0.88 0.98 0.93 

PPM NH3 @ 15% O2 0.78 0.87 0.83 5 

Ib/hr NH3 0.64 0.71 0.67 

Ib/MMscf fuel NH3 1.20 1.32 1.26 

Stack ROG(1), ppm @ 15% O2 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. 

R0410688 21 
TABLE 4-6 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 4 

PM -50% LOAD 

FEBRUARY 12,2013 

Test Number S-4/STK-PM-50-1 Average Limit 

Condition 55MW 

Test Date 2/12/2013 

Start Time 11 :45 

Stop Time 15:52 

Fuel Flow, hscfh 5,354 

Stack Flow Rate, dscfm 241,434 

Stack 0 " % 14.23 

Stack CO" % 3.79 

Moisture Fraction, % 0.079 

Particulate Emissions 

Grain Loading, gr/dscf 0.0007 0.0007 

Grain Loading @ 3% 0, 0.0018 0.0018 0.01 

Grain Loading @ 15% 0, 0.0006 0.0006 

Grain Loading @ 12% CO, 0.0022 0.0022 0.1 

Mass Emissions, Ib/hr 1.42 1.42 11111 

Emission Rate, Ib/MMscf 2.65 2.65 5.71 1'1 

(1) 11 bllhr PM limit from SCAQMD Rule 475. 

(2) This is stated in the permit as an emission factor. 

R0410688 22 jJell~ 
R0410688 

Test Number 

Condition 

Test Date 

SOx, Ib/MMBtu 

gr H,S/1 00 sci 

TABLE 4-7 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 4 

SOx FROM FUEL ANALYSIS 

FEBRUARY 22,2013 

Average 

100% 

2/22/2013 

0.00002 

0.009 

Limit 

0.06 

0.25(1) 

(1) 0.25 H,S/100 sci sulfur content limit is based on annual average of monthly 

sample results. 

23 
5.0 DISCUSSION AND TEST CRITIQUE 

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 NO, and CO at the 100%, 75% and 50% load 

conditions to ensure that sufficient valid data were collected. 

R0410688 24 
APPENDIX A QUALITY ASSURANCE 

R041 0688 A-1 
Appendix A.1 Quality Assurance Program Summary 

R041 0688 A-2 
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 "living" 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 rneetings 

• 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 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 

R041 0688 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. 

OA 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 OA 

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. 

R0410688 A-4 
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 flow 

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 1. Sample 

R041 0688 

degradation less 

than 2% 

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 

A-5 

through line until 

dry. 
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 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 Daily NO, -> NO converter > 90% 

efficiency 

S-type pitot tube Semi-annually Dimensional calibration Meet dimensional 

criteria 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 

criteria of Method 2 

Differential Pressure Semi-annually Correction factor based +/- 5% 

Gauges (except for on 5-point comparison 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 standard 

Dry gas meter Bi-monthly Calibration check at 2 +/- 2%,1 of semi-annual 

flow rates using a NIST factor 

traceable standard 

Dry gas meter orifice Annually 4-point calibration for 

LlH@ 

Temperature sensors Semi-annually 3-point calibration vs. +/- 1.5% 

NIST traceable standard 

R041 0688 A-6 
Appendix A.2 SCAQMD and CARB Certifications 

R041 0688 A-7 
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 ofthe 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 

USEPA 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:GKlgk 

cc: Mike Garibay 

Glenn Kasai 

121218 LapRenewal.doc 

~ Laboratory 

R,dyF4~. Services s,~ & 

Source Test Engineering 
State of California 

Air Resources Board 

Approved Independent Contractor 

Delta Air Quality Servic~s~ Incorporated . 

This is to certify that the company'listed above has been approved 

by the AirResources Board to conduct comp.nance testing 

pursuant to tHle 17, California Goqe of-Regulatlons,~ection 91207 

until Jun~ 30, 2013: for thOse teSt methods 'Ii$ted below: 

.ARB s'll'itrce. TestMethods: I 

1-; 2. 3, 4; 5, 6,8,17,20, SQl 

100 (CO, ~, NO .. Qz, 8(2) .. 

Alberto Aya~. Ph.D. , M.S.E. 

Chief, Monitoring and Laboratory Division 
State of California 

Air Resources Board 

Approved I ndependent Contractor 

Delta Air Quality Servic~, Incorporated 

This is to certify that the company'listed above has been approved 

by the Air Resources Board 'to tonducleoil-tpl\ance testing 

pursuant to title 17, California Coqe of·Regulatlons. section 91207 

until June 30, 2013: f-or those test metf\o'ds Hl?ted below: 

, ,ARB Source, Test Methods: 

" ,1-,2,3;,4,-5,6,-8, 17, 20~.5qr 

100 '(Co., COz, NO .. Qz, 802) . ... . -

Alberto Aya~, Ph.D" M.S.E, 

Chief, Monitoring and Laboratory Division 
Appendix A.3 Equipment Calibration and Calibration Gas Certificates 

R041 0688 A-8 
Pnlxair 

5700 SOllth Alameda Street 

Los Angeles, ell 90058 

DocNumber 000045707 

Tel: (323) 585-21 54 Fax~714) 54i ·6689 

r(jVPIl): F22012 

CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS 

{IISfO, 

CA Delta Air Quality /-,1/1)",,· 10/~1I20 '7. 

1845 N. Case st. 

Orange, CA 92865 

{Jrawir Order Numher: 21912990 

OWoml!r P. 0. 'vI/mInI"" 04138286 

('us/ollle/'Referel1ce .Numher: 

I'wl ::"",he,.. LV NICDOXI (e AS 

109:>3Cib06 

7050 ():I/I;kI'S~I'lc & ()lrIk! AS CCA!J90 OJ... q . q 8 r-E-xp--ra-t-io-n-D-at-e-----l-l-/l-:-~2-ro-f;:.. · 5_le_d_C_{)_I1_C_e_It_I_rt_rl_i_o_n_: ___ N_IS_T'_:_':_~_:_'~_;:_~'_~'_"_"_'_""_'''....,JJ''': 

r ~ ", q, Cyirnder Number: CC72997 Analytical Uncertainty: 

\...V'I-t ~ 4.96 % CARBON DIOXI()E ± 1 % 

:'000 ~s;g 

1l1l7 9.9B % OXYGEN ± 1 % cc. 7.2....,., Balance NITROGEN 

€f.f 11/1' 11~~r----------------1 Cel'fifcafi(}11 II!formflfion: Certification Date: 11116/2012 Term: 3b Months Expiration Date: 11/1612015 

ThiS cylinder was certified according to the 1997 EPA Traceability Protocol, Document #EPA-600/R-97/121, using Procedure G1 

Do Not Use this Standard If Pressure is less than 150 PSIG 

Allalytictll Du((l: (H Nc frmnr.c StandDrd i' . Zero G,15. C' GDS CiJndid<Jtc) 

, . Component: CARBON DIOXIDE 

f{cqucsl<..>O (;on<..or1ll.,llon ~ % 

C':I\,j,cd COr1CCnlIHllOll -1 96 % 

Ilistrument US.)o.l Il-;r;tn VI/\ ·.1 r"l !;I!'J ~80{O't\ 

I\n<lIf\K: ,I MOlhoo NIlII< 

L.nl Mullipoint Calibration· 11/11 0012 

First Analysis Data: 

z, 0 R' £i.15 

R ' :iY; z, 0 

z· 0 c: <,. 

UQM; % 

2. Component; OXYGEN 

H, quested COI\cel'l~rat.o n: 

C",1iflCd Conccnlration 

Instrumenl Used 

Anal,lln! Ml.lhod 

1. :\SI Mullipoinl Calioralion. 

First Analysis Data : 

Z, o 

Oale: 

C, ",,, Conc· 

C: '''' Conc, 

R, !>. ~ Conc: 

Mean Test Assay : 

10 % 

9~8 % 

O)(YMAT5[ 

I'AHAMAGNI·l IC 

'1/1 1//01? 

Date 

9.98 Conc: 

11/12/2012 

-1.95 

-1.96 

<.913 

-1,96 "!. 

99a 

R: lO U1 

R; 1001 

Z; 0 C: 9.98 Cone; 9.98 

Z, o c, 9,J8 

UOM: 

HolofCl)Cf) Stlln~;lfd Tl pe 

He! Sid C:;llndor it 

Bel Std Cone: 

I~cf fild i"raceable to sr~ M /J 

St{M Sampll) II 

S){M Cyi.ndcr It 

Second Analysis Data: 

Z 0 R, 0 

R, 0 Z, 0 

Z, 0 C, 0 

GM1S 

CC2<13320 

5.15",. 

v~ . 1<,7-1b 

1-I'-3? 

CI\t.Ol-!G45 

Date: 

C, 0 Cone: 

C, 0 Cone: 

R, 0 Cone: 

UDM : % Moan Test Assay: 

Hdercncc Slonourd Type 

Het Sid Cytind<!r # . 

Her Sid, CMt; 

Hd Std. Traccablo 10 SHM # : 

SHI,I Samplo ;l 

SHM Cylinder II . 

Second Analysis Data: 

z: 0 R, 0 

R, 0 Z, 0 

z, 0 c, 0 

c 

C· 

R' 

GMIS 

SA159?!;. 

1001% 

7658a 

,2·;'>0-8 

CI M·.{)()6696 

o 

o 

o 

Dalc· 

Cone : 

Cone: 

Cone: 

0 

0 

0 

0" 

o 

o 

o 

UOM: '\ Mean Tesl Assay; 0 % 

1-10cu fI 

" Analyzed bY·'" T'\',"J . ,"'8 % 

R, 10 C, 7[2C OO' 9.98 

RO ID1 a aywood 

Certified by: --s==l.-----~~ 

Shameela Jiffrey 

, 

Informlll io" contained nero;n hJ5 boen prcpawd ;:It your request by qualified experts Within Pm""'1 rlislnbu\IOIl. Ine While we bellcl'o that Iho Information is accurate .\I th~ l Iho lim its of iilf) .10il;, IrQll 

methods {) oployrd and IS compl.-lc 10 II>!! oxlonl of the speCIfiC anatyses perforrnoo. WQ nlSKn no w W In!y or represemalion ,]s to tho suilab~ ly of 1m, usc of the ,nfOlm .1 1Ion for ,my purpo~o Ill,. 

H1fmmalio i~ of:owd wllh lhe undorSlilndlng thai ;JflY usc ot tho IIlrormol icm is (litho solo discretIon and risk of Iho uscr In no ovent shall the ),ablii!, of Praxillr Distnbuliofl. Inc .. ans~ng oul 01 tim 

ow 0' "" ,,101m"'"", coo " ",,,,0 '"ro" ,,~""m ,," ""obe",,, ,,, P'0"""9 M" ",'~m "'oc I ~ ~ / 7_ I 2/ ~ 

I 
Hffli!6PRAXAIR 

DocNumber: 000036684 -- ---.....,,~ -----c--..:.;.:..:.:.:_;---_~ .• ~.~, ~a~ 

Praxair 

5700 South Alameda Street 

Los Angeles, CA 90058 

Telephone: (323) 585-2154 

Facsimile: (714) 542-6689 

CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS 

Customer & Order Information: 

Fill /Jail!: 312312012 

-, 

DELTA AIR QUALITY 

SERVICE INC 

Praxair Order Number: 19799780 

Customer P. 0. Number: GARY 

Customer Reference Number: 

F'(f/ Number: Nt CD9.503E-AS 

Lol Number; 109208304 ORANGE CA 928654 Cylinder Style & Olltlet: AS eGA 590 

,,,., 11,90 

~'" 'I., t,/ 

Expiration Date : 

Cylinder Number: 

9,62 

18,90 

% 

% 

Certified Concentration: 

4/4/2015 

CC199067 

CARBON DIOXIDE 

OXYGEN 

('}fil~(er l'rt' :lIrc & I'oll/me: 

NIST Traceable 

Analytical Uncertainty: 

± 1 % 

± 1 % : c ,qqO,7 Balance NITROGEN 

!,y.ff)tf/8+"~ ___ -------l 

Cerf/fcmiotl Iliformatioll: Certification Date: 4/412012 Term: 36 Months Expiration Oats: 4/4/2015 

2000 psig 

This cylinder was certified according to the 1997 EPA Traceability Protocol, Document #EPA-600/R-97/121, using Procedure G1 

Do Not Use this Standard if Pressure is less than 150 PSIG 

PGVP 1.0.# F22012 

Analytical Data: (R:Referef1ce Standard, Z-::.Zero Gas, C:Gas Candida/e) 

1 . Component: CARBON O!OXIDE 

Requested ConcentraUon: 9.5 % 

Certified Concentration: 9.62 % 

Instrumenl Used: Siemens Ultramat SE SIN A12-730 

Analytical Method' NOtR 

Last Multipoint Calibration: 311112012 

First Analysis Data: Date: 414/2012 

I 96, 

z. 0 R. 10.06 C. 9.62 Cone: 

z. 0 C: 9.62 Cone: 

9.62 

9.62 I Z. 0 C. 9.62 R: 10.08 Conc: 

UOM: .. Mean Test Assay: 

I R. 10.0. 

- -... -- 9.62 % 

------' 

2. Component: OXYGEN 

Requested Concenlration. 19 % 

Certified Concentration: 18.90 % 

Instrument Used: OXYMAT SE 

Analytical Method PARAMAGNETIC 

last Mullipoini Calibration: 311112012 

f ;Ir; AnaIYSIS ;-a~ ---- --D-; ;; ~';~~~---l 

I Z: 0 R: 20 C: 169 Cone: 1B.9 I ! R: 20 Z; 0 C: 18.9 Conc: 18.9 

Reference Standard Type: 

Ref. Std. Cyltnder # : 

Ref. Std. Cone: 

Ref. Std. Traceable to SRM fI : 

SRM Semple fI : 

SRM Cylinder # . 

GMIS 

SA1471 

10.08% 

vs. 16750 

6-F-Sl 

CAL014538 

i Second Analysis Data: Date: 

!~ ~.~ Z: 0 C: 0 

UDM: 0", 

_.'- -----

c: 

C. 

R. 

o 

o 

o 

Conc: 

Cone: 

Cone: 

Mean Test Assay: 

Reference Standerd Type: GMIS 

Ref. Std. Cylinder # : SA12B32 

ReI. Std. Cone: 20.00% 

Ret Std. Traceable to SRM # : 2659a 

SRM Sample # : 71 -37-B 

SRM Cylinder # . CLM-008734 

: Second Analysis Data: Date: 

z. 0 R. 

i R: 0 Z: , 0 

0 

c. 

C. 

o 

o Conc: 

Cone: 

o 

o 

o 

0% 

o 

o 

140 cu. It. 

I 

I Z: 0 C; 18.9 R: 20 Conc: 18.9 I' 

I UOM: % MeanTOstAssay: 16.9% 

Z: 0 C: 0 , I UOM: % R: 0 Cone: 0 

~~n Test AS8.aY_: _ _ _ ~J 

Analyzed by: Certified by: ~ ___ _ 

") 

Shameela Jiffrey 

Infonnation contained herein has been prepared al your request by qualified experts within PrB:l:air Distribution, Inc, VVhile we believe that the InfOfmation is accurate within the limBs of the analytical 

methods employe{j and is c:ompJele to the eJdef11 of the specific analyses performed. we make no warranty or representation as to the suitability of the use of the Information for any purpose. The 

informaHon Is offered with the understanding [hat any use of the information is at the sole discretion and risk of the user In no event shail lhe liability of Praxair Oistnbulion, Inc., arising out of the 

use of the informaHon con lained herein exceed the fee established for pro .... iding such information. 

c(- --/7 -/2-Y 
!fff~PRAXAIR Praxair 

5700 South Alameda Street 

Los Angeles, CA 90058 

DocNumber; 000046490 

Tel: (323) 585-2 154 Fax:(7 14) 542-6689 

PGVPID: F22012 

CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS 

ClIsto 

• Delta Ai FIJI Our." ""212012 r Quality 

1845 N. Case St. 

Orange, CA 92865 -

Praxair Order Number: 22054687 

Customer P. 0. Number: 04159883 

Customer Reference Number: 

}Jorl Nil"''''',. !.mN""'''''r: 

NI N02.SMZ1 E-AS 

109231805 

C,:ylint1cr l>'l~ & Ollflol: AS eGA 660 

NO~".~Z 

Cc.'~S2. 

~/"IIO/l 

Expiration Date: 

Cylinder Number: 

2.52 ppm 

Balance 

NOx= 

Certified Concentration: 

12110/2015 

CC7352 

NITRIC OXIDE (as NOx ) 

NITROGEN 

Iylllltkr n.·~ I1"" & 1'",1,,111:: 

NIST Traceable 

Analytical Uncertainty: 

±2 % 

NOx for Reference Only 

Cerli/catiOlt Information: Certificarion Date: 12/10/20 12 Tenn: 36 Months Expiration Dale: 12/10/2015 

2000 psig 

This cylinder was certified according 10 Ihe 1997 EPA Traceability Protocol, Document #EPA-600/R-97/121, using Procedure G1 

Do Not Use this Standard if Pressure is less than 150 PSIG 

140 cu. ft. 

rNO]= 2.48 ppm;for refe rence only, The certification expiration date i~, assigned using the May 2012 revision of the EPA Traceability 

Protocol document. 

Allolytical Dntu: {R= Reference SI<Jndard, 2"Zero Gas, C:;Gas Candidate} 

1 . Component: NITRIC OXiOE tas NOx) 

RequOlltao Concsntration. 

Certified Concentration: 

Instrument Used. 

Analylicel Method: 

Last Multipoint Calibration. 

r; AnilIYS~---

I ~ 0 R 968 I R 968 Z 0 

I z: a C: 2.51 

O!,,: ppm 

Analyzed by: 

2 5ppm 

2.52 ppm 

Thermo Electron 42C SIN 516112467 

Chemiluminescence 

1111 112012 

Oalo: t tf2S120t2 

C, 2.51 Conc: 251 

C, 2.51 Cone : 2.51 

R, 9.sa Clme: 2.51 

Moan Test Assay: 2.51 ppm 

l 

I 

I 

Reference Siandard Type: 

Ref. Std. Cylinder # , 

Ref Std. Cone: 

Ref. SId. Traceable to SRM II : 

SRM Sample 1# : 

SRM Cylinder N : 

Z: 0 R: 9.88 

R: 9.88 Z: 0 

Z: 0 C: 2.53 

UOM : ppm 

GMIS 

CC335699 

9sa ppm 

262ge 

5Q.G·l09 

FF31631 

Date: 

2.S3 Cone: 

2.53 Cone: 

9.88 Cone; 

12!J12012 

2.53 

2 53 

2.53 

~O AA 'Y ;' ~'~~ ; 

- - -------,...<:::-=----

InformatiQr1 contained herein has been prepared at your request by qualified experts within Praxeir Dislributlon, Inc:. While we believe that the information 1& accuralo within the limits of the analytical 

methods employed and is complete to the extent 01 the specilic: analyses pericrmed, we make no Wllrranty or representation as to the suilabWty of the use of the information for sny purpose. The 

information is offered wilh the understanding that any use of tho Information 1& at the $ole discretion and risk of the user, In no event shall the liability of P(8)(air DiSlributiOr'l, Inc. , arising out of the 

use of lho information con tsinod herein exceed the fee established for providing SUCh Information "? I ,, ~ P / _ // -,(' 7j' 

I 
/'ftfflflPRAXAIR 

DocNumber: 000038766 

I' .. axa;r 

5700 South .\Inmcd<l Sirect 

Los Angeles. CA 90058 

Telephone: (323) 585·2151-

Facsimile: (714) 542-6689 

CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS 

CA Delta Air Quality 413012012 

1845 N. Case st. 

Orange, CA 92865 

Praxair Order Number: 20155225 

Customer P. O. Number: 03870012 

ells/omer Reference Nllmber: 

,'"n ,Vllmh.,.. 

l,tJ/ ,yUh" ",',.: 

(')'limkr Slyl~ ~ Gillin: 

NI N04.7MZE-AS 

109217109 

AS CGA660 

No~tf·it, 

CC ,~.", 'J 09 

fy.ros/f,cfp 

Expiration Date: 

Cylinder Number: 

4.82 ppm 

Balance 

Cerl!fied Concentration: 

5/2412014 

CC362309 

NITRIC OXIDE {as NOx) 

NITROGEN 

NIST Traceable 

Analytical Uncertainty: 

± 2 % 

Cali/cOli()" In/ormation: Certification Date: 5/24/2012 Term: ~4 Months Expiration Date: 5/24/201 4 

2000 ig 

This cylinder was certified accord ing to the 1997 EPA Traceability Protocol, Document #EPA~600/R~97/121, using Procedure G 1 

Do Not Use this Standard if Pressure is less than 150 PSIG 

INO]=4.80 ppm (for reference only). PGVP 1.0.# F22012 

Analytical Dato: (RoBe/cronce SI<Jndard, 7.. Zero Gas, C"'Gas Candida/e) 

1 , Componont : NITRIC OXIOE (as NO)!:) 

Requested COOClmtrllilon 

Cort<ll.;-d Conclmtr;l\lon 

Instrument Usoo 

,r ~tlc,,1 MOlhod: 

l. 1St l.tulliPOll11 Calibration' 

First Analysis Data : 

o R: 10.03 

Z: 0 

UOM: ppm 

R: 10,03 

Z: 0 

C: 4,61 

4.7 ppm 

<l.82:ppm 

Tnermo Etcclron <12C SIN 5181 12467 

Cncmiluminesccnce 

5/1012012: 

Oate: :.Jl1i 20 12 

C, ' .86 Cone : '.M 

C, 4,61 Cone: 4,61 

R, 10,03 Cone: <1,81 

Mean Test Assily : 4,83 ppm 

Analyzed bY~ 

~ 

Roference Standard Type: 

Rof Std, Cylinder 1# : 

Ref Sid Cone: 

Ref. Sid Traeeabie 10 SRM II 

SRM Samplo# 

SRM Cylinder # : 

Second Anatysis Data : 

Z, 0 R, 10,03 C, 

R, 10.03 Z, 0 C, 

Z, 0 C, 4.133 R, 

GMIS 

CC3352 

10.03 ppm 

2629a 

50·G·109 

FF31631 

Dato: 

4.81 Cone: 

4 ,82 Cone: 

1003 Cone: 

UOM: ppm M8an Test Assay: 

Certified by, ~ 

5fl{V?012 

'" 4.82 

4.83 

482 pprn 

~ 

\ 40 cu. II 

Illfurm .1tlQJl cont,:uf"lOd herein has been prcpared at your rcquesl by quab!'led experts Within Prax;;)lr Distribution, Inc. W 1IIo we believe that the information is accurate within tho Iom,ls of Ih-J and) 11C 11 

methods employed and IS complete to the extent of (ho speclrlC anaiysp.s performed, we make no \ arranty or representation as to Iha suilabjilly of the usa 01 Iha inlormation lor any purpOS,1. 1 ne 

,'110rmt>lion IS offored ",!HI thc understanding that any use ollhe Information IS at tna sole discrcuon and Iisk of the user In no even! shaillno l1abll~y 01 Praxaif O'stribution, Inc. ansmQ out of ttlO 

"""' ,"" ,,,,,,rna",,, 00" '.'00' ","" ,,~od ,he foo ""bi.,h,' foe p~,id,,,g ,eoh "'oem",,,,,. { r / 2- _ / 2-? 

I 
/jjf.§fffJ PRAXAIR I' nn: ai r 

":'(Jf) SI'uli1 ,'.i(llllCda \ II LCI 

L,IS .\Ilgcks. C,\ 9lJ{J'i!l 

Doc Number. 000047511 

rd (3n) :'IRS':! 15 i l'iI-,;:( i 11) :q2-{,() ~" 

[l( ;V]'!!): F22013 

('ERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS ('11 .\"1(1 

Delta Air Quality 

1845 N. Case St. 

Orange, CA 92865 

Prawlir Order ,\'l/IlIh(.T 22355996 

('/Is/nine" V 0. .\'WI,/J1'r 04204373 

("".\"/UIII,.I' f«('r~'/"<.!I:cc .','/111111<'1' 

~o.", tf, O~ Certified COll centratiol1 : 

.-------------~-

Expira ti on Date" 

Cylinde r Number" 

7/9/20 13 

CC11 3404 

CC II' cf () cf 4. 02 ppm NITROGEN DIO;(JQE (as NO'i 

. ill J~II,-' 

I" " ''. /tlll/'''' 

1,,/ : ","h, 

,,,r·, I 'll ' ,' (),,/ - ,. 

, ., ·,t'T. " 

1 ( '" ", · 

NIST Traceable 

Analytical Uncertainty' 

6~r D7/09f~~_B"_anc TR_OGE_ N _____ -----' 

Cr'I"(ifi'lIfilill rorlllll'i () II.' Certification Date " 1/91201 3 Term: 6 Months Expirdtion Oale 719/201 3 

t:>.711:>o t / 

I .... • N1NX 'U 11 

1u.1 ? J-, :)7 

AS 

;;,,}{) (lS 

This cy linde r was certified accord ing to the 1997 EPA Traceability Prt,tocol, Docurnent #EPA~600/R 97/121, using Procedure G1 

00 Not Use thiS Standard If Pres sure is less than 150 PSIG 

[NO]=O,06 pprn: for reference only 

1 Componunt: r~lrrlOGEN DIOXIDE (a5 NOx) 

ih.-!"('~I < r ';on ',.nt, ~11 

(;UI.1o.'1 (; ')f. :, 11,r;lh(m 

II": ;,1 le,,1 'J. ' 

1111. JII< .. 11 f '.:11' .. )" 

l .. fln"~'~ll"ll :a ll ... r .,nrl 

rifSl Analys l!> 0111.'1 

2' " e, J ;If 

R ~) .1I Z, 

1. : () c: 

UQM. '~ III 

Analyzed by 

-"l pp:n 

" O? ppm 

r 1. 'InC) 1' 1. ;I( ,~ ,p, IN (J ~'r ·); "l::.~'C 

CII!. n,lurnlrl()sc, 11<:('; 

lI1r'{)1;! 

Date: 1'0l 1"0 1" 

C, , 01 Cone: ·1()1 

C, -I.U:' Cone: 'ltl;> 

eo 0 " Cone' '1,j;.> 

MeilH Tnst Assay' -"lO;'>ppm 

~ w U'CAWI 

Jack Fu 

HCJte em.'.' SI;l!Id .Id l , pe 

Hd SId Cyhw1:Jr iI 

Hd Std Com: 

SIUI SHmpk, II 

SI.(n C hl1:::!'n ~ 

Second An-,Iysis Da la: 

z· " 

R, ':G 

R, <llll; Z, {) 

Z, , C. '10" 

UOM PJ)1Il 

C 

C· 

R 

(;MiS 

CC:kx ~' 

!H..I ppm 

::.,1 

:'0 C 109 

I I ,H,;:,' 

Dale 

oj " ;'> Cone: 

1111 Cone: 

U W C" ne : 

Mean Tes t Assay: 

Certified by 

1~ ;'>')\3 

" " 

1 ',1 

. 0;.> 

' \ [)' > ppm 

,\:> 

CC ., ) cu " 

InlC:II"l'I"){\ r :ll '11U' .J t\ t'fll'" 1.;1' b l oo n "r"l'Jr,.d ']1 , ( ;Jr C" l1( ~e t t), qu;,hli(. J c .. p. rL ,Ihln j> r.! ~ ~' Il ~! n\"lI'tKl n, Inc: \\ ~ 'V(~ b, ':,. (~Ihl!t thc inlorm,,11oll i~ a("-' lflJiC \ ,Ill." Ih ., IIr ~ DI n 'I' ,n,,:, I 11 

n., ," , I . ', f.l plll,· .(j .,11(' IS C(lfllp;,:le t'l 11],. L I, '11 ..r 1."'- ">P(lClll\, IflfJl, ,lOS rmiormc:J, ... (, m ,i-.c no', " n fll, Of ! epr,. S(J;lt;lliO!l ;l, :0 tlh. ;.uitaoih\, of !1m !J,,! l.! the Injnrmaliun lv' an .. PLI![lO.iC I ( 

"\!. Im I 1n ,. ol1.:r, j 'ttl lh'_ "o: ll)l~t '11.1'11<1 TIl'\ III, usc of lin: >llfOff l1 11 n I .. ;\ 11'(: ,oln (j,<..retIOO) .,f, 1 r sk !lIthe usn In no, . · .... \1 sh III !h'1I'Olt j 011'( I. -,r fl " triIJlJ..'''l. Ir' . I" ,'11'1 (lui DI II;;, 

I 

"",'" " ,',,"",'" ""," ,," "",,",, . '""' " ," "." ,,,' ,,""''''' .",m >""oj '" .if-'" """"'",,, ( ~I g - /) 7 
f!ff1!!lPRAXAlR Praxair 

5700 South Alameda Street 

Los Angeles, CA 90058 

DocNumber: 000041947 

Tel : (323) 585-2154 F4x:(7 14) 542-6689 

PGYPID: F22012 

CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS CuSIO 

Delta Air Quality 

1845 N. Case St. 

Orange, CA 92865 

Praxair Order Number' 

Customer P. O. Number: 

Customer Reference Number: 

21015531 

03998407 

co '/·'19 Certified Concentration: 

Expiration Dale: 212012013 

CC325462 

cc"':t '" I!! • ~~., :llnder N

4

um

49

ber ppm 

iI ~ ~ ~ _ CARBON MONOXIDE 

"''''/')(,w 

""rlNl(mi)t;L" 

1.01 N"mm:r: 

(")'lmdiU" SI) Ie ~ O"llel; 

Cyli"<lcr I'n',",l'IIrc & V()/lIm(" 

NIST Traceable 

Analytical Uncertainty: 

±2% 

Balance NITROGEN 

~~o/~~ -----------~ Certijcation Informalion: Certification Date: 8/20/2012 Term: 6 Months Expiration Date: 212012013 

7/271201 2 

NI C04.7ME-AS 

109220904 

AS e GA 350 

2000 pslQ 140 cu, fl 

This cylinder was certified according to the 1997 EPA Traceability Protocol, Document #EPA 600/R-97/121, using Procedure G1 

Do Not Use this Standard if Pressure is less than 150 PSIG 

Analytical Data: (R=Refcrence Standard, Z"'Zero Gas, C"'Gas Candide/e) 

1 . Component: CARBON MONOXIDE 

Requested Concentration 

Canine<! Concentration 

Instrument Used. 

Anatytlcal Method: 

Last Mut11pomt Calibration 

! First Analysis Data: 

z· 0 R, 84.3 

R, 84.1 Z, 0 

Z, 0 C, 369 

UOM : ppm 

1 7 ppm 

4 I\$l porn 

Horibl) VtA-510 SIN 5768760 15 

NDIR 

8111/2012 

Dale: 61712012 

C, 368 Cone: 4,45 

C, 37 Cone : 4.49 

R, 84 Cone: 4.48 

Mean Test Assay: 4.47 ppm 

Analyzed ~:¢/ 

Reference Slandard Type: GMIS 

ReI. SId. Cylinder /I : SA66B7 

Ref. SId, Conc' 10.2 ppm 

Ref. Std. Traceable to SRM /I : 1677c 

SRM Sample II : 5-1-42 

SRM Cylinder 1/ XF oo2 143B 

, Second Analysis Data: Date' 811512012 

Z, 0 R, B4 .3 C, 37.3 Cone' ", R, B4A Z, 0 C, 37.4 Cene: 451 

Z, 0 C, 37,3 R, 84.4 Cone : 45 

UOM: ppm Mean Test Assay: 4 S1 ppm 

Certified by: 

Informat'(){1 contained herein has been prepared <it your request by qual;riod p.xpans wilhin P(a~a ( Distribution, Inc l/IIhile we belie~e that tho information IS accurate wlthi(lthe li'f,ils of the anal] tical 

mothods employed and is compiete to the e~tef1t of the specific analysos pertormed, we make no WtllTanty or representation as to the suitabiltty of the use 01 tho information for any purpose, Tho 

informatloo is offered with the understanding that any use of tho Information is at the sole d:scretion and risk of the user In no event shall the liability 01 Pra:>:air Distribution, Inc .. ariSing out o/ the 

"" of Iho "room"", '" ",,,d I",." ""'0 Ih' ro, ""bll,,,d f" pc"."" Mh ',r"m,IIo, 1; _ 1 ( _ / Z ;0/' 

I 
Doc Number: 000041846 

PnlXllir 

5700 South Alameda Street 

Los Angeles, CA 90058 

Tel: (323) 585·2154 Fax·(714) 542·6689 

PGVPID F22012 

CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS 

CuMOI 

Delta Air Quality Fill Date' 712612012 

1845 N. Case St. 

Orange, CA 92865 

Praxair Order Number: 20981153 

Customer P. 0. Numb!!,.. 03994448 

Customer Reference Number: 

PWI Number" NI COR5ME·AS 

I,VI Nllm/>.!r; 109220812 

Cyfmdur Sryle,{ (JIII!..'I: AS CGA 350 

Co 'I,'/-, 

Cc. '311 ca 

~('OI/1'/1 

Certified Concentration: ryli"",:r I'r~ssllu <f: I (}III"' ' 2000 psig 140 cu fl. 

Expiration Date: 

Cylinder Number: 

9,47 ppm 

Balance 

811612015 

CC313840 

CARBON MONOXIDE 

NITROGEN 

NIST Traceable 

Analytical Uncertainty: 

± 1 % 

CertifcotiOlr1nformation: Certification Date: 8/16/2012 Term: 36 Months Expiration Date: 8/16/2015 

This cylinder was certified according to the 1997 EPA Traceability Protocol, Document #EPA-600fR-97/121, using Procedure G1 

00 Not Use this Standard if Pressure is less than 150 PSIG 

Analytical Data; (R=Reference Standard, Z=Zero Gas, C::.Gas Candidate) 

1 . Component: CARBON MONOXIDE 

Requc$ted Concoolralion; 9.5 ppm 

Certified Conccntrntion' 9,'17 ppm 

Inslrumenl Used' Horiba VIA-510 StN 576876015 

Analytical Method NDIR 

l ast Multipoint Calibfation: 711112012 

~~IYSIS Data- -

Z ° R 845 

R 844 Z 0 

Z 0 C 789 

UOM ppm _ ~ ____ . ____ -,---__ ,--_J 

Dale: 8/212012 

C, 78.2 Cone: 9.44 

C, 76.4 Cone: 9.47 

R, 84.4 Cone: 9.54 

Mean Test Assay: 948 ppm 

Analyzed by: 

~ Shameela JiHrey 

Reference Slano'ard Type' 

Ref. Std. Cylinder # : 

Ref. Std. Cone: 

Ref. Std Traceable to SRM Ii : 

SRM Sample II ; 

SRM Cylinder /I 

GMIS 

SAS687 

10,2 ppm 

l677c 

5-1-42 

XF 002 1436 

I SeeOnd~aIYS! :-;;~ -----~Oate ~;;;;- l 

I Z 0 R 844 C· 783 Cone 942 I Z: 0 C; 78.7 R: 84.5 Cone: 9.49 1 

I. 

R. " . 5 Z. 0 C 786 Cone. 9.48 

UOM _~p_m Mean Test A~~:.:. ___ 9. ~ ppm J 

Certified by: 

Informa:ion contained herein has been prepared at your request by qualified experts within Praxair Distribullon, lne While we believe thai the information is accurale within the limlls of the analytical 

methodS employed and is complete to the extent of the specific analyses performed. we make no walranty or representation as to the suitability of Ihe use of the inforfTl<ltion fOI any purpose. The 

Iflforrnalion is offered with the understanding thai any lJse Of thE! information Is :31 the sola ciscreti{)n a(ld risk 01 the user. In no event shalilhe liabiflly of Praxair OistripUlion. Inc., OIrising out of the 

"" 0' Ih' 'o'o<m,lioo 000 "'0,", he",o ,,,"" lhe ", "''''',h,' lix pco,'dio, '""' 'o'"m.Ii". /2 -'f ~ ! v,? 

I 
J/f~PRAXAIR. Praxair Distribution, Inc. 

5700 S. Alameda St. 

Los Angeles, CA 90058 

Tei: 323-585-2154 

Fax: 714-542-6689 

10/22/2012 

Delta Air Quality 

1845 N. Case St. 

Orange, CA 92865 

Praxair Order 

-

No. 21690846 

Customer Reference No. 

Product LoVBatch No. N109228006 

Praxair Part No. NI 5.5CE.AS 

Analytes 

Nitrogen 

Carbon Dioxide 

Carbon Monoxide 

Total Hydrocarbons 

Oxides of Nitrogen 

Oxygen 

Sulfur Dioxide 

Water 

Analytical Instruments: 

Cylinder Style 

Cylinder Pressure @70F: 

Cylinder Volume: 

Valve Outlet Connection: 

Cylinder No(s). 

CERTIFICATE OF ANALYSIS 

Nitrogen, 5.5 Continuous Emission Monitoring Zero 

Analytical Analytical 

S~ecification Results Pr nci~le 

>99.9995 % >99.9995 % N 

< 1 ppm < 0.019 ppm L 

< 0,5 ppm < 0.020 ppm L 

< 0.1 ppm < 0.05 ppm Q 

< 0.1 ppm < 0_0034 ppm U 

< 0.5 ppm < 0.5 ppm W 

< 0.1 ppm <0.1 ppm Z 

< 2 ppm < 1.1 ppm P 

Horiba Instruments Inc.-GA-360E-NDIR-Non-dispersive Infrared 

Analytical 

Accuracy 

± 10% 

± 15 % 

± 15 % 

± 15 % 

± 15 % 

± 15 % 

± 0.4 ppm 

Rosemount Analytical-NGA-2000-THC - Total Hydrocarbon Analyzer-FlO· Flame 

Ion ization Detector 

Thermo Environmental-42i-Nitric Oxide Analyzer-Chemiluminescence 

DeltaF-Nanotrace-Trace Oxygen-Electrochemical 

AMETEK-921 CE-UV S02 Analyzer-Ultraviolet Absorption 

Meeco-Aquavolt -Moisture-Electolytic Hygrometer 

AS Filling Method: 

2000 psig Date of Fill: 

168 ft3 

CGA·580 

CC93915 

Tern perature/P ressu re 

10/06/2012 

Analyst: Henry Koung ob Approved 

Signer: 

I , 

A 

E Gn Cl'Irom~l0gr;0llhy with ~ PhoIomelllC Oeledor 

Ou CIIrom,IOQf'pny wiI1I Re'I).ldion Gas Anatyz8r 

M Min SpeClt_ry. illS 01 GC/'MS 

Q Tol.! Hyorocarbon AnalYZIr 

U ClI'milOJmit\eseeflce 

Y Pulsed Flt/ofeilGllftCe 

IMPORTANT 

B Gu Chrom.logr.phy w.tn OIl.C!la<ge lonolf\lOn .,...,~ 

f On Chromillogr.ptly ... It. Htijum lo:'l/zaUon 

Ofl"'~ J G.s ChromilIOOJf'pt:y w,lh Th4!"IIlll Cooouoel/Y~y 

O<tteClQ( 

N By Oil'fe~m;e 01 TypiullmPl-'liel 

R Wet Cherl'ltc.1 

V Gravlmelrie Z W Sp&drometry 

C Gas CtvomalOgrllJl/ly wM ElealOlyUc. COllduc1~y 

D'iector G Gas ClwOmatClgfaphy wih Ml!IhanlzerC..oonlz.If 

K Binary Gas Anolyter willt ~rm" CondoolYity 

Oelectar 

o P."megnelic; $ DeteClar Tube 

W Elodrotytie CeNS.ctrodlell"ical 

o GIS Cllfomacograpny WIllI amllOriz~ 

Oetector 

H GIS (;hrOfl1itooraJlhy ... ~h Photoiof'Oiutioo [)ele(;far 

l Infrlled· fT~ Or NDIR 

P Sl)KIr,c Wale. Ane;y<tr 

, "'~ X Pt'lQloIotIitlllion 

The informalion contained heruln has been prepared at your request by pef$OOIl&i with,n Praxair Distribution, Wh~e we belieYe !he informalion is accurate within the limits of the analytical methods 

employed and is completo to tho oxton! of the specific analyses per/ormed, we make no warranty or representation as to the suitability of tne use 01 !he InforrnOition for any particular purpose, The 

information is offered Wi th the understanding that any usc of the Information is £It tha sole discre1ion and risk of !he user. In no even! sh liliabil~y of Praxair Distribution, inc:, aristng out 01 the use of the 

Inlo(lnatfQr1 contained horein exceed the fee established for providtng such information 

Pg.1 of 1 /2.-/1 -/ 2 ;P 
Orifice Method · Tnplicale Runs/Four Calibration Points 

English Meter BOK Units, English K' Factor 

SEMI·ANNUAL DRY GAS METER/ORIFICE CALIBRATION 

Model #: 

10 #: 

Filename: F,\compdala\Delia PubliclCalibrations\Melers\17-wcs1201~Semi·Annual MeIer Callbrallon 9·19-12 wcs.KlsJWCS Date: 

C5000 

17WCS 

9/19/2012 

File Modified Froor APEX 522 Series MeIer boK Calibration Bar. Pressure: 29.79 (In. Hg) 

ReVised 4/812005 Performed By: 3A,RY BRIDGE 

DRY GAS METER READINGS CRlTlCAL ORIFICE READINGS 

Volume Volume Volume Initial Temps Final Temps Orifice K'Orifice Actual 

dH Time Initial Final Total Inlet Outlet Inlel Outie! Senal# Coefficient Vacuum Initial 

in H2O) (min) (cu tt) (cuft) (cu It) 'do, Fi do, , (d.eg F) (deC! F) (numt)er) (see abo~e in Hg). (d., ') 

0.1 I 26.00 368.900 374.275 5.375 74.0 73.0 74.0 73.0 33 0.1553 23.5 73.0 

0.11 26.00 374.275 379.658 5.383 74.0 730 770 75.0 33 0,1553 23.5 73.0 

0.11 26 00 380.200 385.581 5.381 J 770 750 77.0 75.0 33 0.1553 23.5 73.0 

0.55 12.00 389,200 394,650 5450 73.0 73.0 740 73.0 " 0.3465 20.0 74.0 

0.55 12.00 394.650 400,128 5.478 740 73.0 75.0 74.0 " 0, 3465 20.0 74.0 

0.55 12.00 400.128 405,593 5.465 75.0 74.0 760 74.0 " 0,3465 20.0 74.0 

170 700 405.593 411.028 5435 760 740 77.0 75.0 63 05888 16.5 74.0 

1.70 7.00 411.028 416.485 5.457 770 750 78.0 75.0 I 63 0.5888 16.5 74.0 

1.70 700 416.485 421.937 5.452 780 750 790 76.0 63 0.5888 '65 74.0 

3.30 500 421937 427.253 5316 790 76.0 81.0 76.0 73 08202 13.0 74.0 

330 500 427253 I 432.550 5297 81.0 76.0 82.0 76.0 73 0.8202 13.0 74.0 

330 5.00 432.550 437.886 5336 820 76.0 63.0 77.0 73 08202 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(std) Vm(std) VCl"{std) Vcr(std) Vee Value Value 0.95 < Y YmaK· Ymin 

(00 ' ) (liters) (cu ft) (liters) (eu tt) (number) (in H2O) < lOS? < 0.010? 

5.296 150,0 5.210 147,6 5285 0.984 1,520 Pass 

5.291 149,8 5.210 147,6 5.285 0.985 1,517 Pass 

5.277 149.4 5.208 147,5 5287 0,987 1.515 Pass 

Average 0.985 1.517 Pass 

5,378 152.3 5.360 151.8 5.447 0.997 1.529 Pass 

5,398 152.9 5.360 151 8 5 447 0.993 1.528 Pass 

5.376 1523 536<l 1518 5 447 0997 1.526 Pass 

Aver"ge 0.995 1.528 Pass 

5.356 151.7 5.313 1505 5399 0992 1.632 Pass 

5370 1521 5.313 1505 5.399 0.989 1.631 Pass 

5358 151.7 5.313 150.5 5399 0.992 1.629 Pass 

Average 0.991 1.631 Pass 

5235 148.2 5.287 149.7 5372 1 010 1.628 Pass 

52<>9 1475 5.287 1497 5.372 1.015 1.628 Pass 

5.240 1484 5.284 1497 5375 '008 1.628 Pass 

AveraQe 1.011 1.628 Pass 

Allerage Yd: 0.996 dH@: 1.576 

Q@dH=1: 0.597 

SIGNED: Date' 

Ambient Temperature 

Final erage 

,d., ') (d., ') 

73.0 73.0 

73.0 73.0 

74.0 735 

74,0 74,0 

74,0 74,0 

74.0 74.0 

74.0 74.0 

74.0 740 

74.0 7<0 

74.0 740 

74.0 740 

75.0 745 

Orifice Orifice 

Average Average 

0.98 < YlYd dH@ · dH@av 

< 1.02? 

Pass 

Pass 

Pass 

Pass 

< 0 ISS? 

Pass 

Pass 

Pass 

Pass 

Semi·Annual Meter C,lit><III"" 9·19·12 WCI WCS ,no,,,, 

2.SPM 
Orifice Method - Triplicate Runs/Four Calibration Paints 

English Meter Bo)( Units, English K' Factor 

SEMI-ANNUAL DRY GAS METER/ORIFICE CALIBRATION 

Filename' F:\compdataIDelta PublicICalibrations\MetersI9-P&M\2012\[Semi-Annual Meter Calibration -9-pm 9-21-12.xlsjWCS 

Model #: 

10. 

Date 

9P&M 

912112012 

File Modified From: APEX 522 Series Meter box Calibration Bar. Pressure: 29.72 (in, Hg) 

Revised' 4/812005 Performed By M. Edmondson 

DRY GAS METER READINGS CRITICAL ORifiCE READINGS 

Volume Volume Volume Initial Temps Final Temps. Orifice K' Orifice Actual 

dH Time Initial Final Total Inlet Outlet Inlet Outlet Serial# Coefficient Vacuum Initial 

(in H2O) (min) (cu tt) (eu tt) (eu tt) (deg F) (deg f) (deg F) (deg F) (number) (see above) (in Hg) (deg F) 

0. 14 26.00 383.400 388.805 5.405 78 ,0 77.0 79.0 78,0 33 0 ,1553 23.0 770 

0.14 26.00 388.805 394.205 5.400 79,0 78.0 80.0 79,0 33 0.1553 23.0 78.0 

0.14 26.00 394.205 399.615 5.410 80,0 79.0 81 .0 80,0 33 0,1553 23.0 79.0 

0.64 12.00 350.820 356.270 5.450 75.0 74.0 75.0 74 ,0 " 0,3465 20.0 75.0 

0.64 12.00 I 356,270 I 361 .730 5.460 75.0 74,0 76.0 75,0 " 0,3465 20,0 75.0 

064 12.00 361 .730 367 ,175 5,445 76.0 75,0 770 76,0 " 0,3465 20.0 76.0 

1,90 7.00 I 367.175 I 372,585 5.410 770 76,0 770 76.0 63 0,5888 17.0 77.0 

1,90 7.00 372.585 377990 5.405 77.0 76,0 78,0 77.0 63 0,5888 17,0 77.0 

1.90 700 377990 383,400 5.410 78.0 770 78,0 77.0 63 0.5888 17.0 78.0 

3.70 5.00 334.700 340,065 5,365 720 72.0 730 73.0 73 0.8202 15,0 73.0 

3.70 5.00 340.065 345.430 5.365 73,0 73.0 74.0 74,0 73 0.8202 15,0 74.0 

3.70 500 I 345.430 350.810 I 5.380 74,0 74.0 74.0 74.0 73 0.8202 15.0 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(std) Vm(std) Ver(std) Vcr(sld) V" Value Value 0,95 <: Y Ymax- Ymin 

(cu tt) liters) (eu ttl (liters) (eu tt) (number) (in H2O) <: 1,05? <: 0.010? 

5,269 149.2 5.176 146.6 5,307 0.982 1.939 Pass 

5,254 148.8 5.171 146.5 5,312 0.984 1.939 Pass 

5,254 148.8 5.167 146,3 5,317 0.983 1,939 Pass 

Average 0.983 1.939 Pass 

5.354 151 ,6 5,343 151,3 5.452 0.998 1.784 Pass 

5.359 151 ,8 5,340 151 ,2 5.455 0,997 1.784 Pass 

5,334 151 .1 5,335 151.1 5.460 1,000 1.784 Pass 

Average 0.998 1.784 Pass 

5,311 150.4 5.286 149.7 5.414 0.995 1.834 Pass 

5.302 150.1 5.284 149.6 5,417 0.997 1.834 Pass 

5,302 150.1 5.281 149.6 5.419 0.996 1.834 Pass 

Average 0.996 1.834 Pass 

5.330 151,0 5,277 149.4 5.370 0,990 1,840 Pass 

5.320 150,7 5,274 149,4 5.372 0,991 1,839 Pass 

5.330 151 .0 5,274 149.4 5.372 0.990 1.837 Pass 

Average 0.990 1.839 Pass 

AverageYd: 0.992 dH@: 1.849 

Q@dH><I : 0.552 

SIGNED: Signature on File Date' 912112012 

Ambient Temperature 

final Average 

(deg F) (deg F) 

78.0 77,5 

79.0 78,5 

80,0 79,5 

75,0 75,0 

76.0 75,5 

770 76,5 

770 770 

78.0 77,5 

78,0 78,0 

74,0 73,5 

74.0 74,0 

74,0 74,0 

Orifice Orifice 

Average Average 

0,98 <: YfYd dH@-dH@av 

<: 1.02? <: 0.155? 

Pass Pass 

Pass Pass 

Pass Pass 

Pass Pass 

Sefni.Annual Meter Calibration -9-pm 9-21-12 WCS 

212612013 

2;49 PM 
Standard Pitot Tube Dimensional Calibration Record 

A - , @ A 

"2 , " Okood 

Sedion AA 

• 02 

r 

Tip 

ccep,I,:,lllly 

Crileria y" y" "" "" "" ",. -0.101 M1 :>6 01 M2:>801 

Hemispherical, 90· Bend wIth 

PitotlO Dale Calibrated B Elliptical, or &urved or mitered 01 0' M1 M' Ratio 02101 601 801 Status 

Coni&al Tip junction 

8 y y 0.31 0.029 2.110 2.550 0.094 1.860 2.5 Pass 
1 

__ ---e A "JEt , 

Side View 

Acceptability 

Criteria z < 1/8" w < 1132" 

Side View, Side View, 

Impact Impact 

openings openings PitotlD Date Calibrated By Properly Properly 

aligned, Z < aligned, W 

1/8" < 1/32" 

026 y Y 

S Type Pitot Tube Dimensional Calibration Record 

l 

.. 

i 

"3/16" < 01 < 

y" 3/8" 

Tubing PazPb Diameter, dt 

Y 0.374 

~ M, -I ~ 

~ End M, 

View 

~ 

n/. n" nl' 

M1 M2 M3 

0.882 0.870 0.882 

n/. n/. 

M' MS 

0.876 0.437 

Reference "A Type-S Pilot Tube Calibration Study, Robert F. Vollaro, October IS, 1975 

If tube is not visibly deformed it is assumed that Pa '" Pb" .5 x avg. of Ml M2, and that average lace opening plane angles represent individual angles to tube axis 

M. 

n/. 

M. 

0.457 

--I M, r-

;< ;t( P:b i -,- M

M: , p, 

+ L 

--I Too View ~ 

1.050t<P<1.5 

10 degrees 5 degrees Ot 

Average Face Average Face Opening Plane Opening Plane Angle, offset Frontal Ang le from Ratio of PlOt Status 

perpendicular from para1Jello 

to transverse Longitudinal 

axis Axis 

0.9 0.4 1.2 Pass ... 
S Type Pitot Tube Dimensional Calibration Record 

cccccC A B31J , 

1 t:xij 

~ M, ~ 

~ 

i 

Side View 

End View 

Acceptability "3/16" <: Dt < 

Criteria z < 116" w < 1132" y" 3/8" "'a "'a ",. ",. ",. 

Side View, Side View, 

Impact Impact 

PilotlD Date Calibrated By openings openings Pa :Pb Tubing MI M2 MJ M' M' Properly Properly Diameter, dt 

aligned, Z <: aligned, W 

118" <: 1132" 

04B y Y Y 0.373 1.030 1.010 1.009 1.004 0.40B 

Reference "A Type-S Pitot Tube Calibration Study, Robert F. Vallare, October 15,1975 

If lube is not visibly deformed it is assumed that Pa = Pb = .5 x 3\19. of Ml M2, and that average face opening plane angles represent individual angles to tube axis 

-/ M, r- ~;:=:::::::::;;-. ~ P:b 1 - , - M

M; , 

Pa 

+ 1 

M, -/ Too View 

~ 

1.050t <P< 1.5 

"'a 10 degrees 5 degrees 01 

Average Face Average Face Opening Plane 

Angle, offset Opening Plane 

M6 from Frontal Angle Ratio of PlOt Status 

perpendicular from parallel to 

to transverse Longitudinal 

axis Axis 

0.414 1.5 0.3 1.4 Pass 
WATER PTC·S 

OIL PTC-10 

WATER PTC-10 

Oil PTC-11 

WATER PTC-11 

WATER 

I 

OIL PTC·23 

WATER PTC-23 

OIL PTC-24 

WATER PTC-24 

I 

Calibrated By: DMW, RM, RMO, DA, ME 

361 

212 

362 

213 

21' 

360 

21' 

361 

21' 

TEMPERATURE SYSTEM CALIBRATION 

STANDARD 

361 

212 

362 

21' 

21' 

360 

214 

361 

213 

21' 

361 

212 

362 

213 

213 

360 

21. 

'61 

21' 

#8 

361 

212 

362 

21' 

21' 

360 

21. 

361 

21' 

360 

21' 

360 

,,, 

212 

360 

212 

360 

212 

212 

360 

212 

212 

360 

21' 

360 

212 

212 

360 

212 

January 2, 2013 
Reference Thermometer LD 

TIC Readout 

1.0 LD. 

.. Reading 1 

OIL PTC-25 362 

WATER PTC-25 213 

ICE PTC-2S 31 

OIL PTC-26 362 

WATER PTC-26 211 

ICE PTC-26 32 

OIL PTC-27 362 

WATER PTC-27 213 

ICE PTC-27 30 

OIL PTC-28 361 

WATER PTC-28 213 

ICE PTC-28 33 

OIL PTC-29 362 

WATER PTC-29 213 

ICE PTC-29 32 

OIL PTC-30 360 

WATER PTC-30 212 

ICE PTC-3D 32 

OIL TRO-l 360 

WATER TRO-l 213 

ICE TRO-l 31 

OIL TRO-4 359 

WATER TRO-4 213 

ICE TRO-4 31 

OIL TRO-5 361 

WATER TRO-5 213 

ICE TRO-5 33 

OIL TRO-6 360 

WATER TRO-6 211 

ICE TRO-6 30 

OIL TRO-a 361 

WATER TRO-a 213 

ICE TRO-a 33 

OIL TRO-9 359 

WATER TRO-9 211 

ICE TRO-9 32 

OIL TRO-11 359 

WATER TRO-" 213 

ICE TRO-l1 33 

OIL TRO-12 360 

WATER TRO-12 212 

ICE TRO-12 32 

OIL TRO-13 360 

WATER TRO-13 21' 

ICE TRO-13 31 

OIL TRO-1S 360 

WATER TRO-1S 213 

ICE TRO-1S 30 

OIL TRO-16 361 

WATER TRO-16 213 

ICE TRO-16 31 

OIL TRO-18 361 

WATER TRO-18 213 

ICE TRO-18 34 

OIL TRO-19 360 

WATER TRO-19 212 

ICE TRO-19 33 

OIL TR0-20 362 

WATER TRO-20 213 

ICE TRO-20 32 

OIL TRO-22 363 

WATER TRO-22 213 

ICE TRO-22 32 

OIL TRO-23 363 

WATER TRO-23 213 

ICE TRO-23 32 

OIL TRO-24 362 

WATER TRO-24 211 

ICE TRO-24 32 

Calibrated By: DMW, RM, RMO, DA. ME 

T1 

TEMPERATURE SYSTEM CALIBRATION 

STANDARD 

#8 F95-195 T2 F95-195 TO F95-Hl5 

TIC - Readout Reference Thermometer 

'F 'F 

Reading 2 Readin9 3 Average Reading 1 Reading 2 Reading 3 Average 

3'" 362 362 360 360 360 360 

213 213 213 212 212 212 212 

31 31 31 32 32 32 32 

362 362 362 360 360 360 360 

211 211 211 212 212 212 212 

32 32 32 32 32 32 32 

362 362 362 360 360 360 360 

213 213 213 212 212 212 212 

30 3lJ 30 32 32 32 32 

361 361 361 360 360 360 360 

213 213 213 212 212 212 212 

33 33 33 32 32 32 32 

362 362 362 360 360 360 360 

213 213 213 212 2" 212 212 

32 32 32 32 32 32 32 

360 360 360 360 360 360 360 

212 2" 2" 212 212 2" 212 

32 32 32 32 32 32 32 

360 360 360 360 360 360 360 

213 213 213 212 212 212 212 

31 31 31 32 32 32 32 

359 359 359 360 360 360 360 

213 213 213 212 212 212 212 

31 31 31 32 32 32 32 

361 361 361 360 360 360 360 

213 213 213 212 212 212 212 

33 33 33 32 32 32 32 

360 360 360 360 360 360 360 

211 211 211 212 212 2" 212 

30 30 30 32 32 32 32 

361 361 361 360 360 360 360 

213 2" 213 212 212 212 212 

33 33 33 32 32 32 32 

359 359 359 360 360 360 360 

211 211 211 212 212 212 212 

32 32 32 32 32 32 32 

359 359 359 360 360 360 360 

213 213 213 212 212 212 212 

33 33 33 32 32 32 32 

360 360 360 360 360 360 360 

212 212 212 212 212 2" 212 

32 32 32 32 32 32 32 

360 360 360 360 360 360 360 

21' 21. 21. 212 2" 212 212 

31 31 31 32 32 32 32 

360 360 360 360 360 360 360 

213 213 213 212 212 212 212 

30 3lJ 30 32 32 32 32 

361 361 361 360 360 360 360 

213 213 213 212 212 212 2" 31 31 31 32 32 32 32 

361 361 361 360 360 360 360 

213 213 213 212 212 212 212 

34 34 34 32 32 32 32 

360 360 360 360 360 360 360 

212 212 212 212 2" 212 212 

33 33 33 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 

32 32 32 32 32 32 32 

363 363 363 360 360 360 360 

213 213 213 212 212 212 212 

32 32 32 32 32 32 32 

362 362 362 360 360 360 360 

211 211 211 212 212 212 212 

32 32 32 32 32 32 32 

Difference 

'F 

2 

1 

1 

2 

1 

0 

2 

1 

2 

1 

1 

1 

2 

1 

0 

0 

0 

0 

0 

1 

1 

1 

1 

1 

1 

1 

1 

0 

1 

2 

1 

1 

1 

1 

1 

0 

1 

1 

1 

0 

0 

0 

0 

2 

1 

0 

1 

2 

1 

1 

1 

1 

1 

2 

0 

0 

1 

2 

1 

0 

3 

1 

0 

3 

1 

0 

2 

1 

0 

%,C'R) 

0.2% 

0.1% 

0.2% 

0.2% 

.1 ·~ 

0.0% 

0.2% 

0.1% 

0.4% 

0.1% 

0.1% 

0.2% 

0.2% 

0.1% 

0.0% 

0.0% 

0.0% 

0.0% 

0,0% 

0.1% 

0.2% 

0.1% 

0.1% 

0.2% 

0.1% 

0.1% 

0.2% 

0.0% 

0.1% 

0.4% 

0.1% 

0.1% 

0.2% 

0.'% 

0.1% 

0.0% 

0.1% 

0.1% 

0.2% 

0.0% 

0.0% 

0.0% 

0.0% 

0.3% 

0.2% 

0.0% 

0.1% 

0.4·~ 

0.1% 

0.1% 

0.2% 

0.1% 

0.1% 

0.4% 

0.0% 

0.0% 

0,2% 

0.2% 

0.1% 

0.0% 

0,4% 

0,1% 

0.0% 

0.4% 

0,1% 

0.0% 

0,2% 

0.1% 

0.0% 

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 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

January 2, 2013 
WATER PTC-22 

OIL PTC-23 

WATER PTC-23 

OIL PTC-24 

WATER PTC-24 

I 

Calibrated By: DMW, RM, RMO, DA, ME 

213 

363 

211 

361 

212 

213 

363 

211 

361 

212 

TEMPERATURE SYSTEM CALIBRATION 

STYPE 

213 

363 

211 

361 

'" 

363 

211 

361 

212 

212 

360 

212 

360 

212 

212 

360 

212 

360 

212 

212 

360 

212 

360 

212 

212 

360 

212 

360 

212 o 

January 2, 2013 
Reference Thennometer 1. 0 .: 

TIC Readout 

1.0. ID 

'26 Reading 1 

all PTC-2S 362 

WATER PTC-2S 213 

ICE PTC-2S 32 

all PTC-26 362 

WATER PTC-26 212 

ICE PTC-26 31 

all PTC-27 363 

WATER PTC-27 213 

ICE PTC-27 30 

all PTC-28 362 

WATER PTC-28 212 

ICE PTC-28 30 

all PTC-29 361 

WATER PTC-29 211 

ICE PTC-29 31 

all PTC-30 361 

WATER PTC-30 212 

ICE PTC-3D 31 

all TRO-1 361 

WATER TRO-1 212 

ICE TRO-1 33 

all TRO-4 362 

WATER TRO-4 211 

ICE TRO-4 32 

all TRO-S 362 

WATER TRO-S 214 

ICE TRO-S 32 

all TRO-6 362 

WATER TRO-6 212 

ICE TRO-6 31 

all TRO-8 362 

WATER TRO-8 213 

ICE TRO-8 35 

all TRO-9 361 

WATER TRO-9 212 

ICE TRO-9 32 

all TRO-11 360 

WATER TRO-11 214 

ICE TRO-11 31 

all TRO-12 360 

WATER TRO-12 213 

ICE TRO-12 32 

all TRO-13 361 

WATER TRO-13 212 

ICE TRO-13 31 

all TRO-15 364 

WATER TRO-1S 213 

ICE TRO-1S 31 

all TRO-16 364 

WATER TRO-16 212 

ICE TRO-16 32 

all TRO-18 362 

WATER TRO-1 8 213 

ICE TRQ-18 32 

all TRO-19 363 

WATER TRO-19 213 

ICE TRO-19 31 

all TRO-20 364 

WATER TRO-20 212 

ICE TRO-20 33 

all TRO-22 363 

WATER TRO-22 213 

ICE TRO-22 31 

all TRO-23 362 

WATER TRO-23 212 

ICE TRO-23 31 

all TRO-24 362 

WATER TRO-24 213 

ICE TRO-24 32 

Calibrated By: DMW, RM, RMO, DA, ME 

T1 

TIC 

TEMPERATURE SYSTEM CALIBRATION 

STYPE 

#26 F95-195 T2 F95-195 T3 F9S-195 

- Readout Reference Thermometer 

of of 

ReadinJ:l2 Reading 3 Average Reading 1 Reading 2 ReadinQ 3 Average 

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 3'" 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 

214 214 214 212 212 212 212 

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 

362 362 362 360 360 360 360 

213 213 213 212 212 212 212 

35 35 35 32 32 32 32 

361 361 361 360 360 360 360 

212 212 212 212 212 212 212 

32 32 32 32 32 32 32 

360 360 360 360 360 360 360 

214 214 214 212 212 212 212 

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 

Difference 

of 

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 

%,fR) 

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% 

0.0% 

0.2% 

0.1% 

0.0% 

0.2% 

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% 

0.0% 

0.1% 

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% 

0.4% 

0.1% 

0.2% 

0.2% 

0.0% 

0.2% 

0.2% 

0.1% 

0.0% 

Pess 

Pass 

Pass 

Pass 

Pass 

Pass 

Pass 

Pass 

Pass 

P '" Pass 

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 

P 

P 

P 

P 

P 

P 

'" '" '" '" '" '" '" 

P 

P 

P 

P 

P 

P 

'" '" '" '" '" '" 

January 2, 2013 
Reference Thennometer 1.0.: 

TIC Readout 

1.0. 1.0. 

#48 Readina 1 

OIL 3WCS 358 

WATER 3WCS 212 

ICE 3WCS 

OIL SWCS 360 " WATER SWCS 212 

ICE SWCS J2 

OIL 6WCS 357 

WATER 6WCS 212 

ICE 6WCS 32 

OIL 7WCS 358 

WATER 7WCS 213 

ICE 7WCS 34 

OIL 12WCS 359 

WATER 12WCS 212 

ICE 12WCS JJ 

OIL 14WCS 358 

WATER 14WCS 211 

ICE 14WCS J2 

OIL 17WCS 360 

WATER 17WCS 211 

ICE 17WCS 30 

OIL laWCS 360 

WATER lawcs 213 

ICE laWCS 30 

OIL 19WCS 360 

WATER 19WCS 213 

ICE 19WCS 32 

OIL PTC-a 360 

WATER PTC-8 213 

ICE PTC-8 J2 

OIL PTC-9 361 

WATER PTC-9 212 

ICE PTC-9 32 

OIL PTC-IO 360 

WATER PTC-tO 212 

ICE PTC-l0 JJ 

all PTC-l1 361 

WATER PTC-l1 212 

ICE PTC-lt 34 

all PTC-12 360 

WATER PTC-12 214 

ICE PTC-12 33 

all PTC-13 359 

WATER PTC-13 213 

ICE PTC-13 J2 

all PTC-14 360 

WATER PTC-14 213 

ICE PTC-14 34 

all PTC-1S 358 

WATER PTC-1S 212 

ICE PTC-1S J2 

all PTC-16 358 

WATER PTC-t6 211 

ICE PTC-t6 32 

all PTC-,7 360 

WATER PTC-17 212 

ICE PTC-17 30 

all PTC-20 360 

WATER PTC-20 213 

ICE PTC-20 3S 

all PTC-21 361 

WATER PTC-21 212 

ICE PTC-21 33 

Oil PTC-22 361 

WATER PTC-22 212 

ICE PTC-22 J2 

all PTC-23 360 

WATER PTC-23 211 

ICE PTC-23 J2 

all PTC-24 360 

WATER PTC-24 212 

ICE PTC-24 34 

Calibrated By: DMW, RM, RMO, DA, ME 

T1 

TEMPERATURE SYSTEM CALIBRATION 

STYPE 

#48 F9S-19S T2 F9S-19S T3 F95-19S 

TIC - Readout Reference Thennometer 

'F 'F 

Readina 2 Readina 3 Averaae Readina 1 Reading 2 Reading 3 Average 

358 358 358 360 360 360 360 

212 212 212 212 212 212 212 

" " " J2 J2 J2 J2 

360 360 360 360 360 360 360 

212 212 212 212 212 212 212 

J2 J2 J2 J2 J2 J2 J2 

357 357 357 360 360 360 360 

212 212 212 212 212 212 212 

J2 J2 J2 J2 32 32 J2 

358 358 358 360 360 360 360 

213 213 213 212 212 212 212 

34 34 34 J2 32 32 32 

359 359 359 360 360 360 360 

212 212 212 212 212 212 212 

JJ JJ JJ J2 J2 32 32 

358 358 358 360 360 360 360 

211 211 211 212 212 212 212 

J2 J2 32 J2 32 32 J2 

360 360 360 360 360 360 360 

211 211 211 212 212 212 212 

30 30 30 32 32 32 J2 

360 360 360 360 360 360 360 

213 213 213 212 212 212 212 

30 30 30 J2 J2 J2 J2 

360 360 360 360 360 360 360 

213 213 213 212 212 212 212 

J2 J2 J2 J2 J2 32 J2 

360 360 360 360 360 360 360 

213 213 213 212 212 212 212 

J2 J2 J2 32 32 32 32 

361 361 361 360 360 360 360 

212 212 212 212 212 212 212 

32 32 32 32 32 32 32 

360 360 360 360 360 360 360 

212 212 212 212 212 212 212 

33 33 33 32 32 32 32 

361 361 361 360 360 360 360 

212 212 212 212 212 212 212 

34 34 34 32 32 32 32 

360 360 360 360 360 360 360 

214 214 214 212 212 212 212 

33 33 33 32 J2 J2 J2 

359 359 359 360 360 360 360 

213 213 213 212 212 212 212 

J2 J2 J2 J2 J2 J2 J2 

J60 360 360 360 360 360 360 

213 213 213 212 212 212 212 

34 34 34 J2 J2 J2 32 

358 358 358 360 360 360 360 

212 212 212 212 212 212 212 

32 32 32 32 32 32 32 

358 358 358 360 360 360 360 

211 211 211 212 212 212 212 

32 32 32 32 32 32 32 

360 360 360 360 360 360 360 

212 212 212 212 212 212 212 

30 30 30 32 J2 32 32 

360 360 360 360 J60 360 360 

213 213 213 212 212 212 212 

3S 3S 3S 32 32 32 32 

361 361 361 360 360 360 360 

212 212 212 212 212 212 212 

33 33 33 32 J2 J2 J2 

361 361 361 360 360 360 360 

212 212 212 212 212 212 212 

J2 J2 J2 J2 J2 J2 32 

360 360 360 360 360 360 360 

211 211 211 212 212 212 212 

J2 J2 J2 32 32 32 32 

360 360 360 360 360 360 360 

212 212 212 212 212 212 212 

34 34 34 32 32 32 32 

Oifference 

'F %,(OR) 

2 0.2% 

0 0.0% 

1 0.2% 

0 0.0% 

0 0.0% 

0 0.0% 

3 0.4% 

0 0.0% 

0 0,0% 

2 0,2% 

1 0,1% 

2 0,4% 

1 0.1% 

0 0.0% 

1 0.2% 

2 0.2% 

1 0.1% 

0 0.0% 

0 0.0% 

1 0.1% 

2 0,4% 

0 0.0% 

1 0,1% 

2 0.4% 

0 0.0% 

1 0.1% 

0 0.0% 

0 0.0% 

1 0.1% 

0 0.0% 

1 0.1 % 

0 0.0% 

0 0.0% 

0 0.0% 

0 0.0% 

1 0.2% 

1 0.1% 

0 0.0% 

2 0.4% 

0 0.0% 

2 0,3% 

1 0.2% 

1 0.1% 

1 0.1% 

0 0.0% 

0 0.0% 

1 0.1% 

2 0.4% 

2 0.2% 

0 0.0% 

0 0,0% 

2 0.2% 

1 0.1% 

0 0.0% 

0 0.0% 

0 0.0% 

2 0.4% 

0 0.0% 

1 0.1% 

3 0.6% 

1 0.1% 

0 0.0% 

1 0.2% 

1 0.1% 

0 0.0% 

0 0.0% 

0 0.0% 

1 0.1% 

0 0.0% 

0 0.0% 

0 0.0% 

2 0.4% 

Pass 

Pass 

Pass 

Pass 

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 

P 

P '" '" '" 

P 

P 

P '" '" '" 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

P 

'" '" 

'" '" '" '" 

'" 

'" '" '" '" '" '" 

'" '" 

January 2, 2013 
OIL 

WATER 

I 

1.0. 

PTC-25 

PTC-25 

Calibrated By: DMW, RM, RMO, DA, ME 

356 

213 

TEMPERATURE SYSTEM CALIBRATION 

STYPE 

356 

213 

#48 

358 

213 

360 

212 

January 2, 2013 
NOZZLE CALIBRATION DATA 

Nozzle 1.0. 4 .v.J.JM'·( (!J • ..>.3 'i 5z -51iL Date ) - i).6- 13 

Material 55 By .;::! tA t/i..~A... 

Configuration (L or Hook) l.f.vtAC 

O2 = O J- 33 

Maximum Difference Dj - Dj = 0·,,1. (must be 0.004") 

Average Dn = 0 -J 3 vI 

Note: Measure three diameters with micrometer 

D5934098 _A 

Date of last revision 9/28/2012 Master Document 5torage\FormslDatasheetslCalibration Forms 
Appendix A.4 

R041 0688 

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: 

R041 0688 

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. 

A-10 /III/tall 
PROCEDURES AND CALCULATIONS: 

Figure 1 presents a flow 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, 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 

is expected 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% 

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 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 Linearity = Analyzer Response - Predicted Response * 100% 

Analyzer Range 

where: 

Response to High Gas - Response to Zero Gas 

Predicted Response = * Mid Gas Value + Response to Zero Gas 

High 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 0688 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. 

Post - Test System Bias Resonse - Pre - Test System Bias Response Analyzer Drift = • 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: 

where: 

C, = Drift/bias corrected concentration 

C = Raw Test Average 

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

Co = Average of pre- and post-test to sample system bias zero 

Cm• = 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 N02 to 

NO converter. This test will be performed once on the day of the test. The converter 

efficiency must be 90% or greater. 

R041 0688 A-12 
Analyzer 

Cal 

Cal No 

Error < 2% 

Yes I Yes 

No 

System Nn System 

Bias < 5% Problem? 

Yes 

Don't Know Stratified No 

Location? 

Yes 

Multi-Point Single Point 

Test Test 

System No 

Bias < 5% 

Yes 

Cal No 

Drift < 3% 

1 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 

1 checks are performed within 2 hours Yes 

of the previous bias check. No No 

Analyzer Cal 

Cal? Error < 2% 

Yes 

No 1 Yes 

Yes System ( Finish 

1 Bias < 5% tFIGURE 1: SCAQMD METHOD 100.1 CALIBRATION AND TEST SEQUENCE 

R041 0688 A-13 
APPENDIX B PROCESS DATA 

R041 0688 8-1 
Appendix B.1 Process and CEMS Data 

R041 0688 8-2 
Appendix 8.1.1 Sentinel Unit 4 Stratification Test 

R041 0688 B·3 
Data Summary Report 

Company : CPV Sentinel, LLC 

62575 Powerline Road 

Source : 

Data Group: 

Report Name : 

Start of Report: 

Desert Hot Springs, CA 92240 

Turbine 4 

4>1-Min Cales 

4>Summary - I-Min RATA 

02/11/2013 09,02 

S~nllt \ UV'i+ L{ 

s¥ 1\ +- (,£\((.1L 

End of Report, 02/11/2013 09,36 

G3 4 -C4 G34-Cll G34-C20 G34 -C3 G34 -Cl3 

TRACE 

Environmental S y stems, In c. 

Validation: All Available Data 

Group#-Channel# G34 -CIO G34-C6 G34-C7 G34 - C8 G34-C18 G34-C 

Long -Descrip . 

Short Descrip. 

Units 

G34-C2 

4,Stk NOx 

Stk NOx 

4>Stk 02 4>NOx Mass 4>StkFlow 4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk CDc 4>Gas Flow 4>NH3 Inj 4>MW La 

Range 

02/11/2013 09:02 

02/11/2013 09:03 

02/11/2013 09:04 

02/11/2013 09:05 

02/11/2013 09;06 

02/11/2013 09:07 

02/11/2013 09:08 

02/11/2013 09:09 

02/11/2013 09:10 

02/11/2013 09:11 

02/11/2013 09:12 

02/11/2013 09:13 

02/11/2 013 09:14 

02/11/ 2 013 09:15 

02/11/ 2 013 09:16 

02/11/ 2 013 09:17 

02/11/2013 09;18 

02/11/2013 09:19 

02/11/2013 09:20 

02/11/2013 09:21 

02/11/2013 09:22 

02/11/2013 09:23 

02/11/201 3 09:24 

02/11/2013 09:25 

02/11/2013 09:26 

02/11/2013 09:27 

02/11/2013 09:28 

02/11/2 013 09:29 

02/11/ 2 013 09:30 

02/11/2013 09:31 

Date/Time Printed: 

ppm 

0-150 

2.9 

2.9 

3.0 

3.0 

2.9 

3.0 

3.0 

2.9 

2.9 

3.0 

2.8 

2.9 

2.9 

2.8 

2.9 

2.9 

2.8 

2.9 

2.9 

2.9 

2.9 

2.9 

2.9 

3.0 

2.8 

3.0 

2.9 

2.8 

2.9 

3.0 

Stk 02 

• 

0-25 

12.90 

12.91 

12.89 

12.88 

12.88 

12.88 

12.88 

12.88 

12.88 

1 2 .87 

12.91 

12.92 

12.92 

12 .93 

12. 9 0 

12.89 

1 2 .91 

12.90 

12.91 

12.90 

12.92 

12. 91 

12.91 

12.88 

12 . 90 

12.89 

12 . 89 

12 . 91 

12 .91 

12.91 

02/11/2013 09,49 

NOx Mass 

Ib/hr 

0-100 

7.44 

7.43 

7.45 

7.47 

7.45 

7.46 

7.45 

7.46 

7.47 

7.48 

7.42 

7.40 

7.43 

7.40 

7.45 

7.43 

7.41 

7.42 

7.42 

7.42 

7.39 

7.40 

7.40 

7.42 

7.40 

7.42 

7.42 

7.40 

7.40 

7.41 

StkFlow 

kscfh 

0-300000 

21172 

21150 

21164 

21185 

2 1 145 

21172 

21129 

21159 

21191 

21190 

21121 

21113 

21185 

21115 

21181 

21119 

21105 

21118 

21127 

21099 

21073 

21081 

21071 

21061 

21058 

21091 

21078 

21081 

21075 

21103 

Stk CO 

ppm 

0-1000 

l.7 

2.0 

2.1 

2.2 

2.2 

2.3 

2.2 

2.3 

2.3 

2.3 

2.7 

3.1 

2.9 

3.3 

3.3 

2.8 

3 . 0 

2.9 

3.0 

2.8 

2.9 

2.9 

2.8 

2.6 

2.8 

2.7 

2.5 

2.8 

3.0 

2.9 

CO Mass 

Ib/hr 

0-100 

2.79 

2.78 

2.79 

3.73 

3.73 

3.73 

3.72 

3.73 

3.73 

3.74 

3.71 

4.63 

4.64 

4 . 62 

4 . 65 

4.65 

4.63 

4.64 

4.64 

4.64 

4.62 

4.63 

4.62 

3.71 

4.63 

3.71 

3.71 

4 .63 

4.63 

4.63 

NOx Rate 

Ib!mmBtu 

0-1 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

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 

2.14 

2.14 

2.21 

2.21 

2.13 

2.21 

2.21 

2.13 

2.13 

2.20 

2.07 

2.14 

2.14 

2.07 

2.14 

2.14 

2.07 

2.14 

2.14 

2.14 

2.14 

2.14 

2.14 

2.21 

2.07 

2.21 

2.14 

2.07 

2.14 

2.22 

Stk CDc Gas hscfh 

hscfh 

0 -10000 

ppm 

0-1000 

1. 25 

1 .4 8 

1. 55 

1. 62 

1. 62 

1. 69 

1. 62 

1. 69 

1. 69 

1. 69 

1. 99 

2 . 29 

2 . 14 

2 .4 4 

2 .43 

2 . 06 

2 . 22 

2.14 

2.22 

2.07 

2.14 

2.14 

2.07 

1. 91 

2.07 

1. 99 

1. 84 

2.07 

2 .2 2 

2.14 

8861.4 

8841.0 

8869.2 

8889.0 

8872.2 

8883.6 

8865.6 

8878.2 

8891.4 

8902.2 

8829.0 

8814.6 

8844.6 

8804.4 

8865.0 

8850.0 

8822.4 

8838.6 

8831.4 

8830.8 

8797.8 

8812.2 

8808.0 

8836.8 

8813.4 

8838.6 

8833.2 

8812.2 

8809.8 

8821.2 

NH3Inj 

Ib/hr 

0 -1 000 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

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 

107. : 

107 .. 

107. ( 

107. 

108.1 

106. 

106.: 

107. : 

107. ! 

107. : 

106. ! 

106. ! 

106. : 

106.! 

106. ' 

106.: 

106 

106. 

106. 

106, . 

105 .. 

IDS. ! 

106. 

106 . : 

106. ! 

106 .. 

106. ! 

106 .. 

105 . : 

106, ' 

PagE 
Group#-Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/11/2013 09:32 

02/11/2013 09:33 

02/11/2013 09:34 

02/11/2013 09:35 

02/11/2013 09:36 

Period Average 

Period Max Value 

Period Min Value 

Period Totals = 

Period % Recovery 

Date/Time Printed: 

G34-C2 G34-C4 G34 - C11 G34-C13 G34-C10 G34-C6 G34-C7 G34 - C8 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

G34-C20 

4>StkFlow 

StkFlow 

kscfh 

0 - 300000 

G34-C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

4>CO Mass 4>NOx Rate 4>Stk NOXe 4>Stk CDc 4>Gas Flow 

G34 - C18 

4>NH3 Inj 

NH3Inj 

lb/hr 

0-1000 

G34-C 

4>MW Lo 

Stk 02 MW Lo 

% 

0-25 

NOx Mass 

lb/hr 

0-100 

CO Mass 

lb/hr 

0 - 100 

2.9 12.91 7.42 21128 2.6 3 . 71 

3.0 12.90 7.44 21149 2.7 3 . 72 

2.9 12.90 7.43 21142 2.7 3.72 

2.8 12.91 7.40 21084 2.9 4.63 

2.8 12.90 7.42 21112 3.1 4.64 

2.9 12 .90 7.43 21124 2.7 4.11 

3.0 1 2.93 7.48 21191 3 . 3 4.65 

2.8 12.87 7.39 21058 1.7 2.78 

1.0170E+2 4.5149E+2 2.5993E+2 7.3932E+5 9.3300E+1 1.4386E+2 

100.0 100 . 0 100.0 100.0 100.0 100.0 

02/11/2013 09 , 49 

NOx Rate 

lb/mmBtu 

0-1 

0.008 

0.008 

0 . 008 

0.008 

0 . 008 

0.008 

0.008 

0.008 

2.8000E-1 

1 00.0 

Stk NOXc 

ppm 

0-300 

2.14 

2.21 

2 . 14 

2.07 

2 . 07 

2.14 

2.22 

2.07 

7.5010E+1 

100.0 

Stk COe Gas 

ppm 

0-1000 

hscfh 

hsefh 

0 - 10000 0-1 

1.92 8832.0 110.0 107. ( 

1.99 8851.8 110.0 106. : 

1.99 8848.8 110.0 106.' 

2.14 8813.4 110.0 106.' 

2.29 8836.2 110 . 0 107. ( 

1.97 8841.4 110.0 106.6 

2.44 8902 .2 110.0 108. 

1.25 8797.8 110.0 105. 

6.8820E+1 3.0945E+5 3.8500E+3 3.7335E+ 

100.0 100 . 0 100.~ 100. 

4>Summary - I-Min RATA - Continued PagE 
Appendix B.1.2 Sentinel Unit 4 Ammonia, ROG and NOxlCO Testing 

R041 0688 8-4 
Data Summary Report 

Company : CPV Sentinel, LLC 

62575 Powerline Road 

Desert Hot Springs, CA 92240 

5li'.\Vu\ L{ 

Co~p \1 ~vt I 70~ Source : Turbine 4 

Data Group : 

Report Name : 

Start of Report : 

4>1-Min Cales 

4>Summary - I-Min RATA 

02/12/ 2 013 11,58 

G34 -C4 

End of Report, 02/12/2013 13 , 07 

G34-Cll G34-C13 G34 -CIO 

TRACE 

EIUJironmelllai S.lIsl ems, I nc. 

validation: All Available Data 

Group#- Channel# G34-C6 G34-C7 G34-Ca 

Long Descrip . 

Short Descrip . 

Units 

G34-C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4 >NOx Mass 

G34-C20 

4>StkFlow 

StkFlow 

kscfh 

0-300000 

G34-C3 

4>Stk CO 

Stk co 

4>ca Mass 4>NOx Rate 4>Stk NQXc 4>Stk COc 4>Gas Flow 

Stk CDc Gas hscfh 

G34-C18 

4>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

G34-C 

4>MW Lo 

MW Lo 

Range 

02/12/2013 11:58 

02/12/2013 11:59 

02/12/ 2 013 12:00 

02/12/2013 12:01 

02/12/2013 12:02 

02/12/2013 12:03 

02/12/2013 12:04 

02/12/ 2 013 12:05 

02/12/2013 12:06 

02/12/2013 12:07 

02/12/2013 12:08 

02/12/2013 12:09 

02/12/2013 12:10 

02/12/2013 12:11 

02/12/2013 12:12 

02/12/2013 12:13 

02/12/2013 12:14 

02/12/2 013 12:15 

02/12/2013 12:16 

02/12/2013 12:17 

02/12/2013 12:18 

02/12/2013 12:19 

02/12/2013 12:20 

02/12/2013 12:21 

02/12/2013 12:22 

02/12/2013 12:23 

02/12/2013 12:24 

02/12/ 2 013 12:25 

02/12/2013 12:26 

02/12/2013 12:27 

Date/Time Printed: 

1.6 

1.6 

1.6 

1.6 

1.6 

1.7 

1.7 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.8 

1.8 

1.9 

1.8 

1.B 

1.7 

1.B 

1.9 

1.9 

1.9 

1.9 

1.9 

2.0 

1.9 

1.9 

1.9 

1.9 

Stk 02 

\ 

0-25 

14.09 

14.09 

14.10 

14 .10 

14 .10 

14 .10 

14 .10 

14.09 

14.09 

14.08 

14.08 

14.08 

14.08 

14.08 

14.08 

14.08 

14.09 

14.09 

14.10 

14.10 

14 .10 

14 .10 

14 .10 

14 . 09 

14.08 

14.09 

14.09 

14.08 

14.09 

14.09 

02/12/2013 12,56 

NOx Mass 

1b/hr 

0-100 

2.82 

2.81 

2.81 

2.82 

2.81 

2.82 

2.80 

3.38 

3.40 

2.84 

2.83 

2.83 

2.81 

3.39 

3.39 

3.39 

3.39 

3.38 

2.81 

3.37 

3.37 

3.37 

3.37 

3 . 36 

3.36 

3.36 

3.35 

3.34 

3.35 

3.36 

15062 

15032 

15049 

15103 

15029 

15078 

14995 

15035 

15165 

15138 

15111 

15116 

15020 

15059 

15081 

15099 

15082 

15074 

1503 4 

15054 

15044 

15037 

15035 

14978 

14951 

14966 

14941 

14877 

14907 

14953 

ppm 

0-1000 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D .• 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

0.5 

0.5 

0.5 

0.5 

D.' 

0.5 

0.5 

0.5 

0.5 

0.5 

CO Mass 

1b/hr 

0-100 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.57 

0.57 

0.57 

0.57 

0.56 

0.56 

0.57 

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 

NOx Rate 

Ib/mmBtu 

0-1 

0.005 

0.005 

0.005 

0 . 005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.006 

0.006 

0.006 

0 . 006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0-300 

1. 39 

1. 39 

1. 39 

1. 39 

1. 39 

1.48 

1.48 

1. 56 

1. 56 

1.47 

1.47 

1. 47 

1.47 

1. 56 

1. 56 

1.64 

1. 56 

1. 56 

1.48 

1. 56 

1. 65 

1. 65 

1. 65 

1. 65 

1. 64 

1. 73 

1. 65 

1. 64 

1. 65 

1. 65 

ppm hscfh 

0-1000 0-10000 

0.35 

0.35 

0 . 35 

0 . 35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0 . 35 

0.35 

0 . 35 

0.35 

0.35 

0.35 

0 . 35 

0.35 

0.43 

0.43 

0.43 

0 .4 3 

0.35 

0 . 43 

0.43 

0.43 

0 . 43 

0 . 43 

5366.4 

5355.6 

5353.8 

5373.0 

5346.6 

5364.0 

5334.6 

5356.8 

5403.0 

5401.2 

5391.6 

5393.4 

5359 . 2 

5373.0 

5380 . 8 

5387.4 

5373.6 

5370.6 

5348 .4 

5355.6 

5352.0 

5349.6 

53 4 9.0 

533 6 .4 

5334.6 

5332.2 

5323.2 

5308.2 

5311 . 2 

5327.4 

109.5 

111.2 

109.5 

109.0 

108.3 

108.8 

106.3 

106.5 

108 . 8 

109.3 

108.3 

108.3 

106.7 

107.2 

108.2 

108.5 

107.3 

106.5 

105.3 

105.2 

105.7 

103.5 

104 . 3 

104.7 

103.7 

102.8 

103.8 

102.2 

101.5 

102. 2 

0-1 

55.: 

55. ! 

55.' 

55.' 

55.1 

55.: 

54.: 

55.' 

55. 

55.' 

55.: 

55.' 

55. ! 

S5. : 

55. : 

56.1 

5S. : 

55. ! 

55. ! 

55.! 

S5.1 

55.1 

S4. : 

S5. 1 

54. ! 

55.1 

54. : 

54. : 

54. : 

55.1 

pagE 
Group#-Channel# 

Long Descrip. 

Sh o rt De scrip . 

Units 

Range 

02/12/2013 12:28 

02/12/2013 12:29 

02/12/2013 12:30 

02/12/2013 12:31 

02/12/2013 12:32 

02/12/2013 12:33 

02/12/2013 12:34 

02/12/2013 12;35 

02/12/2013 12;36 

02/12/2013 12:37 

02/12/2013 12;38 

02/12/2013 12:39 

02/12/2013 12:40 

02/12/2013 12 : 41 

02/12/2013 12;42 

02/12/2013 12:43 

02/12/2013 12:44 

02/12/2013 12:45 

02/12/2013 12:46 

02/12/2013 12:47 

02/12/2013 12:48 

02/12/2013 12;49 

02/12/2013 12:50 

02/12/2013 12;51 

02/12/2013 12:52 

02/12/2013 12:53 

02/12/2013 12;54 

Period Ave rage 

Period Max Value 

Period Min Value 

Period Totals ::: 

Period % Recovery 

Date/Time Printed: 

G34-C2 G3 4-C4 G34-C11 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

2.0 

2.0 

2.1 

2.2 

2.' 

2.6 

2.' 

2.6 

2.7 

2.' 

2.6 

2.7 

2.' 

2.' 

2.' 

2.' 

2.' 

2.' 

2.' 

2.' 

2.' 

2.2 

2.B 

2.9 

3.2 

3.0 

2.9 

2.1 

3.2 

1.6 

1.2130E+2 

82,6 

Stk 02 

t 

0-25 

14.09 

14.09 

14.09 

14.09 

14.10 

14.08 

14.09 

14.09 

14.08 

14.09 

14.09 

14.09 

14.09 

14.09 

14.08 

14.09 

14.09 

14.08 

14.08 

14.09 

14.09 

14.09 

14.09 

14.10 

14.09 

14 .10 

14.09 

14.09 

14 .10 

14.08 

8.0312E+2 

8 2 .6 

02/12/2013 12:56 

NOx Mass 

Ib/hr 

0-100 

3.34 

3.35 

3.91 

3.92 

4.48 

4.49 

4.47 

4.46 

5.03 

4.45 

4.45 

5.04 

4.46 

4.45 

4.46 

4.45 

4 .46 

4 .47 

4.48 

4.47 

4.47 

3.90 

5.01 

5.00 

5.57 

5.56 

5.02 

3.79 

5.57 

2.80 

2.1611E+2 

82.6 

G34-C20 

4>StkFlow 

StkFlow 

kscfh 

0-300000 

G34-eJ 

4>Stk CO 

Stk CO 

ppm 

0-1000 

14890 0.5 

14909 0.5 

14922 0.5 

14960 0.4 

15007 0.4 

14995 0.4 

14934 0.4 

14907 0.5 

14906 0.4 

14855 0.5 

14877 0.5 

14981 0.5 

14912 0.5 

14853 0.5 

14885 0.5 

14880 0.5 

14899 0.5 

14926 0.5 

14954 0.4 

14949 0.5 

14938 0.5 

14884 0.5 

14872 0.5 

14867 O.S 

14889 0.5 

14877 0.5 

14912 0.5 

14978 0.5 

15165 0.5 

14853 0.4 

8.5374E+5 2.5800E+l 

82.6 82.6 

G34-C13 G34-C10 G34-C6 

4>CO Mass 4>NOx Rate 4>Stk NOXe 

CO Mass NOx Rate 

lb/hr' lb/mmBtu 

0-100 0-1 

0.56 

0.5 6 

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 

0.5 6 

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 

3 . 1980E+l 

82.6 

0.006 

0.006 

0.007 

0.007 

0.008 

0.008 

0.008 

0.008 

0.009 

0.008 

0.008 

0.009 

0.008 

0.008 

0.008 

0.008 

0 . 008 

0.008 

0.008 

0.008 

0.008 

0.007 

0 . 009 

0.009 

0.010 

0 . 010 

0.009 

0.007 

0.010 

0.005 

3.8600E-1 

82.6 

Stk NOXe 

ppm 

0-300 

1. 73 

1. 73 

1. 82 

1. 91 

2.08 

2.25 

2.08 

2.25 

2.34 

2.08 

2.25 

2.34 

2.17 

2.08 

2.16 

2.17 

2.17 

2.16 

2.08 

2.08 

2.08 

1. 91 

2.43 

2.52 

2.77 

2.60 

2.51 

1. 84 

2.77 

1. 39 

1.0514E+2 

82.6 

G34-C7 G34-C8 

4 >Stk COe 4>Gas Flow 

Stk COe Gas hsefh 

ppm hsefh 

0-1000 0-10000 

0.43 

0.43 

0.43 

0.35 

0.35 

0.35 

0.35 

0. 4 3 

o 3. 

0.43 

0.43 

0.43 

0.43 

0 . 43 

0.43 

0.43 

0 . 43 

0.43 

0.35 

0. 43 

0.43 

0.43 

0.43 

0.43 

0.43 

0 . 43 

0.43 

0.39 

0.43 

0.35 

2.2350E+1 

8 2 . 6 

5305.2 

5311. 8 

5316.6 

5329.8 

5338.8 

5350.2 

5320.8 

5311.2 

5318.4 

5292.6 

5300.4 

5337.6 

5313. a 

5292.0 

5311. 2 

5301.6 

5308.2 

5325.6 

5335.8 

5326.2 

5322.0 

5302.8 

5298.6 

5289.0 

5304.6 

5292.6 

5313.0 

5336.5 

5 4 03,0 

5289.0 

3.04 1 8E+5 

82.6 

G34-C18 

4>NH3 Inj 

NH3Inj 

1b/hr 

0-200 

101.7 

101.7 

102.7 

100.5 

98.3 

99.0 

98.0 

97 . 5 

98.0 

97.7 

96.5 

98.5 

97.3 

97.2 

96.7 

97.8 

97 . 7 

97.8 

99.3 

99.2 

99.2 

97.5 

93.8 

92.2 

93.2 

92.3 

95.0 

102.3 

111. 2 

92.2 

5,8294E+3 

82 . 6 

4>Summary - I-Min RATA - Continued 

G34 - C 

4>MW Lo 

MW Lo 

0 - 1 

54. : 

54.: 

54 .. 

55.1 

55.1 

55.: 

54. ! 

54.1 

54.: 

54.: 

54.: 

54.' 

54.1 

54.1 

54.' 

54. ! 

54. : 

54. ' 

55.1 

54.: 

54. ! 

54.: 

54." 

54. ' 

54. : 

53: 

54.' 

54.8 

56. 

53. 

3.1273E+ 

B2. 

PagE 
Data Summary Report 

Company : CPV Sentinel, LLC 

62575 Powerline Road 

Desert Hot Springs, CA 

Source: 

Data Group: 

Report Name: 

Start of Report : 

Turbine 4 

4>1-Min Cales 

4>Summary - l-Min RATA 

02/12/2013 13,30 

G34-C4 

92240 

5eAfi,f(,l if 

C(?~f\iW1Lt Z 

?o'l, 

End of Report, 02/12/2013 14,39 

G34 - Cl1 G34 - C13 

TRACE 

Environmental Systems, II/C. 

Validation: All Available Data 

Group#-Channel# G34-CIO G34-C6 G34-C7 G34-CB G34-C 

Long Descrip . 

Short Descrip . 

Units 

G34 -C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

G34 -C20 

4;:.StkF!ow 

StkFlow 

kscfh 

0-300000 

G34 -C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

4>CO Mass 4>NOx Rate 4>Stk NQXc 4>Stk COc 4 >Gas Flow 

G34 -C18 

4>NH3 Inj 

NH3Inj 

lb(hr 

0 - 200 

4>MW La 

Range 

02/12/2013 13:30 

02/12/2013 13:31 

02/12/2013 13: 32 

02/12/2013 13:33 

02/12/2013 13:34 

02/12 /2013 13:35 

02/12/2013 13:36 

02/12/2013 13:37 

02/12/2013 13:38 

02/12/2013 13:39 

02/12/2013 13:40 

02/12/2013 13:41 

02/12/2013 13:42 

02/12/2013 13:43 

02/12/2013 13:44 

02/12/2013 13:45 

02/12/2013 13:46 

02/12/2013 13:47 

02/12/2013 13:48 

02/12/2013 13:49 

02/12/2013 13:50 

02/12/2013 13:51 

02/12/2013 13:52 

02/12/2013 13:53 

02/12/2013 13:54 

02/12/2013 13:55 

02/12/2013 13:56 

02/12/2013 13:57 

02/12/2013 13:58 

02/12/2013 13:59 

Date/Time Printed: 

1.6 

1.8 

1., 

1.8 

1.7 

1.7 

1.8 

1.8 

1.8 

1.. 

1.. 

2.0 

1.8 

1.8 

2.0 

1.' 

1.. 

1.. 

2.1 

1.. 

1.. 

1.. 

2.0 

2.1 

1.' 

1.8 

1.8 

1.8 

1.8 

1.8 

Stk 02 

% 

0-25 

14.07 

14.06 

1 4.06 

14.06 

14 . 07 

14.07 

14.07 

14.07 

14.06 

14.06 

14.06 

14.06 

14 . 07 

14.07 

14.07 

14.07 

14.07 

14.07 

14.07 

14.07 

14.07 

14 . 07 

14.06 

14.05 

14.05 

14.05 

14.04 

14.04 

14.04 

14.04 

02/12/2013 17,45 

NOx Mass 

lb(hr 

0 - 100 

2.79 

3.36 

3.38 

3.37 

2.79 

2.78 

3.35 

3.35 

3.35 

3.36 

3.35 

3.35 

3.34 

3.34 

3.33 

3.33 

3.34 

3.34 

3.90 

3.34 

3.34 

3.36 

3.36 

3.94 

3.39 

3.39 

3.40 

3.40 

3.38 

3.39 

14880 

14896 

14969 

14951 

14891 

14810 

14864 

14889 

14857 

14884 

14880 

14880 

14825 

14820 

14805 

14796 

14832 

14827 

14833 

14835 

1 4 845 

1 4 917 

14897 

14946 

15011 

15026 

15034 

15034 

1 4 934 

14976 

D.' 

D.' 

D.' 

0 . 4 

0.4 

0.5 

0.4 

0.5 

0.4 

0.4 

D.' 

0.4 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.4 

0.5 

0.4 

0.4 

0.4 

0.4 

0.4 

D.' 

0.4 

0.4 

0.4 

CO Mass 

lb(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 

0.56 

0.56 

0.56 

0.56 

0.57 

0.57 

0.57 

0.56 

0.56 

NOx Rate 

IbjmmBtu 

0-1 

0.005 

0.006 

0.006 

0 . 006 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.00 6 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

0.006 

0.00 6 

0.00 6 

0.006 

0.007 

0.006 

0.006 

0.006 

0 . 00 6 

0.00 6 

0.006 

Stk NDXc 

ppm 

0-300 

1. 38 

1. 55 

1. 64 

1. 55 

1. 47 

1. 47 

1. 55 

1. 55 

1. 55 

1. 64 

1.64 

1. 73 

1. 55 

1. 55 

1.73 

1. 64 

1. 64 

1. 64 

1. 81 

1. 64 

1. 64 

1. 64 

1. 73 

1. Bl 

1.64 

1.55 

1. 55 

1.55 

1.55 

1. 55 

Stk COc Gas hscfh 

ppm 

0-1000 

0.35 

0.35 

0.35 

0.35 

0.35 

0.43 

0 . 35 

0.43 

0.35 

0.35 

0.35 

0.35 

0 .4 3 

0 . 43 

0.43 

0.43 

0.43 

0.43 

0.43 

0 . 35 

0.43 

0 . 35 

0.35 

0.34 

0.34 

0.34 

0.34 

0.34 

0 . 3 4 

0.34 

hscfh 

0-10000 

5317.2 

5330.4 

5356.8 

5350.2 

5320.8 

5292.0 

5311.2 

5320.2 

5316.6 

5326.2 

5325.0 

5325.0 

5297.4 

5295 . 6 

5290.2 

5287.2 

5299.8 

5298.0 

5300.4 

5301. a 

5304.6 

5330.4 

5331. a 

5356.2 

5379.6 

5385.0 

5395.8 

5395.8 

5359.8 

5374.8 

107.7 

107.5 

107.0 

10B.S 

10 7 .2 

104.8 

105.0 

106.7 

105.5 

105.2 

106.7 

10 4 .7 

105.5 

103.2 

103.2 

104.5 

103.2 

103.7 

104.3 

103.5 

103.7 

104.2 

104.2 

104.2 

109.2 

109.B 

109 .7 

110.8 

109.2 

108.7 

MW La 

0-1 

54. 

55. r 

S5.: 

54. : 

54. : 

54 . . 

55. r 

54 .. 

54 . . 

54.: 

54 . . 

54. : 

54. r 

54.1 

54.: 

54 . . 

54 . . 

S4.1 

54.' 

54.' 

54.' 

55.1 

54.' 

54.: 

55, ' 

55,' 

55.! 

55,: 

55 . ' 

S5. ! 

pagt 
Group#-Channel# 

Long Descrip . 

Short Descrip . 

units 

Range 

02/12/2013 14:00 

02/12/2013 14:01 

02/12/2013 14:02 

02/12/2013 14:03 

02/12/2013 14:04 

02/12/2013 14:05 

02/12/2013 14:06 

02/12/2013 14;07 

02/12/2013 14:08 

02/12/2013 14;09 

02/12/2013 14:10 

02/ 12 / 2 013 14:11 

02/12/2013 14;12 

02/12/2013 14:13 

02/12/ 2013 14;14 

02/12/2013 14:15 

02/12/2013 14:16 

02/12/2013 14;17 

02/12/2013 14:18 

02/12/2013 14:19 

02/12/2013 14;20 

02/12/2013 1 4:21 

02/12/2013 14:22 

02/12/2013 14;23 

02/12/2013 1 4:24 

02/12/2013 14:25 

02/12/2013 14;26 

02/12/2013 14:27 

02/12/2013 14:28 

02/12/ 2013 14;29 

02/12/2013 14:30 

02/12 / 2 013 14:31 

02/12/2013 14:32 

02/12/2013 14:33 

02/12/ 2013 14:34 

02/12/2013 14:3 5 

02/12/2013 14:36 

02/12/2013 14;37 

02/12/2013 14;38 

02/12/2013 14;39 

Date/Time Printed: 

G34-C2 G34-C4 G34 -ell G3 4 -C20 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 4>StkFlow 

1.8 

1.9 

1.9 

1.8 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

2.0 

2.0 

1.8 

1.6 

1.6 

1.6 

1.6 

1. 6 

1.7 

1.7 

1.7 

1.8 

1.7 

1.8 

1.7 

1 . 7 

1.8 

1.8 

1.7 

1.8 

1.8 

1.9 

1.9 

1.9 

2.0 

1.8 

1.9 

1.9 

1.9 

1.9 

Stk 02 

• 

0-25 

14.04 

14.03 

14.02 

14.03 

14.03 

14.04 

14.04 

14.05 

14. OS 

14.05 

14.05 

14.05 

14.04 

14.05 

14.04 

14.05 

14.04 

14.04 

14.03 

14.04 

14. 04 

14 . 03 

14.04 

14.04 

14.04 

14.04 

14.04 

14 . 04 

14.04 

14.04 

14.03 

14.04 

14. 04 

14.04 

14.03 

14.03 

14.04 

14.05 

14.05 

14. OS 

02/12/2013 17,45 

NOx Mass 

lb/hr 

0 - 100 

3.38 

3.39 

3.40 

3.40 

3.39 

3.37 

3.36 

3.36 

3.36 

3.35 

3.3 5 

3.37 

3.36 

2.81 

2.81 

2.80 

2.81 

2.81 

2.81 

2.81 

2.81 

3.38 

2.81 

3.37 

2.81 

2.80 

3.37 

3.37 

2.80 

3.36 

3.37 

3.36 

3.36 

3.37 

3.38 

3.38 

3.37 

3.37 

3.37 

3.37 

StkFlow 

kscfh 

0-300000 

14934 

14964 

15007 

15004 

14972 

14921 

14867 

14896 

14860 

14839 

14845 

14921 

14869 

14907 

14916 

14899 

14937 

14899 

14906 

14912 

14929 

14922 

14892 

14892 

14887 

14857 

14887 

14919 

14864 

14881 

14877 

14864 

14852 

14897 

14936 

14911 

14901 

1 4 914 

14912 

14944 

G34-C3 G34-C13 G34-C10 G34-C6 G34-C7 G34 -C8 G34-C18 G34-C 

4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk COc 4>Gas Flow 4>NH3 Inj 4>MW La 

Stk CO 

ppm 

0-1000 

0.4 

0.4 

0.4 

0.4 

0.' 

0.4 

0.4 

0.4 

0. ' 

0. 4 

0 .• 

0.4 

0.' 

0. 4 

0 .' 

0.4 

0.4 

0. 4 

0.4 

0.' 

0 . 5 

0.' 

0.' 

0.4 

0 .4 

0.' 

0.' 

0.' 

0 .4 

0.4 

0.4 

0.4 

0.4 

0.4 

0 .4 

0.' 

0.4 

0.5 

0.5 

0.5 

CO Mass 

lb/hr 

0-100 

0.56 

0.56 

0.57 

0.57 

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 

0.56 

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 

NOx Rate 

Ib/mmBtu 

0-1 

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 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.005 

0.006 

0.005 

0.005 

0.006 

0.006 

0.005 

0.006 

0.006 

0.006 

0.006 

0 . 006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0-300 

1. 55 

1. 63 

1. 63 

1. 55 

1. 63 

1. 63 

1. 63 

1. 64 

1. 64 

1. 64 

1. 72 

1. 72 

1. 55 

1. 38 

1. 38 

1. 38 

1. 38 

1. 38 

1. 46 

1. 46 

1. 46 

1. 55 

1.46 

1. 55 

1.46 

1. 46 

1. 55 

1. 55 

1. 46 

1. 55 

1. 55 

1. 63 

1. 63 

1. 63 

1.72 

1. 55 

1. 63 

1. 64 

1. 64 

1. 64 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0 . 34 

0.34 

0.34 

0.3 4 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.3 4 

0.34 

0.3 4 

0.3 4 

0.34 

0.34 

0.34 

0 .34 

0.34 

0.43 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.3 4 

0 .34 

0.34 

0 .3 4 

0.34 

0.34 

0.34 

0.43 

0.43 

0.43 

5359.8 

5378. 4 

5401.8 

5392.8 

5381.4 

5355.0 

5335.8 

5338.2 

5325.6 

5317.8 

5320.2 

5347.2 

5336.4 

534 2 .4 

5353.2 

5339.4 

5361.0 

5347.2 

5357.4 

5352.0 

5358.0 

5363.4 

53 44.S 

5344.8 

5343.0 

5332.2 

5343.0 

5354.4 

5334.6 

5340.6 

5347.2 

5334.6 

5330.4 

5346.6 

536S.2 

5359.2 

5347.8 

534 4. f! 

5344.2 

5355.6 

NH3Inj 

1b/hr 

0 - 200 

107.5 

10S.5 

108.S 

109.2 

10S.3 

10S.3 

106.8 

106.2 

106.3 

104.8 

104.7 

106.S 

109.8 

110.8 

110.3 

110.2 

110.2 

Ill. 7 

110.0 

110.2 

109.5 

109.3 

109 .2 

107.7 

108.5 

107.7 

107.3 

108.7 

107.7 

106.7 

108.3 

1 06.8 

104.8 

105.S 

106.0 

106.S 

106.0 

105.0 

105.5 

105.3 

4 >Summary - I-Min RATA - Continued 

MW Lo 

0-1 

55. ' 

55 

55 . . 

55. ' 

55 .. 

55. : 

54 .. 

55. : 

54. : 

54. : 

5' 

54 

55. : 

55 . . 

55. : 

55. : 

55.1 

55.: 

55 . ~ 

55.: 

55.1 

55.1 

55.1 

54 .. 

55 . . 

5 4. 

54. : 

55. : 

54.: 

54.: 

55 . . 

54. : 

54 . . 

55.1 

55. : 

55 . . 

54. : 

55. : 

5' 

55.: 

pagE 
Period Average E: loB 14 . 05 3.26 14901 0.4 0.56 0.006 1. 58 0.36 5340.8 107.0 54.9 

Period Max Value 2.1 14.07 3.94 15034 0.5 0.57 0.007 1. 81 0.43 5401.8 111. 7 55. 

Period Min Value 1.6 14.02 2.78 14796 0.4 0.56 0.005 1. 38 0.34 5287.2 103.2 54. 

Period Totals = 1.2820E+2 9.8344E+2 2.2827E+2 1.0430E+6 2.9400E+l 3.9260E+1 4.0700E- 1 1.1042E+2 2 . 5190E+l 3.7385E+5 7.4933E+3 3.8448E+ 

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. 
Data Summary Report 

Company: CPV Sentinel, LLC 

62575 Powerline Road 

Desert Hot Springs, CA 92240 

5v.h~\ '1 

~r:"rlt.<. ~{ Source : Turbine 4 

Data Group : 4>1-Min Cales 

Report Name : 

Start of Report : 

4>Summary - I-Min RATA 

02/11/2013 15,45 

G)4-C4 

1?~ 

End of Report: 02/11/2013 16:52 

G34-Cll G34-C20 G34 -C13 

Q~~l{ TRACE --- .-. 

EnlJironmental Systems, Illc . 

validation: All Available Data 

Group#-Channel# G34-CIO G34 -C6 G34 -C7 G3 4-CB G34-C 

Long Descrip . 

Short Descrip. 

Units 

G34-C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 4>StkFlow 

StkFlow 

kscfh 

0 -30000 0 

G34-C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk CDc 4>Gas Flow 

Stk CDc Gas hscfh 

G34 -C18 

4>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

4>MW Lo 

MW Lo 

Range 

02/11/2013 15:45 

02/11/2013 15:46 

02/11/ 2 013 15:47 

02/11/2013 15:48 

02/11/2013 15:49 

02/11/2013 15:50 

02/11/2013 15:51 

02/11/2013 15:52 

02/11/2013 15:53 

02/11/ 2013 15 :54 

02/11 / 2013 15 :55 

02/11/2013 15: 56 

02/11/2013 15:57 

02/11/2013 15:58 

02/11/2013 15:59 

02/11/ 2013 16:00 

02/11/2013 16:01 

02/11/2013 16:02 

02/11/2013 16:03 

02/11 /2013 16:04 

02/11/2013 16:05 

02/11/2013 16:06 

02/11/2 013 16:07 

02/11/2013 16:08 

02/11/2013 16:09 

02/11/2013 16:10 

02/11/2013 16:11 

02/11/ 2013 16:12 

02 / 11/2013 16:13 

02/11/2013 16;14 

Date/Time Printed : 

2.2 

2.2 

2.2 

2.0 

2.0 

2.1 

2.1 

2.2 

2.1 

2.0 

2.1 

2.1 

2.1 

2.1 

2.0 

2.0 

2.1 

2.2 

2.1 

2.2 

2.3 

2.1 

2.1 

2.2 

2.1 

2.1 

2.1 

2.2 

2.3 

2.3 

Stk 02 

% 

0-25 

13.52 

13.52 

13.52 

13.53 

13.53 

13.54 

13.54 

13.54 

13 .54 

13.54 

13.54 

13.53 

13.54 

13.54 

13 .54 

13 .55 

13.55 

13.55 

13.54 

13 .55 

13.55 

13.55 

13.54 

13.53 

13.54 

13.54 

13 .54 

13.53 

13.53 

13 .53 

02/11/2013 19,07 

NOx Mass 

1b/hr 

0-100 

4.42 

4.42 

4.42 

4.41 

4.40 

4.39 

4.39 

4 .3 9 

4.39 

4.39 

4 .40 

4.41 

4.41 

4.42 

4.41 

4 .40 

4 .40 

5.15 

4.41 

5 .14 

5.15 

4.41 

4.42 

4.42 

4.40 

4.41 

4.39 

4.41 

5.15 

5.16 

18163 

18172 

18183 

18164 

18111 

18114 

18100 

18086 

18108 

18089 

18139 

18135 

18180 

18202 

18195 

18142 

18172 

18218 

18183 

18176 

18211 

18215 

18202 

18199 

18156 

18187 

18111 

18169 

18163 

18217 

1.7 

1.8 

1.6 

1.6 

1.9 

2.2 

2.3 

2.3 

2.6 

2.3 

2.0 

1.9 

1.7 

1.6 

1.6 

1.7 

1.8 

1.6 

1.6 

1.6 

1.3 

1.2 

1.' 

1.' 

1.. 

1.5 

1.6 

1.6 

1.5 

1.5 

CO Mass 

1b/hr 

0-100 

2.21 

2.21 

2.21 

2.21 

2.20 

2.93 

2.93 

2.92 

3.66 

2.93 

2 . 93 

2.20 

2.21 

2.21 

2.21 

2.20 

2.20 

2.21 

2.21 

2.20 

1.47 

1.47 

2.21 

2.21 

2.20 

2.21 

2.20 

2.21 

2.21 

2.21 

NOx Rate 

Ib/mmBtu 

0-1 

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 

0.006 

0.006 

0.006 

0.007 

0.006 

0.007 

0.007 

0.006 

0 . 006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.00 7 

0.007 

Stk NOXc 

ppm 

0-300 

1. 76 

1. 76 

1. 76 

1. 60 

1. 60 

1. 68 

1. 68 

1. 76 

1. 68 

1. 60 

1.68 

1. 68 

1. 68 

1. 68 

1. 60 

1. 61 

1. 69 

1. 77 

1. 68 

1. 77 

1. 85 

1. 69 

1. 68 

1. 76 

1. 68 

1. 68 

1. 68 

1. 76 

1. 84 

1. 84 

ppm hscfh 

0-1000 0-10000 

1. 36 

1.44 

1. 28 

1. 28 

1. 52 

1. 76 

1. 84 

1. 84 

2.08 

1.84 

1.60 

1. 52 

1. 36 

1.28 

1. 28 

1. 36 

1. 44 

1. 28 

1. 28 

1. 28 

1.04 

0.96 

1.12 

1.12 

1.12 

1.20 

1.28 

1.28 

1.20 

1.20 

7012.8 

7016.4 

7020 .6 

7003.8 

6983.4 

6975.0 

6969 . 6 

6964.2 

6972.6 

6965.4 

6984.6 

6992.4 

7000.2 

7008.6 

7006 .2 

6976.2 

6987.6 

7005 .6 

7001.4 

6989.4 

7002.6 

7004. 4 

7008.6 

7017.0 

6991. 2 

7003.2 

6973.8 

7005.6 

7003.2 

7024.2 

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 

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 

0 - 1 

81.' 

81.1 

81." 

81.! 

80 . ! 

80. : 

80. : 

79. 

80 . . 

80.1 

80. : 

80.: 

81.1 

81.1 

81.' 

80 .. 

80 .. 

81. : 

80. : 

80 .. 

81.: 

80 . . 

81.1 

81.: 

80. : 

81.: 

80 . . 

81.: 

80. : 

81." 

Pag~ 
Group#-Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/11/2013 16:15 

02/11/2013 16:16 

02/11/2013 16:17 

02/11/2013 16:18 

02/11/2013 16:19 

02/11/2013 16:20 

02/11/2013 16:21 

02/11/2013 16:22 

02/11/2013 16:23 

02/11/2013 16:24 

02/11/2013 16;25 

02/11/2013 16:26 

02/11/2013 16:27 

02/11/2013 16:28 

02/11/2013 16:29 

02/11/2013 16:30 

02/11/2013 16:31 

02/11/2013 16:32 

02/11/2013 16:33 

02/11/2013 16:34 

02/11/2013 16:35 

02/11/2013 16:36 

02/11/2013 16:37 

02/11/2013 16:38 

02/11/2013 16 : 39 

02/11/2013 16:40 

02/11/2013 16:41 

02/11/2013 16,42 

02/11/2013 16:43 

02/11/2013 16:44 

02/11/2013 16:45 

02/11/2013 16:46 

02/11/2013 16:47 

02/11/2013 16:48 

02/11/2013 16:49 

02/11/2013 16;50 

02/11 /2013 16 : 51 

02/11/2013 16:52 

Date/Time Printed: 

G34-C2 G34-C4 G34-C11 G34-C20 G34 -C3 G34-C13 G34-C10 G34-C6 G34-C7 G34-C8 G34-C18 G34-C 

4>Stk NOx 

Stk NOx 

ppm 

0-15 0 

4>Stk 02 4>NOx Mass 4>StkFlow 4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk COc 4>Gas Flow 4>NH3 Inj 4>MW Lo 

2.1 

2.1 

2.2 

2.2 

2.2 

2.2 

2.3 

2.4 

2 .• 

3.0 

2.9 

2.9 

2.8 

2.8 

2.8 

2.6 

2.8 

2.8 

2.7 

2.8 

2.7 

2.7 

2.6 

2.7 

2.7 

2.7 

2 .• 

2.4 

2.5 

2.6 

2.6 

2.7 

2.6 

2.6 

2.5 

2.5 

2.' 

2.3 

Stk 02 

• 

0-25 

13.53 

13.53 

13.53 

13.53 

13.53 

13.53 

13.54 

13.53 

13.53 

13.54 

13.55 

13.55 

13.55 

13.55 

13.55 

13.55 

13.53 

13 .54 

13.54 

13.55 

13.55 

13.55 

13 .55 

13.54 

13.55 

13.54 

13 .54 

13.53 

13.52 

13.52 

13.52 

13.53 

13.52 

13.53 

13.54 

13.54 

13.55 

13 .56 

02/11/2013 19,07 

NOx Mass 

1b/hr 

0-100 

4.42 

4.42 

4.42 

4.42 

4.43 

4.42 

5.17 

5.16 

5.90 

6.66 

6.63 

6.64 

5.90 

5.92 

5.91 

5.87 

5.89 

5.92 

5.91 

5.89 

5.89 

5.89 

5.89 

5.91 

5.90 

5.92 

5.93 

5.19 

5.18 

5.93 

5.93 

5.93 

5.94 

5.95 

5.19 

5.20 

5.19 

5.16 

StkFlow 

kscfh 

0-300000 

18197 

18177 

18178 

18178 

18245 

18211 

18264 

18211 

18220 

18300 

18233 

18270 

18261 

18321 

18295 

18175 

18199 

18289 

18258 

18250 

18247 

18242 

18228 

18284 

18261 

18312 

18320 

18298 

18264 

18287 

18276 

18314 

18317 

18362 

183 25 

18368 

18379 

18282 

Stk CO 

ppm 

0-1000 

1., 

1.4 

1.5 

1.5 

1.7 

1.4 

1.3 

1.2 

1.2 

1.0 

1.0 

1.0 

1.0 

1.0 

1.0 

1.1 

1.1 

1.0 

1.0 

1.0 

1.1 

1.1 

1.1 

1.1 

1.0 

1.0 

0.9 

1.0 

1.0 

0.9 

0.9 

0.9 

0.9 

0.9 

0.9 

0.9 

0.9 

1.0 

Co Mass 

1b/hr 

0-100 

2.21 

2.21 

2.21 

2.21 

2.22 

2.21 

1. 48 

1.47 

1. 48 

1.48 

1.47 

1.48 

1.47 

1.48 

1.48 

1. 47 

1. 47 

1.48 

1.48 

1.47 

1.47 

1. 47 

1. 47 

1.48 

1.47 

1. 48 

1. 48 

1.48 

1.48 

1.48 

1.48 

1.4B 

1. 49 

1. 49 

1. 4B 

1.49 

l.4B 

1.47 

NOx Rate 

Ib/mmBtu 

0-1 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

0.007 

0.008 

0 . 009 

0.009 

0.009 

O.OOB 

0.008 

0.008 

O. OOB 

0.008 

O.OOB 

0.008 

0.008 

0.008 

O.OOB 

0.008 

0.008 

0.008 

0.008 

0.008 

0.007 

0.007 

0.008 

0.008 

O.OOB 

0.008 

0.008 

0.007 

0.007 

0 . 007 

0.007 

Stk NOXc 

ppm 

0-300 

1. 68 

1. 68 

1. 76 

1. 76 

1. 76 

1. 76 

1. 84 

1. 92 

2.08 

2.40 

2.33 

2.33 

2.25 

2.25 

2.25 

2.09 

2.24 

2.24 

2.16 

2.25 

2.17 

2.17 

2.09 

2.16 

2.17 

2.16 

2.08 

1. 92 

2.00 

2.08 

2.08 

2.16 

2.08 

2.0B 

2.00 

2.00 

1. 93 

1. 85 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

1.12 7016.4 

1.12 7008.6 

1.20 7009.2 

1.20 7009.2 

1.36 7035.0 

1.12 7021. 8 

1.04 7032.6 

0.96 7021.8 

0.96 7025.4 

0.80 7046.4 

0.80 7011.0 

0.80 7025.4 

0.80 7021.8 

0 . 80 7045 .2 

0.80 7035.0 

0.88 6988.8 

0.88 7017.0 

0.80 7042.2 

0.80 7030.2 

0.80 7017.6 

0.88 7016.4 

0.88 7014.6 

0.88 7009.2 

0.88 7040.4 

0.80 7021.8 

0.80 7051.2 

0.72 

0.80 

0.80 

0.72 

0.72 

0.72 

0.72 

0.72 

0.72 

0.72 

0. 72 

0 . 80 

7054.2 

7055.4 

7051.8 

7060.8 

7056.6 

7061. 4 

7072.2 

7080.0 

7056.0 

7072.8 

7067.4 

7020.6 

NH3Inj 

1b/hr 

0-200 

110.0 

110.0 

118.5 

118.5 

119.2 

117.7 

120.2 

119.2 

114.5 

116.2 

115.0 

113.7 

115.5 

118.2 

116.0 

116.0 

116.2 

118.7 

118.2 

118.3 

117.2 

116.0 

116.3 

118.3 

118.2 

119.3 

120.3 

120.5 

121.7 

122.3 

121.0 

122.8 

122.0 

124.2 

121. 2 

121. 3 

123.3 

117.7 

4>Summary - I-Min RATA - Continued 

MW Lo 

0 -1 

81.! 

81.1 

81.! 

81.! 

81. 

82.1 

80 .. 

81.: 

81. ! 

81.: 

81.: 

81. : 

81.' 

81.! 

82.1 

81.: 

81. . 

82. : 

81. : 

81. : 

81. : 

80 . . 

81.: 

81.: 

81. . 

81.! 

82. [ 

82.: 

83.1 

82. r 

82. : 

82 . ! 

81.' 

82. : 

82. ! 

81.: 

81. . 

81.! 

PaqE 
Period Average :c 2.' 13.54 5.12 18220 1.. 1. 92 0.007 1. 90 1.10 7017.5 114.6 81. 2 

Period Max Value 3.0 13 .S6 6.66 18379 2.6 3.66 0.009 2.40 2.08 7080.0 124.2 83. 

Period Min Value 2.0 13.52 4.39 18086 0.' 1.47 0.006 1.60 0.72 6964.2 110.0 7'. 

Period Totals :IE 1.61S0E+2 9.2059E+2 3.479lE+2 1.2389E+6 9.3l00E+l 1.3034E+2 4.7200E-l 1. 293 9E+2 7 . 4480E+l 4.7719E+S 7.7934E+3 S.S27lE+ 

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. 
Dat a Summary Repor t 

Company : CPV Sentinel, LLC 

62575 Powerline Road 

Desert Hot Springs, CA 92240 

Source : Turbine 4 

Dat a Group : 4>1-Min Cales 

Report Name: 

Start of Re por t : 

4>Summary - I-Min RATA 

02/11/2013 17,10 

5e;.~' tf 

c,....pl;(Jr1«. ;If-t. 

1-7'% 

End of Report: 02/11/2013 18:19 

G34-C4 G34 - Cl1 G34 - C20 G34 - C3 G34 -C13 

(2Ifff\- {2wt 5 TRACE 

Environmental Systems, Inc. 

Validation: All Available Data 

Group#-Channel# G34-CIO G34 - C6 G34-C7 G34-CB G34 -C18 G34-C 

Lo ng Descrip . 

Short Descrip. 

Units 

G34-C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 4>StkFlow 4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk CDc 4>Gas Flow 4>NH3 Inj 4>MW La 

Range 

02/11/2013 17:10 

02/11/2013 17:11 

02/11/2013 17:12 

02/11/2013 17:13 

02/11/2013 17:14 

02/11/2013 17:15 

02/11/2013 17:16 

02/11/2013 17:17 

02/11/2013 17:18 

02/11/2013 17:19 

02/11/2013 17:20 

02/11/2013 17:21 

02/11 /2013 17:22 

02/11/2013 17:23 

02/11/2013 17:24 

02/11/2013 17:25 

02/11/2013 17:26 

02/11/2013 17:27 

02/11/2013 17;28 

02/11/2013 17:29 

02/11/2013 17:30 

02/11/2013 17:31 

02/11/2013 17:32 

02/11/2013 17:33 

02/11/2013 17:34 

02 / 11/2013 1 7:35 

02/11/2013 17:36 

02/11/2013 17:37 

02/11/2013 17:38 

02/11/2013 17:39 

Date/Time Printed: 

2.8 

2.B 

2.8 

2.7 

2.7 

2.6 

2.6 

2.5 

2.5 

2.5 

2.' 

2.3 

2.' 

2.5 

2.6 

2.5 

2.5 

2.5 

2.6 

2.5 

2.5 

2.' 

2 . 5 

2.7 

2.7 

2.7 

2.7 

2.6 

2.7 

2.7 

Stk 02 

\ 

0-25 

13.54 

13.54 

13.54 

13 .54 

13 .56 

13.56 

13.55 

13.55 

13.56 

13.56 

13.56 

13 . 57 

13.56 

13.57 

13.58 

13.58 

13.58 

13.56 

13.55 

13.56 

13.56 

13.57 

13.57 

13.55 

13.55 

13.56 

13.55 

13.55 

13.55 

13.54 

02/11/2013 19,07 

NOx Mass 

1b/hr 

0-100 

5.89 

5.89 

5.89 

5.89 

5.90 

5.91 

5.92 

5.18 

5.18 

5.18 

5.17 

5.16 

5.17 

5.16 

5.90 

5.15 

5.14 

5.15 

5.90 

5.14 

5.14 

5.12 

5.11 

5.84 

5.B4 

5.83 

5.86 

5.85 

5. BS 

5.86 

StkFlow 

kscfh 

0-300000 

18200 

18205 

18200 

18203 

18293 

18315 

18332 

18329 

18359 

18356 

18332 

18295 

18332 

18310 

18329 

18281 

18260 

18251 

18265 

18212 

18193 

18157 

18123 

18083 

1B072 

18059 

18128 

18115 

18111 

18 127 

Stk CO 

ppm 

0-1000 

1.3 

1.3 

1.3 

1.3 

1.2 

1.2 

1.1 

1.1 

1.1 

1.0 

1.1 

1.1 

1.1 

1.1 

1.1 

1.2 

1.3 

1.3 

1.2 

1.3 

1.3 

1.3 

1.5 

1.5 

1.5 

1.5 

1.5 

1.3 

1.3 

1.3 

CO Mass 

1b/hr 

0-100 

1.47 

1. 47 

1. 47 

1. 47 

1.48 

1.48 

1.48 

1.48 

1.48 

1. 48 

1.48 

1.47 

1 .4 8 

1.47 

1. 47 

1.47 

1.47 

1.47 

1.48 

1. 47 

1.47 

1.46 

2.19 

2.19 

2.19 

2.18 

2.20 

1.46 

1.46 

1.47 

NOx Rate 

Ib/mmBtu 

0-1 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.008 

0.007 

0.007 

0.007 

0.008 

0.007 

0.007 

0.007 

0.007 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

Stk NOXc 

ppm 

0-300 

2.24 

2.24 

2.24 

2.16 

2.17 

2.09 

2.09 

2.01 

2.01 

2.01 

1. 93 

1. 85 

1. 93 

2.01 

2.10 

2.02 

2.02 

2.01 

2.09 

2.01 

2.01 

1. 93 

2.01 

2.17 

2.17 

2.17 

2.17 

2 . 09 

2.17 

2.16 

Stk CDc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

1.04 

1.04 

1. 04 

1.04 

0.96 

0.96 

0.B8 

0.88 

0 . 88 

0.80 

0.88 

0.89 

0.88 

0.89 

0.B9 

0.97 

1. 05 

1.04 

0.96 

1. 04 

1. 04 

1.05 

1.21 

1.20 

1.20 

1. 21 

1. 20 

1. 04 

1. 04 

1.04 

7008.0 

7009 . 8 

7008.0 

7009.2 

7024.8 

7033.2 

7049 . 4 

7048.2 

7050.0 

7048.8 

7039.8 

7015.8 

7039 . 8 

7021.8 

7019.4 

7000.8 

6993.0 

7008.6 

7023.6 

6993.6 

6986.4 

6963.0 

694 9.8 

6953.4 

6949.2 

6934.8 

6970.8 

6966.0 

6964 .2 

6979.8 

NH3Inj 

1b/hr 

0-200 

115.0 

113.7 

115.7 

114.5 

I1B.2 

117.3 

118.8 

118.7 

119.8 

119.8 

119.8 

11B.7 

118 . 3 

118.3 

117.2 

115.5 

115.2 

115.8 

117.5 

116.0 

114.8 

116.7 

112.3 

111.8 

111. a 

111.0 

112.0 

114.0 

114 .3 

114.5 

MW La 

0-1 

81. : 

80 .. 

81.1 

80. : 

81. : 

81. : 

81. . 

81.' 

82.1 

81. ~ 

81.: 

82.1 

82.1 

81.~ 

81. . 

Sl.~ 

BO .. 

81.: 

81 

81 

81 

80. 

SO .. 

so . ~ 

80. : 

79. : 

80.: 

80. : 

80 . . 

80. : 

Pagt 
Group#-Channel# 

Long Descrip . 

Short Descri p . 

Units 

Range 

02/11/2013 17,40 

02/11/2013 17:41 

02/11/ 2 013 17:42 

02/11/2013 17:43 

02/11/2013 17:44 

02/11/2013 17:45 

02/11/2013 17:46 

02/11/2013 17:47 

02/11/2013 17:48 

02/11/2013 17:49 

02/11/2013 17:50 

02/11/2013 17:51 

02/11/ 2 013 17:52 

02/11/ 2 013 17:53 

02/11/2013 17:54 

02/11/2013 17:55 

02/11/2013 17:56 

02/11/2013 17:57 

02/11/2013 17:58 

02/11/2013 17:59 

02/11/2013 18:00 

02/11/2013 18:01 

02/11/2013 18:02 

02/11/2013 18:03 

02/11/2013 18:04 

02/11/2013 18:05 

02/11/2013 18:06 

02/11/ 2 013 18,07 

02/11/2013 18:08 

02/11/2013 18:09 

02/11/2013 18:10 

02/11/2013 18:11 

02/11/2013 18:12 

02/11/2013 18:13 

02/11/2013 18:14 

02/11/2013 18 :15 

02/11/2013 18:16 

02/11/2013 18:17 

02/11/2013 18:18 

02/11/2013 18:19 

Date/Time Printed: 

G34-C2 G34-C4 G34-Cll 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

2.7 

2.7 

2.6 

2.5 

2.' 

2.7 

2 . 5 

2.9 

2 . 9 

2.8 

2.8 

2.7 

2.6 

2.6 

2 . 7 

2.7 

2.7 

2 .7 

2.6 

2.6 

2.5 

2.5 

2. 6 

2.5 

2.5 

2.6 

2.5 

2.5 

2.5 

2.5 

2.7 

3.1 

3.1 

3.1 

2.9 

3.0 

3.0 

2.8 

2.B 

2.8 

Stk 02 

• 

0-25 

13 . 55 

13.55 

13.56 

13.56 

13.58 

13.57 

13.57 

13.58 

13.58 

13.58 

13.57 

13 .58 

13.59 

13 .58 

13.58 

13.57 

13.57 

13.57 

13.57 

13.58 

13.58 

13.58 

13.57 

13.56 

13.57 

13.57 

13.57 

13.57 

13.57 

13.56 

13 .56 

13.56 

13 .5 6 

13.57 

13.57 

13.58 

13.58 

13.57 

13.58 

13.58 

02/11/2013 19, 07 

NOx Mass 

lb/hr 

0-100 

5.85 

5.86 

5.85 

5.13 

5.09 

5.85 

5.10 

6.57 

6.56 

5.84 

5.84 

5.82 

5.81 

5.80 

5.80 

5.82 

5.82 

5.81 

5.80 

5.79 

5.06 

5.06 

5.80 

5.10 

5.08 

5.82 

5.08 

5.09 

5.09 

5.09 

5.B2 

6.55 

6.57 

6.54 

6.55 

6.53 

6.55 

5.83 

5.81 

5.B2 

G34 -C20 

4>StkFlow 

StkFlow 

kscfh 

0 - 300000 

1810B 

1B144 

1B145 

IB159 

18096 

18166 

18107 

1B151 

1B140 

18138 

1B140 

18099 

1 8072 

18031 

18027 

1 8071 

18059 

18044 

17999 

17988 

17984 

17963 

18016 

18067 

18038 

18054 

18038 

18055 

18046 

1B021 

18054 

18064 

18093 

18054 

18073 

18055 

18111 

18087 

18064 

18097 

G34-C3 

4 >Stk CO 

Stk CO 

ppm 

0-1000 

1.3 

1.4 

1.3 

1.3 

1., 

1., 

1.4 

1.4 

1.5 

1., 

1.' 

1.5 

1.6 

1.7 

1.6 

1.6 

1.4 

1.4 

1.5 

1.6 

1.6 

1.7 

1.7 

1.' 

1.' 

1.5 

1.5 

1.5 

1.5 

1.4 

1.4 

1.4 

1.4 

1.4 

1.5 

loS 

1.5 

1.5 

1.5 

1.5 

G34-C13 G34 - CI0 G34-C6 

4>CO Mass 4>NOx Rate 4>Stk NOXc 

CO Mass 

1b/hr 

0 - 100 

1. 46 

2.20 

1. 46 

1. 46 

2.18 

2.19 

2.19 

2.19 

2.19 

2.19 

2.19 

2.18 

2.18 

2.18 

2.17 

2.18 

2.18 

2.18 

2.17 

2.17 

2.17 

2.17 

2.18 

2.19 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.19 

2.18 

2.1B 

2.18 

2.18 

2.18 

2.18 

2.18 

NOx Rate 

l b /mmBtu 

0-1 

0.008 

0.008 

0.008 

0.007 

0.007 

0.008 

0.007 

0.009 

0.009 

0.008 

0.008 

0.008 

0.008 

0.008 

0.00 8 

0 . 008 

0.008 

0.008 

0.008 

0.008 

0.007 

0.007 

0.008 

0.007 

0.007 

0.008 

0.007 

0 . 007 

0.007 

0.007 

0.008 

0.009 

0.009 

0.009 

0.009 

0.009 

0.009 

0.008 

0.008 

0.008 

Stk NOXc 

ppm 

0-300 

2.17 

2.17 

2.09 

2.01 

1. 93 

2.17 

2.01 

2.34 

2.34 

2.26 

2.25 

2.18 

2.10 

2.10 

2.18 

2 . 17 

2.17 

2 . 17 

2.09 

2.10 

2.02 

2.02 

2.09 

2.01 

2.01 

2.09 

2.01 

2.01 

2.01 

2.01 

2.17 

2.49 

2 . 4 9 

2.50 

2.33 

2.42 

2.42 

2.25 

2.26 

2.26 

G34-C7 G34 -C8 

4>Stk CDc 4>Gas Flow 

Stk CDc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

1. 04 

1.12 

1. 04 

1. 04 

1.13 

1.13 

1.13 

1.13 

1. 21 

1.13 

1.13 

1.21 

1.29 

1.37 

1. 29 

1. 29 

1.13 

1.13 

1. 21 

1. 29 

1.29 

1.37 

1. 37 

1.13 

1.13 

1.21 

1. 21 

1. 21 

1.21 

1.13 

1.13 

1.13 

1.13 

1.13 

1. 21 

1.21 

1.21 

1. 21 

1. 21 

1 21 

6963.0 

6976.8 

6967.8 

6973.2 

6930.0 

6966.6 

6943.8 

6951 . 0 

6946.8 

6946.2 

6956 . 4 

6931 . 2 

6911. 4 

6905.4 

6903.6 

6930.0 

6925 . 2 

6919.8 

6902.4 

688 8 .6 

6887.4 

6879.0 

6909 . 0 

6937 . 8 

6917.4 

6923.4 

6917.4 

6924.0 

6920.4 

6920.4 

6933.0 

6936.6 

6948 .0 

6923.4 

6930.6 

6914.4 

6936 . 0 

6936 . 0 

6918 . 0 

6930.6 

G34-C18 

4>NH3 Inj 

NH3Inj 

1b/hr 

0-200 

113 .3 

115.0 

114 . 5 

114.8 

112.5 

114.7 

112.0 

109.7 

111.2 

109. 5 

Ill. 8 

110.0 

109.5 

109.5 

110.7 

109.2 

111. 8 

112.0 

109.7 

11 0.7 

109.2 

110.7 

109.2 

113.0 

112.2 

112.8 

113.2 

110.7 

111.7 

113.8 

109.8 

109.0 

108 .2 

108. 2 

108.5 

109.0 

108 . 7 

110.8 

110.0 

110.8 

4>Summary - 1-Min RATA - Continued 

G34-C 

4>MW Lo 

MW Lo 

0-1 

80 . ~ 

80. : 

BO. 

BO 

79.: 

80.1 

79. : 

80. ! 

80.: 

BO. : 

80. ~ 

79. : 

79. ! 

79.: 

79.: 

79. : 

79 .. 

80. c 

79 .. 

79.1 

7B .. 

79.: 

79. : 

79. ! 

79. : 

BO .1 

79. : 

80. : 

79.! 

79. : 

80.: 

79 .. 

BO . ! 

80. C 

80.1 

79 .. 

80 .. 

79.! 

79.! 

79 . : 

Pag( 
Period Average = 2.6 13.57 5.67 1B139 1.' 1. 90 O.OOB 2.13 1.11 6960.6 113 .1 80.3 

Period Max Value = 3.1 13.59 6.57 1B359 1.7 2.20 0.009 2.50 l.37 7050.0 119.8 82. 

Period Min Value ~ 2.3 13.54 5.06 17963 1.0 1. 46 0.007 1. B5 O.BO 6B79.0 10B.2 78. 

Period Totals = 1.B540E+2 9.4957E+2 3.96B2E+2 1.2697E+6 9.6600E+1 1 .32B5E+2 5.4300E-1 1.4915E+2 7.7720E+l 4.B724E+5 7.917BE+3 5.6275E+ 

Period % Recovery 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 1 00.0 100.0 100. 
Data Summary Report 

Company: CPV Sentinel, LLC 

62575 Powerline Road 

Desert Hot Springs, CA 

Source : Turbine 4 

Da ta Gro up : 

Report Narne : 

Start of Report : 

4>1 -Min Cales 

4>Summary - I-Min RATA 

02/11/2013 10,06 

G34 - C4 

92240 

~i1.u.\ l)""rL-f 

Cov'\ ~l.v.L ~ \ 

\CifJf + ~ f\ 

End of Report: 02/11/2013 11:19 

G34 - Cll G34 -C20 G34 -C3 G34 -CD G34 - CI0 

TRACE 

EnlJironmenlal Systems, Inc. 

validation: All Available Data 

Group# - Channel# G34 - C6 G34 - C7 G3 4 -C8 G34 - C18 G34 - C 

Lo ng Des crip . 

Short Descrip . 

Units 

G34 -C2 

4:>Stk NOx 

Stk NOx 

ppm 

0-150 

4 >Stk 02 4>NOx Mass 4>StkFlow 4>Stk CO 4 >CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk CDc 4>Gas Flow 4>NH3 Inj 4>MW Lo 

Range 

02/11/2013 10 : 06 

02/11/2013 10:07 

02/11/2013 10:08 

02 /11/2013 10:09 

02/11/2013 10:10 

02/11/2013 10:11 

02/11/2013 10:12 

02/11/2013 10:13 

02/11/2013 10:14 

02/11/2013 10:15 

02/11/2013 10:16 

02/11/2013 10:17 

02/11/2013 10:18 

02/11/2013 10:19 

02/11/2013 10:20 

02/11/2013 10:21 

02 / 11/2013 10 : 22 

02/11/2013 10:23 

02/11/2013 10:24 

02/11/2013 10,25 

02/11/2013 10:26 

02/11/2013 10:27 

02/11/2013 10:28 

02/11/2013 10:29 

02/11/2013 10:30 

02/11/2013 10:31 

02/11/2013 10:32 

02/11/2013 10:33 

02/11/2013 10:34 

02/11/2013 10:35 

Date/Time Printed: 

2.8 

2.7 

2.8 

2.7 

2.8 

2.9 

2 .7 

2.7 

2.9 

2.8 

2.8 

2.8 

2.8 

2.7 

2.7 

2.6 

2.7 

2.8 

2.7 

2.6 

2.7 

2.7 

2 .6 

2.7 

2.7 

2.7 

2.7 

2.6 

2.7 

2.6 

Stk 02 

t 

0-25 

12.91 

12.93 

12.93 

12.93 

12.93 

12.92 

12.94 

12.94 

12.92 

12.91 

12.91 

12.91 

12.94 

12.94 

12.95 

12.95 

12.95 

12.93 

12.94 

12.96 

12.94 

12.95 

12.97 

12.96 

12.95 

12.95 

12.96 

12.97 

12.96 

12.97 

02/11/2013 11,47 

NOx Mass 

1b/hr 

0-100 

7.44 

6.50 

7.44 

6.50 

7.4.3 

7.45 

6.49 

6.48 

7 . 44 

7.44 

7.44 

7.44 

7.42 

6.46 

6.46 

6.45 

6.45 

7.40 

6.45 

6 .44 

6.45 

6.43 

6.42 

6.44 

6 . 45 

6.44 

6.45 

6.43 

6.44 

6.44 

StkFlow 

kscfh 

0-300000 

21186 

21210 

21236 

21213 

21223 

21245 

21198 

21175 

21201 

21186 

21186 

21186 

21209 

21101 

21124 

21093 

21092 

21118 

21084 

21092 

21074 

21038 

21047 

21092 

21092 

21079 

21134 

21086 

21097 

21106 

Stk co 

ppm 

0-1000 

2.8 

3.1 

3.2 

3.' 

3.1 

3.1 

3.0 

3.1 

2.8 

2.8 

2.8 

2.8 

2 . 9 

3.2 

3 .2 

3.2 

3.2 

2.7 

2.9 

3.1 

3.1 

3 .0 

3.3 

3.3 

3.0 

2.9 

3.0 

3.0 

3 . 2 

3.2 

CO Mass 

1b/hr 

0-100 

4.65 

4.64 

4 . 65 

5.57 

4.65 

4.66 

4.63 

4.63 

4.65 

4.65 

4.65 

4.65 

4.64 

4.61 

4.61 

4.61 

4.61 

3.70 

4.61 

4.60 

4.61 

4.59 

5.50 

4.60 

4.61 

4.60 

4.61 

4.59 

4.60 

4.60 

NOx Rate 

Ib/mmBtu 

0-1 

0.008 

0 . 007 

0.008 

0.007 

0.008 

0.008 

0.007 

0.007 

0.008 

0.008 

0.008 

0.008 

0.008 

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 

2.07 

2.00 

2.07 

2.00 

2.07 

2.14 

2.00 

2.00 

2 .14 

2.07 

2.07 

2.07 

2.08 

2.00 

2.00 

1. 93 

2.00 

2.07 

2.00 

1. 93 

2.00 

2.00 

1. 93 

2.01 

2.00 

2.00 

2 .01 

1. 93 

2.01 

1. 93 

Stk CDc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

2.07 8856.0 

2.29 8844.0 

2 .37 885 4 .8 

2.52 

2.29 

2.29 

2.22 

2.30 

2.07 

2.07 

2.07 

2.07 

2.15 

2.37 

2.37 

2.37 

2.37 

2 . 00 

2.15 

2.30 

2.30 

2.23 

2.46 

2.45 

2.23 

2.15 

2.23 

2.23 

2.38 

2.38 

8845.2 

8849.4 

8869.8 

8827.8 

8818.2 

8851.2 

8856.0 

8856.0 

8856.0 

8832 . 6 

8787.6 

8785.8 

8773.2 

8772.6 

8805.6 

8780.4 

8761.8 

8776.2 

8750.4 

8731.8 

8761.8 

8772.6 

8767.2 

8779.2 

8748.0 

8763.6 

8756.4 

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 

MW Lo 

0-1 

107 . 1 

107.1 

106 . ~ 

106.1 

106. : 

106.1 

106. : 

106 .. 

107 

106. : 

106. : 

1 0 6 .: 

106 . ~ 

106.1 

1 06. : 

105 .. 

105. : 

106 .. 

IDS. : 

106 .. 

106.1 

IDS. : 

105. : 

105.: 

106. : 

106. 1 

106. : 

105 . ~ 

106 . : 

105 . : 

Pag( 
Group#-Channe l # 

Long De scrip . 

Short Descri p . 

Units 

Rang e 

02/11/2013 10:36 

02/11/2013 10:37 

02/11/2013 10,38 

02/11/2013 10:39 

02/11/2013 10:40 

02/11/2013 10:41 

02/11/2013 10:42 

02/11/2013 10:43 

02/11/2013 10:44 

02/11/2013 10:45 

02/11/2013 10:46 

02/11/2013 10:47 

02/11/2013 10:48 

02/11/2013 10:49 

02/11/2013 10:50 

02/11/201 3 10:51 

02/11/2013 10:52 

02/11/2013 10,53 

02/11/2013 10:54 

02/11/2013 10 :55 

02/11/2013 10:56 

02/11/2013 10:57 

02/11/2013 10:58 

02/11/2013 10:59 

02/11/2013 11:00 

02/11/2013 11:01 

02/11/2013 11 :0 2 

02/11/2013 11:03 

02/11/2013 11:04 

02/11/2013 11:05 

02/11/2013 11:06 

02/11/2013 11:07 

02/11/2013 11:08 

02/11/2013 11:09 

02/11/2013 11:10 

02/11/2013 11:11 

02/11/2013 11 :12 

02/11/2013 11:13 

02/11/2013 11:14 

02/11/2013 11:15 

Date/Time Printed: 

G34-C2 G34-C4 G34-Cll G34 -C20 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4 >Stk 02 4>NOx Mass 4>StkFlow 

2.7 

2.7 

2.7 

2.7 

2.7 

2.7 

2.8 

2.7 

2.8 

2.7 

2.8 

2.7 

2.7 

2.7 

2.7 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.9 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.7 

2.8 

2.9 

2.7 

2.7 

Stk 02 

• 

0-25 

12.95 

12.95 

12.95 

12.94 

12.94 

12.94 

12.93 

12.93 

12.91 

12.92 

12.92 

12.93 

12.93 

12.94 

12.93 

12.92 

12.91 

12.90 

12.91 

12.90 

12.90 

12.90 

12.90 

12.88 

12.89 

12.89 

12.88 

12.89 

12.87 

12.87 

12.88 

12.88 

12.88 

12.89 

12 . 89 

12.90 

12.91 

12.90 

12.91 

12.92 

02/11/2013 lL 47 

NOx Mass 

lb/hr 

0-100 

6.47 

6.46 

6.45 

6.47 

6.46 

6.47 

7.40 

6.47 

7.42 

6.48 

7.42 

6.47 

6.49 

6.47 

6.48 

7.42 

7.45 

7.46 

7.-45 

7.45 

7 . 47 

7.46 

7.47 

7.47 

7.46 

7.45 

7.46 

7.46 

7.48 

7.48 

7.47 

7 . 48 

7.48 

7 . 47 

7.47 

6 . 52 

7.43 

7 . 46 

6. SO 

6.48 

StkFlow 

kscfh 

0-300000 

21148 

21121 

21101 

21126 

21119 

21130 

21128 

21120 

21134 

21116 

21143 

21107 

21181 

21145 

21155 

21172 

2 1217 

21217 

21217 

21201 

21235 

21221 

21237 

21192 

21186 

21170 

21164 

21182 

21196 

21195 

21192 

21234 

21232 

21233 

21219 

21179 

21170 

21209 

21156 

21125 

G34-C3 G34-C13 G34-C10 G34-C6 G34 -C7 G34-C8 G34-C18 G34-C 

4 >Stk CO 4 >CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk COc 4>Gas Flow 4>NH3 Inj 4>MW Lo 

Stk co 

ppm 

0-1000 

3.0 

3.0 

3.1 

3.0 

3.0 

2.9 

3.0 

2.9 

2.7 

2.7 

2.9 

2.8 

3 . 0 

2.9 

3.1 

2.9 

2.6 

2.' 

2 . 5 

2.5 

2.' 

2.5 

2.2 

2.1 

2.0 

1.9 

2.0 

2.0 

2.0 

2.0 

1.9 

1.8 

1.8 

1.8 

1.7 

2.0 

2.0 

2.0 

2.0 

2.' 

CO Mass 

lb/hr 

0-100 

4.62 

4 .61 

4.61 

4.62 

4.62 

4.62 

4.63 

4.62 

3.71 

3.70 

4 .63 

4.62 

4.64 

4.62 

4 .63 

4.64 

3.73 

3.73 

3.73 

3.73 

3.73 

3.73 

3.73 

2.80 

2.80 

2.79 

2.80 

2.80 

2.81 

2.80 

2.80 

2.81 

2.81 

2.80 

2.80 

2 . 79 

2.79 

2.80 

2.79 

3.70 

NOx Rate 

Ib/mmBtu 

0-1 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.008 

0.007 

0.008 

0.007 

0.008 

0. 0 07 

0.007 

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 

0.008 

0.007 

0.008 

0.008 

0.007 

0.007 

stk NOXc 

ppm 

0-300 

2.00 

2.00 

2.00 

2.00 

2.00 

2.00 

2.07 

2.00 

2.07 

2.00 

2.07 

2.00 

2.00 

2.00 

2.00 

2.07 

2.07 

2.07 

2.07 

2.07 

2.07 

2.07 

2.07 

2.06 

2.06 

2.06 

2.06 

2.06 

2.13 

2.06 

2.06 

2.06 

2.06 

2.06 

2.06 

1. 99 

2.07 

2.14 

1. 99 

2.00 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

2.23 8796.0 

2.23 8784.6 

2.30 8776.2 

2.22 8797.8 

2.22 8794.8 

2.15 8799.6 

2.22 8809.8 

2.15 8806.2 

1.99 8834.4 

2.00 8815.8 

2.14 8827.2 

2.07 8800.8 

2.22 8832 . 0 

2.15 8805.6 

2.29 

2.14 

1. 92 

1. 77 

1. 85 

1. 84 

1. 77 

1. 84 

1. 62 

1. 54 

1. 47 

1.40 

1.47 

1.47 

1.47 

1.47 

1.40 

1. 32 

1. 32 

1. 33 

1.25 

1.48 

1.48 

1.48 

1.48 

1. 7 7 

88 21.2 

8839.2 

8869. 2 

8880.0 

8869.2 

8873. 4 

8887.8 

8881.8 

8888.4 

8892.0 

8878.2 

8871.6 

8880.0 

8876.4 

8904 . 6 

8904.0 

8892.0 

8909.4 

8908.8 

8898.0 

8892.0 

8864. 4 

8849.4 

8877.0 

8843.4 

8819.4 

NlBlnj 

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 

4>Summary - l-Min RATA - Continued 

MW Lo 

0 - 1 

106 . ~ 

106. : 

106 .: 

106. : 

106. : 

106. : 

105.: 

107 . t 

105 .. 

106. : 

105. : 

106. : 

105.1 

106 .. 

107. t 

106. : 

107. t 

106 . ~ 

106. : 

106. ~ 

108. t 

107 .: 

107. : 

106. : 

106 .. 

106. ! 

108. ( 

107. : 

107. : 

107. : 

107. ( 

106 . . 

1 07. : 

106 .. 

107.: 

105. : 

106 . . 

107 

106 

106.1 

Pag( 
Group#-Channel# G34-C2 G34-C4 G34-C11 G34 -C20 G34 -C3 G34-C13 G34-C10 G34-C6 G34 -C7 G34 -C8 G34-C1S G34-C 

Long Descrip. 4 >Stk NOx 4>Stk 02 4>NOx Mass 4>StkFlow 4 >Stk CO 4>CO Mass 4 >NOx Rate 4>Stk NOXc 4>Stk COc 4>Gas Flow 4 >NH3 Inj 4>MW La 

Short Descrip . Stk NOx Stk 02 NOx Mass StkFlo ..... Stk CO CO Mass NOx Rate Stk NOXc Stk COc Gas hscfh NH3Inj MW Lo 

Units ppm • lb/hr kscfh ppm lb/hr Ib/mmBtu ppm ppm hscfh 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 

02/11/2013 11:16 '.7 12.93 6.48 21141 '.7 3.70 0.007 2.00 2.00 8815.2 110.0 106. : 

02/11/2013 11:17 '.7 12.92 6.49 21139 '.6 3.71 0.007 2.00 1. 92 8825.4 110.0 106 .: 

02/11/2013 11:18 2.7 12.93 6.48 21143 '.6 3.70 0.007 2.00 1. 92 8S15.S 110 . 0 106. ! 

02/11/2013 11:19 2.8 12.91 7.43 21173 '.4 3.72 0.008 2.07 1. 77 8850.6 110.0 106.! 

Peri od Average ' . 7 12.92 6.94 21158 '.7 4.07 0.007 2.03 1. 99 8830.4 110 .0 106.4 

Period Max Value 2.9 12.97 7.48 21245 3.4 5.57 0.008 2.14 2.52 8909.4 110.0 108. 

Period Min Value '.6 12.87 6.42 21038 1.7 2.79 0.007 1. 93 1.25 8731.8 110.0 105. 

Period Totals = 2.0330E+2 9.5629E+2 5.1382E+2 1.5657E+6 1.9910E+2 3.0115E+2 5.S400E-l 1.5035E+2 1. 4729E+2 6.5344E+5 8.1400E+3 7.8748E+ 

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: 02/11/2013 11,47 4>Summary - l-Min RATA - Continued pag( 
Data Summary Report 

Company: CPV Sentinel, LLC 

62575 Powerline Road 

Desert Hot Springs, CA 92240 

Source : Turbine 4 

Data Group : 

5 Q.J\ \\oM-\ 

\ ~o'7t 

1..\ 

lOW\f y, W'lLt TRACE ~~ ~ 1.-

Environmental Systems, Inc. 

Report Name: 

start of Report : 

4>1-Min Cales 

4>Summary - I-Min RATA 

02/11/2013 11,40 End of Report , 02/11/2013 12,54 Validation : All Available Data 

Group#-Channel# 

Long Descrip. 

Short Descrip. 

units 

Range 

02/11/2013 11:40 

02/11/2013 11:41 

02/11/2013 11:42 

02/11/2013 11:43 

02/11/2013 11:44 

02/11/2013 11:45 

02/11/2013 11:46 

02/11/2013 11:47 

02/11/2013 11:48 

02/11/2013 11:49 

02/11/2013 11:50 

02/11/2013 11:51 

02/11/2 013 11:52 

02/11/2013 11:53 

02/11/2013 11:54 

02/11/2013 11:55 

02/11/2013 11:56 

02/11/2013 11:57 

02/1 1/2013 11:58 

02/11/2013 11:59 

02/11/2013 12:00 

02/11/2013 12:01 

02/11/2013 12:02 

02/11/2013 12:03 

02/11/2013 12:04 

02/11/2013 12:05 

02/11/2013 12:06 

02/11/2013 12:07 

02/11/2013 12:08 

02/11/2013 12:09 

Date/Time Printed: 

G34-C2 G34-C4 G34-Cl1 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

2.6 

3.6 

2.8 

2.7 

2.' 

2.3 

2.6 

2.8 

3.4 

3.1 

2.8 

2.8 

2.6 

2.7 

2.8 

2.8 

2.8 

2.8 

2.8 

3.2 

3.2 

2.7 

2.4 

2.7 

2.7 

2.7 

2 . 8 

2.7 

2.7 

2.7 

Stk 02 

t 

0-25 

12 .90 

12.90 

12.95 

12.93 

12.93 

12.92 

12.90 

12.91 

12.91 

12.94 

12.93 

12.91 

12.92 

12.90 

12.89 

12.90 

12.90 

12.89 

12.89 

12.90 

12.92 

12.91 

12.93 

12.91 

12 .91 

12.92 

12.90 

12.90 

12.92 

12.92 

02/11/2013 13,18 

NOx Mass 

1b/hr 

0-100 

6.51 

9.28 

7.38 

6.48 

6.48 

5.56 

6.52 

7.43 

8.36 

7.40 

7.41 

7.43 

6.49 

6.52 

7.46 

7.44 

7.45 

7.45 

7.46 

8.36 

8.34 

6.49 

6.48 

6.51 

6.51 

6.50 

7.46 

6.51 

6.49 

6.49 

GJ4-C20 

4>StkFlow 

StkFlow 

kscfh 

0-300000 

21156 

21119 

21119 

21134 

21150 

21151 

21189 

21169 

21163 

21160 

21145 

21148 

21163 

21202 

21182 

21169 

21185 

21164 

21182 

21136 

21140 

21134 

21154 

21190 

21193 

21175 

21207 

21168 

21163 

21163 

G34 - C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

3.0 

2.4 

0.3 

0.3 

0.5 

1.7 

3.2 

3.7 

3 . 3 

0.5 

0.4 

0.4 

0.9 

2.6 

3.2 

3.3 

3.2 

3.5 

3.4 

3.5 

0.5 

0.4 

0.7 

1.2 

1.7 

2.2 

2.1 

2.2 

2.3 

2.5 

G34-C13 G34-CIO G34-C6 

4>CO Mass 4>NOx Rate 4>Stk NOXc 

CO Mass 

1b/hr 

0-100 

4.65 

3.71 

0.00 

0.00 

0.93 

2.78 

4.66 

5.57 

4.64 

0.93 

0.93 

0.93 

0.93 

3.73 

4.66 

4.65 

4.66 

5.59 

5.59 

5.57 

0.93 

0.93 

0.93 

1.86 

2.79 

3.71 

2.80 

3.72 

3.71 

3.71 

NOx Rate 

Ib/mmBtu 

0-1 

0.007 

0.010 

0.008 

0.007 

0.007 

0.006 

0.007 

0.008 

0.009 

0.008 

0.008 

0.008 

0.007 

0.007 

0.008 

0 . 008 

0.008 

0.008 

0.008 

0.009 

0.009 

0.007 

0.007 

0.007 

0.007 

0.007 

0.008 

0.007 

0.007 

0.007 

Stk NOXc 

ppm 

0-300 

1.92 

2.66 

2.08 

2.00 

1.78 

1.70 

1.92 

2.07 

2.51 

2.30 

2.07 

2.07 

1. 92 

1. 99 

2.06 

2.07 

2.07 

2.06 

2.06 

2.36 

2.37 

1. 99 

1. 78 

1.99 

1. 99 

2.00 

2.07 

1. 99 

2.00 

2.00 

G34-C7 G34 -CB 

4>Stk CDc 4>Gas Flow 

Stk CDc Gas hscfh 

ppm hscfh 

0 - 1000 0- 10000 

2 . 21 

1. 77 

0.22 

0.22 

0.37 

1. 26 

2.36 

2.73 

2.44 

0.37 

0.30 

0.30 

0.67 

1. 92 

2.36 

2.43 

2.36 

2.58 

2.50 

2.58 

0.37 

0.30 

0.52 

0.89 

1.26 

1.63 

1. 55 

1. 62 

1. 70 

l. 85 

8854.8 

8839.2 

8784. a 

8812.2 

8818.8 

8830.2 

8868.6 

8848.8 

8846 . 4 

8812.2 

8817.0 

8840.4 

8835.6 

8874.0 

8876.4 

8860.2 

8866.8 

8869.2 

8876.4 

8846.4 

8826.0 

8834.4 

8820.6 

8857.8 

8859.0 

8840.4 

8875.8 

8859.6 

8835.6 

8835.6 

G34-CIB 

4>NlB 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. 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 

G34-C 

4>MW Lo 

MW Lo 

0-1 

106. ! 

106 .. 

106.1 

107.1 

105. ! 

105. : 

106. : 

106 .. 

106.1 

106. ! 

106.1 

106 .. 

105. : 

106. ! 

107.: 

106.1 

106. : 

106.! 

107.: 

106.1 

106. : 

106.: 

105 .. 

105 .. 

106. ! 

106. : 

106. : 

106. : 

106.: 

106.: 

pagt 
Group#-Channel# 

Long Des crip. 

Short Descrip . 

Units 

Range 

02/11/2013 12:10 

02/11/2013 12:11 

02/11/2013 12:12 

02/11/2013 12:13 

02/11/2013 12:14 

02/11/2013 12:15 

02/11/2013 12:16 

02/11/2013 12:17 

02/11/2013 12:18 

02/11/2013 12:19 

02/11/2013 12:20 

02/11/2013 12:21 

02/11/2013 12:22 

02/11/2013 12:23 

02/11/2013 12:24 

02/11/2013 12:25 

02/11/2013 12:26 

02/11/2013 12:27 

02/11/2013 12:28 

02/11/2013 12:29 

02/11/2013 12:30 

02/11/2013 12:31 

02/11/ 2 013 12:32 

02i11/2013 12:33 

02/11/2013 12:34 

02/11/2013 12:35 

02/11/2013 12:36 

02/11/2013 12:37 

02/11/2013 12:38 

02/11/2013 12:39 

02/11/2013 12:40 

02/11/2013 12:41 

02/11/2013 12:42 

02/11/2013 12:43 

02/11/2013 12:44 

02/11/2013 12:45 

02/11/2013 12:46 

02/11/2013 12:47 

02/11/2013 12:48 

02/11/2013 12:49 

Date/Time Printed: 

G34-C2 G34-C4 G34-C11 G34 -C20 

4>Stk NOx 

Stk NOx 

4>Stk 02 4>NOx Mass 4>StkFlow 

ppm 

0-150 

2.7 

2.6 

2.8 

2.7 

2.6 

2.6 

2.6 

2.6 

2.7 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.7 

2.7 

2.7 

2.7 

2.6 

2.7 

2.6 

2.7 

2.7 

2.7 

2.6 

2.7 

2.7 

2.6 

2.7 

2.6 

2.6 

2.6 

2.7 

2.6 

2.6 

2.7 

2.7 

2.7 

2.7 

Stk 02 

• 

0-25 

12.93 

12.92 

12.91 

12.91 

12.92 

12.92 

12.91 

12.90 

12.89 

12.89 

12.88 

12.87 

12.88 

12.89 

12.88 

12.88 

12.89 

12.90 

12 . 91 

12.90 

12.89 

12.91 

12.90 

12.90 

12.90 

12.91 

12.89 

12.89 

12.89 

12.88 

12 . 88 

12.87 

12.88 

12.88 

12.87 

12.88 

12.88 

12.88 

12.87 

12 . 88 

02/11/2013 13,18 

NOx Mass 

lb/hr 

0-100 

6.48 

0.00 M 

7.42 

6.49 

6.48 

6.48 

6.50 

6.49 

6.51 

7.45 

7 . 46 

7.46 

7.46 

7.45 

7.44 

6.52 

6.51 

0 . 00 M 

6 . 51 

6.52 

6.52 

6.50 

6.51 

6.51 

6.51 

6.50 

6.5 1 

6.52 

6.52 

6 . 52 

6 . 52 

6.52 

6.51 

6.52 

6.53 

6.52 

6.53 

6.52 

6.53 

6.52 

StkFlow 

ksefh 

0-300000 

21140 

21079 

21121 

21121 

21100 

21113 

21144 

21112 

21131 

21157 

21159 

21153 

21165 

21170 

21119 

21157 

21144 

21191 

2 1200 

21192 

21169 

21147 

2 1168 

21168 

21146 

21143 

21144 

21164 

21172 

21152 

21157 

21129 

21117 

21147 

21136 

21134 

21159 

21152 

21159 

21151 

G34-C3 G34-C13 G34-C10 G34-C6 G34-C7 G34 -C8 G34 - C18 G34-C 

4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXe 4>Stk COe 4>Gas Flow 4>NH3 Inj 4>MW Lo 

Stk co 

ppm 

0-1000 

2.3 

2.3 

2.1 

1.7 

1.6 

1.5 

1.6 

1.8 

2.0 

1.9 

2.0 

1.8 

1.7 

1.7 

1.8 

2.2 

2. 5 

2.7 

2.8 

3.0 

3.0 

3.3 

3.1 

2.9 

3.2 

3.3 

3.2 

2.9 

2.8 

2.7 

2.7 

2.9 

3.2 

3.2 

3.2 

3.2 

3.1 

3.0 

2.9 

3.0 

CO Mass 

lb/hr 

0-100 

3.70 

0.00 M 

2.78 

2.78 

2.78 

1. 8S 

2.78 

2.78 

2.79 

2.79 

2.80 

2.80 

2.80 

2.79 

2.79 

3.73 

3.72 

0.00 M 

4.65 

4.66 

4.66 

4.64 

4.65 

4.65 

4.65 

4.64 

4.65 

4.66 

4.66 

3.73 

3.73 

4.66 

4.65 

4.66 

4.66 

4.66 

4.66 

4.66 

4.67 

4.66 

NOx Rate 

Ib/mmBtu 

0-1 

0.007 

0.007 

0.008 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0 .008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

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 

2.00 

1. 92 

2.07 

1. 99 

1. 92 

1. 92 

1. 92 

1. 92 

1. 99 

2.06 

2.06 

2.06 

2.06 

2.06 

2.06 

l. 99 

1.99 

1. 99 

1. 99 

1. 92 

l. 99 

1. 92 

1. 99 

1. 99 

1. 99 

1. 92 

1. 99 

1. 99 

1. 92 

1. 99 

1. 91 

1. 91 

1. 91 

1. 99 

1. 91 

1. 91 

1. 99 

1. 99 

1. 98 

1. 99 

Stk Cae Gas hsefh 

hscfh 

0-10000 

ppm 

0-1000 

1. 70 

1. 70 

1. 55 

1. 26 

1.18 

1.11 

1.18 

1. 33 

1. 47 

1.40 

1. 47 

1.32 

1.25 

1.25 

1. 32 

1. 62 

1. 84 

1. 99 

2.07 

2.21 

2.21 

2.44 

2.29 

2.14 

2.36 

2.44 

2.36 

2.14 

2.06 

1. 99 

1. 99 

2.13 

2.35 

2.35 

2.35 

2.35 

2.28 

2.21 

2.13 

2.21 

8814.6 

8800 . 2 

8829.0 

8829.0 

8809.2 

8814.6 

8838.G 

8836.2 

8855.4 

8866.2 

8878.2 

8886.G 

8880.6 

8871.6 

8861.4 

8877.0 

8860.8 

8869.2 

8862.0 

8869.8 

8871.0 

8839.8 

8859.6 

8859.6 

8850.6 

8838.0 

8860 .8 

8869.2 

8872.2 

8875.2 

8877.0 

8876 . 4 

8860.2 

8872.8 

8879.4 

8867.4 

8878.2 

8875.2 

8889.0 

8874.6 

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 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110 . 0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

4>Summary - I - Min RATA - Continued 

MW La 

0-1 

105 .. 

IDS.! 

106.! 

106. : 

106.! 

106. : 

106. : 

106. : 

107.: 

106 .. 

107.1 

107.1 

107. 

107 

1 06 .. 

106. : 

106. ! 

107 .. 

107. ( 

107. ! 

107 .. 

lOG .: 

106.l 

106.! 

106. l 

106.: 

106 .. 

107.: 

106 . : 

106.: 

107. : 

107. : 

106. ! 

107.1 

106. : 

106. ! 

106 .. 

107. : 

107. ! 

106 .. 

Pagt 
Group#-Channel# G34-C2 G34-C4 G34-Cll G34-C20 G34-C3 GJ4-C13 G34 -CIO G34 -C6 G34-C7 G34-C8 G34 -C18 G34-C 

Long Descri p . 4>Stk NOx 4>Stk 02 4 :>NOx Mass 4>StkFlow 4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk CDc 4>Gas Flow 4>NH3 Inj 4>MW La 

Short Descri p. 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 1b/hr Ib/mmBtu ppm ppm hscfh 1b/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 

02/11/2013 12:50 2.7 12.88 6.53 21161 2.9 4.66 0.007 1. 99 2.13 8878.8 110.0 106 .. 

02/11/2013 12:51 2.7 12.87 6.51 21093 2.8 4.65 0.007 1. 98 2.06 8861.4 110.0 107. c 

02/11/2013 12:52 2.7 12.88 6.52 21134 2.8 4.66 0.007 1. 99 2.06 8867.4 110 . 0 107 .. 

02/11/2013 12:53 2.7 12.87 6.53 21133 2.8 4 .66 0.007 1. 98 2.06 8878.2 110.0 107. : 

02/11/2013 12;54 2.7 12.87 6.52 21113 2.8 4.66 0.007 1. 98 2.06 BB69.8 110.0 106. : 

Period Average 2.7 12.90 6.66 21152 2.3 3.47 0.007 2.01 1.72 8853.B 110.0 106.6 

Pe riod Max Value 3.6 12.95 9.28 21207 3.7 5.59 0.010 2.66 2.73 8889.0 110 . 0 107. 

Period Min Value 2.3 12.87 0.00 21079 0.3 0.00 0.006 1. 70 0.22 8784.0 110.0 105. 

Period Totals = 2.0450E+2 9.6744E+2 4.9923E+2 1.5863E+6 1.7500E+2 2.6052E+2 5.5100E-l 1.5084E+2 1.2901E+2 6.6403E+5 8.2500E+3 7.9957E+ 

Period % Recovery 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 1 00.0 100.0 100.0 100. 

Date/Time Printed: 02/11/2013 13,18 4~Summary - I-Min RATA - Continued Pag~ 
Appendix B.1.3 Sentinel Unit 4 PM Testing 

R041 0688 8-5 
Data Summary Report 

Company: CPV Sentinel, LLC 

62575 Powerline Road ~ 1\o1J.. \ L{ 

Desert Hot Springs, CA 92240 fM Source: Turbine 4 

Data Group: 4>!-Min Cales 

Report Name: 

Start of Report : 

4>Summary - I-Min RATA 

02/11/2013 08,41 

G34-C4 

100'\ 

End of Report , 02/11/2013 12,55 

G34 -ell G34 -C13 

TRACE 

Ellvirnnmental Systems, Illc. 

validation : All Available Data 

Group#-Channel# G34 -CIO G34-C6 G34-C7 G34 -CB 

Long Descrip. 

Short Descrip. 

Units 

G34-C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

G34-C20 

4>StkF!ow 

StkFlow 

kscfh 

0 -3 00000 

G34-C3 

4>Stk CO 

Stk CO 

4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk CDc 4>Gas Flow 

Stk CDc Gas hscfh 

G34 -CIB 

4>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

G34-C 

4>MW Lo 

MW La 

Range 

02/11/2013 08:41 

02/11 /2013 08:42 

02/11/ 20 13 08: 4 3 

02/11/2013 08:44 

02/11/2013 08:45 

02/11/2013 08:46 

02/11/2013 08:47 

02/11 /2013 08:48 

02/11/2013 08:49 

02/11/2013 08:50 

02/11/ 2013 08:51 

02/11/2013 08:52 

02/11/2013 08:53 

02/11/2013 08:54 

02/11/2013 08:55 

0 2/11/2013 08:56 

02/11/20 13 08:57 

02/11/2013 08:58 

02/11/2013 08:59 

02/11/2013 09:00 

02/11/2013 09:01 

02/11/2013 09:02 

02/1 1 /2013 09:03 

02/11/ 2 013 09:04 

02/11/2013 09:05 

02/11/2013 09:06 

02/11/2013 09:07 

02/11/2013 09:08 

02/11/2013 09:09 

02/11/2013 09:10 

Date/Time Printed: 

3.0 

2.9 

3.0 

3.1 

3.1 

2.9 

3.0 

2.9 

3.1 

3.0 

3.6 

3.0 

2.7 

2.9 

2.9 

2.9 

2.9 

3.0 

2.9 

3.0 

3.0 

2.9 

2.9 

3.0 

3.0 

2.9 

3.0 

3.0 

2.9 

2.9 

Stk 02 

% 

0-25 

12.88 

12.88 

12. 88 

12.88 

12.88 

12.87 

12.87 

12.87 

12.87 

12.87 

12.89 

12.89 

12.89 

12.88 

12.91 

12.91 

12.91 

12.89 

12.90 

12.90 

12 .89 

12.90 

12.91 

12 .89 

12.88 

12.88 

12.88 

12 .88 

12.88 

12.88 

02/11/2013 16,39 

NOx Mass 

1b/hr 

0-100 

7.52 

7.51 

7.51 

7.52 

7.51 

7.51 

7.52 

7.51 

7.52 

7.51 

9 . 36 

7. 4 8 

6.55 

7.48 

7.45 

7.43 

7.44 

7.46 

7.46 

7.45 

7.47 

7.44 

7.43 

7.45 

7.47 

7.45 

7.46 

7.45 

7.46 

7.47 

21324 

21300 

21301 

21332 

21302 

21294 

21307 

21284 

21297 

21274 

21276 

21259 

21267 

21220 

21225 

21163 

2 1193 

21186 

21231 

21197 

21212 

21172 

21150 

21164 

21185 

21145 

21172 

2 1129 

21159 

21191 

ppm 

0-1000 

1.8 

2.0 

2.1 

2.1 

1.9 

2.1 

2.' 

2.7 

2.6 

2.5 

1.6 

0.3 

0.6 

1.3 

1.8 

1.7 

1.7 

1.5 

1.7 

1.6 

1.8 

1.7 

2.0 

2.1 

2.2 

2.2 

2.3 

2.2 

2 .3 

2.3 

CO Mass 

Ib/hr 

0-100 

2.82 

2.82 

2.82 

2.82 

2.82 

2.82 

3.76 

3.76 

3.76 

3.75 

2.81 

0 .0 0 

0.94 

1. 87 

2.79 

2.79 

2.79 

1. 86 

2.80 

2.79 

2.80 

2.79 

2.78 

2.79 

3.73 

3.73 

3.73 

3.72 

3.73 

3.73 

NOx Rate 

Ib/mmBtu 

0-1 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.010 

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 

Stk NOXc 

ppm 

0-300 

2.21 

2.13 

2 .21 

2.28 

2.28 

2.13 

2.20 

2.13 

2.28 

2.20 

2 .65 

2.21 

1. 99 

2.13 

2.14 

2.14 

2.14 

2.21 

2.14 

2.21 

2.21 

2.14 

2.14 

2.21 

2.21 

2.13 

2.21 

2.21 

2.13 

2.13 

ppm hscfh 

0-1000 0-10000 

1. 32 

1.47 

1. 54 

1. 54 

1.40 

1. 54 

1. 76 

1. 98 

1. 91 

1. 84 

1.18 

0.22 

0.44 

0.96 

1. 33 

1.26 

1.26 

1.10 

1. 25 

1.18 

1.33 

1.25 

1.48 

1. 55 

1. 62 

1. 62 

1. 69 

1. 62 

1. 69 

1. 69 

8947.2 

8937.0 

8937.6 

8950.8 

8938.2 

8 946.0 

8951.4 

8941. 8 

894 7.2 

8937.6 

8916.0 

8908.8 

8912.4 

8903.4 

8872.2 

8846.4 

8859.0 

8878.2 

8886.0 

8871.6 

8889.0 

8861 .4 

8841.0 

8869.2 

8889.0 

8872.2 

8883.6 

8865.6 

8878.2 

8891.4 

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 

0-1 

107. ; 

109.: 

107. ; 

107. ; 

107. 

108.! 

107. : 

107. : 

107. : 

108. « 

107. c 

107 .. 

1 0 7. 

107 . . 

106. 

106. ! 

107. « 

107 .. 

107. : 

106 . . 

107.: 

107. : 

107. : 

107. c 

107.! 

108. « 

106. 

106. : 

107. : 

107. ! 

PagE 
Group#-Channel# 

Long Descrip . 

Short Descrip . 

Units 

Range 

02/11 /2013 09:11 

02/11/2013 09:12 

02/11/2013 09:13 

02/11/2013 09:14 

02/11/2013 09:15 

02/11/2013 09:16 

02/11/2013 09:17 

02/11/20 13 09:18 

02/11/2013 09:19 

02/11/2013 09:20 

02/11/2013 09:21 

02/11/2013 09:22 

02/11/2013 09:23 

02/11/2013 09:24 

02/11/2 013 09:25 

02/11/2013 09:26 

02/11/20 1 3 09:27 

02/11/2013 09:28 

02/11/2013 09:29 

02/11/2013 09:30 

02/11/2013 09:31 

02/11/2013 09:32 

02/11/2013 09:33 

02/11/2013 09:34 

02/11/2013 09:35 

02/11/2013 09:36 

02/11/2013 09:37 

02/11/2013 09:38 

02/11/2013 09:39 

02/11/ 2013 09:40 

02 /11 /2 013 09:41 

02/11/2013 09:42 

02/11/2013 09:43 

02/11/2013 09:44 

02/11/2013 09:45 

02/11/2 013 09:46 

02/11/ 2013 09:47 

02/11/ 2013 09:48 

02/11/2013 09:49 

02/11/2013 09:50 

Date/Time Printed: 

G34-C2 G34 - C4 G34 -C11 G34-C20 

4>Stk NOx 

Stk NOx 

ppm 

0 - 150 

4>Stk 02 4>NOx Mass 4>StkFlow 

3.0 

2.8 

2.9 

2.9 

2.8 

2.9 

2.9 

2.8 

2.9 

2.9 

2.9 

2 . 9 

2.9 

2.9 

3.0 

2.8 

3.0 

2.9 

2.8 

2.9 

3.0 

2.9 

3.0 

2.9 

2.8 

2.8 

2.9 

2.9 

3.0 

2.8 

2.9 

3.0 

3.0 

2.8 

2.9 

2.9 

2.9 

3.0 

2.9 

2.9 

Stk 02 

% 

0-25 

1 2.8 7 

12 . 91 

12.92 

12.92 

12.93 

12.90 

12.B9 

12 . 91 

12.90 

12.91 

12.90 

12.92 

12.91 

12.91 

12 . 8 8 

12 .90 

12 . 89 

12 . 89 

12.91 

12.91 

12.91 

12.91 

12. 90 

1 2 .90 

12 . 91 

12.90 

12.89 

12.91 

12 . 89 

12 . 91 

12 .90 

12 .90 

12.91 

12.91 

12.91 

12.92 

12 . 92 

12 .93 

1 2. 92 

12.94 

02/11/2013 16,39 

NOx Mass 

lb/hr 

0-100 

7.48 

7.42 

7.40 

7.43 

7.40 

7.45 

7.43 

7.41 

7.42 

7.42 

7.42 

7.39 

7.40 

7.40 

7.42 

7.40 

7.42 

7.42 

7.40 

7.40 

7.41 

7.42 

7.44 

7.43 

7.40 

7.42 

7.42 

7.41 

7.43 

7.40 

7.41 

7.40 

7.39 

7.39 

7.39 

7.38 

7.39 

7.39 

7.40 

7.38 

StkFlow 

kscfh 

0-300000 

2 1190 

21121 

21113 

21185 

21115 

21181 

21119 

21105 

2 1118 

21127 

21099 

21073 

21081 

21071 

2 1061 

2 1058 

21091 

21078 

21081 

21075 

21103 

21128 

21149 

21142 

21084 

21112 

21090 

21111 

21120 

21074 

2 1070 

21050 

21045 

21054 

21038 

21053 

21063 

21091 

2 1096 

21096 

G34-C3 G34-C13 G34-C10 G34-C6 G34 -C7 G34-C8 G34-C18 G34-C 

4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk COc 4>Gas Flow 4>NH3 Inj 4>MW La 

Stk CO 

ppm 

0 - 1000 

2.3 

2.7 

3.1 

2.9 

3.3 

3.3 

2 .• 

3.0 

2.9 

3.0 

2 .• 

2.9 

2.9 

2 .• 

2.6 

2 .• 

2.7 

2.5 

2 .• 

3.0 

2.9 

2.6 

2.7 

2.7 

2.9 

3.1 

3.0 

2.7 

2 .• 

2.7 

2.9 

2.5 

1.9 

2.1 

2.5 

2.1 

1.9 

1.. 

1.6 

1.3 

CO Mass 

lb/hr 

0-100 

3.74 

3.71 

4.63 

4.64 

4.62 

4.65 

4.65 

4.63 

4.64 

4.64 

4.64 

4.62 

4.63 

4.62 

3 . 71 

4 .63 

3.71 

3.71 

4.63 

4.63 

4.63 

3.71 

3.72 

3 . 72 

4.63 

4.64 

4.64 

3.71 

4.65 

3.70 

4.63 

3.70 

2.77 

2.77 

3.69 

2.77 

2.77 

2.77 

2.77 

1. 84 

NOx Rate 

lb/mmBtu 

0-1 

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 

0.008 

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 

O.OOB 

0.008 

0.008 

O.OOB 

0.008 

0.008 

0.008 

0.008 

0 . 00 8 

0 . 008 

Stk NOXc 

ppm 

0-300 

2.20 

2.07 

2.14 

2.14 

2.07 

2.14 

2.14 

2.07 

2.14 

2.14 

2.14 

2.14 

2.14 

2.14 

2.2 1 

2.07 

2.21 

2.14 

2.07 

2.14 

2.22 

2.14 

2.21 

2.14 

2.07 

2.07 

2.14 

2.14 

2.21 

2.07 

2 . 1 4 

2.21 

2.22 

2.07 

2.14 

2.14 

2.14 

2.22 

2.14 

2.15 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0 - 10000 

1 . 69 8902.2 

1.99 8829.0 

2.29 8814.6 

2.14 8844.6 

2.44 

2.43 

2.06 

2. 22 

2.14 

2.22 

2.07 

2.14 

2.14 

2 . 07 

1. 91 

2.07 

1. 99 

1. 84 

2.07 

2.22 

2.14 

1. 92 

1. 99 

1. 99 

2.14 

2 . 29 

2.21 

1. 99 

2.06 

1. 99 

2 . 14 

1. 8 4 

1.40 

1. 55 

1. 85 

1. 55 

1. 40 

1.33 

1. 18 

0 . 96 

8804.4 

8865.0 

8850.0 

8822. 4 

8838.6 

8831. 4 

8830.8 

8797.8 

8812.2 

8808.0 

8836.8 

8813.4 

8838.6 

8833.2 

8812.2 

8809.8 

8821.2 

8832.0 

8851.8 

8848.8 

8813.4 

8836.2 

8838.0 

8824.8 

8850.6 

8809.2 

8818.8 

8810.4 

8797.2 

8800.8 

8794.2 

8789.4 

8793.6 

8 794.2 

8807.4 

8785.2 

NH3Inj 

lb/hr 

0-200 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

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 

1 1 0.0 

110.0 

110 . 0 

4>Summary - I-Min RATA - Continued 

MW Lo 

0-1 

107. : 

106. ~ 

106. ! 

106. : 

106. 

106 .. 

106. : 

106 . 

106. 

106.! 

106 . . 

105 .. 

105 . 

106. ! 

106 . : 

106 . 

106 .. 

106. ! 

106 .. 

105. : 

106. ! 

107.1 

106.: 

106 .. 

106 .. 

107.1 

105. ! 

106 . . 

106. 

106.: 

105 .. 

106 . . 

lOS.! 

106. : 

106.! 

105 .. 

106.: 

106.1 

106. 1 

106. ! 

PagE 
Group#-Channe l# 

Long Descrip . 

Short Descrip . 

Units 

Range 

02/11/2013 09:51 

02/11/2013 09:52 

02/11/2013 09:53 

02/11/2013 09:54 

02/11/2013 09:55 

02/11/2013 09:56 

02/11/2013 09:57 

02/11/2013 09:58 

02/11/2013 09:59 

02/11/2013 10:00 

02/11/2013 10:01 

02/11/2013 10:02 

02/11/2013 10:03 

02/11/2013 10:04 

02/11/2013 10:05 

02/11/2013 10:06 

02/11/2013 10:07 

02/11/2013 10:08 

02/11/2013 10:09 

02/11 /2013 10:10 

02/11/2013 10:11 

02/11/2013 10:12 

02/11/2013 10:13 

02/11/2013 10:14 

02/11/2013 10:15 

02/11/2013 10:16 

02/11/2013 10:17 

02/11/2013 10:18 

02/11/2013 10:19 

02/11/2013 10:20 

02/11/2013 10:21 

02/11/2013 10:22 

02/11/2013 10:23 

02/11/2013 10:24 

02/11/2013 10:25 

02/11/2013 10:26 

02/11/2013 10:27 

02/11/2013 10:28 

02/11/2013 10:29 

02/11/2013 10:30 

Date/Time Printed: 

G34-C2 G34-C4 G34-Cll 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

2.8 

3.0 

2.9 

3.0 

2.9 

2.8 

2.8 

2.8 

2.8 

2.8 

2.9 

2.7 

2.7 

2.8 

2.8 

2.8 

2.7 

2.8 

2.7 

2.8 

2.9 

2.7 

2.7 

2.9 

2.8 

2.7 

2.8 

2.7 

2.7 

2.7 

2.6 

2.7 

2.8 

2.7 

2.6 

2.7 

2.7 

2.6 

2.7 

2.7 

Stk 02 

, 

0-25 

12.92 

12.91 

12.91 

12.90 

12.91 

12.91 

12.91 

12.91 

12.91 

12.92 

12.91 

12.93 

12.94 

12.93 

12.93 

12.91 

12.93 

12.93 

12.93 

12.93 

12.92 

12.94 

12.94 

12.92 

12.91 

12.95 

12.94 

12.93 

12.94 

12.95 

12.95 

12.95 

12 . 93 

12.94 

12.96 

12.94 

12.95 

12.97 

12.96 

12.95 

02/11/2013 16,39 

NOx Mass 

lb/hr 

0 - 100 

7.40 

7.42 

7.41 

7.44 

7.42 

7.44 

7.43 

7.43 

7.42 

7.42 

7.42 

6.49 

6.47 

7.42 

7.43 

7.44 

6.50 

7.44 

6.50 

7.43 

7.45 

6.49 

6.48 

7.44 

7.44 

6.47 

7.42 

6.48 

6.46 

6.46 

6.45 

6.45 

7.40 

6.45 

6.44 

6.45 

6.43 

6.42 

6.44 

6.45 

G34-C20 

4>StkFlow 

StkFlow 

ksefh 

0-300000 

21089 

21123 

21113 

21155 

21137 

21193 

21170 

21170 

21118 

21145 

21131 

21161 

21133 

21194 

21223 

21186 

21210 

21236 

21213 

21223 

21245 

21198 

21175 

21201 

21186 

21152 

21209 

21135 

21101 

21124 

21093 

21092 

21118 

21084 

21092 

21074 

21038 

21047 

21092 

21092 

G34 -C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

1.4 

1.7 

1.5 

1.2 

1.3 

1.1 

1.2 

1.1 

1.3 

1.5 

1.6 

1.8 

2.7 

2.9 

2.8 

2.8 

3.1 

3.2 

3.4 

3.1 

3.1 

3.0 

3.1 

2.8 

2.8 

2.8 

2.9 

2.8 

3.2 

3.2 

3.2 

3.2 

2.7 

2.9 

3.1 

3. 1 

3.0 

3.3 

3.3 

3.0 

G34 -C13 G34-C10 G34 -C6 

4>CO Mass 4>NOx Rate 4>Stk NOXe 

CO Mass 

lb/hr 

0 - 100 

1. 85 

2.78 

1. 85 

1. 86 

1. 86 

1. 86 

1. 86 

1. 86 

1. 85 

1. 85 

2.78 

2.78 

3.70 

4.64 

4.6 5 

4.65 

4.64 

4.65 

5.57 

4.65 

4.66 

4.63 

4.63 

4.65 

4.65 

4.62 

4.64 

4.63 

4.61 

4.61 

4.61 

4.61 

3.70 

4.61 

4.60 

4.61 

4.59 

5.50 

4.60 

4.61 

NOx Rate 

lb/mmBtu 

0-1 

0.008 

0.008 

0 . 008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.007 

0.007 

0.008 

0.008 

0.008 

0.007 

0.008 

0.007 

0.008 

0.008 

0.007 

0.007 

0.008 

0.008 

0.007 

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 

Stk NOXe 

ppm 

0 - 300 

2.07 

2.22 

2.14 

2.21 

2.14 

2.07 

2.07 

2.07 

2.07 

2.07 

2.14 

2.00 

2.00 

2.07 

2.07 

2.07 

2.00 

2.07 

2.00 

2.07 

2.14 

2.00 

2.00 

2.14 

2.07 

2.00 

2.08 

2.00 

2.00 

2.00 

1. 93 

2.00 

2.07 

2.00 

1. 93 

2.00 

2.00 

1. 93 

2.01 

2.00 

G34 -C7 G34-C8 

4>Stk COe 4>Gas Flow 

Stk COe Gas hsefh 

ppm hscfh 

0-1000 0 - 10000 

1. 04 

1. 26 

1.11 

0.89 

0.96 

0.81 

0.89 

0.81 

0.96 

1.11 

1.18 

1. 33 

2.00 

2.15 

2.07 

2.07 

2.29 

2.37 

2.52 

2.29 

2.29 

2.22 

2.30 

2.07 

2.07 

2.08 

2.15 

2.07 

2.37 

2.37 

2 . 37 

2.37 

2.00 

2.15 

2.30 

2.30 

2.23 

2.46 

2.45 

2.23 

8804.4 

8829.6 

8825.4 

8854.2 

8835.6 

8859.0 

8849.4 

8849 . 4 

8827.8 

8827.8 

8833.2 

8823.6 

8800.8 

8837.4 

8849.4 

8856.0 

8844.0 

8854.8 

8845.2 

8849.4 

8869.8 

8827.8 

8818.2 

8851.2 

8856.0 

8797.8 

8832.6 

8812.8 

8787.6 

8785.8 

8773.2 

8772.6 

8805.6 

8780.4 

8761.8 

8776.2 

8750.4 

8731.8 

8761.8 

8772.6 

G34 -C18 

4>NH3 Inj 

NH3Inj 

lb/hr 

0-200 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

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 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

4>Summary - I-Min RATA - continued 

G34 - C 

4>MW Lo 

MW La 

0-1 

105 .. 

106.1 

105. : 

107. : 

107. t 

107. t 

106 . . 

106. ! 

106. ! 

106 .. 

106. 

105 

105. : 

106. 

106. 

107. t 

107.1 

106. 

106.1 

106. : 

106. t 

106 .. 

106 .. 

107. : 

106. : 

106 

106. 

106 .. 

106. t 

106. : 

105. : 

105 .. 

106. ' 

105. : 

106. : 

106. ( 

105. 

105. : 

lOS. : 

106. : 

Pagt 
Group#-Channel# 

Lo ng Descrip. 

Short Descrip. 

Units 

Range 

02/11/2013 10:31 

02/11/2013 10:32 

02/11/2013 10:33 

02/11/2013 10:34 

02/11/2013 10:35 

02/11/ 2 013 10:36 

02/11/2013 10:37 

02/11/2013 10:38 

02/11/2013 10:39 

02/11/2013 10:40 

02/11/2013 10:41 

02/11/2013 10:42 

02/11/2013 10:43 

02/11/2013 10:44 

02/11/2013 10:45 

02/11/2013 10:46 

02/11/2013 10:47 

02/11/2013 10:48 

02/11/2013 10:49 

02/11/2013 10:50 

02/11/2013 10:51 

02/11/2013 10:52 

02/11/2013 10:53 

02/11/2013 10:54 

02/11/2013 10:55 

02/11/2013 10:56 

02/11/2013 10:57 

02/11/2013 10:58 

02/11/2013 10:59 

02/11/2013 11:00 

02/11/2013 11:01 

02/11/2013 11: 02 

02/11/2013 11:03 

02/11/2013 11:04 

02/11/2013 11:05 

02/11/2013 11:06 

02/11/2013 11:07 

02/11/2013 11.08 

02/11/2013 11:09 

02/11/2013 11:10 

Date/Time Printed: 

G34-C2 G34-C4 G34 -Cll G34-C20 

4>Stk NOx 

Stk NOx 

ppm 

0 - 150 

4 >Stk 02 4 >NOx Mass 4 >StkFlow 

2.7 

2.7 

2.6 

2.7 

2.6 

2.7 

2.7 

2.7 

2.7 

2.7 

2.7 

2.8 

2.7 

2 .8 

2.7 

2.8 

2.7 

2.7 

2.7 

2.7 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

2.9 

2.8 

2.8 

2.8 

2.8 

2.8 

2.8 

Stk 02 

% 

0-25 

12.95 

12.96 

12.97 

12.96 

12.97 

12 .95 

12 .95 

12.95 

12 . 94 

12.94 

12 .94 

12.93 

12.93 

12.91 

12.92 

12.92 

12.93 

12.93 

12.94 

12.93 

12. 92 

12 . 91 

12.90 

12.91 

12.90 

12.90 

12 .90 

12.90 

12.88 

12.89 

12.89 

12.88 

12 . 89 

12.87 

12 .87 

12 .88 

12.88 

12 .88 

12.89 

12.89 

02/11/2013 16,39 

NOx Mass 

lb/hr 

0-100 

6.44 

6.45 

6.43 

6.44 

6.44 

6.47 

6.46 

6.45 

6.47 

6.46 

6.47 

7.40 

6.47 

7.42 

6.48 

7.42 

6 .47 

6.49 

6.47 

6.48 

7.42 

7.45 

7.46 

7.45 

7.45 

7.47 

7.46 

7.47 

7.47 

7.46 

7.45 

7.46 

7.46 

7.48 

7.48 

7.47 

7. 48 

7.48 

7.47 

7.47 

StkFlow 

ksefh 

0-300000 

21079 

21134 

21086 

21097 

21106 

21148 

21121 

21101 

21126 

21119 

21130 

21128 

21120 

21134 

21 1 16 

21143 

21107 

21181 

21145 

21155 

21172 

21217 

21217 

21217 

21201 

21235 

21221 

21237 

21192 

21186 

21170 

21164 

21182 

21196 

21195 

21192 

21234 

21232 

21233 

21219 

G34-C3 G34-C13 G34 - CI0 G34-C6 G3 4 -C7 G34-C8 G34-C18 G34-C 

4>Stk CO 4>CO Mass 4 >NOx Rate 4>Stk NOXe 4>Stk COe 4>Gas Flow 4>NH3 Inj 4>MW La 

Stk CO 

ppm 

0-1000 

2.9 

3.0 

3.0 

3.2 

3.2 

3.0 

3.0 

3.1 

3.0 

3.0 

2.9 

3.0 

2.9 

2.7 

2.7 

2.9 

2.8 

3.0 

2.9 

3.1 

2.9 

2.6 

2.' 

2.5 

2.5 

2.4 

2.5 

2.2 

2.1 

2.0 

1.9 

2.0 

2.0 

2.0 

2.0 

1.9 

1.8 

1.8 

1.8 

1.7 

CO Mass 

Ib/hr 

0-100 

4.60 

4.61 

4.59 

4.60 

4 . 60 

4.62 

4.61 

4.61 

4.62 

4.62 

4.62 

4.63 

4.62 

3.71 

3.70 

4.63 

4.62 

4.64 

4.62 

4.63 

4.64 

3.73 

3.73 

3.73 

3.73 

3. 7 3 

3.73 

3.73 

2.80 

2.80 

2.79 

2.80 

2.80 

2.81 

2.80 

2.80 

2.81 

2.81 

2.80 

2.80 

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 

0.007 

0.008 

0.007 

0.008 

0.007 

0.007 

0.007 

0.007 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

O.OOB 

O.OOB 

0.008 

O.OOB 

0.008 

O.OOB 

0 . 008 

O.OOB 

O.OOB 

0 . 008 

0.008 

Stk NOXe 

ppm 

0-300 

2.00 

2.01 

1. 93 

2.01 

1. 93 

2.00 

2.00 

2.00 

2.00 

2.00 

2.00 

2.07 

2.00 

2.07 

2.00 

2.07 

2.00 

2.00 

2.00 

2.00 

2.07 

2.07 

2.07 

2.07 

2.07 

2.07 

2.07 

2.07 

2.06 

2.06 

2.06 

2.06 

2.06 

2.13 

2.06 

2.06 

2.06 

2.0 6 

2.06 

2 .06 

Stk COe Gas 

ppm 

0-1000 

hsefh 

hsefh 

0 - 10000 

2.15 

2.23 

2 . 23 

2 . 38 

2.38 

2.23 

2.23 

2.30 

2.22 

2.22 

2.15 

2.22 

2.15 

1. 99 

2.00 

2.14 

2.07 

2.22 

2.15 

2.29 

2.14 

1. 92 

1. 77 

1. 85 

1. 84 

1. 77 

1. 8 4 

1. 62 

1. 54 

1.47 

1.4 0 

1. 47 

1.47 

1.47 

1.47 

1.40 

1. 32 

1. 32 

1. 33 

1. 2 5 

B767.2 

8779.2 

8748.0 

8763.6 

8756.4 

8796.0 

8784.6 

8776.2 

8797.8 

8794.8 

8799.6 

8809.8 

8806.2 

8834.4 

8815.8 

8827.2 

8800.8 

8832.0 

8805.6 

8821.2 

8839.2 

8869.2 

8880.0 

8869.2 

8873.4 

8887.8 

8881.8 

8888.4 

8892.0 

8878.2 

8B71.6 

8B80.0 

8876.4 

8904.6 

8904.0 

8892.0 

8909.4 

890B.8 

8898.0 

8892.0 

NH3Inj 

lb/hr 

0-200 

110.0 

110.0 

1l0.0 

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 

1l0.0 

llO.O 

110.0 

110.0 

110 0 

110.0 

110.0 

llO.O 

110.0 

llO. a 

110.0 

110 .0 

110.0 

4>Summary - I-Min RATA - Continued 

MW La 

0-1 

106. c 

106 . . 

105 . ~ 

106 . . 

105 .. 

106. 

106. 

106 

106. : 

106.: 

106 . : 

105. 

107. c 

105 . . 

106 .. 

105.: 

106 .. 

105. : 

106 . . 

107. c 

106.: 

107. c 

106. 

106. 

106 . 

108. ( 

107 .. 

107. 

106 . . 

106 .. 

106. 

108. r 

107.: 

107. : 

107.: 

107.1 

106 .. 

107 .. 

106 .. 

107.: 

Pag{ 
Group#-Channel # 

Long Des crip . 

Short Descrip. 

Uni ts 

Range 

02/11/2013 11: 11 

02/11/2013 11:12 

02/11/2013 11:13 

02/11/2013 11:14 

02/11/2013 11:15 

02/11/2013 11:16 

02/11/2013 11:17 

02/11/2013 11:18 

02/11/2013 11:19 

02/11/ 2 013 11:20 

02/11/2013 11:21 

02/11/2013 11:22 

02/11/2013 11:23 

02/11/2013 11:24 

02/11/2013 11:25 

02/11/2013 11:26 

02/11/2013 11:27 

02/11/2013 11:28 

02/11/2013 11:29 

02/11/2013 11:30 

02/11/2013 11:31 

02/11/2013 11:32 

02/11/2013 11:33 

02/11/2013 11:34 

02/11/2013 11:35 

02/11/2013 11:36 

02/11/2013 11:37 

02/11/2013 11:38 

02/11/2013 11:39 

02/11/2013 11:40 

0 2 /11/ 2013 11:41 

02/11/2013 11:42 

02/11/2013 11:43 

02/11/2013 11:44 

02/11/2013 11:45 

02/11/2013 11:46 

02/11/2013 11:47 

02/11/2013 11:48 

02/11/2013 11:49 

02/11/2013 11:50 

Date/Time Printed: 

G34-C2 G34 -C4 G34-C11 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

2.7 

2.8 

2.' 

2.7 

2.7 

2.7 

2.7 

2.7 

2.8 

2.6 

2.7 

2.7 

2.7 

2.7 

2.8 

2.7 

2.7 

2.7 

2.8 

2.8 

2.8 

2.7 

2.8 

2.' 

3.8 

3.0 

2.8 

2.7 

2.7 

2.6 

3.6 

2.8 

2.7 

2.4 

2.3 

2.6 

2.8 

3.4 

3.1 

2.8 

Stk 02 

% 

0-25 

12.90 

12.91 

12.90 

12.91 

12.92 

12.93 

12.92 

12 . 93 

12 . 91 

12.93 

12.91 

12.93 

12.92 

12.92 

12.91 

12.92 

12.92 

12.92 

12 . 92 

12.90 

12.90 

12.90 

12.90 

12.90 

12 . 90 

12.91 

12.89 

12.90 

12.91 

12.90 

12.90 

12.95 

12.93 

12.93 

12.92 

12.90 

12.91 

12 . 91 

12.94 

12.93 

02/11/2013 16,39 

NOx Mass 

Ib/hr 

0-100 

6.52 

7.43 

7.46 

6.50 

6.48 

6.48 

6.49 

6.48 

7.43 

6.47 

6.49 

6.48 

6.49 

6.48 

7.43 

6.49 

6.48 

6.48 

7.42 

7.44 

7.44 

6.51 

7.43 

7.45 

9.30 

7.45 

7.46 

6.52 

6.51 

6.51 

9.28 

7.38 

6.48 

6.48 

5.56 

6.52 

7.43 

8.36 

7.40 

7.41 

G34-C20 

4>StkFlow 

StkFlow 

kscfh 

0-300000 

21179 

21170 

21209 

21156 

21125 

21141 

21139 

21143 

21173 

21121 

21110 

21141 

21136 

21122 

21148 

21139 

21123 

21132 

21149 

21158 

21168 

21161 

21138 

21179 

21172 

21212 

21190 

21182 

21193 

21156 

21119 

21119 

21134 

21150 

21151 

21189 

21169 

21163 

21160 

21145 

G34-C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

2.0 

2.0 

2.0 

2.0 

2.' 

2.7 

2.6 

2.6 

2.4 

2.6 

2.6 

2.6 

2.7 

2.' 

3.0 

2.8 

2.8 

3.0 

2.8 

2.6 

2.6 

2.7 

2.6 

2.6 

2.6 

2.5 

2.6 

2.5 

2.8 

3.0 

2.4 

0.3 

0.3 

0.5 

1 7 

3.2 

3.7 

3.3 

0 . 5 

0.4 

G34 -C13 G34-CI0 G34-C6 

4>CO Mass 4>NOx Rate 4>Stk NOXc 

CO Mass 

Ib/hr 

0-100 

2.79 

2.79 

2.80 

2.79 

3.70 

3 . 70 

3.71 

3.70 

3.72 

3.70 

3.71 

3.70 

3.71 

4.63 

4.64 

4.63 

4.63 

4.63 

4.64 

3.72 

3.72 

3.72 

3.72 

3.72 

3.72 

3.72 

3.73 

3.72 

4.65 

4.65 

3.71 

0.00 

0.00 

0.93 

2.78 

4.66 

5.57 

4.64 

0.93 

0.93 

NOx Rate 

lb/mmBtu 

0-1 

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 

0.008 

0.007 

0.007 

0.007 

0.008 

0.008 

0.008 

0.007 

0.008 

0.008 

0.010 

0.008 

0.008 

0.007 

0.007 

0.007 

0.010 

0.008 

0.007 

0.007 

0.006 

0.007 

0.008 

0.009 

0.008 

0.008 

Stk NOXc 

ppm 

0-300 

1. 99 

2.07 

2 . 14 

1. 99 

2.00 

2.00 

2.00 

2.00 

2.07 

1. 92 

1. 99 

2.00 

2.00 

2.00 

2.07 

2.00 

2.00 

2.00 

2.07 

2.07 

2.07 

1. 99 

2.07 

2.14 

2.80 

2.22 

2.06 

1. 99 

1. 99 

1. 92 

2.66 

2.08 

2.00 

1. 78 

1. 70 

1. 92 

2.07 

2.51 

2.30 

2.07 

G34-C7 G34-C8 

4>Stk COc 4>Gas Flow 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

1.48 

1. 48 

1.48 

1.48 

1. 77 

2.00 

1. 92 

1. 92 

1. 77 

1. 92 

1. 92 

1. 92 

2.00 

2.14 

2.22 

2.07 

2.07 

2.22 

2.07 

1. 92 

1. 92 

1. 99 

1. 92 

1. 92 

1. 92 

1. 85 

1. 92 

1. 84 

2.07 

2.21 

1. 77 

0.22 

0.22 

0.37 

1. 26 

2.36 

2.73 

2.44 

0.37 

0.30 

8864.4 

8849.4 

8877.0 

8843.4 

8819.4 

8815.2 

8825.4 

8815.8 

8850.6 

8806.8 

8824.2 

8815.2 

8824.2 

8818.2 

8840.4 

8825.4 

8818.8 

8822.4 

8829.6 

8855.4 

8859 . 6 

8856.6 

8847.0 

8864.4 

8861.4 

8866.8 

8880.0 

8865.6 

8859.0 

8854.8 

8839.2 

8784.0 

8812.2 

8818.8 

8830.2 

8868.6 

8848.8 

8846.4 

8812.2 

8817.0 

G34-C18 

4 >NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110 .0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110 . a 

110. a 

110.0 

110.0 

110.0 

110. a 

110.0 

110.0 

110.0 

110.0 

4>Summary - I-Min RATA - Continued 

G34-C 

4>MW Lo 

MW Lo 

0- 1 

105. : 

106. : 

107. : 

106. : 

106. ! 

106 . . 

106. : 

106 . 

106. 

105 . . 

106 . . 

105. 

105. 

107. 

106.1 

106. : 

105. 

106 .. 

105. ! 

106. 

106. : 

106 . . 

106.: 

106.: 

106. 

107. ! 

106 .. 

106 .. 

1 06. 

106. 

106 .. 

106. ! 

107. [ 

105. 

105 . : 

106. 

106 .. 

106.1 

106 

106.1 

PagE 
Group#-Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/11/2013 11:51 

02/11/2013 11:52 

02/11/2013 11:53 

02/11/2013 11:54 

02/11/2013 11:55 

02/11/2013 11:56 

02/11/2013 11:57 

02/11/2013 11 :58 

02/11/2013 11:59 

02/11/ 2 013 12:00 

02/11/2013 12;01 

02/11/2013 12:02 

02/11/2013 12;03 

02/11/2013 12:04 

02/11/2013 12:05 

02/11/2013 12:06 

02/11/2013 12:07 

02/11/2013 12:08 

02/11/2013 12:09 

02/11/ 2 013 12:10 

02/11/ 2 013 12:11 

02/11/2013 12:12 

02/11/2013 12:13 

02/11/2013 12:14 

02/11/2013 12:15 

02/11/2013 12:16 

02/11/2013 12:17 

02/11/ 2 013 12:18 

02/11/2013 12:19 

0 2 /11/2013 12:20 

02/11/2013 12:21 

02/11/2013 12:22 

02/11/2013 12:23 

02/11/2013 12:24 

02/11/2013 12:25 

02/11/2013 12:26 

02/11/2013 12:27 

02/11/2013 12:28 

02/11/2013 12:29 

02/11/2013 12:30 

Date/Time Printed: 

G34-C2 G34-C4 G34 -C11 

4>Stk NOx 

Stk NOx 

4>Stk 02 4>NOx Mass 

ppm 

0-150 

2.B 

2.6 

2.7 

2.B 

2.B 

2.B 

2.B 

2 . B 

3.2 

3.2 

2. 7 

2.4 

2.7 

2.7 

2 . 7 

2.B 

2.7 

2.7 

2.7 

2.7 

2.6 

2.B 

2.7 

2.6 

2.6 

2.6 

2.6 

2.7 

2.B 

2.B 

2.B 

2.B 

2.B 

2.B 

2.7 

2.7 

2.7 

2.7 

2.6 

2.7 

Stk 02 

% 

0-25 

12.91 

12.92 

12.90 

12.89 

12.90 

12 .9 0 

12.89 

12.89 

12.90 

12.92 

12.91 

12.93 

12.91 

12 .91 

12.92 

12.90 

12 . 90 

12.92 

12.92 

12.93 

12.92 

12.91 

12.91 

12.92 

12.92 

12.91 

12.90 

12.89 

12 . 89 

12.88 

12.87 

12.88 

12 . 89 

12.88 

12.88 

12.89 

12.90 

12 . 91 

12.90 

12.89 

02/11/2013 16,39 

NOx Mass 

lb/hr 

0-100 

7.43 

6.49 

6.52 

7.46 

7.44 

7.45 

7.45 

7.46 

8.36 

8 . 34 

6.49 

6.48 

6.51 

6.51 

6.50 

7.46 

6.51 

6.49 

6.49 

6.48 

6. 4 7 

7.42 

6.49 

6.48 

6.48 

6.50 

6.49 

6 . 51 

7.45 

7.46 

7.46 

7.46 

7.45 

7.44 

6.52 

6.51 

6.52 

6.51 

6.52 

6.52 

G34-C20 

4>StkFlow 

StkFlow 

kscfh 

0-300000 

21148 

21163 

2 1202 

21182 

21169 

21185 

21164 

21182 

21136 

21140 

21134 

21154 

21190 

21193 

21175 

21207 

21168 

21163 

21163 

21140 

21079 

21121 

21121 

21100 

21113 

21144 

21112 

21131 

21157 

21159 

21153 

21165 

21170 

21119 

21157 

21144 

21191 

21200 

21192 

21169 

G34 -C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

0.4 

0.9 

2.6 

3.2 

3.3 

3.2 

3.5 

3.4 

3.5 

0.5 

0.4 

0.7 

1.2 

1.7 

2.2 

2.1 

2.2 

2.3 

2.5 

2.3 

2.3 

2.1 

1.7 

1.6 

1.5 

1.6 

loB 

2.0 

1.9 

2.0 

loB 

1 . 7 

1.7 

loB 

2.2 

2.5 

2.7 

2.B 

3.0 

3.0 

G34-C13 G34-C10 G34-C6 

4>CO Mass 4>NOx Rate 4>Stk NOXc 

CO Mass 

lb/hr 

0-100 

0 . 93 

0 . 93 

3.73 

4 . 66 

4.65 

4.66 

5.59 

5.59 

5.57 

0.93 

0.93 

0.93 

1. 86 

2.79 

3.71 

2.80 

3.72 

3.71 

3.71 

3.70 

3.70 

2.78 

2 . 78 

2.78 

1. 85 

2 .78 

2.78 

2.79 

2 . 79 

2.80 

2 . 80 

2.80 

2.79 

2.79 

3.73 

3 . 72 

3 . 73 

4.65 

4.66 

4.66 

NOx Rate 

l b/mmBtu 

0-1 

0.008 

0.007 

0.007 

0.008 

0.008 

0.008 

0.008 

0.008 

0.009 

0.009 

0.007 

0.007 

0.007 

0.007 

0 . 007 

0.008 

0.007 

0.007 

0.007 

0 . 007 

0 . 007 

0.008 

0 . 007 

0.007 

0.007 

0.007 

0.007 

0 . 007 

0.008 

0.008 

0.008 

0.008 

0 . 008 

0.008 

0.007 

0.007 

0.007 

0.007 

0.007 

0.007 

Stk NOXc 

ppm 

0-300 

2.07 

1. 92 

1. 99 

2.06 

2.07 

2 . 07 

2.06 

2.06 

2.36 

2.37 

1. 99 

1. 78 

1. 99 

1. 99 

2.00 

2.07 

1. 99 

2.00 

2.00 

2.00 

1. 92 

2.07 

1. 99 

1. 92 

1. 92 

1. 92 

1. 92 

1. 99 

2.06 

2.06 

2.06 

2.06 

2.06 

2.06 

1. 99 

1. 99 

1. 99 

1. 99 

1. 92 

1. 99 

G3 4 -C7 G34-C8 

4>Stk COc 4>Gas Flow 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.30 

0.67 

1. 92 

2.36 

2.43 

2.36 

2.58 

2.50 

2.58 

0 . 37 

0.30 

0 . 52 

0 . 89 

1. 26 

1. 63 

1. 55 

1. 62 

1. 70 

1. 85 

1. 70 

1. 70 

1. 55 

1. 26 

1.18 

1.11 

1.18 

1. 33 

1. 47 

1. 40 

1. 47 

1. 32 

1. 25 

1.25 

1.32 

1. 62 

1. 84 

1. 99 

2.07 

2.21 

2.21 

8840.4 

8835.6 

8874.0 

8876.4 

8860.2 

8866 . 8 

8869 . 2 

8876.4 

8846.4 

8826 . 0 

8834 . 4 

8820.6 

8857.8 

8859.0 

8840.4 

8875.8 

8859.6 

8835.6 

8835.6 

8814 . 6 

8800.2 

8829.0 

8829.0 

8809.2 

8814.6 

8838.6 

8836 . 2 

8855 .4 

8866.2 

8878.2 

8886.6 

8880 . 6 

8871.6 

8861. 4 

8877.0 

8860.8 

8869 . 2 

8862.0 

8869.8 

8871.0 

G34-C18 

4>NH3 Inj 

NH3Inj 

1b/hr 

0-200 

110.0 

110.0 

110.0 

110.0 

110.0 

110 . 0 

110 . 0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110 . 0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110 . 0 

110.0 

110.0 

110 . 0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

4>Summary - l-Min RATA - Continued 

G34-C 

4>MW Lo 

MW Lo 

0-1 

106 .. 

105. : 

106. ! 

107. : 

106.1 

106 .. 

106. 

107. : 

106. 

106. : 

106. ; 

105 .. 

105 .. 

106. 

106 .. 

106. : 

106 .. 

106. : 

106 .. 

105 . 

105. 

106.! 

106. 

106. 

106 .. 

106. 

106. 

107. : 

106 .. 

107.1 

107.1 

107. ' 

107. : 

106 .. 

106. 

106. 

107 . 

107. ( 

107. 

107 .. 

Pag~ 
Group# - Channel# 

Long Descrip . 

Short Descrip. 

Units 

Range 

02/11/2013 12:31 

02/11/2013 12:32 

02/11/2013 12:33 

02/11/2013 12:34 

02/11/2013 12:35 

02/11/2013 12:36 

02/11/2013 12:37 

02/11/2013 12:38 

02/11/2013 12:39 

02/11/2013 12:40 

02/11/2013 12:41 

02/11/2013 12:42 

02/11/2013 12:43 

02/11/2013 12:44 

02/11/2013 12:45 

02/11/2013 12:46 

02/11/2013 12:47 

02/11/2013 12:48 

02/11/2013 12:49 

02/11/2013 12:50 

02/11/2013 12:51 

02/11/2013 12:52 

02/11/2013 12:53 

02/11/2013 12:54 

02/11/2013 12:55 

Period Average 

Period Max Value 

Period Min Value 

Period Totals = 

Period % Recovery 

Date/Time Printed: 

G3 4 -C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

2.6 

2.7 

2.7 

2.7 

2.6 

2.7 

2 . 7 

2.6 

2.7 

2.6 

2.6 

2.6 

2.7 

2.6 

2 . 6 

2.7 

2.7 

2.7 

2.7 

2.7 

2.7 

2.7 

2.7 

2.7 

2.6 

2.8 

3.8 

2.3 

G3 4 -C4 G34 -C11 G34-C20 

4>Stk 02 4>NOx Mass 4>StkFlow 

Stk 02 

% 

0-25 

12 . 91 

12.90 

12.90 

12.90 

12.91 

12.89 

12.89 

12.89 

12 . 88 

12.88 

12 . 87 

12.88 

12.88 

12 . 87 

12.88 

12.88 

12 . 88 

12.87 

12.88 

12.88 

12.87 

12.88 

12.87 

12.87 

12.89 

12.91 

12 . 97 

12.87 

NOx Mass 

Ib/hr 

0-100 

6.50 

6.51 

6.51 

6.51 

6.50 

6.51 

6.52 

6.52 

6.52 

6.52 

6.52 

6.51 

6.52 

6.53 

6.52 

6.53 

6.52 

6 . 53 

6 . 52 

6.53 

6.51 

6.52 

6.53 

6.52 

6.51 

7.07 

9.36 

5.56 

StkFlow 

ksefh 

0-300000 

21147 

21168 

21168 

21146 

21143 

21144 

21164 

21172 

21152 

21157 

21129 

21117 

21147 

21136 

21134 

21159 

21152 

21159 

21151 

21161 

21093 

21134 

21133 

21113 

21127 

21154 

21332 

21038 

G34-C3 G34 -CD G34-C10 G34-C6 G34-C7 G34 -C8 G34 - C18 G34-C 

4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXe 4>Stk Cae 4>Gas Flow 4>NH3 Inj 4>MW Lo 

Stk CO 

ppm 

0-1000 

3.3 

3.1 

2.9 

3.2 

3.3 

3.2 

2 . 9 

2.8 

2.7 

2.7 

2 . 9 

3.2 

3.2 

3. 2 

3.2 

3.1 

3.0 

2.9 

3.0 

2.9 

2.8 

2.8 

2.8 

2.8 

2.9 

2. 4 

3.7 

0.3 

CO Mass 

Ib/hr 

0-100 

4.64 

4 . 65 

4.65 

4.65 

4.64 

4.65 

4.66 

4.66 

3.73 

3.73 

4.66 

4.65 

4.66 

4.66 

4.66 

4.66 

4.66 

4.67 

4.66 

4 . 66 

4.65 

4.66 

4.66 

4.66 

4.65 

3.69 

5.59 

0.00 

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 

0.008 

0.010 

0.006 

Stk NOXe 

ppm 

0-300 

1. 92 

1. 99 

1. 99 

1. 99 

1. 92 

1. 99 

1. 99 

1.92 

1. 99 

1. 91 

1. 91 

1. 91 

1. 99 

1. 91 

1. 91 

1. 99 

1. 99 

1. 98 

1. 99 

1. 99 

1. 98 

1. 99 

1. 98 

1. 98 

1. 92 

2.07 

2.80 

1. 70 

Stk COe Gas 

ppm 

hsefh 

hscfh 

0-1000 

2.44 

2 . 29 

2.14 

2.36 

2.44 

2.36 

2.14 

2 . 06 

1. 99 

1. 99 

2.13 

2.35 

2 . 35 

2.35 

2.35 

2.28 

2.21 

2 .13 

2.21 

2.13 

2 . 06 

2.06 

2.06 

2.06 

2.14 

1. 79 

2.73 

0.2 2 

0-10000 

8839.8 

8859.6 

8859.6 

8850.6 

8838.0 

8860.8 

8869.2 

8872.2 

8875.2 

8877 . 0 

8876.4 

8860.2 

8872.8 

8879 . 4 

8867.4 

8878.2 

8875.2 

8889.0 

8874.6 

8878.8 

8861 . 4 

8867 . 4 

8878.2 

8869 . 8 

8853.6 

8845.2 

8951. 4 

8731.8 

NH3Inj 

Ib/hr 

0-200 

110 . 0 

110 . 0 

110.0 

110.0 

110.0 

110.0 

110.0 

110 . 0 

110.0 

110.0 

110.0 

110 . 0 

110.0 

110 . 0 

110.0 

110.0 

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 

106. : 

106. : 

106. ! 

106.1 

106 . . 

106 .. 

107. : 

106. : 

106. 

107. 

107. : 

106. ! 

107. 1 

106 . 

106. 

106 .. 

107 . . 

107.! 

106 .. 

106 .. 

107.1 

107.: 

107.: 

106.: 

106 .. 

106.5 

109 . 

105. 

7.1410E+2 3.2915E+3 1.8019E+3 5.3943E+6 6.1890E+2 9.3972E+2 1.9399E+0 5.2719E+2 4.5692E+2 2.2555E+6 2 . 8050E+4 2.7175E+ 

100.0 100.0 100 . 0 100 . 0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100. 

02/11/2013 16,39 4>Summary - I-Min RATA - Continued Pag~ 
Data Summary Report 

Company: CPV Sentinel, LLC 

62575 Powerline Road 

7uh~\ L{ 

Desert Hot Springs, CA 92240 PM 

:}-7~ Source : Turbine 4 

Data Group: 4>1-Min Cales 

Repo rt Name: 

Start of Report : 

4>Summary - l-Min RATA 

02/11/2013 14,48 

G34-C4 

End of Report, 02/11/2013 18,56 

G34 -CII G34 - C20 G34-C3 G34-C13 

TRACE 

EmJironmellt ai Sy stems, Inc. 

Validation: All Available Data 

Group#-Channel# G34 - CIO G34-C6 G34-C7 G34-C8 G34 - C18 G34-C 

Long Descrip. 

Short Descrip. 

Units 

G34-C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 0 2 4>NOx Mass 4>StkFlow 4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk COc 4>Gas Flow 4>NH3 Inj 4>MW La 

Range 

02(11(2013 14:48 

02(11( 2013 14:49 

02(11(2013 14:50 

02(11(2013 14:51 

02(11(2013 14:52 

02(11(2013 14:53 

02(11(2013 14:54 

02(11/2013 14:55 

02(11(2013 14:56 

02(11(2013 14:57 

02(11(2013 14:58 

02(11(2013 1 4 :59 

02(11(2 013 15:00 

02 (11(2013 15:01 

02(11(2013 15:02 

02(11(2013 15:03 

02(11(2013 15;04 

02(11(2013 15;05 

02(11(2013 15:06 

02(11/2013 15:07 

02/11/2013 15:08 

02/11(2013 15:09 

02/11(2013 15:10 

02/11/2013 15:11 

02/11/2013 15:12 

02/11/2013 15:13 

02/11/2013 15:14 

02(11(2013 15;15 

02(11(2013 15:16 

02 (11(2013 15:17 

Date/Time Printed: 

1.9 

2.0 

1.9 

2.0 

2.1 

2.0 

2.0 

2.0 

2.0 

2.0 

2.1 

2.0 

2.1 

2.1 

2.0 

2.1 

2.2 

2.1 

2.1 

2.2 

2.1 

2.1 

2.0 

2.0 

2.2 

2.2 

2.2 

2.0 

1.7 

1.9 

Stk 02 

• 

0 - 25 

13.56 

13.55 

13.56 

13 _ 54 

13.53 

13.54 

13.53 

13.53 

13.53 

13.53 

13 . 53 

13.55 

13 . 55 

13 . 55 

13.55 

13.57 

13.55 

13.56 

13.56 

13.55 

13.56 

13.56 

13.56 

13 . 56 

13 . 55 

13.56 

13 . 56 

13.55 

13.54 

13 . 54 

02/11/2013 19,08 

NOx Mass 

Ib/hr 

0-100 

4.38 

4.39 

4.37 

4.40 

4.42 

4.40 

4.40 

4.41 

4.41 

4.40 

4.40 

4.38 

4.38 

4.39 

4.39 

4.37 

5.12 

4.37 

4.37 

5.11 

4.38 

4.37 

4.38 

4.38 

5.11 

5.12 

5 . 10 

4.39 

3.66 

4.39 

StkFlow 

kscfh 

0-300000 

18107 

18125 

18076 

18152 

18185 

18141 

18129 

18150 

18150 

18108 

18130 

18087 

18069 

18122 

18117 

18104 

18126 

18076 

18075 

18089 

18087 

18081 

18103 

18092 

18064 

18137 

18075 

18125 

18086 

18092 

Stk CO 

ppm 

0-1000 

0 . 5 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.7 

0.7 

0.7 

0.7 

0.6 

0.7 

0.6 

0.7 

0.6 

0.7 

1. 4 

2.3 

CO Mass 

Ib/hr 

0-100 

0.73 

0.73 

0.73 

0.73 

0.74 

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 

2.19 

2.93 

NOx Rate 

Ib/mmBtu 

0-1 

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 

O.OOG 

O.OOG 

0.007 

0.006 

O.OOG 

0.007 

0.006 

0.006 

0.006 

0.006 

0.007 

0.007 

0.007 

0.006 

0.005 

0.006 

Stk NOXc 

ppm 

0 - 300 

1. 53 

1. 61 

1. 53 

1. 60 

1. 68 

1. 60 

1. 60 

1. 60 

1. 60 

1. 60 

1. 68 

1. 61 

1. 69 

1. 69 

1. 61 

1. 69 

1. 77 

1. 69 

1. 69 

1. 77 

1. 69 

1. 69 

1. 61 

1. 61 

1. 77 

1. 77 

1. 77 

1. 61 

1.36 

1. 52 

Stk CDc Gas hscfh 

ppm 

0-1000 

0. 4 0 

0. 4 8 

0. 4 8 

0.48 

0.48 

0.48 

0.48 

0.48 

0.48 

0.48 

0.48 

0.48 

0. 4 8 

0.48 

0.48 

0.48 

0.48 

0.48 

0.56 

0.56 

0.5G 

0.56 

0.48 

0.56 

0.48 

0.56 

0.48 

0.56 

1.12 

1. 84 

hscfh 

0 - 10000 

6953.4 

6969.G 

6941. 4 

6989.4 

7011.6 

6985.2 

6990.0 

6998.4 

6998.4 

6982.2 

6990.6 

6955.2 

6948.0 

6968.4 

6966.6 

6942.6 

6970.2 

6941. 4 

6940.8 

6955.8 

6945. G 

6943 . 2 

6951. 6 

6947.4 

6946.2 

6964.8 

694 0.8 

6969.6 

6964 .2 

6966.6 

NH3Inj 

Ib(hr 

0 - 200 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

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 

80 _. 

BO. 

BO. 

81.: 

81. ~ 

80 . . 

81.( 

80 . ~ 

81. : 

81.' 

80. ' 

80. : 

80 . 1 

80. : 

80. : 

80. : 

80. : 

80. : 

BO. 

80.1 

80 . . 

80. : 

80 .. 

80 .. 

80. t 

80 . . 

79. 

B1. 

80 

80.: 

PagE 
Group#-Channel# 

Long Descrip. 

Short Descrip . 

units 

Range 

02/11/2013 15:18 

02/11/2013 15:19 

02/11/2013 15:20 

02/11/2013 15:21 

02/11/2013 15:22 

02/11/2013 15:23 

02/11/2013 15:24 

02/11/2013 15:25 

02/11/2013 15:26 

02/11/2013 15:27 

02/11/2013 15:28 

02/11/2013 15:29 

02/11/ 2013 15:30 

02/11/2013 15:31 

02/11/2013 15:32 

02/11/2013 15:33 

02/11/2013 15:34 

02/11/2013 15:35 

02/11/2013 15:36 

02/11/2013 15:37 

02/11/2013 15:38 

02/11/2013 15:39 

02/11/2013 15:40 

02/11/2013 15:41 

02/11/2013 15:42 

02/11/2013 15:43 

02/11/2013 15:44 

02/11/2013 15:45 

02/11/2013 15:46 

02/11/2013 15:47 

02/11 /2013 15:48 

02/11/2013 15:49 

02/11/2013 15:50 

02/11/2013 15:51 

02/11/2013 15:52 

02/11/ 2 013 15:53 

02/11/2013 15:54 

02/11/2013 15:55 

02/11/2013 15:56 

02/11/2013 15:57 

Date/Time Printed: 

G34 - C2 G34-C4 G34 - C11 

4 , Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

2.2 

2.1 

2.1 

2.1 

2.1 

2.2 

2.1 

2.1 

2.1 

2.1 

2 . 3 

2.2 

2.0 

2.1 

2.1 

2.2 

2.1 

2.2 

2.2 

2.3 

2.1 

2.2 

2.1 

2.1 

2.1 

2.1 

2.1 

2.2 

2.2 

2.2 

2.0 

2.0 

2.1 

2.1 

2.2 

2.1 

2.0 

2.1 

2.1 

2.1 

Stk 02 

• 

0-25 

13 .52 

13.52 

13.51 

13.52 

13.51 

13.50 

13.52 

13.51 

13.53 

13.54 

13 . 53 

13.53 

13.54 

13.54 

13.53 

13.53 

13.54 

13.54 

13.53 

13.53 

13.54 

13.53 

13.53 

13.54 

13.53 

13 . 53 

13.52 

13.52 

13.52 

13.52 

13.53 

13 .53 

13.54 

13.54 

13.54 

13.54 

13.54 

13.54 

13.53 

13.54 

02/11/2013 19,08 

NOx Mass 

Ib/hr 

0-100 

4.40 

4.39 

4.40 

4.41 

4.41 

4.42 

4.41 

4.42 

4.40 

4.40 

5.15 

4.41 

4.39 

4.39 

4.40 

4.41 

4.40 

4.40 

4.40 

5.15 

4.41 

4.42 

4.41 

4.40 

4.41 

4.42 

4.43 

4.42 

4.42 

4.42 

4.41 

4.40 

4.39 

4.39 

4.39 

4.39 

4 .39 

4.40 

4 . 41 

4.41 

G34-C20 

4>StkFlow 

StkFlow 

ksefh 

0-300000 

18092 

18060 

18075 

18130 

18112 

18111 

18137 

18140 

18101 

18130 

18171 

18174 

18108 

18097 

18101 

18146 

18131 

18130 

18130 

18153 

18173 

18186 

18175 

18134 

18166 

18189 

18191 

18163 

18172 

18183 

18164 

18111 

18114 

18100 

18086 

18108 

18089 

18139 

18135 

18180 

G34-C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

2.0 

1.6 

1.7 

1.7 

1.8 

1.7 

1.7 

1.8 

2.0 

2.3 

2.2 

2.0 

2.4 

2.5 

2.7 

2.3 

2.3 

2.3 

2.3 

1.9 

1.8 

1.9 

1.7 

1.9 

1.9 

1.7 

1.7 

1.7 

1.8 

1.6 

1.6 

1.9 

2.2 

2.3 

2.3 

2.6 

2.3 

2.0 

1.9 

1.7 

G34 -CD G34 - C10 G34 - C6 

4>CO Mass 4>NOx Rate 4>Stk NOXe 

CO Mass 

lb/hr 

0-100 

2.93 

2.20 

2.20 

2.21 

2 . 21 

2.21 

2.21 

2.21 

2.93 

2.93 

2.94 

2.94 

2.93 

2.93 

3.66 

2.94 

2.93 

2.93 

2.94 

2.21 

2.20 

2.21 

2.21 

2.20 

2.21 

2.21 

2.21 

2.21 

2.21 

2.21 

2.21 

2.20 

2.93 

2.93 

2.92 

3.66 

2.93 

2.93 

2.20 

2.21 

NOx Rate 

lb/mmBtu 

0 - 1 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

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 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

Stk NOXe 

ppm 

0-300 

1. 76 

1. 68 

1. 68 

1. 68 

1. 68 

1. 75 

1. 68 

1. 68 

1. 68 

1. 68 

1. 84 

1. 76 

1. 60 

1. 68 

1. 68 

1. 76 

1. 68 

1. 76 

1. 76 

1. 84 

1. 68 

1. 76 

1. 68 

1. 68 

1. 68 

1. 68 

1. 68 

1. 76 

1. 76 

1. 76 

1. 60 

1. 60 

1. 68 

1. 68 

1. 76 

1. 68 

1. 60 

1. 68 

1 .68 

1. 68 

G34-C7 G34-C8 

4>Stk COe 4>Gas Flow 

Stk COe Gas hsefh 

ppm hsefh 

0-1000 0-10000 

1. 60 

1. 28 

1. 36 

1. 36 

1.44 

1.36 

1. 36 

1.44 

1. 60 

1. 84 

1. 76 

1. 60 

1. 92 

2.00 

2.16 

1. 84 

1. 84 

1. 84 

1. 84 

1. 52 

1.44 

1. 52 

1. 36 

1. 52 

1. 52 

1 36 

1.36 

1.36 

1. 44 

1.28 

1.28 

1. 52 

1. 76 

1. 84 

1. 84 

2.08 

1. 84 

1. 60 

1. 52 

1.36 

6985.2 

6973.2 

6988.2 

7000.2 

7002.6 

7011.6 

7002.6 

7013.4 

6979.2 

6981.0 

7006.2 

7007.4 

6972.6 

6968.4 

6979.2 

6996.6 

6981.6 

6981.0 

6990.6 

6999.6 

6997.8 

7012.2 

7008.0 

6982.8 

7004.4 

7013.4 

7023.6 

7012.8 

7016.4 

7020.6 

7003.8 

6983.4 

6975.0 

6969.6 

6964.2 

6972.6 

6965.4 

6984.6 

6992.4 

7000.2 

G34 - C18 

4 >NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

110.0 

110.0 

110.0 

110 .0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

110.0 

4>Summary - I-Min RATA - Continued 

G34 - C 

4>MW La 

MW Lo 

0-1 

80. 

80. 

80 . ~ 

80. 

80 .. 

81. : 

81. : 

81.t 

80 .. 

80.1 

80. 

80 .. 

80. : 

79. 

80. -

80 .. 

80. 

80. 

80. 

81.1 

80. 

Bl.: 

81.: 

80 . . 

81 

BO .. 

B1.: 

81.t 

81.1 

81.: 

B1.! 

80. 

80 

80.: 

79. 

BO .. 

BO .1 

80 . . 

80 . . 

81.1 

PagE 
Group#-Channel# 

Long Descri p. 

Short Des c r i p . 

units 

Range 

02/11/2013 15:58 

02 /11/2013 15:59 

02/11/2013 16:00 

02/11/2013 16:01 

02/11/2013 16:02 

02/11/2013 16:03 

02/11/2013 16:04 

02/11/2013 16:05 

02/11/2013 16:06 

02/11/2013 16:07 

02/11/2013 16:08 

02/11/2013 16:09 

02/11/2013 16:10 

02/11/2013 16:11 

02/11/2013 16:12 

02/11/2013 16:13 

02/11/2013 16:14 

02/11/2013 16:15 

02/11/2013 16:16 

02/11/2013 16:17 

02/11/2013 16:18 

02/11/2013 16:19 

02/11/2013 16:20 

02/11/2013 16:21 

02/11/2013 16:22 

02/11/2013 16:23 

02/11/2013 16:24 

02/11/2013 16:25 

02/11/2013 16:26 

02/11/2013 16:27 

02/11/2013 16:28 

02/11/2013 16:29 

02/11/2013 16:30 

02/11/2013 16:31 

02/11/2013 16:32 

02/11/2013 16:33 

02/11/2013 16:34 

02/11/2013 16:35 

02/11/2013 16:36 

02/11/2013 16:37 

Date/Time Printed: 

G34-C2 G34 -C4 G34 -C11 G34-C20 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 4>StkFlow 

2.1 

2.0 

2.0 

2.1 

2.2 

2.1 

2.2 

2.3 

2.1 

2.1 

2.2 

2.1 

2.1 

2.1 

2.2 

2.3 

2.3 

2.1 

2.1 

2.2 

2.2 

2.2 

2.2 

2.3 

2.4 

2.6 

3.0 

2.9 

2.9 

2.8 

2.8 

2.8 

2.6 

2.8 

2.8 

2.7 

2.8 

2.7 

2.7 

2.6 

Stk 02 

% 

0-25 

13.54 

13.54 

13.55 

13.55 

13.55 

13.54 

13 . 55 

13.55 

13 . 55 

13.54 

13.53 

13 .54 

13.54 

13.54 

13.53 

13.53 

13.53 

13.53 

13.53 

13.53 

13.53 

13.53 

13.53 

13.54 

13.53 

13.53 

13.54 

13.55 

13.55 

13.5S 

13.55 

13.55 

13.55 

13 . 53 

13.54 

13. S4 

13 . 55 

13 . 55 

13.55 

13 . 55 

02/11/2013 19,08 

NOx Mass 

lb/hr 

0-100 

4.42 

4.41 

4.40 

4.40 

5.15 

4.41 

5.14 

S .15 

4.41 

4.42 

4.42 

4.40 

4.41 

4.39 

4.41 

5.15 

5.16 

4.42 

4.42 

4.42 

4.42 

4.43 

4.42 

5.17 

5.16 

5.90 

6.66 

6.63 

6.64 

5.90 

5.92 

5.91 

5.87 

5.89 

5.92 

5.91 

5.89 

5.89 

5.89 

5.89 

StkFlow 

ksefh 

0-300000 

18202 

18195 

18142 

18172 

18218 

18183 

18176 

18211 

18215 

18202 

18199 

18156 

18187 

18111 

18169 

18163 

18217 

18197 

18177 

18178 

18178 

18245 

18211 

18264 

18211 

18220 

18300 

18233 

18270 

18261 

18321 

18295 

18175 

18199 

18289 

18258 

18250 

18247 

18242 

18228 

G34-C3 G34 -CD G34-C10 G34-C6 G34-C7 G34 -C8 G34-C18 G34-C 

4>Stk CO 4>CO Mass 4 >NOx Rate 4>Stk NOXe 4>Stk COe 4>Gas Flow 4>NH3 Inj 4>MW Lo 

Stk CO 

ppm 

0-1000 

1.6 

1.6 

1.7 

1.8 

1.6 

1.6 

1.6 

1.3 

1.2 

1.4 

1.4 

1.4 

1.5 

1.6 

1.6 

1.5 

1.5 

1.4 

1.4 

1.5 

1.5 

1.7 

1.4 

1.3 

1.2 

1.2 

1.0 

1.0 

1.0 

1.0 

1.0 

1.0 

1.1 

1.1 

1.0 

1.0 

1.0 

1.1 

1.1 

1.1 

CO Mass 

lb/hr 

0-100 

2.21 

2.21 

2.20 

2.20 

2.21 

2.21 

2.20 

1. 47 

1.47 

2.21 

2.21 

2.20 

2.21 

2.20 

2.21 

2.21 

2.21 

2.21 

2.21 

2.21 

2.21 

2.22 

2.21 

1.48 

1.47 

1.4B 

1.4B 

1.47 

1. 48 

1. 47 

1. 4B 

1.48 

1. 47 

1. 47 

1. 48 

1. 48 

1.47 

1.47 

1.47 

1.47 

NOx Rate 

Ib/mmBtu 

0-1 

0.006 

0.006 

0.006 

0.006 

0 .007 

0.006 

0.007 

0.007 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

0.007 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

0.007 

0.008 

0.009 

0.009 

0.009 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

O.OOB 

Stk NOXc 

ppm 

0-300 

1. 68 

1. 60 

1. 61 

1. 69 

1. 77 

1. 68 

1. 77 

1. 85 

1. 69 

1. 68 

1. 76 

1. 68 

1. 68 

1. 68 

1. 76 

1. 84 

1. 84 

1. 68 

1. 68 

1. 76 

1. 76 

1. 76 

1. 76 

1. 84 

1. 92 

2.08 

2.40 

2.33 

2.33 

2.25 

2.25 

2.25 

2.09 

2.24 

2.24 

2.16 

2.25 

2.17 

2.17 

2.09 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

1.28 

1. 28 

1.36 

1.44 

1.28 

1.28 

1. 28 

1. 04 

0.96 

1.12 

1.12 

1.12 

1.20 

1. 28 

1. 28 

1. 20 

1.20 

1.12 

1.12 

1. 20 

1. 20 

1. 36 

1.12 

1. 04 

0 . 96 

0.96 

O.BO 

0.80 

0.80 

0.80 

0.80 

0.80 

0.88 

0 . 88 

O.BO 

0.80 

0 . 80 

0.88 

0.88 

0.88 

7008.6 

7006.2 

6976.2 

6987.6 

7005.6 

7001.4 

6989.4 

7002.6 

7004.4 

7008.6 

7017.0 

6991.2 

7003.2 

6973.8 

7005.6 

7003.2 

7024.2 

7016.4 

7008.6 

7009.2 

7009.2 

7035.0 

7021.8 

7032.6 

7021.8 

7025.4 

7046.4 

7011.0 

7025.4 

7021. 8 

7045.2 

7035.0 

6988.8 

7017.0 

7042.2 

7030.2 

7017.6 

7016.4 

7014.6 

7009.2 

NH3Inj 

lb/hr 

0-200 

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 

118.5 

118.S 

119.2 

117.7 

120.2 

119.2 

114.5 

116.2 

115.0 

113.7 

115.S 

118 .2 

116.0 

116.0 

116.2 

118.7 

118.2 

118.3 

117.2 

116.0 

116.3 

4>Summary - 1-Min RATA - Continued 

MW Lo 

0-1 

81.1 

81.1 

80 .. 

80 .. 

81.: 

80. : 

80 .. 

81.: 

80 .. 

81.1 

81. 

80. 

81. . 

80 

81.: 

80. 

81. 

81. 

81.1 

81. 

81.! 

81.1 

82. I 

BO .. 

81. : 

81.! 

81. : 

81.: 

81.' 

81.' 

81. 

82.1 

81.: 

81. . 

82.: 

81. . 

81. 

81. 

80 .. 

81.: 

Pag( 
Group#-Channel# 

Long Descrip . 

Short Descrip . 

Units 

Range 

02/11/2013 16:38 

02/11/2013 16:39 

02/11/2013 16:40 

02/11/2013 16:41 

02/11/2013 16:42 

02/11/2013 16:43 

02/11/2013 16:44 

02/11/2013 16:45 

02/11/2013 16:46 

02/11/2013 16:47 

02/11/2013 16:48 

02/11/2013 16:49 

02/11/2013 16:50 

02/11/2013 16:51 

02/11/2013 16:52 

02/11/2013 16:53 

02/11/2013 16:54 

02/11/2013 16:55 

02/11/2013 16:56 

02/11/2013 16:57 

02/11/2013 16:58 

02/11/2013 16:59 

02/11/2013 17:00 

02/11/ 2 013 17:01 

02/11/2013 17:02 

02/11/2013 17:03 

02/11/2013 17:04 

02/11/2013 17:05 

02/11/2013 17:06 

02/11/2013 17:07 

02/11/2013 17:08 

02/11/2013 17:09 

02/11/2013 17:10 

02/11/2013 17:11 

02/11/2013 17:12 

02/ 11/2013 17:13 

02/11/2013 17:14 

02/11/2013 17:15 

02/11/2 013 17:16 

02/11/2013 17:17 

Date/Time Printed: 

G34 -C2 G34-C4 G34-C11 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

2.7 

2.7 

2.7 

2.6 

2.4 

2.5 

2.6 

2.6 

2.7 

2.6 

2.6 

2.5 

2.5 

2.4 

2.3 

2.6 

2.9 

3.1 

3.1 

3.1 

3.0 

3.0 

2.8 

3.0 

2.8 

2.8 

2.9 

2.9 

2.8 

2.8 

2.7 

2.7 

2.8 

2.8 

2.8 

2.7 

2.7 

2.6 

2.6 

2.5 

Stk 02 

% 

0-25 

13.54 

13.55 

13 . 54 

13.54 

13.53 

13.52 

13.52 

13 . 52 

13 . 5 3 

13.52 

13.53 

13 . 54 

13 . 54 

13.55 

13.56 

13.56 

13.56 

13.56 

13.54 

13 . 54 

13 . 55 

13.55 

13 . 55 

13 . 55 

13.54 

13.56 

13.55 

13.56 

13.55 

13.54 

13.54 

13.55 

13 . 54 

13.54 

13 . 54 

13.54 

13.56 

13.56 

13 . 55 

13.55 

02/11/2013 19,08 

NOx Mass 

lb/hr 

0-100 

5.91 

5.90 

5.92 

5.93 

5.19 

5.18 

5.93 

5.93 

5.93 

5.94 

5.95 

5.19 

5.20 

5.19 

5.16 

5.B8 

6.58 

6.57 

6.57 

6 .58 

6.56 

6.57 

5.82 

6.57 

5.84 

5.83 

6.58 

6.60 

5.87 

5.87 

5.86 

5.87 

5.89 

5.89 

5.89 

5.89 

5.90 

5.91 

5.92 

S.18 

G34-C20 

4>StkFlow 

StkFlow 

kscfh 

0-300000 

18284 

18261 

18312 

18320 

18298 

18264 

18287 

18276 

18314 

18317 

18362 

18325 

18368 

18379 

18282 

18243 

18134 

18096 

18061 

18085 

18056 

18092 

18017 

18086 

18061 

18071 

18120 

18178 

18162 

18153 

18113 

18170 

18200 

18205 

18200 

18203 

18293 

18315 

18332 

18329 

G34 -C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

1.1 

1.0 

1.0 

0.9 

1.0 

1.0 

0 . 9 

0.9 

0.9 

0.9 

0.9 

0.9 

0.9 

0.9 

1.0 

1.2 

1.2 

1.4 

1.4 

1.4 

1.4 

1.5 

1.5 

1.6 

1.5 

1.5 

1.5 

1.4 

1.4 

1.3 

1.4 

1.3 

1.3 

1.3 

1.3 

1.3 

1.2 

1.2 

1.1 

1.1 

G34-C13 G34-C10 G34-C6 

4>CO Mass 4>NOx Rate 4>Stk NOXc 

CO Mass 

1b/hr 

0-100 

1.48 

1.47 

1.48 

1.48 

1.48 

l.48 

1.48 

1.48 

1.48 

1.49 

l.49 

l. 48 

1.49 

l.48 

l.47 

1 47 

1.46 

2.19 

2.19 

2.19 

2.19 

2.19 

2 . 18 

2.19 

2.19 

2.19 

2.19 

2.20 

2.20 

1. 47 

2.20 

1. 47 

1. 47 

1. 47 

1. 47 

l. 4 7 

l.48 

1. 48 

l.48 

l.48 

NOx Rate 

lb/mmBtu 

0-1 

0.008 

0.008 

0.008 

0.008 

0.007 

0.007 

0.008 

0.008 

0.008 

0.008 

0.008 

0.007 

0.007 

0.007 

0.007 

0.008 

0.009 

0.009 

0.009 

0.009 

0.009 

0.009 

0.008 

0.009 

0.008 

0.008 

0.009 

0.009 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.008 

0.007 

Stk NOXc 

ppm 

0-300 

2.16 

2.17 

2.16 

2.08 

1. 92 

2.00 

2.08 

2.08 

2.16 

2.08 

2.08 

2.00 

2.00 

1. 93 

1 85 

2.09 

2.33 

2.49 

2.49 

2.49 

2.41 

2.41 

2.25 

2.41 

2.24 

2.25 

2.33 

2.33 

2.25 

2.24 

2.16 

2.17 

2.24 

2.24 

2.24 

2.16 

2.17 

2.09 

2.09 

2.01 

G34 -C7 G34-C8 

4>Stk COc 4>Gas Flow 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.88 

0.80 

0.80 

0.72 

0.80 

0.80 

0 . 72 

0 . 72 

0 . 72 

0.72 

0.72 

0.72 

0.72 

0.72 

0.80 

0.96 

0.96 

l.13 

1.12 

1.12 

l.12 

1. 2 0 

1. 20 

1. 28 

l. 20 

1.21 

l. 20 

l.13 

l.12 

1.04 

l. 12 

1. 04 

1. 04 

l. 04 

1.04 

l.04 

0.96 

0.9 6 

0 .8 8 

0 . 88 

7040.4 

7021.8 

7051.2 

7054.2 

7055.4 

7051.8 

7060.8 

7056.6 

7061.4 

7072.2 

7080.0 

7056.0 

7072.8 

7067.4 

7020.6 

7005.6 

6963.6 

6949.2 

6954.6 

6963.6 

6943.2 

6957.0 

6928.2 

6954.6 

6954.6 

6939.6 

6967.8 

6980.4 

6984.0 

6990.0 

6974.4 

6987.0 

7008.0 

7009.8 

7008.0 

7009.2 

7024.8 

7033.2 

7049.4 

7048.2 

G34-C18 

4>NH3 Inj 

NH3Inj 

1b/hr 

0-200 

118.3 

118.2 

119.3 

120.3 

120.5 

121.7 

122.3 

121.0 

122.8 

122.0 

124.2 

121. 2 

121. 3 

123.3 

117.7 

111. 8 

110.3 

109.8 

109.5 

109.2 

109.3 

109.3 

110.3 

109.8 

110.8 

110.5 

111. 3 

112.3 

112.7 

115.8 

113. 7 

113.5 

115.0 

113.7 

115.7 

114.5 

118.2 

117.3 

118.8 

118.7 

4 >Summary - I-Min RATA - Continued 

G34-C 

4;:.MW La 

MW Lo 

0-1 

8l. : 

81.' 

81.~ 

82.1 

82 

83.1 

82.1 

82 . . 

82.1 

81. . 

82.: 

82. I 

8l.: 

81 

81.! 

81.' 

80 . . 

80 .. 

80. ! 

80 .. 

79 . 

80 .. 

79. : 

80 .. 

80. 

79 .. 

80 .. 

80. 

81. 1 

81.-

80 . . 

80. 

81.: 

80 .. 

81.1 

80. 

81 

81. . 

81. . 

81. . 

PagE 
Group#-Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/11 /2013 17:18 

02/11/2013 17:19 

02/11/2013 17:20 

02/11/2013 17:21 

02/11/2013 17:22 

02/11/2013 17:23 

02/11/2013 17:24 

02/11/2013 17:25 

02/11/2013 17:26 

02/11/2013 17:27 

02/11/2013 17:28 

02/11/2013 17:29 

02/11/2013 17:30 

02/11/2013 17:31 

02/11/2013 17:32 

02/11/2013 17:33 

02/11/2013 17:34 

02/11/2013 17:35 

02/11/2013 17:36 

02/11/2013 17:37 

02/11/2013 17:38 

02/11/2013 17:39 

02/11/2013 17:40 

02/11/2013 17:41 

02/11/2013 17:42 

02/11/2013 17:43 

02/11/2013 17:44 

02/11/2013 17:45 

02/11/2013 17:46 

02/11/2013 17:47 

02/11/2013 17:48 

02/11/2013 17:49 

02/11/2013 17:50 

02/11/2013 17:51 

02/11/2013 17:52 

02/11/Z013 17: 53 

02/11/2013 17:54 

02/11/ 20 13 17:55 

02/11/2013 17:56 

02/11/2013 17:57 

Date/Time Printed: 

G34 -C2 G34-C4 G34-C11 

4>Stk NOx 

St k NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 

2.5 

2.5 

2.4 

2.3 

2.4 

2.5 

2.6 

2.5 

2.5 

2.5 

2.6 

2.5 

2.5 

2.4 

2.5 

2.7 

2.7 

2.7 

2.7 

2.6 

2.7 

2.7 

2.7 

2.7 

2.6 

2.5 

2. ' 

2.7 

2.5 

2.9 

2.9 

2.8 

2.8 

2.7 

2.6 

2.6 

2.7 

2.7 

2.7 

2.7 

Stk 02 

\ 

0-25 

13.56 

13.56 

13.56 

13.57 

13.56 

13 . 57 

13 . 5 8 

13 . 58 

13. 58 

13.56 

13.55 

13.56 

13.56 

13.57 

13.57 

13.55 

13.55 

13.56 

13.55 

13.55 

13.55 

13.54 

13.55 

13.55 

13 . 56 

13.56 

13.58 

13.57 

13.57 

13.58 

13.58 

13.58 

13.57 

13.58 

13.59 

13.58 

13.58 

13.57 

13.57 

13.57 

02/11/2013 19,08 

NOx Mass 

Ib/hr 

0 -10 0 

5.18 

5.18 

5.17 

5.16 

5.17 

5.16 

5.90 

5.15 

5.14 

5.15 

5.90 

5.14 

5.14 

5.12 

5.11 

5.84 

5.84 

5.83 

5.86 

5.85 

5.85 

5.86 

5.85 

5.86 

5.85 

5.13 

5.09 

5.85 

5.10 

6.57 

6.56 

5.84 

5.84 

5.82 

5.81 

5.80 

5.80 

5.82 

5.82 

5.81 

G34-C20 

4>StkFlow 

StkFlow 

kscfh 

0-300000 

18359 

18356 

18332 

18295 

18332 

18310 

18329 

18281 

18260 

18251 

18265 

18212 

18193 

18157 

18123 

18083 

18072 

18059 

18128 

18115 

18111 

18127 

18108 

18144 

18145 

18159 

18096 

18166 

18107 

18151 

18140 

18138 

18140 

18099 

18072 

18031 

18027 

18071 

18059 

18044 

G34-C3 

4>Stk CO 

Stk CO 

ppm 

0-1000 

1.1 

1.0 

1.1 

1.1 

1.1 

1.1 

1.1 

1.2 

1.3 

1.3 

1.2 

1.3 

1.3 

1.3 

1.5 

1.5 

1.5 

1.5 

1.5 

1.3 

1.3 

1.3 

1.3 

1.4 

1.3 

1.3 

1.. 

1.4 

1.4 

1.4 

1.5 

1.4 

1.4 

1.5 

1.6 

1.7 

1.6 

1.6 

1.4 

1.4 

G34-C13 G34-C10 G3 4 -C6 

4>CO Mass 4>NOx Rate 4>Stk NOXc 

CO Mass 

1b/hr 

0-100 

1.48 

1.48 

1. 48 

1. 47 

1.48 

1. 47 

1.47 

1.47 

1.47 

1.47 

1.48 

1.47 

1.47 

1.46 

2.19 

2.19 

2.19 

2.18 

2.20 

1.46 

1.46 

1. 47 

1. 46 

2.20 

1. 46 

1. 46 

2.18 

2.19 

2.19 

2.19 

2.19 

2.19 

2.19 

2.18 

2.18 

2.18 

2 . 17 

2.18 

2.18 

2.18 

NOx Rate 

Ib/mmBtu 

0-1 

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 

0.007 

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 

0.007 

0.009 

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 

2.01 

2.01 

1. 93 

1. 85 

1. 93 

2.01 

2.10 

2.02 

2.02 

2.01 

2.09 

2.01 

2.01 

1. 93 

2.01 

2.17 

2.17 

2.17 

2.17 

2.09 

2.17 

2.16 

2.17 

2 . 17 

2.09 

2.01 

1. 93 

2.17 

2.01 

2.34 

2.34 

2.26 

2.25 

2.18 

2.10 

2.10 

2.18 

2.17 

2.17 

2.17 

G34-C7 G34 -C8 

4>Stk COc 4>Gas Flow 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.88 

0.80 

0.88 

0 . 89 

0.88 

0.89 

0.89 

0.97 

1. 05 

1. 04 

0 . 96 

1. 04 

1. 04 

1. 05 

1. 21 

1.20 

1.20 

1.21 

1.20 

1. 04 

1. 0 4 

1. 04 

1. 04 

1.12 

1. 04 

1. 04 

1.13 

1.13 

1.13 

1.13 

1. 21 

1.13 

1.13 

1.21 

1.29 

1.37 

1.29 

1. 29 

1.13 

1.13 

7050.0 

7048.8 

7039.8 

7015.8 

7039.8 

7021. 8 

7019.4 

7000.8 

6993.0 

7008.6 

7023.6 

6993.6 

6986.4 

6963.0 

6949.8 

6953.4 

6949.2 

6934.8 

6970.8 

6966.0 

6964.2 

6979.8 

6963.0 

6976.8 

6967.8 

6973.2 

6930.0 

6966.6 

6943.8 

6951.0 

6946.8 

6946.2 

6956.4 

6931. 2 

6911.4 

6905.4 

6903.6 

6930.0 

6925.2 

6919 . 8 

G34 - C18 

4 >NH3 Inj 

NH3Inj 

lb/ hr 

0 - 200 

119.8 

119.8 

119.8 

118.7 

118.3 

118.3 

117.2 

115.5 

115.2 

115 .8 

117.5 

116.0 

ll4.8 

116.7 

112.3 

111.8 

111.0 

111.0 

112.0 

114. a 

114.3 

114.5 

113.3 

115.0 

114.5 

114.8 

112.5 

114.7 

112.0 

109.7 

111.2 

109.5 

111. 8 

110. a 

109.5 

109.5 

110.7 

109 . 2 

ll1.8 

112.0 

4>Summary - I-Min RATA - Continued 

G34-C 

4>MW Lo 

MW Lo 

0-1 

82. t 

81. ! 

81. 

82. 1 

82. 1 

81. 

81.' 

81. 

80 .. 

81.: 

81. : 

81.: 

81.: 

80 . . 

80 .. 

80. ! 

80.: 

79. 1 

80. : 

80 .. 

80 . . 

80.: 

80. ! 

80. : 

80. : 

80 .. 

79 

80.1 

79. 1 

80. ! 

80 .: 

80 .. 

80. 

79. 

79. 

79 . . 

79.: 

79. : 

79 .. 

80.1 

Pag{ 
Group#-Channel# 

Long Descrip . 

Short Descrip. 

Units 

Range 

02/11/2013 17:58 

02/11/2013 17:59 

02/11/2013 18:00 

02/11/2013 18:01 

02/11/2013 18:02 

02/11/2013 18:03 

02/11/2013 18:04 

02/11/2013 18:05 

02/11/2013 18:06 

02/11/2013 18:07 

02/11/2013 18:08 

02/11/2013 18:09 

02/11/2013 18:10 

02/11/2013 18:11 

02/11/2013 18:12 

0 2 /11/2013 18:13 

02/11/2013 18:14 

02/11/2013 18:15 

02/11/2013 18:16 

02/11/2013 18:17 

02/11/2013 18 : 18 

02/11/2013 18:19 

02/11/2013 18:20 

02/11/2013 18:21 

02/11/2013 18;22 

02/11/2013 18:23 

02/11/2013 18:24 

02/11/2013 18:25 

02/11/2013 18:26 

02/11/2013 18:27 

02/11/2013 18:28 

02/11/2013 18:29 

02/11/2013 18:30 

02/11/2013 18:31 

02/11/2013 18:32 

02/11/2013 18:33 

02/11/2013 18:34 

02/11/2013 18:35 

02/11/2013 18:36 

02/11/2013 18:37 

Date/Time Printed: 

G34 - C2 G34 - C4 G34-C11 G34-C20 

4>Stk NOx 

Stk NOx 

4>Stk 02 4>NOx Mass 4>StkFlow 

ppm 

0-150 

2.6 

2.6 

2.5 

2.5 

2.6 

2. 5 

2.5 

2.6 

2.5 

2.5 

2.5 

2.5 

2.7 

3.1 

3.1 

3.1 

2.9 

3.0 

3.0 

2.8 

2.8 

2.8 

2.B 

2.7 

2.6 

2.6 

2.7 

2.8 

2.7 

2.7 

2 . 6 

2.5 

2.5 

2.5 

2.5 

2.5 

2.7 

2.7 

2.7 

2.8 

Stk 02 

• 

0-25 

13 .57 

13.58 

13.58 

13.58 

13 .5 7 

13.56 

13.57 

13.57 

13.57 

13.57 

13.57 

13 . 56 

13 . 56 

13.56 

13 . 56 

13.57 

13.57 

13.58 

13.58 

13.57 

13.58 

13 . 58 

13.58 

13.58 

13.59 

13.59 

13.59 

13.5 9 

13.59 

13.59 

13.58 

13 .60 

13.60 

13.59 

13.59 

13.59 

13 . 58 

13.59 

13.59 

13.59 

02/11/2013 19,08 

NOx Mass 

1b/hr 

0-100 

5.80 

5.79 

5.06 

5.06 

5.80 

5.10 

5.08 

5.82 

5.08 

5.09 

5.09 

5.09 

5.82 

6.55 

6.57 

6.54 

6.55 

6.53 

6.55 

5.83 

5.81 

5.82 

5.82 

5.82 

5.82 

5.83 

5.83 

5.82 

5.82 

5.83 

5.83 

5.09 

5.08 

5.09 

5.09 

5 . 07 

5.81 

5.80 

5.80 

5.80 

StkFlow 

kscfh 

0-300000 

17999 

17988 

17984 

17963 

18016 

18067 

18038 

18054 

18038 

18055 

18046 

18021 

18054 

18064 

18093 

18054 

18073 

18055 

18111 

18087 

18064 

18097 

18107 

18093 

18103 

18146 

18141 

18127 

18111 

18161 

18110 

18123 

18103 

18092 

18091 

18050 

18058 

18069 

18061 

18058 

G34 -C3 G34-C13 G34 - C10 G34 - C6 G34-C7 G34-C8 G34 -C18 G34-C 

4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXe 4>Stk COe 4>Gas Flow 4>NH3 Inj 4>MW Lo 

Stk co 

ppm 

0-1000 

1.5 

1.6 

1.6 

1.7 

1.7 

1.4 

1. 4 

1.5 

1.5 

1.5 

1.5 

1.4 

1.4 

1.4 

1.4 

1.4 

1.5 

1.5 

1.5 

1.5 

1.5 

1.5 

1.6 

1.6 

1.6 

1.6 

1.6 

1.7 

1.7 

1.6 

1.6 

1.7 

1.8 

1.8 

1.7 

1.6 

1.8 

1.7 

1.9 

1.8 

CO Mass 

1b/hr 

0-100 

2.17 

2.17 

2.17 

2.17 

2 .18 

2.19 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.19 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.18 

2.19 

2.19 

2.18 

2.18 

2 .19 

2.18 

2.18 

2.18 

2.18 

2.18 

2.17 

2.18 

2.18 

2.18 

2.18 

NOx Rate 

Ib/mmBtu 

0-1 

0.008 

0.008 

0.007 

0.007 

0 . 008 

0.007 

0.007 

0.008 

0.007 

0.007 

0.007 

0.007 

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 

0.008 

0.008 

0.008 

0 . 008 

0.007 

0 . 007 

0.007 

0.007 

0.007 

0.008 

0 . 008 

0.008 

0.008 

Stk NOXe 

ppm 

0-300 

2.09 

2.10 

2.02 

2.02 

2.09 

2.01 

2.01 

2.09 

2.01 

2.01 

2.01 

2.01 

2 . 17 

2.49 

2.49 

2.50 

2.33 

2.42 

2.42 

2.25 

2.26 

2.26 

2.26 

2.18 

2.10 

2 . 10 

2 . 18 

2.26 

2.18 

2.18 

2.10 

2.02 

2.02 

2.02 

2.02 

2.02 

2.18 

2.18 

2.18 

2.26 

Stk COe Gas hscfh 

ppm hscfh 

0-1000 0-10000 

1.21 

1.29 

1.29 

1.37 

1.37 

1.13 

1.13 

1. 21 

1.21 

1.21 

1. 21 

1.13 

1.13 

1.13 

l.13 

1.13 

l. 21 

1. 21 

1. 21 

1. 21 

1. 21 

1.21 

1. 29 

1.29 

1.29 

1. 29 

l. 29 

1. 37 

1. 37 

1. 29 

1. 29 

1. 37 

1. 45 

1. 45 

1. 37 

1.29 

1.45 

1.37 

1. 53 

1.45 

6902.4 

6888.6 

6887.4 

6879.0 

6909.0 

6937.8 

6917.4 

6923.4 

6917.4 

6924.0 

6920.4 

6920.4 

6933.0 

6936.6 

6948.0 

6923 . 4 

6930.6 

6914.4 

6936.0 

6936 .0 

6918.0 

6930.6 

6934.2 

6928 . 8 

6923.4 

6939.6 

6937.8 

6932.4 

6926.4 

6945.6 

6935.4 

6921. 6 

6913.8 

6919.2 

6918.6 

6903.0 

6915 .6 

6910.2 

6907.2 

6906.0 

NH3Inj 

Ib/hr 

0-200 

109.7 

110.7 

109.2 

110.7 

109.2 

113.0 

112.2 

112.8 

113 .2 

110.7 

111. 7 

113.8 

109.8 

109.0 

108.2 

108.2 

108.5 

109.0 

108.7 

110 .8 

110.0 

110.8 

111.8 

110.8 

111.3 

111 .2 

112 . 5 

111. 2 

110 . 7 

111. 8 

111 .8 

112.0 

110.2 

111.2 

111.0 

112.2 

109.5 

109.7 

109.2 

109 . 7 

4>Summary - I-Min RATA - Continued 

MW Lo 

0-1 

79 . . 

79. ! 

78 . . 

79. : 

79 . 

79. 

79. 

80. ( 

79. 

80 . : 

79. 

79 . : 

80. : 

79 .. 

80. ! 

80. ( 

80 . ( 

79 . . 

80 .. 

79 . ~ 

79. ! 

79.: 

80 . ( 

80. ( 

80. ( 

79 . . 

80.: 

80.: 

79 .. 

80 . ~ 

80.1 

79.: 

79 . ~ 

79 .. 

79 .. 

79 . ~ 

79. 

79. : 

80. ( 

79.: 

PagE 
Group#-Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/11/2013 18:38 

02/11/2013 18:39 

02/11/2013 18:40 

02/11/2013 18 :41 

02/11/2013 18:42 

02/11/2013 18:43 

02/11/2013 18:44 

02/11/2013 18 : 45 

02/11/2013 18:46 

02/11/2013 18:47 

02/11/2013 18:48 

02/11/2013 18:49 

02/11/2013 18:50 

02/11/2013 18:51 

02/11/2013 18:52 

02/11/2013 18:53 

02/11/2013 18:54 

0 2 /11/2013 18:55 

02/11/2013 18:56 

Period Average 

Period Max Value 

Period Min Value 

Period Totals = 

Period % Recovery 

Date/Time Printed: 

G34-C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

2.8 

2.7 

2.6 

2.6 

2.6 

2.6 

2.6 

2 . 5 

2.6 

2.5 

2.4 

2.7 

2.8 

2.8 

2.7 

2.7 

2.4 

2.7 

2.7 

2.5 

3 . 1 

1.7 

G34-C4 G34 -C11 G34-C20 

4>stk 02 4>NOx Mass 4>StkFlow 

Stk 02 

• 

0-25 

13.58 

13.58 

13.58 

13.58 

13.58 

13.58 

13.58 

13.58 

13.58 

13.58 

13.58 

13 . 59 

13.59 

13.58 

13.59 

13.58 

13.59 

13.59 

13.59 

13.55 

13.60 

13.50 

NOx Mass 

1b/hr 

0-100 

5.81 

5.80 

5.81 

5.80 

5.80 

5.80 

5 . 82 

5.07 

5.81 

5.08 

5.08 

5.80 

5.81 

5.82 

5.81 

5.80 

5.06 

5.79 

5.80 

5.28 

6.66 

3.66 

StkFlow 

kscfh 

0-300000 

18055 

18025 

18050 

18033 

18041 

18025 

18088 

18006 

18066 

18058 

18030 

18061 

18078 

18080 

18075 

18039 

18014 

18037 

18040 

18145 

18379 

17963 

G34 - C3 G34-C13 G34-C10 G34-C6 G34-C7 G34-C8 G34-C18 G34-C 

4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXe 4>Stk COe 4>Gas Flow 4>NH3 Inj 4>MW Lo 

Stk CO 

ppm 

0-1000 

1.7 

1.7 

1.7 

1.6 

1.8 

1.7 

1.6 

1.7 

1.6 

1.6 

1.7 

1.9 

1.8 

1.7 

1.7 

1.8 

2.0 

1.9 

1.9 

1.4 

2 . 7 

0.5 

CO Mass 

Ib/hr 

0-100 

2.18 

2.17 

2 . 18 

2.18 

2.18 

2.17 

2.18 

2.17 

2.18 

2.18 

2 . 18 

2 .18 

2 . 18 

2.18 

2.18 

2.18 

2.89 

2.17 

2.17 

1. 90 

3.66 

0.73 

NOx 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 . 008 

0.008 

0.008 

0.008 

0.008 

0.007 

0.008 

0.008 

0.007 

0.009 

0.005 

Stk NOXc 

ppm 

0-300 

2.26 

2.18 

2.10 

2.10 

2.10 

2.10 

2.10 

2.02 

2.10 

2 . 02 

1. 93 

2.18 

2 .2 6 

2.26 

2.18 

2.18 

1. 94 

2.18 

2.18 

1. 98 

2.50 

1. 36 

Stk COe Gas 

ppm 

0-1000 

1.37 

1.37 

1. 37 

1. 29 

1. 45 

1. 37 

1. 29 

1. 37 

1. 29 

1. 29 

1.37 

1. 53 

1.45 

1.37 

1. 37 

1.45 

1. 61 

1. 53 

1. 53 

1.13 

2.16 

0.40 

hsefh 

hscfh 

0 - 10000 

6914.4 

6903.0 

6912.6 

6906.0 

6909.0 

6903.0 

6927.0 

6895.8 

6918.6 

6915.6 

6904.8 

6907.2 

6913.8 

6924.0 

6912.6 

6908.4 

6889.2 

6898.2 

6899.4 

6974 . 0 

7080 . 0 

6879 . 0 

NH3Inj 

1b/hr 

0-200 

111. 3 

1 10 .7 

111. 2 

111.7 

109.7 

111.3 

111.7 

111. 5 

112.7 

112 . 3 

110.7 

108.3 

107.8 

109.2 

109.5 

110 . 3 

108.3 

109.0 

108 . 0 

112.3 

124 . 2 

107.8 

MW Lo 

0-1 

79 .. 

79 .. 

80 .. 

79 .. 

78. : 

80. ! 

79 . . 

79.! 

79. 

79 . . 

79.: 

79 

79. 

79 .. 

79. 

80. ! 

79. ! 

79. : 

79. : 

80.5 

83. 

78. 

6.1250E+2 3.3748E+3 1.3141E+3 4.S182E+6 3.5200E+2 4.7350E+2 1.7950E+0 4.9208E+2 2.8244E+2 1. 7365E+6 2.7964E+4 2.0066E+ 

100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100. 

02/11/2013 19,08 4>Summary - I-Min RATA - Continued PagE 
Data Summary Report 

Company : CPV Sentinel, LLC 

62575 Powerline Road 

Source: 

Data Group : 

Report Name : 

Start of Report: 

Desert Hot Springs, CA 92240 

Turbine 4 

4>!-Min Cales 

4>Summary - I-Min RATA 

02/12/2013 11,45 

StM1"'-\ L{ 

0"\ 7rflo 

End of Report, 02/12/2013 15,52 

G34-C4 G34 - Cll G34 -C2 0 G34-C3 G34-C13 

TRACE 

Environmental S ystems, IIIC. 

Validation : All Available Data 

Group#-Channel# G)4-CIO G34-C6 G34-C7 G34-CB G34-C18 G34 -C 

Long Descrip . 

Short Descrip. 

Units 

G34-C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 4>StkFlow 4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk CDc 4>Gas Flow 4>NH) Inj 4>MW La 

Range 

02/12/2013 11:45 

02/12/2013 11:46 

02/12/2013 11:47 

02/12/2013 11:48 

02/12/2013 11:49 

02/12/2013 11:50 

02/12/2013 11:51 

02/12/2013 11:52 

02/12/2013 11:53 

02/12/2013 11:54 

02/12/2013 11:55 

02/12/2013 11:56 

02/12/2013 11:57 

02/12/2013 11:58 

02/12/2013 11:59 

02/12/2013 12:00 

02/12/2013 12:01 

02/12/2013 12:02 

02/12/2013 12:03 

02/12/2013 12:04 

02/12/ 2 013 12:05 

02/12/2013 12:06 

02/12/2013 12:07 

02/12/2013 12:08 

02/12/2013 12;09 

02/12/2013 12:10 

02/12/2013 12:11 

02/12/2013 12:12 

02/12/2013 12:13 

02/12/2013 12:14 

Date/Time Printed: 

2.' 

2.G 

2.5 

2.5 

2.3 

2.2 

2.0 

loG 

1.5 

loG 

loG 

1.5 

1.5 

loG 

loG 

lo G 

loG 

loG 

1.7 

1.7 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.8 

1.8 

1.. 

1.8 

Stk 02 

• 

0-25 

14 .13 

14 .11 

14 .11 

14.10 

14.09 

14.09 

14.09 

14.08 

14.09 

14.08 

14.08 

14.09 

14.09 

14.09 

14.09 

14 .10 

14.10 

14.10 

14.10 

14 .10 

14.09 

14.09 

14.08 

14.08 

14.08 

14.08 

14.08 

14.08 

1 4 .08 

14.09 

02/12/2013 17,44 

NOx Mass 

1b/hr 

0-100 

4.43 

4.48 

4.49 

4.50 

3.95 

3.94 

3.37 

2.82 

2.82 

2.83 

2.83 

2.83 

2.81 

2.82 

2.B1 

2.81 

2.B2 

2.81 

2.82 

2.80 

3 . 38 

3.40 

2.84 

2.83 

2.83 

2.81 

3.39 

3.39 

3.39 

3.3 9 

StkFlow 

kscfh 

0-300000 

14882 

15009 

15034 

15047 

15067 

15037 

15018 

15060 

15088 

15097 

1 5116 

15116 

15040 

15062 

15032 

15049 

15103 

15029 

15078 

14995 

15035 

15165 

15138 

15111 

15116 

15020 

15059 

15081 

15099 

15082 

Stk CO 

ppm 

0-1000 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

D.' 

CO Mass 

Ib/hr 

0-100 

0.55 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.57 

0.57 

0.57 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.57 

0.57 

0.57 

0.57 

0.56 

0.56 

0.57 

0.57 

0.56 

NOx Rate 

Ib/mmBtu 

0-1 

0.008 

0.008 

0.00 8 

0.008 

0.007 

0.00 7 

0.006 

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 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0-300 

2,09 

2.26 

2.17 

2.17 

1. 99 

1. 91 

1. 73 

1. 38 

1. 30 

1. 38 

1. 38 

1.30 

1.30 

1.39 

1. 39 

1. 39 

1. 39 

1. 39 

1. 48 

1. 48 

1. 56 

1. 56 

1.47 

1.47 

1.47 

1. 47 

1. 56 

1. 56 

1. 64 

1. 56 

Stk CDc Gas 

ppm 

hscfh 

hscfh 

0-1000 

0.35 

0.35 

0.35 

0.35 

0.35 

0,35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0-10000 

5271 . 0 

5331. 6 

5340.6 

5353.2 

5368.2 

5357. 4 

5350.8 

5373.6 

5375.4 

53 86.8 

5393.4 

5385.6 

5358,6 

5366.4 

5355.6 

5353.8 

5373.0 

5346.6 

5364 . 0 

5334.6 

5356 . 8 

5403.0 

5401.2 

5391,6 

5393.4 

5359.2 

5373.0 

5380.8 

5387.4 

5373.6 

NH3Inj 

Ib/hr 

0-200 

99 . 0 

101. 8 

101. 3 

101. 3 

1 03 .2 

101,8 

107.S 

111.2 

112.2 

112.0 

112.0 

110.8 

109.S 

109.5 

111.2 

109.5 

109.0 

10B.3 

108.8 

106.3 

106.5 

108.8 

109.3 

108.3 

108.3 

106.7 

107.2 

10S.2 

108.5 

107.3 

MW Lo 

0 - 1 

53. : 

55.1 

55.1 

55.! 

56.1 

55 ' 

55. : 

55.' 

55.: 

55. 

55.' 

55.! 

55. 

55, ' 

55, ! 

55 . . 

55, . 

55.1 

55, ' 

54.: 

55 

55.: 

55, ' 

55. 

55,' 

55. ! 

55.: 

55. : 

56.1 

55.: 

Pag( 
Group#-Channe l# 

Long Desc rip . 

Short Descrip . 

Units 

Range 

02/12/2013 12:15 

02/12/2013 12:16 

02/12/2013 12:17 

02/12/2013 12:18 

02/12/2013 12:19 

02/12/2013 12:20 

02/12/2013 12:21 

02/12/2013 12:22 

02/12/2013 12:23 

02/12/2013 12:24 

02/12/2013 12:25 

02/12/2013 12:26 

02/1 2 /2013 12:27 

02/12/2013 12:28 

02/12/2013 12:29 

02/12/2013 12:30 

02/12/2013 12:31 

02/12/2013 12:32 

02/12/2013 12:33 

02/12/2013 12:34 

02/12/2013 12:35 

02/12/2013 12:36 

02/12/2013 12:37 

02/12/2013 12:38 

02/12/2013 12:39 

02/12/2013 12:40 

02/12/2013 12:41 

02/12(2013 12:42 

02(12(2013 12:43 

02(12(2013 12:44 

02/12/2013 12:45 

02/12(2013 12:46 

02(12/2013 12:47 

02(12(2013 12:48 

02(12/2013 12:49 

02/12(2013 12:50 

02/12/2013 12:51 

02/12/2013 12:52 

02/1 2 /2013 12:53 

02/12/2013 12:54 

Date/Time Printed: 

G34-C2 G34 -C4 G34 -C11 

4>Stk NOx 

Stk NOx 

ppm 

0 - 150 

4>Stk 02 4>NOx Mass 

1.8 

1.7 

1.8 

1.9 

1.9 

1.9 

1.9 

1.9 

2.0 

1.9 

1.9 

1.9 

1.9 

2.0 

2.0 

2.1 

2.2 

2 . 4 

2.6 

2.4 

2.6 

2.7 

2.4 

2.6 

2.7 

2.5 

2.4 

2.5 

2 .5 

2.5 

2.5 

2.4 

2.4 

2.4 

2.2 

2.8 

2.9 

3.2 

3.0 

2.9 

Stk 02 

• 

0-25 

14.09 

14.10 

14 .10 

14 .10 

14.10 

14 . 1 0 

14.09 

14.08 

14.09 

14.09 

14.08 

14.09 

1 4. 09 

14 . 09 

14.09 

14. 09 

14 . 09 

14 .10 

14 . 08 

14.09 

14.09 

14.08 

14.09 

14.09 

14.09 

14.09 

14.09 

14 . 08 

14 . 09 

14.09 

14.08 

14.08 

14.09 

14.09 

14.09 

14.09 

14.10 

14.09 

14 . 10 

14 . 09 

02/12/2013 17,44 

NOx Mass 

1b/hr 

0-100 

3.38 

2.81 

3.37 

3.37 

3.37 

3.37 

3.36 

3.36 

3.36 

3.35 

3.34 

3.35 

3.36 

3.3 4 

3.35 

3.91 

3.92 

4.48 

4.49 

4.47 

4.46 

5.03 

4. 45 

4.45 

5.04 

4.46 

4.45 

4.46 

4 . 45 

4.46 

4.47 

4.48 

4.47 

4.47 

3.90 

5.01 

5.00 

5.57 

5.56 

5.02 

G34-C20 

4>StkFlow 

StkFlow 

kscfh 

0-300000 

15074 

15034 

15054 

15044 

15037 

15035 

14978 

14951 

14966 

14941 

14877 

14907 

14953 

14890 

14909 

14922 

14960 

15007 

14995 

14934 

14907 

14906 

14855 

14877 

14981 

14912 

14853 

14885 

14880 

14899 

14926 

14954 

14949 

14938 

14884 

14872 

14867 

14889 

14877 

14912 

G34 -C3 

4>Stk CO 

Stk .CO 

ppm 

0-1000 

0.4 

0.4 

0.4 

0.5 

0.5 

0.5 

0.5 

0.4 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.4 

0.4 

0.4 

0.4 

0.5 

0.4 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.4 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

G34 -Cl3 G34 -C10 G34 - C6 

4>CO Mass 4>NOx Rate 4>Stk NOXc 

co Mass 

1b/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 

0.56 

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 

NOx Rate 

Ib/mmBtu 

0-1 

0.006 

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 

0.007 

0.007 

0.008 

0.008 

0.008 

0.008 

0.009 

O.OOS 

O.OOS 

0.009 

0.008 

O.OOS 

0.008 

O.OOS 

O.OOS 

0.008 

0.008 

0.008 

0.008 

0.007 

0.009 

0.009 

0.010 

0.010 

0.009 

Stk NOXc 

ppm 

0-300 

1. 56 

1. 4S 

1. 56 

1. 65 

1.65 

1. 65 

1. 65 

1. 64 

1. 73 

1. 65 

1. 64 

1. 65 

1. 65 

1. 73 

1. 73 

1. S2 

1. 91 

2.08 

2.25 

2.08 

2.25 

2.34 

2.08 

2.25 

2.34 

2.17 

2.0S 

2.16 

2.17 

2.17 

2.16 

2.08 

2.08 

2.08 

1. 91 

2.43 

2.52 

2.77 

2.60 

2.51 

G34-C7 G34-C8 G34-C18 

4>Stk COc 4 >Gas Flow 4>NH3 Inj 

Stk COc Gas hscfh NH3Inj 

ppm hscfh Ib/hr 

0-1000 0-10000 0-200 

0.35 

0.35 

0.35 

0.43 

0.43 

0.43 

0.43 

0.35 

0.43 

0.43 

0.43 

0.43 

0. 4 3 

0.43 

0.43 

0.43 

0.35 

0 . 35 

0.35 

0.35 

0.43 

0.35 

0.43 

0.43 

0.43 

0.43 

0.43 

0 . 43 

0 . 43 

0.43 

0.43 

0.35 

0.43 

0 .4 3 

0.43 

0.43 

0.43 

0.43 

0.43 

0.43 

5370.6 

5348.4 

5355.6 

5352.0 

5349.6 

5349.0 

5336 . 4 

5334.6 

5332.2 

5323.2 

5308.2 

5311.2 

5327 . 4 

5305.2 

5311.8 

5316 . 6 

5329.8 

5338 .8 

5350.2 

5320.S 

5311.2 

531S.4 

5292 . 6 

5300.4 

5337.6 

5313.0 

529 2 .0 

5311.2 

5301.6 

5308.2 

5325.6 

5335.8 

5326 . 2 

5322 . 0 

5302.8 

5298.6 

5289.0 

5304.6 

5292 . 6 

5313.0 

106.5 

105.3 

105 .2 

105.7 

103.5 

104.3 

104.7 

103 . 7 

102.8 

103.8 

102.2 

101.5 

102. 2 

101.7 

101.7 

102.7 

100.5 

98 . 3 

99.0 

98.0 

97.5 

98.0 

97 . 7 

96 . 5 

98.5 

97.3 

97.2 

96. 7 

97 . 8 

97.7 

97.8 

99.3 

99.2 

99 .2 

97.5 

93.S 

92.2 

93 . 2 

92 . 3 

95.0 

4>Summary - I-Min RATA - Continued 

G34-C 

4>MW Lo 

MW Lo 

0-1 

55 . ~ 

5S . ~ 

55 . 

S5. t 

55. t 

54 

55.1 

54. 

55.1 

54. : 

54. : 

54. : 

55.1 

54. : 

54. : 

54 . . 

55.1 

55 . 1 

55.: 

54. 

54. 1 

54. : 

54. : 

54. : 

S4 .. 

54.1 

S4.1 

54 .. 

54.! 

54.: 

54. 

55.1 

54.1 

54.' 

54.: 

54.' 

54.' 

5 4. ' 

53 

54.' 

PagE 
Group#-Channel# 

Long Descrip . 

Short Descrip. 

units 

Range 

02/12/2013 12:55 

02/12/2013 12:56 

02/12/2013 12:57 

02/12/2013 12:58 

02/12/2013 12:59 

02/12/201) 1):00 

02/12/2013 13:01 

02/12/2013 13:02 

02/12/2013 13:03 

02/12/2013 1):04 

02/12/2013 13:05 

02/12/2013 13:06 

02/12/2013 13:07 

02/12/2013 13:08 

02/12/2013 13:09 

02/12/2013 13:10 

02/12/2013 13:11 

02/12/2013 13:12 

02/12/2013 13:13 

02/12/2013 13:14 

02/12/2013 13:15 

02/12/2013 13:16 

02/12/2013 13:17 

02/12/2013 13:18 

02/12/2013 13:19 

02/12/2013 13;20 

02/12/2013 13:21 

02/12/2013 13:22 

02/12/2013 13:23 

02/12/2013 13;24 

02/12/2013 13:25 

02/12/2013 13:26 

02/12/2013 13:27 

02/12/2013 13:28 

02/12/2013 13:29 

02/12/2013 13:30 

02/12/2013 13:31 

02/12/2013 13:32 

02/12/2013 13:33 

02/12/2013 13;34 

Date/Time Printed: 

G)4 - C2 G34-C4 G34 - Cll 

4>Stk NOx 

Stk NOx 

4>Stk 02 4>NOx Mass 

ppm 

0-150 

3.1 

2.9 

2.B 

3.0 

2.7 

2.B 

2.G 

2.7 

2.B 

2.5 

2.G 

2.5 

2.5 

2.4 

2.5 

2.5 

2.5 

2.4 

2.5 

2.3 

2.5 

2.4 

2.4 

2.4 

2.3 

2.2 

2.2 

loB 

loG 

loG 

l.5 

1.7 

1.7 

l.7 

loB 

loG 

loB 

1.9 

1.B 

1.7 

Stk 02 

t 

0-25 

14.08 

14.09 

14.08 

14.08 

14.08 

14.06 

14.07 

14 . 06 

14.06 

14.06 

14.06 

14.06 

14.05 

14.06 

14.06 

14.05 

14. as 

14.06 

14.06 

14.06 

14. 07 

14.06 

14 . 07 

14 . 06 

14. 07 

14.07 

14.06 

14.07 

14.07 

14.07 

14. 07 

14.07 

14. 07 

14.06 

14.06 

14. 07 

14.06 

14 . 06 

14.06 

14 . 07 

02/12/2013 17,44 

NOx Mass 

Ib/hr 

0 - 100 

5.61 

5.03 

5.02 

5.60 

5.04 

5.06 

4.51 

5.09 

5.09 

4.52 

4.53 

4.54 

4.55 

4.53 

4.53 

4.54 

4.53 

4.53 

4.54 

3 . 95 

4.51 

4.51 

4.49 

4.49 

3.92 

3.92 

3.91 

3.36 

2.80 

2.81 

2.80 

2.80 

2.79 

2.79 

3.37 

2.79 

3.36 

3.38 

3.37 

2.79 

G)4-C20 

4>StkFlow 

StkFlow 

kscfh 

0-300000 

14973 

14953 

14887 

14936 

14936 

14964 

15010 

15048 

15046 

15036 

15058 

15098 

15115 

15080 

15083 

15085 

15060 

15058 

15103 

15008 

15011 

14998 

14964 

14941 

14934 

14919 

14877 

14916 

14939 

14964 

14911 

14902 

14874 

14832 

14936 

14880 

14896 

14969 

14951 

14891 

G34-C3 

4 >Stk CO 

Stk CO 

ppm 

0 - 1000 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.5 

0.5 

0.5 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

G34 - C13 G34 -CI0 G34 - C6 

4>CO Mass 4>NOx Rate 4>Stk NOXc 

CO Mass 

lb/hr 

0-100 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

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 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

NOx Rate 

Ib/mmBtu 

0-1 

0.010 

0.009 

0.009 

0.010 

0.009 

0.009 

0.008 

0.00 9 

0.009 

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 

0.007 

0.007 

0.007 

0.006 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.005 

0.006 

0.006 

0.006 

0.005 

stk NOXc 

ppm 

0 - 300 

2.68 

2.51 

2.42 

2.60 

2.34 

2.42 

2.25 

2.33 

2.42 

2.16 

2.24 

2.16 

2.15 

2.07 

2.16 

2.15 

2.15 

2.07 

2.16 

1. 98 

2.16 

2.07 

2.07 

2.07 

1. 99 

1. 90 

1. 90 

1. 55 

1. 38 

1. 38 

1.30 

1.47 

1.47 

1.47 

1. 55 

1. 38 

1. 55 

1. 64 

1. 55 

1. 47 

G34-C7 G34-C8 

4>Stk COc 4>Gas Flow 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.43 

0.43 

0.43 

0.43 

0.43 

0.43 

0.43 

0.35 

0 . 35 

0.35 

0.35 

0.35 

0.34 

0.35 

0.35 

0.34 

0.34 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0 . 35 

0.35 

0.35 

0.43 

0.43 

0.43 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0.35 

0 . 35 

0 . 35 

0.35 

5342.4 

5327.4 

5311.8 

5329.2 

5329.2 

5355.0 

5363.4 

5385.0 

5384.4 

5380.8 

5388.6 

5403.0 

5416.8 

5396.4 

5397.6 

5406.0 

5397.0 

5388.6 

5404.8 

5370.6 

5364.0 

5367.0 

5347.2 

5346.6 

5336.4 

5331.0 

5323.8 

5329.8 

5338.2 

5347.2 

5328.0 

5325.0 

5314.8 

5307.6 

5344.8 

5317.2 

5330.4 

5356.8 

5350.2 

5320.8 

G34 -C18 

4>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

95.0 

94.7 

96.0 

95.5 

96.2 

99.3 

97.3 

100 . 0 

100.0 

101.5 

100.8 

101.7 

103.3 

102.3 

102.8 

103.0 

103.0 

102.8 

103.8 

102.0 

102.5 

102.5 

101.7 

100.2 

101.0 

100.3 

103.0 

108.2 

108.7 

110.2 

109.3 

108.0 

106.7 

108.5 

106.8 

107.7 

107.5 

107.0 

108.5 

107.2 

4>Summary - I-Min RATA - Continued 

G34-C 

4 >MW La 

MW Lo 

0-1 

55. ( 

S5.: 

55.( 

54. : 

54.: 

55.: 

55 .. 

55 . 

55 

55. ! 

55. : 

55. 

56.: 

55 .. 

56.: 

55 .. 

55 .. 

55 .. 

55 .. 

55 .. 

55. : 

55 . . 

54 .. 

55. ( 

55. ( 

54 .. 

54.: 

54 .. 

55. ( 

55. ( 

54. ! 

54 .. 

54. 

54. ( 

S4 .. 

54. 

55. ( 

55 .. 

54. 

54 

pagE 
Group#-Channel# 

Long Descri p . 

Short Descrip . 

units 

Range 

02/12/2013 13:35 

02/12/2013 13:36 

02/12/2013 13:37 

02/12/2013 13:38 

02/12/2013 13:39 

02/12/2013 13:40 

02/12/2013 13:41 

02/12/2013 13:42 

02/12/2013 13:43 

02/12/2013 13:44 

02/12/2013 13:45 

02/12/2013 13:46 

02/1 2 /2013 13:47 

02/12/2013 13 : 48 

02/12/2013 13:49 

02/12/2013 13:50 

02/12/2013 13:51 

Q2/12/2013 13:52 

02/12/2013 13:53 

02/12/2013 13:54 

02/12/2013 13:55 

02/12/2013 13:56 

02/12/2013 13:57 

02/12/2013 13:58 

02/12/2013 13:59 

02/12/2013 14:00 

02/12/2013 14:01 

02/12/2013 1 4 :02 

02/12/2013 14:03 

02/12/2013 14:04 

02/12/2013 14:05 

02/12/2013 14:06 

02/12/2013 14;07 

02/12/2013 14:08 

02/12/ 2013 14:09 

02/12/2013 14:10 

02/12/2013 14:11 

02/12/2013 14:12 

02/12/ 2 013 14 : 13 

02/12/2013 14 : 14 

Date/Time P~inted: 

G34 -C2 G34-C4 G3 4 -C11 G34 -C20 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

4>Stk 02 4>NOx Mass 4>StkFlow 

1.7 

1.8 

1.8 

1.8 

1.9 

1.9 

2.0 

1.8 

1.8 

2.0 

1.9 

1.9 

1.9 

2.1 

1.9 

1.9 

1.9 

2.0 

2.1 

1.9 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.9 

1.9 

1.8 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

2.0 

2.0 

1.8 

1.6 

1.6 

Stk 02 

% 

0-25 

14 . 07 

14.07 

1 4 .07 

14 . 06 

14.06 

14.06 

14.06 

14 . 07 

14.07 

14.07 

14. 07 

14.07 

14.07 

14 . 07 

14 .07 

14.07 

. 14.07 

14.06 

14.05 

14 . 05 

14.05 

14.04 

14.04 

14.04 

14.04 

14.04 

14.03 

14.02 

14.03 

14.03 

14 . 04 

14.04 

14.05 

1 4 .05 

14.05 

14.05 

14.05 

14.04 

14.05 

14.04 

02/12/2013 17,44 

NOx Mass 

lb/hr 

0-100 

2.78 

3.35 

3 . 35 

3.35 

3.36 

3.35 

3.35 

3.34 

3 . 34 

3.33 

3.33 

3.34 

3 . 34 

3.90 

3.34 

3.34 

3.36 

3.36 

3 . 94 

3.39 

3.39 

3.40 

3.40 

3.38 

3.39 

3.38 

3.39 

3.40 

3.40 

3.39 

3.37 

3.36 

3.36 

3.36 

3.35 

3.35 

3.37 

3.36 

2.81 

2.81 

StkFlow 

kscfh 

0-300000 

14810 

14864 

14889 

1 4 857 

14884 

14880 

14880 

14825 

14820 

14805 

14796 

14832 

14 827 

14833 

14835 

14845 

14917 

14897 

1494 6 

15011 

15026 

15034 

15034 

14934 

14976 

14934 

14964 

15007 

15004 

14972 

14921 

14867 

14896 

14860 

14 839 

14845 

14921 

14869 

14907 

14916 

G34-C3 G3 4 -C13 G34-C10 G34-C6 G34-C7 G3 4 -C8 G34 -C18 G34 - C 

4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk COe 4>Gas Flow 4>NH3 Inj 4>MW Lo 

Stk CO 

ppm 

0-1000 

0.5 

0.4 

0.5 

0.4 

0.4 

0.4 

0.4 

0.5 

0.5 

0.5 

0.5 

0.5 

0 . 5 

0.5 

0.4 

0.5 

0.4 

0.4 

0.4 

0.4 

0. 4 

0.4 

0.4 

0.4 

0. 4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0 . 4 

0. 4 

0.4 

0 . 4 

0.4 

0.4 

0.4 

0.4 

0.4 

CO Mass 

lb/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 

0.57 

0.57 

0.57 

0.56 

0.56 

0.56 

0 . 56 

0.57 

0 . 57 

0.57 

0.56 

0 . 56 

0.56 

0.56 

0 . 56 

0.56 

0.56 

0.56 

0.56 

0.56 

NOx Rate 

lb/mmBtu 

0-1 

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 . 007 

0 . 006 

0.006 

0.006 

0.006 

0.007 

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 

0.006 

0 . 006 

0.006 

0.006 

0.006 

0.005 

0.005 

stk NOXe 

ppm 

0-300 

1.47 

1. 55 

1. 55 

1. 55 

1. 64 

1. 64 

1. 73 

1. 55 

1. 55 

1. 73 

1. 64 

1. 64 

1. 64 

1. 81 

1. 64 

1. 64 

1. 64 

1. 73 

1. 81 

1. 64 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 63 

1. 63 

1. 55 

1. 63 

1. 63 

1. 63 

1. 64 

1. 64 

1. 64 

1. 72 

1.72 

1. 55 

1.38 

1. 38 

Stk COe Gas 

ppm 

hsefh 

hsefh 

0-1000 

0.43 

0.35 

0.43 

0.35 

0.35 

0.35 

0 . 35 

0 . 43 

0.43 

0.43 

0.43 

0.43 

0 . 43 

0 . 43 

0.35 

0 . 43 

0.35 

0.35 

0 . 34 

0.34 

0.34 

0.3 4 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.3 4 

0 . 3 4 

0.34 

0.3 4 

0.34 

0.34 

0.3 4 

0.34 

0 . 34 

0.34 

0.34 

0-10000 

5292 . 0 

5311.2 

5320.2 

5316.6 

5326.2 

5325.0 

5325.0 

5297 . 4 

5295.6 

5290.2 

52B7.2 

5299.B 

529B.O 

5300.4 

5301.0 

5304.6 

5330.4 

5331.0 

5356.2 

5379.6 

5385 . 0 

5395.B 

5395.B 

5359.B 

5374.8 

5359 . 8 

537B.4 

5401.8 

5392. B 

5381.4 

5355.0 

5335.B 

5338 . 2 

5325.6 

5317. B 

5320.2 

5347.2 

5336.4 

5342.4 

5353.2 

NH3Inj 

lb/hr 

0-200 

104.8 

105 . 0 

106.7 

105.5 

105.2 

106 . 7 

104.7 

105.5 

103.2 

103.2 

104.5 

103.2 

103 . 7 

104.3 

103.5 

103.7 

104.2 

104.2 

104.2 

109.2 

109.8 

109 . 7 

110 . 8 

109.2 

10B.7 

107.5 

108 . 5 

108.B 

109 . 2 

108.3 

10B.3 

106 . 8 

106.2 

106.3 

104.8 

104.7 

106 . 8 

109.8 

110.B 

110.3 

4>Summary - l-Min RATA - Continued 

MW Lo 

0 - 1 

54. 

55. c 

54 .. 

54. : 

54. : 

54 .. 

54. : 

54. c 

54. c 

54. : 

54.: 

54 .. 

54. c 

54 . . 

5 4 . 

54.: 

55. c 

5 4 .. 

5 4 . : 

55 .. 

55 .. 

55 . ~ 

55. : 

55 . 

55. 

55. ! 

55. ! 

55 .. 

55. 

55 .. 

55 .. 

54 .. 

55. : 

54. : 

54. : 

5 4 . : 

54 . : 

55.: 

55 . . 

55 . . 

pagE 
Group#-Channel# 

Long Descrip. 

Short Descrip . 

Unit s 

Range 

02/12/2013 14:15 

02/12/2013 14:16 

02/12/2013 14:17 

02/12/2013 14:18 

02/12/2013 14:19 

02/12/2013 14:20 

02/12/2013 14:21 

02/12/2013 14;22 

02/12/2013 14:23 

02/12/2013 14:24 

02/12/2013 14:25 

02/12/2013 14:26 

02/12/2013 14 : 27 

02/12/2013 14:28 

02/12/2013 14:29 

02/12/2013 14:30 

02/12/2013 14:31 

02/12/2013 14:32 

02/12/2013 14:33 

02/12/2013 14:34 

02/12/2013 14:35 

02/12/2013 14:36 

02/12/2013 14:37 

02/12/2013 14:38 

02/12/2013 14:39 

02/12/2013 14:40 

02/12/2013 14:41 

02/12/2013 14:42 

02/12/2013 14:43 

02/12/2013 14:44 

02/12/2013 14:45 

02/12/2013 1 4 :46 

02/12/2013 14:47 

02/12/2013 14:48 

0 2 /12/2013 14:49 

02/12/2013 14 : 50 

02/12/2013 14:51 

02/12/2013 14:52 

02/12/2013 14:53 

02/12/2013 14:54 

Date/Time Printed: 

G34-C2 G34 -C4 G34 -C11 G34-C20 

4>Stk NOx 

Stk NOx 

4>Stk 02 4>NOx Mass 4>StkFlow 

ppm 

0-150 

1.6 

1.6 

1.6 

1.7 

1.7 

1.7 

1.8 

1.7 

1.8 

1.7 

1.7 

1.8 

1.8 

1.7 

1.8 

1.8 

1.9 

1.9 

1.9 

2 . 0 

1.8 

1.9 

1.9 

1.9 

1.9 

1.9 

1.8 

1.8 

1.8 

1.7 

1.8 

1.8 

1.8 

1.9 

1.8 

1.8 

1.9 

1.8 

1.9 

1.8 

Stk 02 

• 

0-25 

14.05 

14 . 04 

14.04 

14 . 03 

1 4. 0 4 

14.04 

14.03 

14.04 

14.04 

14.04 

14.04 

14.04 

14.04 

14 . 04 

14.04 

14 . 03 

14 . 04 

14.04 

1 4 .04 

14 . 03 

14.03 

14 . 04 

14.05 

14.05 

14.05 

14.05 

14.04 

14.05 

14 . 04 

14.05 

14 . 04 

14 .04 

14 .04 

14.04 

14.04 

14.04 

14.03 

14 . 03 

14.03 

14.03 

02/12/2013 17,44 

NOx Mass 

lb/hr 

0-100 

2.80 

2.81 

2.81 

2 . 81 

2.81 

2.81 

3.38 

2.81 

3.37 

2.81 

2.80 

3.37 

3.37 

2.80 

3.36 

3.37 

3.36 

3.36 

3.37 

3.38 

3.38 

3.37 

3.37 

3.37 

3.37 

3.38 

3 . 39 

3.38 

3.39 

2.81 

3 . 38 

3.38 

3.38 

3.39 

3 . 39 

3.40 

3 . 40 

3 . 40 

3.40 

3.38 

StkFlow 

kscfh 

0-300000 

14899 

14937 

14899 

14906 

14912 

14929 

14922 

14892 

14892 

14887 

14857 

14887 

14919 

14864 

14881 

14877 

14864 

14852 

14897 

14936 

14911 

14901 

14914 

14912 

14944 

14956 

14981 

14981 

14 974 

14919 

14949 

14956 

14947 

14986 

14993 

15053 

15016 

15019 

1502B 

14931 

G34 -C3 G34 - Cl3 G34-CIO G34-C6 G34 -C7 G34-C8 G34-C18 G34-C 

4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk COc 4>Gas Flow 4>NH3 Inj 4>MW Lo 

Stk CO 

ppm 

0-1000 

0.4 

0. 4 

0.4 

0.4 

0.4 

0.5 

0.4 

0.4 

0.4 

0.4 

0.4 

0 .4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0 . 4 

0.4 

0.4 

0.4 

0.5 

0.5 

0.5 

0.4 

0.4 

0.4 

0.4 

0 . 4 

0.4 

0.4 

0.4 

0. 4 

0 . 4 

0.4 

0.4 

0. 4 

0.4 

0.4 

CO Mass 

lb/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 

0.56 

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 

0.57 

0.57 

0 . 57 

0.57 

0.56 

NOx Rate 

Ib/mmBtu 

0-1 

0.005 

0 . 005 

0 . 005 

0.005 

0.005 

0.005 

0.006 

0.005 

0 . 006 

0.005 

0.005 

0.006 

0.006 

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 

0.006 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0-300 

1. 38 

1. 38 

1. 38 

1. 46 

1. 46 

1. 46 

1. 55 

1. 46 

1. 55 

1.46 

1.46 

1. 55 

1. 55 

1.46 

1. 55 

1. 55 

1. 63 

1. 63 

1. 63 

1. 72 

1. 55 

1. 63 

1. 64 

1. 64 

1. 64 

1. 64 

1. 55 

l.55 

l. 55 

1.46 

1. 55 

l. 55 

l. 55 

1. 63 

1. 55 

1. 55 

l. 63 

1. 55 

1. 63 

1. 55 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.34 5339.4 

0.34 5361 . 0 

0.34 5347.2 

0.34 5357.4 

0.34 5352.0 

0 . 43 5358.0 

0.34 5363.4 

0.34 5344.8 

0 . 34 5344.8 

0.34 5343.0 

0 . 34 5332.2 

0.34 5343.0 

0.34 5354. 4 

0.34 5334.6 

0.34 5340.6 

0.34 5347.2 

0.34 5334.6 

0.34 5330.4 

0.34 5346.6 

0 . 34 5368 . 2 

0.34 5359.2 

0 . 34 5347 . 8 

0.43 5344.8 

0.43 5344.2 

0.43 5355.6 

0.34 5359.8 

0.34 5376.6 

0.34 

0 . 34 

0.34 

0 . 34 

0.34 

0 . 34 

0.34 

0 . 34 

0 . 3 4 

0.34 

0.34 

0.34 

0.34 

5368.8 

5374.2 

5346.6 

5365.2 

5367.6 

5364.6 

5378.4 

5380 . 8 

5402.4 

5397.0 

539B.2 

5401.2 

5366.4 

NH3Inj 

Ib/hr 

0-200 

110.2 

110.2 

1 1 1 . 7 

110.0 

110.2 

109.5 

109.3 

109.2 

107.7 

10B . 5 

107 . 7 

107 . 3 

108.7 

107.7 

106 . 7 

108.3 

106.8 

104.8 

105.8 

106.0 

106 . 8 

106.0 

105 . 0 

105.5 

105.3 

106 . 8 

108 . 0 

108 . 5 

109.0 

108 . 8 

108.3 

10B . 2 

106.8 

108 . 2 

107 . 7 

108.8 

107.3 

108 . 3 

10B . 2 

105.8 

4>Summary - I-Min RATA - Continued 

MW Lo 

0-1 

55. : 

55.1 

55 

55. 

55. ; 

55.1 

55 . ( 

55 . 1 

54 .. 

55.: 

54. ! 

54.: 

55.: 

54.: 

54.: 

55 . : 

54.: 

54.' 

55.1 

55.: 

55.: 

54.: 

55. ' 

54.: 

55 . ' 

55 . : 

55. 

55.1 

55.1 

54.' 

54.: 

55 . 1 

55.: 

55.1 

55.: 

55. ! 

55 .. 

55.! 

55.' 

55.: 

Pag( 
Group#-Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/12/2013 14:55 

02/12/2013 14:56 

02/12/2013 14:57 

02/12/2013 14:58 

02/12/2013 14:59 

02/12/2013 15:00 

02/12/2013 15:01 

02/ 12/2 013 15:02 

02/12/2013 15:03 

0 2 /12/2013 15:04 

02/12/2013 15:05 

02/12/2013 15:06 

02/12/2013 15:07 

02/12/2013 15:08 

02/12/2013 15:09 

02/12/2013 15:10 

02/12/2013 15:11 

02/12/2013 15:12 

02/12/2013 15:13 

02/12/2013 15:14 

02/12/2013 15:15 

02/12/ 2 013 15:16 

02/12/2013 15:17 

02/12/2013 15:18 

02/12/2013 15:19 

02/12/2013 15:20 

02/12/2013 15:21 

02/12/2013 15:22 

02/12/2013 15:23 

02/12/2013 15:24 

02/12/2013 15:25 

02/12/2013 15:26 

02/12/2013 15:27 

02/12/2013 15:28 

02/12/2013 15:29 

02/12/2013 15:30 

02/12/2013 15:31 

02/12 /2013 15:32 

0 2 /12/2013 15:33 

02/12/2013 15:34 

Date/Time Printed: 

G34-C2 G34 -C4 G34-Cl1 

4>Stk NOx 

Stk NOx 

4>Stk 02 4>NOx Mass 

ppm 

0-150 

1.9 

1.9 

2.0 

1.8 

1.9 

2.0 

1.9 

1.9 

2.0 

2.1 

2.0 

2.0 

2.0 

2.0 

2.0 

1.8 

1.8 

1.7 

1.8 

1.8 

1.8 

1.8 

1.9 

1.8 

1.7 

1.9 

1.8 

1.9 

1.9 

1.8 

1.9 

1.9 

1.9 

1.9 

1.8 

1.9 

1.9 

2.0 

1.9 

2.0 

stk 02 

• 

0-25 

14.03 

14.03 

14.03 

14.03 

14 . 05 

14.05 

14.05 

14. OS 

14.05 

14.04 

14.04 

14.05 

14.04 

14.04 

14.03 

14.03 

14.02 

14.02 

14.02 

14.03 

14.03 

14.03 

14 . 03 

14 .03 

14.03 

14.02 

14.03 

14.02 

14.03 

14.03 

14.03 

14.03 

14.03 

14.02 

14 . 03 

14.03 

14 .03 

14. 03 

14 . 03 

14.03 

02/12/2013 17,44 

NOx Mass 

1b/hr 

0-100 

3.39 

3.39 

3.40 

3.37 

3.37 

3.38 

3.36 

3.36 

3.37 

3.95 

3.39 

3.38 

3.38 

3.39 

3.39 

3.38 

3.40 

2.82 

3.37 

3.37 

3.38 

3.39 

3.41 

3.40 

2.82 

3.42 

3.42 

3.41 

3.42 

3.42 

3.41 

3.40 

3.41 

3.42 

3.39 

3.38 

3.39 

3.38 

3.38 

3.38 

G34-C20 

4>StkFlow 

StkF!ow 

kscfh 

0 - 300000 

14964 

14981 

15012 

14891 

14926 

14963 

14870 

14877 

14934 

14991 

14993 

14971 

14966 

15008 

14971 

14939 

14972 

14914 

14861 

14884 

14936 

14989 

15038 

15006 

14954 

15076 

15089 

15059 

15096 

15094 

15054 

15031 

15038 

15072 

14984 

14936 

14964 

14937 

14911 

14936 

G34 -C3 

4>Stk CO 

Stk co 

ppm 

0-1000 

0.5 

0.4 

0.4 

0.4 

0.5 

0.4 

0.5 

0.5 

0.5 

0.5 

0.4 

0.5 

0.5 

0.4 

0.4 

0.5 

0.5 

0.5 

0.5 

0.5 

0.5 

0.4 

0.5 

0 . 4 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

OA 

0.4 

0.4 

0.4 

0.4 

0.4 

0.4 

0 . 5 

0 . 5 

0.5 

G34-C13 G34-CI0 G34-C6 

4>CO Mass 4>NOx Rate 4>Stk NOXc 

CO Mass 

1b/hr 

0-100 

0.56 

0.57 

0.57 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.57 

0.56 

0.56 

0.57 

0.57 

0.56 

0.57 

0.56 

0.56 

0.56 

0.56 

0.57 

0.57 

0.57 

0.56 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.57 

0.56 

0.56 

0.56 

0.56 

0 . 56 

NOx Rate 

Ib/mmBtu 

0-1 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

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 

0.006 

Stk NOXc 

ppm 

0-300 

1. 63 

1. 63 

1. 72 

1. 55 

1. 64 

1. 72 

1. 64 

1. 64 

1. 72 

1. 81 

1. 72 

1. 72 

1. 72 

1.72 

1.72 

1. 55 

1. 54 

1.46 

1. 54 

1. 55 

1. 55 

1. 55 

1. 63 

1. 55 

1. 46 

1. 63 

1.55 

l. 63 

1. 63 

1.55 

1.63 

l. 63 

1. 63 

1. 63 

1. 55 

1. 63 

1. 63 

1. 72 

1. 63 

1. 72 

G3 4 -C7 G34 - C8 

4>Stk CDc 4>Gas Flow 

stk CDc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.43 

0.34 

0.34 

0.34 

0.43 

0.34 

0 . 43 

0 . 43 

0.43 

0.43 

0.34 

0.43 

0.43 

0.34 

0.34 

0.43 

0 . 43 

0.43 

0.43 

0.43 

0.43 

0.34 

0 . 43 

0.34 

0.34 

0.34 

0.3 4 

0.3 4 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.3 4 

0.3 4 

0.34 

0.43 

0.43 

0. 4 3 

5378.4 

5384.4 

5395.8 

5352.0 

5349. a 

5362.2 

5329.2 

5331. 6 

5352.0 

5380.2 

5380.8 

5365.2 

5371.2 

5386.2 

5380.8 

5369.4 

5389.2 

5368.2 

5349.0 

5349.6 

5368.2 

5387.4 

5404 . 8 

5393.4 

5374.8 

5426.4 

5423.4 

5420.4 

5425.8 

5425.2 

5410.8 

5402.4 

5404.8 

5425.2 

5385.6 

5368.2 

5378.4 

5368.8 

5359.2 

5368 . 2 

G34 -C18 

4>NH3 Inj 

NH3Inj 

1b/hr 

0-200 

106.5 

107.7 

108.2 

106.8 

104.3 

104.5 

103.2 

104.0 

103.3 

104.8 

104.5 

105.3 

104.8 

104.8 

106.3 

108.2 

107.8 

108.7 

107.7 

105.8 

108.5 

108.7 

108.0 

108.7 

107.2 

108.7 

108.7 

108.5 

109.0 

108.3 

108.2 

106.2 

106.8 

107.7 

106.3 

106 . 2 

107.0 

105.3 

104.5 

104.0 

4>Summary - I - Min RATA - Continued 

G34-C 

4>MW Lo 

MW Lo 

0-1 

55. : 

55. : 

55. ! 

54. : 

54 .. 

54. : 

54 . 

54. : 

54. : 

55 .. 

55. 

55 . : 

54. : 

55 .. 

55.1 

55 .. 

55 .. 

55.: 

55.: 

55. : 

55 . . 

55 .. 

55. ! 

55.: 

55.: 

56.1 

56.: 

55.' 

55.' 

55. ' 

55. : 

55. ' 

55.: 

56.1 

55.1 

55. ! 

55. ( 

55 . : 

55 .. 

55 . . 

PagE 
Group#-Channel# 

Long Descrip . 

Short Descrip . 

Units 

Range 

02/12/201) 15:35 

02/12/2013 15:36 

02/12/201) 15:37 

02/12/2013 15:38 

02/12/2013 15:39 

02/12/2013 15:40 

02/12/2013 15:41 

02/12/ 2 013 15:42 

02/12/2013 15:43 

02/12/2013 15:44 

02/12/2013 15:45 

02/12/2013 15:46 

02/12/2013 15:47 

02/12/2013 15:48 

02/12/2013 15:49 

02/12/2013 15:50 

02/12/2013 15:51 

02/12/2013 15:52 

Period Average 

Period Max Value 

Period Min Value -

Period Totals = 

Period % Recovery 

Date/Time Printed: 

G34-C2 

4>Stk NOx 

Stk NOx 

ppm 

0-150 

1.9 

2.1 

2.0 

1.9 

2.0 

1.9 

1.8 

1.8 

2.0 

2.0 

2.0 

2.0 

1.9 

2.1 

2.6 

2.7 

3.0 

3.0 

2.0 

3.2 

1.5 

G34-C4 G34 - ell G34-C20 

4>Stk 02 4>NOx Mass 4>StkFlow 

Stk 02 

• 

0-25 

14.03 

14.03 

14.03 

14.04 

14.04 

14.04 

14.04 

14 . 04 

14.04 

14.04 

14.04 

14.03 

14.04 

14.03 

14.03 

14.03 

14.02 

14.03 

14.06 

14.13 

14.02 

NOx Mass 

1b/hr 

0-100 

3.38 

3.96 

3.38 

3.37 

3.38 

3.39 

3.39 

3.37 

3.39 

3.38 

3.39 

3.39 

3.38 

3.95 

4.52 

5.07 

5.11 

5.12 

3.60 

5.61 

2.78 

StkFlow 

kscfh 

0-300000 

14946 

14979 

14906 

14899 

14949 

14991 

15013 

14899 

14974 

14939 

14971 

14966 

14939 

14942 

14959 

14936 

15011 

15061 

14959 

15165 

14796 

G34-C3 G34 -CD G34-CIO G34-C6 G34 - C7 G34 - C8 G34 - C18 G34-C 

4>Stk CO 4>CO Mass 4>NOx Rate 4>Stk NOXc 4>Stk COc 4>Gas Flow 4>NH) Inj 4>MW La 

Stk CO 

ppm 

0-1000 

0.5 

D .• 

D .• 

0.5 

0.5 

0.5 

D .• 

D .• 

D .• 

0.5 

D .• 

D .• 

0.5 

D .• 

0.5 

0.5 

0.5 

D .• 

D .• 

0.5 

D .• 

CO Mass 

1b/hr 

0-100 

0.56 

0.57 

0.56 

0.56 

0.56 

0.56 

0.57 

0 . 56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.56 

0.57 

0.57 

0.56 

0.57 

0 . 55 

NOx Rate 

Ib/mmBtu 

0-1 

0.006 

0.007 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

0.008 

0.009 

0.009 

0.009 

0.006 

0.010 

0.005 

Stk NOXc 

ppm 

0-300 

1. 63 

1. 80 

1. 72 

1. 63 

1. 72 

1. 63 

1. 55 

1. 55 

1. 72 

1. 72 

1. 72 

1. 72 

1. 63 

1. 80 

2.23 

2.32 

2.57 

2.58 

1. 74 

2.77 

1.30 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.43 5371.8 

0.34 5383.8 

0.34 5357.4 

0.43 5347.2 

0.43 5365.2 

0.43 5380.2 

0.34 5388.0 

0 . 34 5347.2 

0.34 5374.2 

0.43 5361.6 

0.34 5373.0 

0.34 5379.0 

0 .43 5361.6 

0.34 5370.6 

0.43 5376.6 

0.43 5368.2 

0.43 5403.0 

0.34 5413.2 

0.37 5354.1 

0.43 5426.4 

0.34 5271.0 

NH3Inj 

1b/hr 

0-200 

105.0 

106.2 

105.5 

104.8 

105.3 

106.8 

106.8 

105.7 

107.0 

105.3 

105.7 

107.3 

103.5 

103.7 

97.8 

97.8 

98.8 

99.3 

105.0 

112.2 

92.2 

MW Lo 

0-1 

55.: 

55. : 

55. : 

5'. 

54. : 

55 .. 

55 .. 

55 

55 

55.1 

55. -

55. 

55.: 

55.: 

54.: 

55.1 

55. 

56.1 

55.0 

56. 

53. 

4.9940E+2 3.4865E+3 8 . 9270E+2 3.7099E+6 1.0730E+2 1.3942E+2 1.5880E+0 4.3087E+2 9.2360E+1 1.3278E+6 2.6040E+4 1.3658E+-

100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100.0 100. 

02/12/2013 17 : 44 4>Summary - I-Min RATA - Continued PagE 
Appendix B.2 Fuel Analysis Data 

R041 0688 8-6 
5aybolt 

A [ORC LAlORATORICS (I"'AIIY 

SAY BOLT LP 

2 1730 S. Wilmington Avenue 

Suite 201 

Carson, CA 90810 

310-518-4400 Telephone 

3 10-518-4455 Facsimile 

Fast To The Point 

SayboIt 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 

2/27/2013 

13091-00008630 

1300169-01 

Sentinel 

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 01945101946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01 945101946 

ASTM 01945/01946 

ASTM 01945101946 

ASTM 01945101946 

ASTM 01945101946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945101946 

ASTM 01945101946 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0 -3588 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0 -3588 

ASTM 0-3588 

Oate Sampled: 2/22/2013 

Product: 

Location: 

Sample 10: 

Vessel: 

Result 

<0.001 

0.469 

<0.001 

2.634 

0.038 

92.299 

<0.001 

3.904 

0.51 3 

<0.001 

0.032 

0.069 

<0.001 

<0.001 

<0.001 

<0.001 

<0.001 

0.016 

0.014 

0.011 

99.999 

0.59574 

0.59787 

0.996 

1019 

1023 

1002 

918 

Natural Gas 

Location 4 

Sample #S4/Fuel Sulfur - 1A 

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 that il has exercised due diligence and care with respect 10 the information and professiORlI judgments embodied in this report. This report reflects only the findings Bllhe time and place ofinspccrion 

and testing. Issuer expressly disc::laims any furth~ indemnity of any kind. This report is not a guarantee or policy of insurance with respect to Ihe goods o.-Ihe conlfactual penonllance of any party. Any person relying 

upon this report should be aware that issuer's activities are carried OUT under their general terms and conditions . 

. !' 

"Precision parameters apply in the evaluation of the test resuhs specified above. Please also refcr to ASTM 0J244 (except for analysis of RFG) and IP 367 with respect to the utili1.ition of the test data to determine 

confonnance with specifications." 

Page 1 of 6 
SAYBOLT LP 

21730 S. Wilmington Avenue 

Suite 20 I 

Fast To The Point 

5aybolt 

A (ORE LABOIIATOHltS CDMPANY 

Carson, CA 90810 

310-518-4400 Telephone 

310-518-4455 Facsimile 

Certificate of Analysis 

DELTA AIR QUALITY SERVICES 

BOB FINKEN 

1845 N. CASE 

ORANGE, CA 92865 

Saybolt LP 

Date Sampled: 2/22/2013 

Report Date: 2/27/2013 

Job No: 13091-00008630 

Sample Number: 1300169-01 

Client Ref: Sentinel 

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: 

Location: 

Sample 10: 

Vessel: 

Method Result 

ASTM 0-3588 14.696 

ASTM 0-3588 <0.001 

ASTM 0-3588 1042 

ASTM 0-3588 0.141 

ASTM 0-3588 <0.001 

ASTM 0-3588 0.010 

ASTM 0-3588 0.022 

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 0.006 

ASTM 0-3588 0.005 

ASTM 0-3588 0.004 

ASTM 0-3588 1.230 

ASTM 0-3588 71.536 

ASTM 0-3588 23.246 

ASTM 0-3588 4.278 

ASTM 0-3588 0.941 

ASTM 0-3588 22018 

ASTM 0-3588 8822 

ASTM 0-3588 17.25 

AQMO 307/ASTM 05504 <0.1 

AQMO 307/ASTM 05504 <0.1 

AQMO 307/ASTM 05504 <0.1 

AQMO 307/ASTM 05504 <0.1 

Natural Gas 

Location 4 

Sample #S4/Fuel Sulfur - 1A 

Units 

psi 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

wt% 

wt% 

wt% 

wt% 

BTU lib 

SCF/mm BTU 

ppm v/v 

ppm v/v 

ppm v/v 

ppm v/v 

. Issuer warrams that it has exercise<:! due diligence lind care with respect to the information and professional judgments embodied in this report. This report reflects only the findings at (he lime and place or inspection 

and testing. Issuer expressly disclaims any further indemnity of any kind. This report is not a guarantee or policy of inS\lranc~ with respect to the goods or Ihe contractual performance of any party. Any person relying 

o.lpon this report should be aware that issuds activities afe carried out under their general terms and conditions 

"Precision parameters apply in the evaluation oflhe test results specified above. Please alw refer 10 ASTM D3244 (except for analysis of RFG) and II' 367 wilh respect 10 the utilization of the test data to determine 

conformance with specifications " 

Page 2 of 6 
SAYBOLT LP 

21730 S. Wilmington Avenue 

Suite 201 

Fast To The Point 

5aybolt 

A [ORt LAIIDRATCRICS COMPANY 

Carson, CA 908 I 0 

3 10-518-4400 Telephone 

3 10-518-4455 Facsimile 

Certificate of Analysis 

DELTA AIR QUALITY SERVICES 

BOB FINKEN 

1845 N. CASE 

ORANGE, CA 92865 

Saybolt LP 

Date Sampled: 2/22/2013 

Report Date: 2/27/2013 

Job No: 13091-00008630 

Sample Number: 1300169-01 

Client Ref: Sentinel 

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 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 0.1 

AQMD 307/ASTM D5504 0.1 

Approved By: 

Natural Gas 

Location 4 

Sample #S4/Fuel Sulfur - 1A 

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 that it has c1tcrci5l':d due diligence and care with respect 10 the information and professiOlll.1 judgments embodied in this rcpo«. Thj~ report renects only the findings 81 the lime and place of inspection 

and testing. lswer expressly disclaims any further indemnity of any kind. This repon is no! a guarantee or policy of insunmce wilh respect to the goods or the conlraClu.1 performance of Bny pany Any person relying 

upon Lhis report should be ..... 'aTC that issuers activities are carried 001 under their general terms and conditions 

'"Prec,sion parameters apply in the evaluation of the lest results specified above. Please also refer to ASTM D3244 (excepl for analysis of RFG) and IP 367 with respecl 10 lhe utilization oflhe lc,t data to determine 

coofonnancc: with specifications " 

Page 3 016 
5aybolt: 

A [ORE lABOIIATOJlI[S COMPANY 

SAY BOLT LP 

2 173 0 S. Wilmington Avenue 

Suite 20 I 

Carson. CA 90810 

310-518-4400 Telephone 

310-518-4455 Facsimile 

Fast To The Point 

Say bolt 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 

2/27/2013 

13091-00008630 

1300169-02 

Sentinel 

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 01945101946 

ASTM 01945101946 

ASTM 01945101946 

ASTM 01945101946 

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 01945101946 

ASTM 01945101946 

ASTM 01945/01946 

ASTM 01945101946 

ASTM 01945/01946 

ASTM 01945101946 

ASTM 01945101946 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0-3588 

Date Sampled: 2/22/2013 

Product: 

Location: 

Sample 10: 

Vessel: 

Result 

<0.001 

0452 

<0.001 

2.774 

0.048 

92.073 

<0.001 

3.957 

0.531 

<0.001 

0.038 

0.084 

<0.001 

<0.001 

<0.001 

<0.001 

<0.001 

0.013 

0.015 

0.014 

99.999 

0.59701 

0.59915 

0.996 

1019 

1023 

1002 

918 

Natural Gas 

Location 4 

Sample #S4/Fuel Sulfur - 1 B 

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 that it his cilcrcised due diligence aoo care with respeclto the information and professional Judgments embodied in this rcpon This reporl renew only the findings lIthe lime and place ofinspeaion 

and testmg. Issuer expressly disclaims any funher indemnity of any kind This repan is not II. guarantee or polity ofinsuTllnce with respect 10 the goods or the conlrKrual performance of any party Any pcrn!II relying 

upon this report should be aware that issuer's activities are carried OU1 under thelT gC1!ef1I1 terms 100 COfldilions 

"~is.ion parameters apply in the evaluation orlhe lest results specified above. Please also refer 10 ASTM 01244 (extepl for analysis of RFG) and lP ]67 IVith resp«t to the utilization of the tesl data (0 determil\e 

conformance with specifications." 

Page 4 016 
SAYBOLTLP 

21730 S. Wilmington Avenue 

Suite 201 

Fast To The Point 

5 aybolt: 

Carson, CA 90810 

310-518-4400 Telephone 

310-518-4455 Facsimile A [DIIE LABDRATDRI[S COM.PANY 

DELTA AIR QUALITY SERVICES 

BOB FINKEN 

1845 N. CASE 

ORANGE, CA 92865 

Report Date: 2/27/2013 

Job No: 13091-00008630 

Sample Number 1300169-02 

Client Ref: Sentinel 

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 

Certificate of Analysis 

Date Sampled: 

Product: 

Location: 

Sample 10: 

Vessel: 

Method Result 

ASTM 0-3588 14.696 

ASTM 0-3588 <0.001 

ASTM 0-3588 1.056 

ASTM 0-3588 0.146 

ASTM 0-3588 <0.001 

ASTM 0-3588 0.012 

ASTM 0-3588 0.026 

ASTM 0-3588 <0001 

ASTM 0-3588 <0001 

ASTM 0-3588 <0.001 

ASTM 0-3588 <0.001 

ASTM 0-3588 <0.001 

ASTM 0-3588 0.005 

ASTM 0-3588 0.005 

ASTM 0-3588 0.006 

ASTM 0-3588 1.256 

ASTM 0-3588 71.393 

ASTM 0-3588 23.186 

ASTM 0-3588 4496 

ASTM 0-3588 0.926 

ASTM 0-3588 21968 

ASTM 0-3588 8823 

ASTM 0-3588 17.29 

AQMO 307/ASTM 05504 <0.1 

AQMO 307/ASTM 05504 <0.1 

AQMO 307/ASTM 05504 <0.1 

AQMO 307/ASTM 05504 <0.1 

Saybolt LP 

2/22/2013 

Natural Gas 

Location 4 

Sample #S4/Fuel Sulfur - 1 B 

Units 

psi 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

wt% 

wt% 

w1% 

wt% 

BTUllb 

SCF/mm BTU 

ppm v/v 

ppm v/v 

ppm v/v 

ppm v/v 

Issuer warrants that it has exercised due diligence and care with respect to lhe information and professional judgments embodied in this rcpoM. This report renecls only the fllldings allhe time and place of inspection 

and testing. Issuer expressly disclaims any funher indemnity of any kind. This report is not a guarantee or policy of insurance with respect \0 the goods or Ih ~ conlraclUal performance of any party. Any person relying 

upon this repon should be aware that issuer's activities are carried out under their general terms and conditiOils 

"Precision parameters apply in the evaluation of the test results specified above. Please also refer to ASTM D3244 (except for analysis of RFG) and IP 367 with respect to the utilization of the test data to detennine 

conformance with specificatiOllS" 

Page 5 016 
SAYBOLT LP 

21730 S. Wilmington Avenue 

Suite 20 I 

Fast To The Point 

5 ayb(]lt: A [ORE lAB~IIATnR[[S COMPANY 

Carson, CA 90810 

310-518-4400 Telephone 

310-518-4455 Facsimile 

Certificate of Analysis 

DELTA AIR QUALITY SERVICES 

BOB FINKEN 

1845 N. CASE 

ORANGE, CA 92865 

Saybolt LP 

Date Sampled: 2/22/2013 

Report Date: 2/27/2013 

Job No: 13091-00008630 

Sample Number: 1300169-02 

Client Ref: Sentinel 

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 Sulfur 

Product: 

Location: 

Sample 10: 

Vessel: 

Method Result 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 <0.1 

AQMD 307/ASTM 05504 0.2 

AQMD 307/ASTM 05504 0.2 

Approved By: 

Natural Gas 

Location 4 

Sample #S4/Fuel Sulfur - 1 B 

Units 

ppm v/v 

ppm v/v 

ppm v/v 

ppm vlv 

ppm v/v 

ppm v/v 

ppm v/v 

ppm v/v 

ppm v/v 

ppm vlv 

ppm v/v 

ppm v/v 

ppm v/v 

ppm v/v 

ppm v/v 

Signature On File 

Francine Hanby 

Laboratory Manager 

Issuer warrants that il has exercised duc diligence and care with respect to the information and professional judgments embodied in this report. This report reflects only the findings at the time and place of inspection 

and testing. Issuer expressly disclaims any further indemnity of any kind. This report is nOl a guarantee or policy of insurance with respect to the goods or the contractual performance of any party. Any person relying 

upon this report should be aware that issuer's activities are carried out under their general tenns and condition. 

"Precision parameters apply in the evaluation of the test results specified above_ Please also refer to ASTM 03244 (except for analysis of RFG) and IP 367 with respeer to the utilization of the test data to determine 

confonnance with specifications." 

Page 6 of 6 
APPENDIX C TEST DATA 

R041 0688 C-1 
Appendix C.1 Stratification and Preliminary Flow Rate Tests 

R041 0688 C·2 
12-POINT STRATIFICATION CHECK 

Gemma 

4 

2/1112013 

02 CO2 NOx CO 

Port Point % % ppm ppm 

S 3 13.18 4.56 3.14 1.50 

S 2 13.18 4.56 3.02 1.89 

S 1 13.13 4.59 3.03 1.84 

E 3 13.15 4.58 3.15 2.03 

E 2 13.19 4.55 3.01 2.75 

E 1 13.19 4.56 2.76 2.51 

W 3 13.19 4.55 3.28 3.11 

W 2 13.19 4.56 3.30 2.98 

W 1 13.18 4.56 3.28 2.81 

N 3 13.20 4.54 3.32 301 

N 2 13.22 4.53 3.43 2.72 

N 1 13.21 4.54 3.50 2.83 

Average 13.2 4.6 3.2 2.5 

Maximum 13.2 4.6 3.5 3.1 

Minimum 13.1 4.5 2.8 1.5 

Maximum Differenl 0.1 0.0 0.4 1.0 

Max Difference (% 0.4% 0.7% 13.4% 40.0% 

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 
RELATIVE ACCURACY TEST 

DATA AND WORKSHEET 

CPV Sentinel-4-CEMS-107-STRAT 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit 4 

Performed By: AA, SS, RM , JM 

Cp: 0.84 

Tref: 68 'F 

Stack Area: 143.14 ft' 

Meter Yd: 0.992 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H2O) sqrt(dP) ' F (Ips) 

4 2.10 1.4491 765 125.73 

3 2.60 1.6125 766 139.96 

2 2.70 1.6432 767 142.68 

1 2.50 1.5811 766 137.24 

4 1.60 1.2649 767 109.84 

3 2.10 1.4491 768 125.88 

2 2.20 1.4832 767 128.79 

1 1.60 1.2649 766 109.79 

4 1.50 1.2247 764 106.22 

3 1.40 1.1832 766 102.70 

2 1.80 1.3416 767 116.50 

1 2.40 1.5492 766 134.47 

4 1.60 1.2649 765 109.75 

3 2.10 1.4491 767 125.83 

2 2.20 1.4832 768 128.85 

1 2.40 1.5492 767 134.52 

Average 2.0294 1.4246 766.4 123.67 

Stack Flow Rate: 1,062.1 kwacfm 

Stack Flow Rate: 407.8 kdscfm 

Dry Gas Meter 

Time Vol. Tm(in) Tm(out) #/Matl. 

Start 515.560 70 67 H,O 

68 67 H,O 

70 68 Emply 

End 534.976 71 68 SG 

U ne Rinse 

Total 19.416 68.6 Total 

NO. ppm 

NO. , ppm@ 15% O2 

NO. IblMMBtu 

NO.Ib/hr 

CO ppm 

CO, ppm@ 15% O2 

CO Iblhr 

0, % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

011l1li RlrqulIl/1Y58MC8S 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

CTLoad MW 

SCR NH3 Injection Iblhr 

NO, IblMMSCF 

CO IblMMBtu 

CO IblMMSCF 

TEST VARIABLES 

Start Date: 2/1 1/2013 

Start/End Time: 9:02 

Load (MW)fReplicate# 107 

Barom. Pressure: 29.64 

Pstack: 2.40 

Pstack: 29.82 

MW: 28.05 

METHOD 100.1 DATA 

0, CO, 

Analyzer Range 20 10 

Cal Gas Value 9.98 4.96 

Pre-Test Direct Zero 0.11 -0.02 

Pre-Test Direct Span 10.00 5.11 

Pre-Test System Zero 0.17 002 

Pre-Test Svstem Soan 10.35 5.05 

Post-Test System Zero 0.24 0 .06 

Post-Test System Span 9.88 5.09 

Post-Test Direct Zero 0.10 0.01 

Post-Test Direct Span 10.04 5.12 

Average 13.19 4.56 

Corr. results 13.07 4.45 

Pre-test zero bias 0.3% 0.4% 

Pre-test span bias 1.7% -0 .6% 

Post-test zero bias 0.7% 0.5% 

Post-test span bias -0.8% -0.3% 

Zero drift 0.4% 0.4% 

Span drift -2.3% 0.4% 

METHOD 4.1 DATA 

Impingers 

End Start Diff. 

824.1 683.9 140.2 Meter Pressure: 

660.8 660.0 0.8 

580.8 580.1 0.7 Sample Votume: 

974.4 968.4 6.0 H20 Volume : 

100.0 -100.0 Moisture Content: 

47.7 

RESULTS 

Ref. Meth CEMS Diff. Ditt. % 

3.22 2.90 0.32 9.8% 

2.42 2.14 0.28 11 .7% 

0.009 0.008 0 .001 11 .1% 

9.39 7.43 1.96 20.9% 

2.55 2.70 -0.15 -5.7% 

1.93 1.97 -0.04 -2.3% 

4.54 4.11 0.43 9 .5% 

13.07 12.90 0.17 1.3% 

24,465,874 21,124,000 3,341,874 13.7% 

- 8,841.4 - - ~ - - - - - - 110.0 - - 10.62 

0.004 

4.53 

9:35 

STRAT 

"'9 

"Hg 

Iblltrmole 

NO, CO 

5 10 

2.52 9.47 

0.Q1 -0.01 

2.54 9 .51 

0.01 -0.05 

2.49 9.50 

0.03 -0.09 

2.51 9.40 

0.03 0.02 

2.51 9.47 

3.18 2.50 

3.22 255 

-0.1% -0.4% 

-1.0% -0.1% 

0 .1% -1 .0% 

-0.2% -D.7% 

0.4% ...().4% 

0.2% -1.0% 

2.0 iwg 

19.151 dscf 

2.251 set 

10.5 % 

Sentinel Unit 4 RATA.x!s 

2/15/2013 

1:25PM 
Port Point Angle 

N 4 1 

N 3 0 

N 2 3 

N 1 0 

E 4 0 

E 3 0 

E 2 1 

E 1 0 

S 4 2 

S 3 0 

S 2 0 

S 1 1 

W 4 3 

W 3 2 

W 2 0 

W 1 

Average 0.9 

Average Angle < 10 deg.? Yes 

No Points w/Reverse Flow? Yes 

Less Than 4 Points> 30 Deg.? Yes 

PASS 
FLUE GAS VELOCITY DATA AND WORKSHEET 

CLIENT: Ccrv1rrir4- PERFORMED BY: .Rf-l "I' - ~ \ :0 

LOCATtpN: " <f dlq 7 BAR. PRESSURE: ~.':t 

UNIT:-/' 't STATIC PRESSURE:-,-,:-.C-f'-"""-i-',_y.L-____ _ 

TEST DATE: 2 -' 1/ - I ' ) TC READOUT 10:,--,,::-, ' "itf-'-'-...!..I...!./....:IJ-''---'G.5'''--____ _ 

TEST NUMBER: ::>- 'i\r;rK- c'1(\"",,< -I<1)-' \ TC 10: :- . ~- ') 

LEAK CH EC K PRE~ r" _c POST _ Y t-,./ P'TOT--:T==-U':::B:-::E:-C'=D=--: -;:1:""::::-'''''-q17l 9''1 -------

~P INDICATOR TYPE: C/o -/c' ~ I PITOT TUBE COEFFICIENT:--..:Cc-)_' ..=:::',,- ' c:./ _' ___ _ 

~P INDICATOR 10: / 7 - '.A_" " .\ ZERO: 1'-, , . ( LEVEL:-;,lt-" -,,' C"'-c--')C-__ _ j 

Yaw Angle, ~P, Temperature, 

Time Port Point Degrees(1) inches H2O of 

I) :F' <t' , hi Y ~ \.5" fbo 

~ tJ l , '-\ I S-q 

.2 3 L;? 1S"'j 

J ro '2.1\ '1 '\. \ 

\ , (0 """ ~l "\. 

() ,~ .. >'2 E L/ 0 l. h ~'i.1 

3 f) z. . \ tb( 

2- l 1..2--- 7LI 

/ tJ L(, iQ' 

..-9;;; 

artJ 'l 5 2./ L 1.\ fL:::'-

3 (] 2(. 11;("'" 

2 0 2-.1 1G ., 

f I 2.. .-::, ,'lick> 

()'lI J LA-.! t/- <, 1.1. 7y-s 

'3 2..... '2. \ 7?-.eJ 

2. b -Z ,.2.., 1'(' l 

J \ 2.,,-\ " 1)'''\ 

Comments: 1) Positive yaw angles correspond to clockwise rotation of the probe, 

Date of last revision 11/13/08 

DS834033 

Master Document StoragelForms\DatasheetslField Datasheets 
WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: 0.tf\k.AA 

LOCATION: ';,5 wr:'VA 

DATE: 2../ l, I ,'S 

RUN NO: ' F.< -- /~ /'-' ~ 

OPERATOR: L- '~ ./.7 

METER BOX NO: '1 1",,1', '-"! 

METER L1H@: ", '" q '7 

METER Yd: q, " ~ ',,_ STACK AREA. FY: i':f'? A,,\ 

TRAVERSE POINTS. MIN/POINT:2fib 

L1 H= Ll P: 

Probe Condition. prelpost test:--.-;J'--__ _ 

Silica Gel Expanded. YIN: tJ 

Filter Condition after T est:--'/----

Check Weight: ~ 

Meter LIP 

Point Time Volume, ft' in, H,O 

15 3 0701-. ~>. 5(;,0 ~ t , 

2- 0'/0,/ , : .,-

f d'lOL - ':!.. '7 

b 8 109., :i i c/ , &,)L, ! 2 , \ 

t: :;: ,) ~ll l 5~'00b '1 i, C-- -'2 t)q /3 , .c.' I 

/ 'if' s- '- 2 . .2.. 

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;z, C Cj'1 1, , ,J, . I 

I ,,'1 ?,~ , 21--

(J ''I ... L- ;':1"-/. 17/"" ' 2, </ 

AveraQe: 

AMBIENT TEMPERATURE: "7 6 

BAROMETRI C PRESSURE':-: -l-~----;;~a'1'--;-""'-i'-------

ASSUMED MOISTURE: '\[.u , PITOT TUBE COEFF. C:-p-: 1/,c'-~.'-~""?'--"ll------

PROBE ID NO/MATERIAL: ¥ &<ii¥ 'f-YJ 5" 5 

PROBE LENGTH: (? r 7- NOZZLE ID NOI MATERIAL:7-j N':'<0"'-_______ _ 

NOZZLE DIAMETER:_ -;J:-''''',''' ',,'--___ ____ _ 

FILTER NOfTYPE: V(.' PRE-TEST LEAK R"'A"'T"'E;-:: "': Ti O-'-Q"-::''-;-:-'C'''F=:M7@~--:-\ ,- ----,i;-:n-., H7 g-,-

POST-TEST LEAK RATE: ~Q "" 7,.CFM@ I c±' n, H , 

PITOT LEAK CHECK - PRE: l.-- POST: ' 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN 

Imp, # Contents Post-Test - Pre-Test = Difference 

,I AI HJ lOLl i?2<\ I c,,'b>.9 

1- , lrV f!, SO,! lsidJ, '2l ~bO.() -

~ ,fT 53b,o/"l S 'bO·l 

'-( <; (7) q(L(,~ "fb'b. '1 

cL H1,U \(JU 

SAMPLER R .. 

SAMPLE CUSTODIAN=::::M: Total: _ _ _ _ ____ _____ _ 

L1H Stack Probe Filter Imp, Out Meter Temp, of Vacuum 0 , p, static 

in, H,O Temp. of Temp. of Temp. of Temp. of In Out in, Hg, % in, H2O 

Z ,D 7 (.:. ~ 'X tA :;; e:; 70 :"-7 ¥ -(2 , 1.{' 

.7 L <v 

''-' J 1~ (, 

:.:z . L ' 7/1, 7 'I :A ~2- he. £/ </ 

??> 8' 

?tv'1 

'7'" ;:, 

.2, LC 7<-- <I "- Y :;' v-- 70> &;, ("-'I q 

7&(" 

:Jl. 7 

'7 c.' LA 0 7&- :; -i I. -c,,( 71 t" c) ~ 

7?- '/ 

? (; <-: 

? c ' -7 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 1/25/2013 Page __ of __ 

DS834049 

Master Document Storage\Forms\Datasheets\Field Datasheets 
Appendix C.2 CEM Data 

R041 0688 C-3 
Appendix C.2.1 CEM Quality Assurance Measurements 

R041 0688 C-4 
Client: Gemma 

Delta Air QualilY SelViees 

CEMS PERFORMANCE DATA SHEET 

Location: CPV Sentinel Unit 4 

Date: 2/11/2013 

Performed By: AA, SS, RM, JM 

CEMS 10#: .:::5c..:-C::;E:;:M:.:.:S"--__________ _ 

Analyzer: O2 CO2 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 Lenqth 200' 

Upscale Response Time: 30 Downscale Response Time: 

Sample Pressure (psi): 6 TECO Vacuum (" Hg): 

Sample Flow Rate: 8 SCFH 

S02 

--

Gas Temp: 

Gas Temp: 

Gas Temp: 

30 

NA 

750 of 

285 of 

33 of 

seconds 

Sentinel Unit 4 CEMS QA 

2/21/2013 

11:58AM 
Source 

Test Date 

AETB Name 

AETB Phone Number 

AETB e-mail 

QI Last Name 

QI First Name 

QI Middle Initial 

QI Exam Date 

Exam Provider 

Exam Contact 

Gemma CPV Sentinel Unit 4 

2/11 /201 3 

Delta Air Quality Services, Inc. 

714-279-6777 

contact@deltaags.com 

Aleshaiker 

Ali 

M 

November 21 , 2008 

Source Evaluation Society 

gstiprogram@gmaii.com 
D8/la Ai, quality Services 

SPAN GAS RECORD AND SCAQMD CALIBRATION ERROR/LINEARITY 

CLiENT/LOCATION: Gemma CPV Sentinel Unit 4 DATE: 2/11/13 

TRUCK/CEM I.D.: ~5~C::.:E::::M::.:S::-__________ _ BY: AA, SS, RM, JM 

Exp. Vendor %01 

Gas Cyl inder # Value Date 10 Range 

ZERO Low CC93915 0.0 10/6/17 F22012 

O2 Mid CC72997 9.98 11 /16/15 F22012 49.9% 

O2 High CC199067 18.90 4/4/15 F22012 94.5% 

CO2 Mid CC72997 4.96 11 /16/15 F22012 49.6% 

CO2 High CC199067 9.62 4/4/15 F22012 96.2% 

NOx Mid CC7352 2.52 12/10/15 F22012 50.4% 

NOx High CC362309 4.82 5/24114 F22012 96.4% 

N02 N02 CC11 3404 402 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 

O2 CO2 NOx CO 

Analyzer Range 20 10 5 10 

Zero Gas Value 0.0 0.0 0.0 0.0 

Analyzer Reads 0.11 -002 0.01 -001 

Error (% of scale) 0.5% -0.2% 0.2% -0.1% 

High Gas Value 18.90 9.62 4.82 9.47 

Analyzer Reads 18.86 9.71 4.79 9.51 

Error (% of scale) -0.2% 0.9% -0.6% 0.4% 

Mid Gas Value 9.98 4.96 2.52 4.49 

Analyzer Reads 10.00 5.11 2.54 4.52 

Error (% of scale) 0.1% 1.5% 0.4% 0.3% 

Linearity at Mid Point -0.1% 1.1% 0.6% 0.2% 

POST-TEST INSTRUMENT CALIBRATION ERROR 

ANALYZER 

O2 CO2 NOx 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 0.12 

Error (% of scale) 0.5% 0.3% 0.4% 1.2% 

High Gas Value 18.90 9.62 4.82 9.47 

Analyzer Reads 19.09 9.73 4.83 9.52 

Error (% of scale) 1.0% 1.1% 0.1% 0.5% 

Mid Gas Value 9.98 4.96 2.52 4.49 

Analyzer Reads 10.05 5.14 2.53 4.60 

Error (% of scale) 0.3% 1.8% 0.2% 1.1% 

Linearity at Mid Point -0.4% 1.1% -0.1% 0.3% 

STATUS 

--

-- PASS 

--

-- PASS 

--

-- PASS 

PASS 

STATUS 

--

-- PASS 

-

-- PASS 

--

--

PASS 

PASS 

Sentinel Unit 4 CEMS QA 

31112013 

11 :28 AM 
Della Air QualllY Services 

SPAN GAS RECORD AND SCAQMD CALIBRATION ERROR/LINEARITY 

CLiENT/LOCATION: Gemma CPV Sentinel Unit 4 DATE: 2/12/13 

TRUCK/CEM LD.: .:::5...::-C::::E:::M::.::S~ _________ _ BY: AA, SS, RM, JM 

Exp. Vendor %of 

Gas Cylinder # Value Date 10 Range 

ZERO Low CC93915 0.0 10/6/17 F22012 

O2 Mid CC72997 9.98 11 /16/15 F22012 49.9% 

O2 High CC199067 18.90 4/4/15 F22012 94.5% 

CO2 Mid CC72997 4.96 11 /16/15 F22012 49.6% 

CO2 High CC199067 9.62 4/4/15 F22012 96.2% 

NO, Mid CC7352 2.52 12/10/15 F22012 50.4% 

NO, High CC362309 4.82 5/24114 F22012 96.4% 

N02 N02 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 

O2 CO2 NO, CO 

Analyzer Range 20 10 5 10 

Zero Gas Value 0.0 0.0 0.0 0.0 

Analyzer Reads 0.12 0.00 0.02 0.08 

Error (% of scale) 0.6% 0.0% 0.4% 0.8% 

High Gas Value 18.90 9.62 4.82 9.47 

Analyzer Reads 18.97 9.66 4.81 9.62 

Error (% of scale) 0.4% 0.4% -0.2% 1.5% 

Mid Gas Value 9.98 4.96 2.52 4.49 

Analyzer Reads 10.03 5.09 2.52 4.61 

Error (% of scale) 0.2% 1.3% 0.0% 1.2% 

Linearity at Mid Point -0.2% 1.1% 0.0% 0.0% 

POST-TEST INSTRUMENT CALIBRATION ERROR 

ANALYZER 

O2 CO2 NO, CO 

Analyzer Range 20 10 5 10 

Zero Gas Value 0.0 0.0 0.0 0.0 

Analyzer Reads 0.11 0.13 000 0.05 

Error (% of scale) 0.5% 1.3% 0.0% 0.5% 

High Gas Value 18.90 9.62 4.82 9.47 

Analyzer Reads 19.01 9.66 4.77 9.60 

Error (% of scale) 0.5% 0.4% -0.9% 1.3% 

Mid Gas Value 9.98 4.96 2.52 4.49 

Analyzer Reads 10.04 5.16 2.50 4.59 

Error (% of scale) 0.3% 2.0% -0.5% 1.0% 

Linearity at Mid Point -0.2% 1.1% 0.0% 0.1% 

STATUS 

--

-- PASS 

--

-- PASS 

--

-- PASS 

PASS 

STATUS 

--

-- PASS 

--

-- PASS 

--

-- PASS 

PASS 

Sentinel Unit 4 CEMS QA 

3/1/20 13 

11 :29AM 
GAS 

Zero 

Zero 

NO 

NO 

N02 

N02 

Della Ail Quality SelViGes 

N02 to NO Converter Efficiency Test 

Analyzer Manufacturer: 

Analyzer Model: 

Analyzer Serial Number: 

Date: 

ANALYZER 

MODE 

NOx 

NO 

NOx 

NO 

NO 

NOx 

Abs. Value CO-C,: 

Abs. Value C2-C,: 

C,/C2 

CE = D2/O, • 100%: 

Gemma CPV SentindIJOr1ilai Gas Value: 4.82 

600CLD 

V10043 

2/11/13 

4.0 

3.9 

0% 

96% 

N02 Cal Gas Value: 4.02 

ANALYZER 

RESPONSE 

0.01 

0.01 

4.82 

4.82 

0.02 

3.87 

Label 

D, 

D2 

D3 

Performed By: AA 

CEMS ID#: 5-CEMS 

CAL 

CORRECTED LABEL 

0.0 

3.9 

Requirement 

<5% 

> 90% 

C, 

C2 

Sentinel Unit 4 CEMS QA 

2/21/2013 

11 :59 AM 
GAS 

Zero 

Zero 

NO 

NO 

NO, 

NO, 

D811a Air qualilY SI/MelJS 

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 = Di D, • 100%: 

Gemma CPV SentinEIIIOr1iJ:aI Gas Value: 4.82 

600CLD 

V10043 

2/12/13 

4.0 

3.8 

0% 

96% 

NO, Cal Gas Value: 4.02 

ANALYZER 

RESPONSE 

0.01 

0.01 

4.81 

4.83 

0.03 

3.86 

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 4 CEMS QA 

2/21/2013 

11 :59 AM 
Appendix C.2.2 NOx and CO Compliance 

R041 0688 C-5 
COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentinel-4·CEMS·100-1 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit: 4 

Performed By: AA, SS, RM, JM 

Cp: 0.99 

Tref: 60 ' F 

Stack Area: 143.1 4 If 

Meter Yd: 0.992 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H2O) sqrt(dP) 'F (Ips) 

4 1.30 1.1402 767 116.53 

3 1.40 1.1832 768 120.98 

2 1.60 1.2649 768 129.34 

1 1.50 1.2247 766 125.13 

4 0.92 0.9592 768 98.07 

3 0 .93 0.9644 759 98.24 

2 1.70 1.3038 760 132.88 

1 1.60 1.2649 762 129.02 

4 0.90 0.9487 762 96.77 

3 1.30 1.1402 765 116.44 

2 1.10 1.0488 760 106.89 

1 1.40 1.1832 758 120.49 

4 0.95 0.9747 760 99.34 

3 1.50 1.2247 757 124.67 

2 1.70 1.3038 758 132.77 

1 1.60 1.2649 760 128.91 

Average 1.3217 1.1496 762.4 117.28 

Stack Flow Rate: 1,007.2 kwacfm 

Slack Flow Rale: 383.0 kdscfm 

Ory Gas Meter 

Time Vol. Tm(in) Tm(out) N/Mal!. 

Start 536.846 62 57 H, O 

62 56 H, O 

End 582.187 61 55 Empty 

63 57 SG 

Total 45.34 1 59.1 Total 

NOx ppm 

NOx , ppm @ 15% O2 

NOx Ib/MM8 tu 

NOx Ib/hr 

CO ppm 

CO, ppm@ 15% O2 

CO Iblhr 

O2 % 

Stack Flow dscfh 

CT Fuel Flow hscth 

Turbine Water Injection gpm 

8,118A1,QuaIIlYSIIMcIIS 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

CTLoad MW 

SCR NH3 Injection Iblhr 

NOx Ib/MMSCF 

CO IblMMBtu 

CO IblMMSCF 

TEST VARIABLES 

Start Date: 2/11 /13 

Start/End Time: 10:06 11 :19 

Load (MW)/Replicale# 100 1 

Barom. Pressure: 29.64 

Pstack: 

Pstack: 

MW: 

Analyzer Range 

Cal Gas Value 

Pre-Test Direc1 Zero 

Pre-Test Direct Soan 

Pre-Test System Zero 

Pre-Test System Span 

Post-Test System Zero 

Post-Test System Span 

Post-Test Direct 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. 

3045.0 684.5 2360.5 

666.0 <;66.0 

581 .6 -581.6 

899.6 -899.6 

Ir 100 113.3 

RESULTS 

Ref. Meth CEMS 

3.02 2.70 

2.34 203 

0.009 0.007 

8.4 1 6.94 

2.68 2.70 

2.08 1.99 

4.48 4.07 

13.29 12.92 

22,981 ,081 21 ,158,000 

- 8 ,830 

-

- 106 

- 110 

9.52 

0.005 

4 .90 

3.40 iwg 

29.89 "Hg 

28.06 Ib/lb-mole 

METHOD 100.1 DATA 

0, CO, NO, CO 

20 10 5 10 

9.98 4.96 2.52 9.47 

0.10 0.01 0.03 0.02 

10.04 5.12 2.51 9.47 

0.24 0.06 0.03 -0.09 

9.88 5.09 2.51 9.40 

0.1 6 0.03 0.Q4 0.02 

10.04 5.08 2.53 9.50 

0.10 -0.01 0 .03 0.01 

10.03 5,10 2.52 9.54 

13.20 4.53 301 2.65 

13.29 4.42 3.02 2.68 

0,7% 0.5% 0.1% -1.0% 

-0.8% -0.3% -0.2% -0.7% 

0.3% 0.3% 0.1% 0 ,1% 

0.0% -0.2% 0.2% -0.3% 

-0.4% -0.3% 0.2% 1.0% 

0.8% -0.1% 0.5% 1.0% 

Meter Pressure: 1.5 iwg 

Sample Volume: 44.795 dscf 

H20 Volume : 5.267 scf 

Moisture Content: 10.5 % 

Sentinel Unit 4 100% NOx·NH3-ROG Compliance.xls 

2/15/2013 

1:54 PM 
3 

2 

4 

3 

2 

1 

4 

3 

2 

1 

4 

3 

2 

Average 

Start 

End 

i 

Unit: 

Performed By: 

Cp: 

Tref: 

Stack Area: 

Meter 

1.20 1.0954 

1.40 1.1832 

0.92 0.9592 

0.98 0 .9899 

1.30 1.1402 

1.70 1.3038 

1.40 1.1832 

0.99 0.9950 

1.20 1.0954 

1.10 1.0488 

0.90 0.9467 

0.91 0.9539 

0.97 0.9849 

1.00 1.0000 

1.1170 1.0569 

583.299 61 

63 

631 .745 61 

4 

M , SS, RM , JM 

0 .99 

60 of 

143.14 It' 

0.992 

766 

766 

765 

766 

767 

768 

767 

766 

766 

766 

765 

766 

767 

767 

766.1 

COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentinel-4-CEMS-100-2 

111 .62 

120.56 

97.69 

100.87 

116.22 

132.96 

120.61 

101 .38 

111 .62 

106.87 

96.63 

97.20 

100.39 

101.94 

107.69 

Start Date: 

StarVEnd Time: 

Load (MW}/Replicate# 

8aram. Pressure: 

Pstack: 

Pstack: 

MW: 

bias 0.3% 

bias 0.0% 

zero bias 0.4% 

span bias -0.1% 

0 .1% 

#/Matl. End 

2/11 /13 

11 :40 

100 

29.64 

2.40 

29.82 

28.28 

0 .3% 

-0.2% 

0.4% 

-0.3% 

0 .0% 

-0.1% 

57 H,O 674.3 Pressure: 

58 H, O 

58 Empty 

NO. ppm 

NO., ppm@ 15% O2 

NO. Ib/MMBlu 

NO. lblhr 

CO ppm 

CO, ppm @ 15% O2 

CO tblhr 

O2 % 

661A 

582.1 

2.67 

2.18 

0 .008 

7.46 

2.00 

1.52 

3.11 

13.15 

660.8 

581 .8 

2.70 

2.01 

0.007 

6.66 

2.30 

1.72 

3.47 

12.90 

0.3 

Content 

12:54 

2 

iwg 

"Hg 

Ibllb-mole 

0 .1% 0.1% 

0 .2% -0.3% 

0 .2% -0.1% 

0 .1% -0.6% 

0.0% -0.1% 

-0.1% 

1.5 iwg 

47.828 dscf 

4.463 scf 

8.5 % 

Turbine Water Injection 9pm 

8,1tJI All Quality S,lVIe" 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

CT load MW 

I 

NO. IblMMSCF 8.42 

CO IblMMBlu 0.003 

I 

Sentinel Unit4 100% NOx-NH3-ROG Compliance. xis 

2/1512013 

1:54PM 
Port 

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 

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 

3 

3 

3 

3 

3 

2 

2 

2 

2 

2 

3 

3 

3 

3 

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 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

2111 /2013 

2111 /2013 

2/11/2013 

211112013 

2111 /2013 

2111/2013 

211112013 

2111 /2013 

2111 /2013 

2111 /2013 

2111/2013 

2/11/2013 

211112013 

2111 /2013 

2111 /2013 

2111 /2013 

2111 /2013 

211112013 

2111 /2013 

2111/2013 

2/11/2013 

211112013 

2111 /2013 

2/11 /2013 

211112013 

211112013 

2111 /2013 

2111 /2013 

2/11 /2013 

2/11/2013 

2111/2013 

2/11/2013 

2111 /2013 

211112013 

211112013 

8.H.A1IQU.IIIYS.MC.S 

1845 N. Case Street 

Orange, California 92865 

714·279-6777 

REFERENCE METHOD 1·MINUTE AVERAGE DATA 

Time O2 CO2 NO" CO 

10:07 13.223 4.527 3.256 2.867 

10:08 

10:09 

10:10 

10:11 

10:12 

10:13 

10:14 

10:15 

10:16 

10:17 

10:16 

10:19 

10:20 

10:21 

10:27 

10:29 

10:30 

10:31 

10:34 

10:35 

10:36 

10:37 

10:36 

10:39 

10:40 

10:41 

10:42 

10:45 

10:46 

10:47 

10:46 

10:49 

10:50 

10:51 

10:52 

10:53 

10:54 

10:55 

10:56 

10:57 

10:56 

10:59 

11 :05 

11 :06 

11 :07 

11:06 

11 :09 

11 :10 

11 :11 

11 :12 

11 :13 

11 :14 

11 :15 

11 :16 

11 :17 

11 :16 

11 :19 

13.222 

13.227 

13.222 

13.219 

13.219 

13.211 

13.227 

13.216 

13.205 

13.222 

13.252 

13.231 

13.254 

13.255 

13.224 

13.216 

13.233 

13.211 

13.206 

13.215 

13.21 

13.207 

13.203 

13.207 

13.197 

13.191 

13.192 

13.193 

13.167 

13.194 

13.197 

13.199 

13.196 

13.206 

13.192 

13.165 

13.182 

13.179 

13.177 

13.162 

13.171 

13.163 

13.176 

13.163 

13.166 

13.176 

13.164 

13.172 

13.173 

13.179 

13.166 

13.171 

13.152 

13.166 

13.164 

13.169 

13.172 

13.20 

4.528 

4.526 

4.526 

4.532 

4.526 

4.533 

4.524 

4.531 

4.543 

4.529 

4.514 

4.523 

4.512 

4.512 

4.522 

4.521 

4.515 

4.524 

4.523 

4.517 

4.52 

4.521 

4.526 

4.524 

4 .528 

4.529 

4.53 

4.531 

4.534 

4.529 

4.526 

4.525 

4.529 

4.521 

4.533 

4.542 

4.546 

4.549 

4.551 

4.556 

4.554 

4.56 

4.547 

4.552 

4.55 

4.543 

4.551 

4.546 

4.544 

4.536 

4.546 

4.541 

4.55 

4.541 

4.543 

4.54 

4.54 

4.53 

3.16 

3.216 

3.176 

3.267 

3.163 

3.343 

3.131 

3.244 

3.25 

3.224 

3.266 

3.422 

3.234 

3.279 

3.079 

3.096 

3.069 

3.12 

3.054 

3.027 

3.034 

3.036 

3.05 

2.964 

2.967 

3.063 

3.002 

2.972 

2.936 

2.901 

2.952 

2.901 

2.699 

2.746 

2.666 

2.911 

2.922 

2.647 

2.766 

2.768 

2.772 

2.659 

2.926 

2.953 

2.947 

2.937 

2.925 

2.938 

2.974 

2.617 

2.656 

2.611 

3 

2.614 

2.775 

2.73 

2.651 

3.01 

3.113 

3.325 

3.414 

3.405 

3.355 

3.073 

3.236 

3.102 

2.902 

2.693 

3.196 

3.037 

3.416 

3.463 

3.261 

3.356 

3.506 

3.241 

3.017 

3.166 

3.232 

3.207 

2.99 

3.101 

3.034 

2.966 

2.946 

2.757 

2.571 

2.629 

2.704 

2.91 

2.71 

2.933 

2.737 

2.488 

2.263 

2.284 

2.225 

2.105 

2.132 

1.966 

1.631 

1.734 

1.776 

1.6 

1.603 

1.569 

1.602 

1.652 

1.656 

1.661 

1.551 

1.99 

2.155 

2.179 

2.034 

2.65 

02·ln NOx-ln CO-In THe·ln 

13.291 32.887 109.561 25.926 

13.31 32.466 120.645 30.51 

13.313 32.49 122.197 30.369 

13.353 32.191 130.969 34.33 

13.352 32.527 121 .007 29.921 

13.311 32.61 119.006 26.312 

13.327 32.397 114.493 26.213 

13.32 32.349 117.66 26.621 

13.301 32.946 106.015 23.609 

13.296 32.676 107.629 24.429 

13.359 32.279 106.441 25.239 

13.34 32.576 111.424 25.647 

13.35 32.267 111 .772 26.14 

13.356 32.005 123.935 31 .175 

13.366 31 .654 124.21 31 .566 

13.324 32.231 119.052 30.009 

13.364 31.26 129.429 34.451 

13.339 31 .782 128.403 34.006 

13.327 32.087 119.159 30.587 

13.329 31 .84 117.541 29.67 

13.324 31 .952 122.26 32.126 

13.346 31 .614 123.56 32.049 

13.329 32.363 115 26.616 

13.319 32.214 115.394 29.226 

13.31 32.097 119.669 30.744 

13.294 32.109 116.514 30.264 

13.264 32.203 11 5.746 26.756 

13.296 32.242 114.07 27.777 

13.271 32.966 104.941 23.977 

13.294 32.542 107.106 24.941 

13.292 32.715 111.473 26.68 

13.306 32.341 111.962 27.449 

13.296 32.672 116.533 29.236 

13.314 32.21 117.075 29.709 

13.294 32.606 120.056 30.544 

13.26 32.946 109.534 26.069 

13.273 33.559 97.155 20.701 

13.266 33.567 93.202 19.247 

13.269 33.391 95.262 20.096 

13.264 33.456 95.135 19.961 

13.252 33.462 95.05 20.132 

13.26 33.497 94.64 19.743 

13.266 33.762 65.923 16.176 

13.23 34.42 75.062 12.256 

13.24 34.166 77.609 13.297 

13.241 34.341 73.927 11 .696 

13.21 34.561 69.496 10.652 

13.215 34.682 66.261 10.159 

13.215 34.519 69.653 10.712 

13.229 34.442 66.699 9.539 

13.256 33.775 76.536 13.744 

13.271 33.666 77.911 13.567 

13.256 34.201 77.147 13.035 

13.277 33.367 62.667 15.449 

13.264 33.04 94.276 19.753 

13.267 32.76 104.766 24.661 

13.276 33.115 96.171 21.529 

13.274 33.053 101 .122 22.876 

13.30 32.65 105.09 

Sentinel Unit 4 100% NOx-NH3-AOG Compliance.xls 

2115/2013 

1:54 PM 
Port 

5 

S 

S 

S 

S 

5 

5 

S 

S 

S 

S 

5 

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 

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 

Date 

211112013 

2111 /2013 

2111/2013 

2111/2013 

2111 /2013 

2111/2013 

2111/2013 

2111/2013 

2111/2013 

2111/2013 

2111 /2013 

211112013 

2111/2013 

2111/2013 

2111/2013 

2111/2013 

2111/2013 

2111/2013 

211 1/2013 

2111/2013 

211112013 

211112013 

2111/2013 

211112013 

211112013 

2111/2013 

2111/2013 

2/11/2013 

2/11/2013 

211112013 

211112013 

2111 /2013 

2111/2013 

2111/2013 

211112013 

211112013 

211112013 

2111/2013 

211112013 

211112013 

2111/2013 

2111 /2013 

211112013 

211112013 

211112013 

2/11/2013 

2/11/2013 

211112013 

211112013 

2111 12013 

2111/2013 

2111/2013 

211112013 

211112013 

2111/2013 

2111/2013 

211112013 

2111 /2013 

Delta AIr QualItY SeMen 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

Time 

11 :41 

11 :42 

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 

12:01 

12:02 

12:03 

12:04 

12:05 

12:06 

12:07 

12:08 

12:09 

12:10 

12:1 1 

12:12 

12:13 

12:14 

12:1 5 

12:21 

12:22 

12:23 

12:24 

12:25 

12:26 

12:27 

12:28 

12:29 

12:30 

12:31 

12:32 

12:33 

12:34 

12:35 

12:40 

12:41 

12:42 

12:43 

12:44 

12:45 

12:46 

12:47 

12:48 

12:51 

12:52 

12:53 

12:54 

REFERENCE METHOD 1-MINUTE AVERAGE DATA 

0, 

13.163 

13.151 

13.184 

13.202 

13.187 

13.188 

13.16 

13.159 

13.16 

13.173 

13.185 

13.153 

13.135 

13.149 

13.111 

13.174 

13.196 

13.185 

13.187 

13.172 

13.177 

13.179 

13.173 

13.177 

13.192 

13.187 

13.198 

13.191 

13.184 

13.188 

13.174 

13.162 

13.159 

13.156 

13.155 

13.157 

13.156 

13.164 

13.178 

13.174 

13.172 

13.168 

13.178 

13.174 

13.176 

13.176 

13.169 

13.165 

13.157 

13.164 

13.145 

13.134 

13.143 

13.139 

13.128 

13.124 

13.127 

13.129 

13.16 

CO, 

4.523 

4.529 

4.505 

4.494 

4.508 

4.505 

4.526 

4.528 

4.529 

4.519 

4.512 

4.536 

4.548 

4.543 

4.568 

4.534 

4.515 

4.522 

4.523 

4.537 

4.534 

4.532 

4.537 

4.535 

4.521 

4.525 

4.518 

4.525 

4.533 

4.528 

4.533 

4.54 

4.541 

4 .543 

4.544 

4.542 

4.542 

4.537 

4.528 

4.531 

4.531 

4.534 

4.528 

4.531 

4.531 

4.527 

4.531 

4.533 

4.534 

4.527 

4.536 

4.538 

4.531 

4.534 

4.544 

4.549 

4.548 

4.548 

4.53 

NO, 

2.85 

2.779 

3.696 

3.055 

2.779 

2.525 

2.632 

2.776 

3.08 

3.651 

3.012 

3.012 

3.006 

2.645 

2.965 

3.915 

3.099 

2.777 

2.701 

2.887 

2.854 

2.819 

2.848 

2.784 

2.805 

2.839 

2.71 

2.664 

2.721 

2.621 

3.003 

2.97 

3.007 

3.021 

2.969 

2.9 

2.867 

2.811 

2.795 

2.829 

2.759 

2.682 

2.681 

2.728 

2.653 

2.785 

2.808 

2.825 

2.79 

2.793 

2.86 

2.801 

2.685 

2.783 

2.849 

2.909 

2.841 

2.908 

2.88 

CO 

2.467 

3 

0.865 

0.148 

0.19 

0.51 

2.259 

2.811 

3.226 

1.528 

0.265 

0.257 

0.415 

1.361 

2.305 

2.333 

0.488 

0.502 

0.936 

1.29 

1.891 

2.126 

1.899 

2.127 

2.234 

2.223 

2.206 

1.954 

1.625 

1.351 

1.866 

1.835 

1.642 

1.596 

1.664 

1.938 

2.283 

2.678 

2.647 

2.713 

2.817 

2.723 

2.914 

2.646 

2.696 

2.55 

2.42 

2.503 

2.745 

2.926 

2.823 

2.75 

2.711 

2.621 

2.551 

2.496 

2.476 

2.433 

2.01 

02-ln 

13.274 

13.288 

13.314 

13.303 

13.294 

13.296 

13.263 

13.284 

13.292 

13.296 

13.291 

13.306 

13.284 

13.265 

13.27 

13.287 

13.277 

13.297 

13.269 

13.278 

13.289 

13.261 

13.272 

13.297 

13.291 

13.303 

NOx-ln 

31.741 

37.77 

39.121 

38.449 

36.096 

32.668 

32.1 81 

31 .356 

34.657 

37.015 

37.042 

36.656 

33.857 

32.755 

32.386 

38.34 

37.143 

34.852 

34.635 

33.679 

33.2 

33.864 

33.271 

33.153 

33.2 

33.126 

CO-In 

123.685 

86.846 

13.841 

14.528 

23.496 

73.698 

124.009 

142.823 

115.755 

23.988 

22.16 

23.474 

49.377 

102.665 

122.938 

19.737 

19.699 

35.267 

48.973 

69.809 

88.112 

81.728 

85.912 

92.354 

95.837 

90.993 

THe-In 

31.977 

20.282 

-0.009 

-0.009 

0.17 

14.808 

32.295 

39.716 

29.76 

0.129 

-0.01 

-0.01 

6.034 

24.465 

30.993 

0.166 

-0.01 

1.674 

4.7 

11 .331 

17.957 

15.329 

17.188 

19.461 

21 .312 

19.761 

13.285 33.309 92.261 20.283 

13.272 33.723 79.013 14.654 

13.268 33.984 64.498 9.185 

13.282 33.581 66.664 10.523 

13.213 33.887 76.19 13.489 

13.208 34.226 71.447 11.836 

13.213 34.029 68.483 10.788 

13.22 33.936 69.025 11.444 

13.218 33.584 72.957 12.7 

13.205 33.139 89.128 18.661 

13.234 32.739 98.762 22.513 

13.241 32.696 103.782 24.951 

13.268 32.296 108.94 27.405 

13.246 32.284 111 .631 28.44 

13.22 32.28 114.703 29.072 

13.259 31 .815 124.366 34.533 

13.247 32.507 116.334 29.706. 

13.249 32.397 112.498 28.257 

13.242 32.186 119.216 31.125 

13.228 32.837 102.615 24.02 

13.234 32.835 101.848 24.144 

13.22 32.599 110.113 26.967 

13.217 32.113 120.677 31 .935 

13.21 32.276 119.395 30.964 

13.202 32.199 121 .694 32.46 

13.189 32.124 119.433 31.011 

13.185 32.304 117.908 30.282 

13.179 32.516 113.128 28.043 

13.197 32.607 111 .052 27.552 

13.199 32.595 106.728 25.04 

13.201 32.644 107.829 26.085 

13.1 98 32.814 105.663 25.002 

13.25 33.64 87.21 

Sentinel Unit 4100% NOx-NH3-ROG Compliance. xis 

2115/2013 

1:54 PM 
COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentlnel-4-CEMS-75-1 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit: 4 

Performed By: AA. SP. SS. JM 

Cp: 0.99 

Tref: 60 ' F 

Slack Area: 143.14 It' 

MeterYd: 0.992 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H2O) sqrt(dP) 'F (Ips) 

4 0.75 0.8660 750 87.85 

3 0.76 0.8718 752 88.51 

2 0.84 0.9165 749 92.94 

1 0.72 0.8485 750 86.08 

4 0.75 0.8660 752 87.93 

3 0.84 0.9165 753 93.09 

2 0.79 0.8888 749 90.13 

1 0.80 0.8944 748 90.66 

4 0.75 0.8660 753 87.96 

3 0.84 0.9165 753 93.09 

2 0.92 0.9592 750 97.30 

1 0.87 0.9327 748 94.54 

4 0.86 0.9274 750 94.08 

3 0.92 0.9592 752 97.38 

2 0.75 0.8660 751 87.89 

1 0.80 0.8944 752 9081 

Average 0.8089 0.8994 750.8 91.27 

Stack Flow Rate: 783.8 kwacfm 

Stack Flow Rate: 304.1 kdscfm 

Dry Gas Meter 

Time Vol. Tm(in) Tm(out) #/Matl. 

Start 665.812 62.0 57.0 H,O 

60.0 57.0 H,O 

End 703.677 60.0 57.0 Empty 

60.0 56.0 SG 

Total 37.865 58.6 Total 

NO. ppm 

NO., ppm@ 15% O2 

NO. Ib/MMBtu 

NO. Iblhr 

CO ppm 

CO, ppm@ 15% O2 

CO Iblhr 

O2 % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

8II1I1I AIr qualfIY S'MCIIS 

1845 N. Case Street 

Orange, California 92865 

714·279·6777 

CT Load MW 

SCR NH3 In·ection Iblhr 

NO. IblMMSCF 

CO IblMM8tu 

CO IblMMSCF 

TEST VARIABLES 

Start Dale: 2111 /13 

Start/End Time: 15:45 16:52 

Load (MW)1Replicate# 75 1 

Barom. Pressure: 29.64 

Pstack: 

Pstack: 

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-Test Direct Span 

Average 

Corr. 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. 

855.7 689.1 166.6 

666.3 665.9 0.4 

487.9 481 .6 6.3 

948.6 938.8 9.8 

Ir 100 83.1 

RESULTS 

Ref. Meth CEMS 

2,49 2,40 

2.07 1.90 

0.008 0.007 

5.50 5.12 

1.23 1.40 

1.02 1.10 

1.63 1.92 

13.81 13.54 

18,246,119 18.220.000 

7.018 . I 

81 

. 115 

7.84 

0.002 

2.41 . 

2.40 iwg 

29.82 "H9 

28.15 Ib/lb-mole 

METHOD 100.1 DATA 

0, CO, NO, CO 

20 10 5 10 

9.99 4.96 2.52 9.47 

0.10 0.0 1 0.03 0.02 

10.04 5.11 254 9.56 

0.20 0.06 0.03 -0.01 

10.02 5.11 2.52 9.51 

0.22 0.08 0.03 ·0.04 

10.05 5.13 2.51 9.50 

0.10 0.03 0.02 0.03 

10.06 5.15 2.53 9.55 

13.81 4.20 2.49 1.21 

13.81 4.06 2.49 1.23 

0.5% 0.5% 0.1% -0.3% 

-0.1% -0.1% -0.3<1/" -0.5% 

0.6% 0.5% 0.2% -0.7% 

-0.1% -0.2% -0.4% -0.5% 

0.1% 0.2% 0.0% -0.3% 

0.1% 0.3% -0.2% -0.1% 

Meier Pressure: 1.5 iwg 

Sample Volume: 37.445 dscf 

H20 Volume : 3.863 scf 

Moisture Conlent 9.4 % 

Sentinel Unit 4 75% NOx-NH3-ROG Compliance. xis 

2/15/2013 

2:04 PM 
COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentinel-4-CEMS-75·2 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit: 4 

Performed By: AA. SP. SS. JM 

Cpo 0.99 

Tret: 60 ' F 

Stack Area: 143.14 ft' 

MeterYtj: 0.992 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H2O) sqrt(dP) ' F (Ips) 

4 0.72 0.8485 749 85.69 

3 0.80 0.8944 750 90.37 

2 0.84 0.9165 751 92.64 

1 0.80 0.8944 750 90.37 

4 0.90 0.9487 751 95.89 

3 0.92 0.9592 752 96.99 

2 0.94 0.9695 752 98.04 

1 0.94 0.9695 750 97.96 

4 0.70 0.8367 750 84.53 

3 0.93 0.9644 751 97.47 

2 0.72 0.8485 748 85.66 

1 0.80 0.8944 750 90.37 

4 0.87 0.9327 752 94.32 

3 0.75 0.8660 751 87.53 

2 0.70 0.8367 752 84.60 

1 0.80 0.8944 749 90.33 

Average 0.8184 0.9047 750.5 91.42 

Stack Flow Rate: 785.2 kwacfm 

Stack Flow Rate: 311.6 kdscfm 

Dry Gas Meter 

Time Vol. Tm(in) Tm(out) #/Matl. 

Start 704.925 60 55 H,O 

61 58 H,O 

End 744.425 59 55 Empty 

58 55 SG 

Total 39.500 57.6 Tolal 

NO. ppm 

NO., ppm@ 15% O2 

NO. IblMMBtu 

NO. Iblhr 

CO ppm 

CO, ppm@ 15% O2 

CO Iblhr 

O2 % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

811118 AIr qualItY SIIMCIIS 

1845 N. Case Street 

Orange, California 92865 

7 14-279-6777 

CT Load MW 

SCR NH3 Iniection Iblhr 

NO. IblMMSCF 

CO IblMMBlu 

CO IblMMSCF 

TEST VARIABLES 

Start Date: 2/11/13 

StarVEnd Time: 17:10 18:19 

Load (MW)/Replicate# 75 2 

Barom. Pressure: 29.64 

Pstack: 

Pstack: 

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-Test Direct Span 

Average 

Corr. 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 Ditt. 

837.2 682.7 154.5 

658.7 658.6 0.1 

581 .6 580.9 0.7 

844.5 833.7 10.8 

I, 100 66.1 

RESULTS 

Ref. Meth CEMS 

2.77 2.60 

2.30 2.13 

0.008 0.008 

6.27 5.67 

1.24 1.40 

1.03 1.11 

1.68 1.90 

13.80 13.57 

18,698,872 18.139,000 

- 6.96 1 

- I - 80 

- 113 

9.01 -

0.002 -

2.42 -

2.40 iwg 

29.82 "Hg 

28.38 Ib/lb-mole 

METHOD 100.1 DATA 

0, CO, NO, CO 

20 10 5 10 

9.98 4.96 2.52 9.47 

0.10 0.03 0.02 0.03 

10.06 5.15 2.53 9.55 

0.22 0.08 0.03 -0.04 

10.05 5.13 2.51 9.50 

0.21 0.09 0.03 -0.02 

10.03 5.13 2.52 9.49 

0.10 0.04 0.02 0.02 

10.05 5.16 2.53 9.56 

13.80 4.20 2.76 1.21 

13.80 4.05 2.77 1.24 

0.6% 0.5% 0.2% -0.7% 

-0.1% -0.2% -0.4% -0.5% 

0.5% 0.5% 0.1% -0.3% 

-0.1% -0.3% -0.2% -0.8% 

-0.1% 0.0% -0.1 % 0.2% 

-0.1% 0.0% 0.1% -0.1% 

Meter Pressure: 1.5 iwg 

Sample Volume: 39.138 dscf 

H20 Volume: 3.073 scf 

Moisture Can lent: 7.3 % 

Senlinel Unit 4 75% NOx-NH3-ROG Compliance. xis 

2/1512013 

2:04 PM 
Port 

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 

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 Date 

3 211112013 

3 211112013 

3 211112013 

3 211112013 

3 211112013 

2 211112013 

2 211112013 

2 211112013 

2 211112013 

3 

3 

3 

3 

2 

2 

2 

2 

3 

3 

3 

3 

3 

2 

2 

2 

2 

2 

3 

3 

3 

3 

3 

2 

2 

2 

2 

2 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

2111 12013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

Dell8A/rQualfIY S.mC'S 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

Time 

15:46 

15:47 

15:48 

15:49 

15:50 

15:51 

15:52 

15:53 

15:54 

15:57 

15:58 

15:59 

16:00 

16:04 

16:05 

16:06 

16:07 

16:10 

16:11 

16:12 

16:13 

16:14 

16:15 

16:16 

16:17 

16:18 

16:21 

16:22 

16:23 

16:24 

16:25 

16:26 

16:27 

16:28 

16:29 

16:30 

16:31 

16:32 

16:33 

16:34 

16:35 

16:39 

16:40 

16:41 

16:42 

16:43 

16:44 

16:45 

16:46 

16:47 

16:48 

16:49 

16:50 

16:51 

16:51 

16:52 

REFERENCE METHOD l-MINUTE AVERAGE DATA 

0 , 

13.827 

13.829 

13.824 

13.83 

13.833 

13.824 

13.829 

13.821 

13.817 

13.772 

13.773 

13.776 

13.774 

13.831 

13.832 

13.834 

13.833 

13.83 

13.827 

13.83 

13.818 

13.805 

13.799 

13.802 

13.804 

13.806 

13.823 

13.814 

13.811 

13.817 

13.819 

13.835 

13.832 

13.831 

13.829 

13.831 

13.823 

13.796 

13.797 

13.807 

13.819 

13.843 

13.831 

13.829 

13.83 

13.825 

13.801 

13.799 

13.801 

13.794 

13.806 

13.756 

13.761 

13.765 

13.765 

13.769 

13.81 

CO, 

4.187 

4.187 

4.188 

4.183 

4.18 

4.187 

4.186 

4.1 91 

4.196 

4.225 

4.226 

4.228 

4.227 

4.2 

4.196 

4.192 

4.194 

4.197 

4.193 

4.186 

4.191 

4.197 

4.201 

4.201 

4.201 

4.202 

4.192 

4.195 

4.198 

4.196 

4.195 

4.188 

4.187 

4.19 

4.194 

4.192 

4.194 

4.212 

4.21 

4.207 

4.2 

4.181 

4.19 

4.189 

4.192 

4.193 

4.207 

4.21 

4.21 

4.215 

4.209 

4.236 

4.236 

4.236 

4.236 

4.24 

4.20 

NO, 

2.286 

2.229 

2.305 

2.219 

2.133 

2.243 

2.184 

2.313 

2.253 

2.185 

2.28 

2.15 

2.163 

2.288 

2.316 

2.451 

2.347 

2.163 

2.1 

2.152 

2.223 

2.234 

2.229 

2.059 

2.084 

2.077 

2.362 

2.439 

2.558 

2.642 

3.151 

3.152 

3.143 

3.106 

3.017 

3.06 

2.833 

2.538 

2.681 

2.532 

2.578 

2.676 

2.769 

2.782 

2.72 

2.579 

2.629 

2.738 

2.585 

2.799 

2.583 

2.761 

2.717 

2.739 

2.739 

2.699 

2.49 

CO 

1.55 

1.671 

1.529 

1.473 

1.721 

1.911 

1.861 

1.794 

1.979 

1.436 

1.279 

1.231 

1.228 

1.55 

1.569 

1.322 

1.174 

1.344 

1.469 

1.489 

1.575 

1.4 

1.39 

1.285 

1.324 

1.374 

1.4 

1.335 

1.229 

1.145 

1.089 

1.037 

1.053 

1.043 

1.03 

1.014 

1.044 

1.058 

0.949 

0.915 

0.934 

0.977 

0.886 

0.922 

0.842 

0.864 

0.788 

0.688 

0.68 

0.68 

0.705 

0.68 

0.675 

0.711 

0.711 

0.738 

1.21 

02-1n 

13.845 

13.844 

13.846 

13.854 

13.862 

13.872 

13.872 

13.877 

13.865 

NOx-ln CO-In THC-In 

26.189 92.085 14 .417 

26.207 99.379 18.71 

26.366 87.895 12.693 

26.001 91.769 14.313 

25.511 107.669 21 .741 

25.2 121.053 29.526 

25.025 127.066 32.946 

25.072 125.007 32.352 

25.1 6 137.838 40.409 

13.86 25.969 104.595 20.844 

13.876 26.137 92.304 14.216 

13.863 26.32 87.058 11.92 

13.86 26.086 90.055 13.338 

13.894 26.241 84.851 11.209 

13.904 26.249 86.049 11.419 

13.885 27.017 71.316 6.732 

13.886 26.764 68.261 6.081 

13.877 26.335 77.949 9.005 

13.873 26.312 81 .901 10.211 

13.879 25.799 87.147 12.107 

13.854 26.301 84.435 11 .179 

13.854 26.254 80.409 9.846 

13.842 26.533 77.234 8.872 

13.846 26.46 76.394 8.551 

13.866 26.426 78.046 8.954 

13.854 26.492 79.314 9.392 

13.855 26.667 76.664 8.668 

13.851 26.815 72.161 7.1 98 

13.849 26.918 67.277 5.933 

13.842 27.104 64.487 5.104 

13.855 27.32 59.029 3.588 

13.867 27.1 21 59.785 3.613 

13.862 27.19 60.119 3.672 

13.861 27.327 58.687 3.426 

13.87 27.411 57.24 3.1 

13.869 27.445 56.467 2.957 

13.861 26.996 61 .277 4.1 41 

13.85 27.15 62.89 4.416 

13.853 27.371 57.425 3.023 

13.858 27.263 56.889 3.051 

13.873 27.203 57.513 2.954 

13.881 27.376 58.904 3.494 

13.85 27.197 56.918 3.119 

13.852 27.381 55.924 2.944 

13.871 27.386 54.231 2.478 

13.872 27.549 53.914 2.467 

13.871 27.66 54.112 2.629 

13.884 27.73 51.273 2.034 

13.872 27.673 52.769 2.371 

13.887 27.674 51 .004 1.773 

13.868 27.563 52.745 2.435 

13.869 27.598 52.048 2.204 

13.885 27.33 54.034 2.548 

13.889 27.536 53.316 2.351 

13.889 27.536 53.316 2.351 

13.908 27.517 53.502 2.359 

13.87 26.71 75.35 

Sentinel Unit 475% NOx-NH3-ROG Compliance.xls 

2115/2013 

2:04 PM 
Port 

5 

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 

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 

2 

2 

2 

2 

3 

3 

3 

3 

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 

211112013 

211112013 

211112013 

21111201 3 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211 112013 

2111 /2013 

211112013 

211112013 

211112013 

211112013 

21 1112013 

211112013 

211112013 

211112013 

211112013 

2111 12013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211 112013 

211 112013 

211112013 

211 112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

211112013 

8BItaAl,QualllY SBMCIIS 

1845 N. Case Street 

Orange, California 92865 

714·279·6777 

REFERENCE METHOD 1·MINUTE AVERAGE DATA 

17:11 13.79 4.192 2.924 1.121 

17:12 

17:13 

17:1 4 

17:17 

17:18 

17:19 

17:20 

17:21 

17:22 

17:23 

17:24 

17:25 

17:29 

17:30 

17:31 

17:32 

17:35 

17:36 

17:37 

17:38 

17:39 

17:40 

17:41 

17:42 

17:43 

17:47 

17:48 

17:49 

17:50 

17;51 

17:52 

17:53 

17:54 

17:55 

17:56 

17:57 

17:58 

17:59 

18:00 

18:01 

18:05 

18:06 

18:07 

18:08 

18:09 

18:10 

18:11 

18:12 

18:13 

18:14 

18:15 

18:16 

18:17 

18:1 8 

18:19 

13.789 

13.794 

13.799 

13.786 

13.783 

13.785 

13.775 

13.765 

13.74 

13.753 

13.756 

13.754 

13.803 

13.804 

13.827 

13.822 

13.799 

13.785 

13.788 

13.778 

13.773 

13.747 

13.765 

13.755 

13.757 

13.825 

13.822 

13.817 

13.808 

13.809 

13.806 

13.818 

13.821 

13.814 

13.814 

13.804 

13.793 

13.797 

13.805 

13.805 

13.806 

13.805 

13.807 

13.816 

13.814 

13.807 

13.812 

13.809 

13.807 

13.812 

13.81 

13.803 

13.804 

13.808 

13.81 

13.80 

4.193 

4.193 

4.193 

4.201 

4.204 

4.205 

4.211 

4.219 

4.23 

4.228 

4.225 

4.226 

4.204 

4.205 

4.194 

4.197 

4.21 

4.218 

4.218 

4.225 

4.23 

4.245 

4.237 

4.245 

4.248 

4.201 

4.1 98 

4.199 

4.197 

4.195 

4.19 

4.184 

4.179 

4.185 

4.186 

4.194 

4.201 

4.201 

4.193 

4.193 

4.187 

4.189 

4.19 

4.187 

4.19 

4.195 

4.197 

4.197 

4.201 

4.199 

4.202 

4.207 

4.208 

4.21 

4.212 

4.20 

2.918 

2.886 

2.769 

2.691 

2.712 

2.642 

2.841 

2.511 

2.677 

2.463 

2.61 3 

2.759 

2.674 

2.574 

2.593 

2.692 

2.712 

2.957 

2.875 

2.884 

2.788 

2.805 

2.717 

3 

2.928 

2.617 

2.951 

3.066 

3.133 

2.992 

2.863 

2.741 

2.66 

2.704 

2.754 

2.817 

2.633 

2.542 

2.46 

2.458 

2.596 

2.72 

2.653 

2.741 

2.712 

2.55 

2.492 

2.98 

3.243 

3.073 

2.952 

2.837 

2.881 

2.796 

2.622 

2.76 

1.117 

1.121 

1.102 

0.89 

0.806 

0.837 

0.821 

0.808 

0.842 

0.884 

0.817 

0.868 

1.077 

1.067 

1.146 

1.164 

1.135 

1.143 

1.178 

1.061 

1.025 

0.995 

0.934 

0.988 

0.971 

1.313 

1.353 

1.391 

1.379 

1.372 

1.388 

1.478 

1.585 

1.624 

1.58 

1.455 

1.356 

1.352 

1.464 

1.516 

1.389 

1.434 

1.41 

1.431 

1.432 

1.418 

1.366 

1.333 

1.293 

1.326 

1.416 

1.35 

1.38 

1.338 

1.36 

1.21 

02·10 NOx-ln CO-In THe-In 

13.805 26.714 69.369 6.265 

13.819 26.73 68.916 6.149 

13.84 26.925 67.541 6.014 

13.835 26.953 68.591 6.25 

13.872 27.295 59.876 3.994 

13.831 27.272 58.603 3.501 

13.845 27.221 58.149 3.327 

13.922 27.223 57.217 3.159 

13.843 27.22 58.783 3.526 

13.84 27.065 60.019 3.853 

8.842 18.686 56.853 8.784 

0.07 0.749 5.84 45.244 

0.043 0.589 0.106 46.703 

13.881 26.844 63.866 5.201 

13.928 26.584 67.747 5.201 

13.942 26.529 71.76 5.201 

13.96 26.283 72.58 5.201 

13.954 26.186 81 .977 5.201 

13.954 25.945 83.571 5.2 

13.918 26.341 80.178 5.2 

13.918 26.509 72.653 5.2 

13.937 26.534 72.136 5.2 

13.935 26.85 72.598 5.201 

13.937 26.674 71.899 5.201 

13.903 26.706 74.177 5.201 

13.921 26.636 71 .262 5.201 

13.943 26.271 75.02 5.199 

13.933 26.235 76.539 5.199 

13.929 26.201 78.564 5.199 

13.949 26.31 76.641 5.199 

13.94 26.37 75.359 5.1 99 

13.977 25.904 80.29 5.2 

13.958 25.597 86.009 5.2 

13.941 25.633 91.446 5.2 

13.927 25.779 88.955 5.201 

13.914 26.105 85.967 5.201 

13.905 26.298 79.37 5.2 

13.918 26.204 78.669 5.2 

13.927 25.928 63.189 5.2 

13.915 25.666 88.673 5.201 

13.939 25.487 91.334 5.201 

13.929 25.955 80.377 5.2 

13.93 26.029 79.319 5.2 

13.939 25.966 82.075 5.201 

13.935 26.059 81 .721 5.202 

13.94 26.118 81 .625 5.202 

13.938 26.198 78.1 11 5.202 

13.939 26.463 74.791 5.202 

13.946 26.292 76.712 5.201 

13.94 26.439 73.232 5.201 

13.939 26.004 77.954 5.2 

13.949 25.965 80.262 5.2 

13.955 25.822 81 .957 5.201 

13.936 26.09 80.462 5.201 

13.948 26.126 80.755 5.201 

13.962 25.962 83.375 5.201 

13.37 25.39 72.71 

Sentinel Unit 4 75% NOx-NH3-ROG Compliance. xis 

211512013 

2:04 PM 
COMPLIANCE TEST 

OATA AND WORKSHEET 

CPV Sentlnel-4-CEMS-50-1 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit 4 

Performed By: M,MC,RM,JM 

Cp: 0.99 

Tref: 60 'F 

Slack Area: 143.14 ft' 

MeterYd: 0.992 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H2O) sqrt{dP) ' F (fps) 

4 0.67 0.8185 779 83.80 

3 0.82 0.9055 781 92.78 

2 0.85 0.9220 782 94.50 

1 0.79 0.8888 780 91 .03 

4 DAD 0.6325 781 64.80 

3 0.46 0.6762 782 69.52 

2 0.71 0.8426 783 86.40 

1 0.77 0.8775 781 89.91 

4 0.42 0 .6481 780 66.37 

3 0.47 0.6856 782 70.27 

2 0.51 0.7141 782 73.20 

1 0.48 0.6928 781 70.98 

4 0.71 0.8426 782 86.37 

3 0.76 0.8718 782 89.36 

2 0.89 0.9434 783 96.74 

1 0.82 0.9055 781 92.78 

Average 0.6470 0.8043 781.4 82.42 

Stack Flow Rate: 707.9 kwacfm 

Stack Flow Rate: 270.9 kdscfm 

Dry Gas Meter 

Time Vol. Tm(in) Tm(out) #lMati. 

Start 848.550 81 77 H,O 

82 78 H,O 

End 894.424 83 83 Empty 

68 69 SG 

Total 45.874 77.6 Tolal 

NOx ppm 

NOx , ppm@ 15% O2 

NOx Ib/MMBtu 

NOx Ib/hr 

CO ppm 

CO, ppm@ 15% O2 

CO Ib/hr 

O2 % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

8,It8A1rQu.11IY S'Me,S 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

CTload MW 

SCR NH3 Injection Iblhr 

NOx Ib/MMSCF 

CO IblMMBtu 

CO IblMMSCF 

TEST VARIABLES 

Start Date: 2/12/13 

Start/End Time: 11 :58 13:07 

Load (MW)/Replicate# 50 1 

Barom. Pressure: 29.74 

Pstack: 

Pstack: 

MW: 

Analyzer Range 

Cal Gas Value 

Pre-Test Direct Zero 

Pre-Test Direct Span 

Pre-Test System Zero 

Pre-Test System Soan 

Post-Test System Zero 

Post-Test System Span 

Post-Test Direct Zero 

Post-Test Direct Span 

Average 

COIT. results 

Pre-test zero bias 

Pre-test span bias 

Post-test zero bias 

Post-test span bias 

Zero drift 

Soan drift 

METHOD 4.1 DATA 

Impingers 

End Start Ditt. 

862.6 687.3 175.3 

664.8 662.1 2.7 

488.2 487.3 0.9 

918.5 908.2 10.3 

Ir 100 89.2 

RESULTS 

Ref. Meth CEMS 

2.43 2.10 

2.16 1.84 

0.008 0.007 

4.79 3.79 

0.36 0.50 

0.32 0.39 

0.43 0.56 

14.27 14.09 

16,254.483 14,978,000 

5.337 

-. 

55 

102 

8.97 

0.001 -

0.76 -

2.40 iwg 

29.92 "Hg 

28,21 Ib/lb-rnole 

METHOD 100.1 DATA 

0, CO, NO, CO 

20 10 5 10 

9.98 4.96 2.52 9.47 

0.10 0.10 0.01 0.06 

10.05 5.20 2.51 9.62 

0.13 0. 12 0.02 0.07 

10 .03 5.18 2.50 9.58 

0 ,14 0 ,15 0.02 0.05 

10.00 5.20 2.49 9.58 

0.10 0 .11 0.D1 0.06 

10.02 5.21 2.51 958 

14.26 4.00 2.41 0.43 

14.27 3.80 2.43 0.36 

0.1% 0.3% 0.3% 0.1% 

-0.1% -0.2% -0.2% -0.4% 

0.2% 0 .4% 0.2% -0.1% 

-0.1% -0.2% -0.3% 0.0% 

0.1% 0 .3% 0.0% -0.2% 

-0.2% 0 .2% -0.3% 0.0% 

Meter Pressure: 1.5 iwg 

Sample Volume: 43.909 dscf 

H20 Volume : 4.146 scf 

Moisture Content: 8.6 % 

Sentinel Unit 4 50% NOx-NH3-AOG Compliance. xis 

2/15/2013 

1:54 PM 
COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentlnel-4-CEMS-50-2 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit: 4 

Perfonned By: M,MC,RM, JM 

Cp: 0.99 

Tref: 60 "F 

Stack Area: 143.14 II' 

Meier Yd: 0.992 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H2O) sqrt(dP) "F (Ips) 

4 0.52 0.7211 788 74.03 

3 0.63 0.7937 790 81 .55 

2 0.68 0.8246 792 84.80 

1 0.82 0.9055 790 93.04 

4 0.49 0.7000 793 72.01 

3 0.52 0.721 1 794 74.21 

2 0.54 0.7348 793 75.60 

1 0.52 0.7211 792 74. 15 

4 0.46 0.6782 795 69.83 

3 0.50 0.7071 796 72.83 

2 0.64 0.8000 796 82.40 

1 0.77 0.8775 794 90.31 

4 0.64 0.8000 793 82.30 

3 0.83 0.9110 795 93.80 

2 0.87 0.9327 796 96.07 

1 0.78 0.8832 794 90.89 

Average 0.6312 0.7945 793.2 81 .74 

Stack Flow Rate: 702.0 kwacfm 

Stack Flow Rate: 267.3 kdscfm 

Dry Gas Meier 

Time Vol. Tm(in) Tm(out) #/Matl. 

Start 895.949 73 71 H,O 

69 69 H,O 

End 937.886 68 68 Empty 

70 69 5G 

Total 41 .937 69.6 Total 

NOx ppm 

NOx , ppm @ 15% O2 

NOx Ib/MMBtu 

NOx Iblhr 

CO ppm 

CO, ppm@ ' 5%02 

CO Iblhr 

O2 % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

811118 AIr QUIlIIty SIIMCII' 

1845 N. Case Streel 

Orange, California 92865 

714-279-6777 

CT load MW 

SCR NH3 hectlon Ib/hr 

NO, IblMMSCF 

CO IblMM9tu 

CO IbiMMSCF 

TEST VARIABLES 

Start Date: 2/12/13 

Start/End Time: 13:30 14:39 

load (MW)lReplicate# 50 2 

Barom. Pressure: 29.74 

Pslack: 

Pstack: 

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-Test Direct Span 

Average 

Corr. results 

Pre-test zero bias 

Pre-test span bias 

PosHest zero bias 

Post-test span bias 

Zero drift 

Span drift 

METHOD 4.1 DATA 

Impingers 

End Start Oitt. 

844.8 680.8 164.0 

658.0 657.3 0.7 

580.2 580.2 0.0 

858.4 844.5 13.9 

Ir 100 78.6 

RESULTS 

Ref. Meth CEMS 

2.09 1.80 

1.86 1.58 

0.007 0.01 

4.06 3.26 

0.43 0.40 

0.38 0.36 

0.50 0.56 

14.26 14.05 

16,037,165 14,901,000 

5,341 

L. 55 

107 

7.61 -

0.001 -

0.91 -

2.40 iwg 

29.92 "Hg 

28.26 Ibllb-mole 

METHOD 100.1 DATA 

0, CO, NO, CO 

20 10 5 10 

9.98 4.96 2.52 9.47 

0.10 0.11 0.01 0.06 

10.02 5.21 2.51 9.58 

0.14 0.15 0.02 0.05 

10.00 5.20 2.49 9.58 

0.14 0.18 0.03 0.04 

10.00 5.24 2.50 9.59 

0.10 0. 13 0.00 0.05 

10.00 5.25 2.50 9.60 

14.22 4.02 2.07 0.48 

14.26 3.79 209 0.43 

0,2% 0.4% 0.2% -0.1% 

-0.1% -0.2% -0.3% 0.0% 

0.2% 0.4% 0.5% -0.1% 

0.0% 0.0% 0.0% -0.1% 

0.0% 0.3% 0.2% -0.1% 

0.0% 0.5% 0.1% 0.0% 

Meter Pressure: 1.5 iwg 

Sample Volume: 40.747 dscf 

H20 Volume : 3.654 scf 

Moisture Content: 8.2 % 

Sentinel Unit 4 50% NOx-NH3-ROG Compliance. xis 

2/15/201 3 

1:54 PM 
Port 

5 

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 

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 

Date 

2112/2013 

2112/2013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

2112/2013 

2112/2013 

211212013 

211212013 

211212013 

211212013 

2112/2013 

211212013 

211212013 

2112/2013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

2/12/2013 

211212013 

211212013 

2112/2013 

211212013 

211212013 

211212013 

211212013 

2/1212013 

2/1212013 

211212013 

2/1212013 

211212013 

211212013 

211212013 

211212013 

211212013 

2/1212013 

2112/2013 

2/12/2013 

211212013 

211212013 

211212013 

211212013 

2/1212013 

2/12/2013 

211212013 

2112/2013 

211212013 

211212013 

211212013 

Of/haA/rOua/fIY S'Me,S 

1845 N. Case Street 

Orange, California 92865 

714·279·6777 

Time 

11 :59 

12:00 

12:01 

12:02 

12:03 

12:04 

12:05 

12:06 

12:07 

12:08 

12:09 

12:10 

12:11 

12:12 

12:13 

12:17 

12:18 

12:19 

12:20 

12:21 

12:22 

12:23 

12:24 

12:25 

12:26 

12:27 

12:28 

12:29 

12:30 

12:31 

12:35 

12:36 

12:37 

12:38 

12:39 

12:40 

12:41 

12:42 

12:43 

12:44 

12:45 

12:46 

12:47 

12:48 

12:49 

12:53 

12:54 

12:55 

12:56 

12:59 

13:00 

13:01 

13:02 

13:03 

13:04 

13:05 

13:06 

13:07 

REFERENCE METHOD 1·MINUTE AVERAGE DATA 

14.269 4.003 1.739 0.345 

14.268 

14.27 

14.283 

14.279 

14.277 

14.242 

14.263 

14.263 

14.246 

14.241 

14.204 

14.204 

14.204 

14.198 

14.286 

14.285 

14.277 

14.278 

14.268 

14.274 

14.271 

14.266 

14.265 

14.264 

14.268 

14.266 

14.259 

14.264 

14.261 

14.241 

14.252 

14.238 

14.242 

14.251 

14.23 

14.207 

14.257 

14.259 

14.255 

14.255 

14.191 

14.176 

14.18 

14.19 

14.286 

14.288 

14.283 

14.277 

14.286 

14.282 

14.279 

14.279 

14.264 

14.262 

14.257 

14.259 

14.256 

14.26 

4.002 

4.001 

3.994 

3.998 

4 

4.017 

4.005 

4.007 

4.015 

4.021 

4.047 

4.048 

4.05 

4.049 

3.995 

3.994 

3.997 

3.995 

3.999 

3.996 

3.996 

3.994 

3.993 

3.991 

3.988 

3.989 

3.992 

3.989 

3.99 

3.999 

3.993 

4 

3.999 

3.995 

4.007 

4.018 

3.991 

3.994 

3.995 

3.996 

4.035 

4.041 

4.04 

4.033 

3.981 

3.978 

3.982 

3.983 

3.978 

3.982 

3.983 

3.983 

3.992 

3.991 

3.995 

3.992 

3.996 

4.00 

1.765 

1.705 

1.683 

1.818 

1.785 

2.245 

2.268 

2.255 

2.32 

2.111 

2.246 

2.178 

2.273 

2.293 

1.871 

1.87 

1.888 

1.932 

2.004 

1.841 

1.851 

1.812 

1.914 

1.825 

1.849 

1.886 

1.788 

1.798 

1.897 

2.798 

2.637 

2.947 

2.776 

2.698 

3.103 

3.322 

3.063 

3.034 

2.952 

2.991 

3.004 

3.117 

2.916 

2.804 

3.228 

3.192 

3.13 

3.101 

2.648 

2.817 

2.696 

2.561 

2.571 

2.506 

2.449 

2.333 

2.403 

2.41 

0.329 

0.35 

0.353 

0.362 

0.344 

0.288 

0.263 

0.235 

0.237 

0.231 

0.308 

0.336 

0.365 

0.334 

0.508 

0.553 

0.535 

0.556 

0.542 

0.542 

0.567 

0.564 

0.525 

0.577 

0.537 

0.579 

0.517 

0.542 

0.528 

0.385 

0.407 

0.388 

0.369 

0.373 

0.349 

0.266 

0.263 

0.274 

0.267 

0.275 

0.379 

0.354 

0.35 

0.344 

0.542 

0.553 

0.543 

0.535 

0.526 

0.524 

0.503 

0.533 

0.492 

0.479 

0.456 

0.492 

0.467 

0.43 

02-ln 

14.323 

14.337 

14.338 

14.34 

14.342 

14.34 

NOx-ln 

26.852 

26.781 

26.731 

26.731 

26.562 

26.692 

50.558 

50.621 

51 .083 

51 .714 

51 .892 

51.607 

THe-In 

1.33 

1.263 

1.238 

1.3 

1.469 

1.44 

14.343 26.497 53.01 1.535 

14.343 26.678 51 .98 1.524 

14.342 27.012 49.591 1.124 

14.342 27.046 48.418 0.968 

14.343 26.859 49.444 1.172 

14.344 26.806 49.908 1.249 

14.347 26.595 51.292 1.322 

14.345 26.713 51.26 1.337 

14.342 26.821 50.506 1.156 

14.338 26.468 52.756 1.485 

14.332 26.463 53.195 1.665 

14.319 26.47 52.917 1.59 

14.318 26.404 53.891 1.62 

14.317 26.414 53.217 1.591 

14.317 26.364 53.887 1.697 

14.317 26.391 53.529 1.623 

14.317 26.392 54.084 1.628 

14.31 7 26.347 53.774 1.587 

14.317 26.212 54.987 1.753 

14.318 26. 164 55.822 1.678 

14.317 26.353 54.852 1.568 

14.317 26.195 55.237 1.738 

14.317 26.235 55.727 1.864 

14.317 

14.317 

14.317 

14.317 

14.317 

14.317 

14.317 

14.335 

14.34 

14.335 

14.34 

26.354 

26.388 

26.327 

26.499 

26.25 

26.181 

26.496 

26.251 

26.086 

26.36 

26.237 

54.492 

53.085 

54.767 

53.048 

55.11 

56.07 

53.822 

54.292 

56.39 

55.162 

54.94 

1.713 

1.434 

1.648 

1.419 

1.613 

1.763 

1.467 

1.586 

1.927 

1.797 

1.638 

14.341 26.189 55.55 1.788 

14 .338 26.382 54.88 1.724 

14.332 26.491 52.693 1.402 

14.333 26.385 53.528 1.449 

14.33 26.396 53.554 

14.337 26.219 55.276 

14.342 26.084 56.717 

14.338 26.251 54.649 

14.339 26.522 53.049 

14.339 26.428 53.688 

14.337 26.399 53.634 

14.328 26.661 51.413 

14.332 26.628 51.871 

1.544 

1.757 

1.931 

1.57 

1.483 

1.548 

1.496 

1.258 

1.185 

14 .326 26.803 50.053 1.01 

14.321 26.921 49.355 0.815 

14.317 26.912 48.919 0.935 

14.317 26.901 49.249 0.933 

14.317 27.027 48.319 0.791 

14.33 26.50 52.93 

Sentinel Unit 4 50% NOx-NH3-ROG Compliance.xls 

211512013 

1:54 PM 
Port 

s 

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 

N 

N 

w 

w 

w 

w 

w 

w 

w 

w 

w 

w 

w 

w 

w 

w 

w 

Average 

Point Date 

3 2112/2013 

3 211212013 

3 211212013 

3 2112/2013 

2 211212013 

2 211212013 

2 2112/2013 

3 

3 

3 

3 

2 

2 

2 

3 

3 

3 

3 

3 

2 

2 

2 

2 

3 

3 

3 

3 

3 

2 

2 

2 

2 

2 

211212013 

211212013 

2112/2013 

211212013 

211212013 

211212013 

211212013 

2112/2013 

211212013 

2112/2013 

211212013 

2112/2013 

211212013 

211212013 

211212013 

211212013 

2112/2013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

2/1212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

211212013 

2/12/2013 

211212013 

211 212013 

211212013 

211212013 

211212013 

88118A1,QU8//tyS8rr1C8S 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

Time 

13:31 

13:32 

13:33 

13:34 

13:37 

13:38 

13:39 

13:42 

13:43 

13:44 

13:45 

13:49 

13:50 

13:51 

13:52 

13:55 

13:56 

13:57 

14:00 

14:01 

14:02 

14:03 

14:07 

14:08 

14:09 

14:10 

14:11 

14:12 

14:13 

14:14 

14:15 

14:18 

14:19 

14:20 

14:21 

14:25 

14:26 

14:27 

14:28 

14:29 

14:30 

14:31 

14:32 

14:33 

14:34 

14:35 

14:36 

14:37 

14:38 

14:39 

REFERENCE METHOD I-MINUTE AVERAGE DATA 

0, 

14.213 

14.227 

14.214 

14.208 

14.201 

14.205 

14.203 

14.171 

14.162 

14.171 

14.171 

14.259 

14 .25 

14.252 

14.251 

14.235 

14.232 

14.232 

14.233 

14.231 

14.224 

14.217 

14.203 

14.203 

14.2 

14 .203 

14.203 

14.203 

14.201 

14.203 

14.203 

14.2 

14.203 

14.203 

14.199 

14.226 

14.227 

14.225 

14.224 

14.216 

14.224 

14.225 

14.232 

14.237 

14.234 

14.229 

14.225 

14.232 

14.234 

14.236 

14.22 

CO, 

3.999 

3.992 

3.997 

4.001 

4.016 

4.01 

4.015 

4.037 

4.038 

4.033 

4.036 

3.988 

3.995 

3.995 

3.996 

4.007 

4.008 

4.009 

4 .012 

4.014 

4.018 

4.022 

4.037 

4.036 

4.041 

4.038 

4.041 

4.042 

4.045 

4.041 

4.041 

4.049 

4.047 

4.047 

4.051 

4.03 

4.028 

4.031 

4.035 

4.035 

4.032 

4.032 

4.028 

4.027 

4.029 

4.032 

4.033 

4.029 

4.027 

4.027 

4.02 

NO, 

2.009 

1.816 

1.974 

2.014 

2.35 

2.228 

2.263 

2.416 

2.466 

2.312 

2.482 

1.919 

2.075 

1.993 

1.896 

2.009 

1.797 

1.653 

1.665 

1.721 

1.663 

1.708 

2.374 

2.308 

2.347 

2.304 

2.394 

2.401 

2.366 

2.013 

1.927 

1.871 

1.798 

1.97 

2.028 

2.027 

1.941 

1.908 

1.934 

2.008 

2.044 

2.07 

2.082 

2.182 

2.178 

2.275 

2.233 

2.279 

2.236 

2.343 

2.07 

CO 

0.34 

0.378 

0.36 

0.291 

0.288 

0.252 

0.25 

0.249 

0.292 

0.299 

0.329 

0.73 

0.705 

0.686 

0.632 

0.549 

0.527 

0.509 

0.526 

0.494 

0.495 

0.479 

0.525 

0.559 

0.544 

0.561 

0.595 

0.541 

0.513 

0.559 

0.53 

0.514 

0.503 

0.533 

0.49 

0.506 

0.538 

0.496 

0.492 

0.501 

0.516 

0.51 

0.518 

0.563 

0.566 

0.553 

0.531 

0.511 

0.544 

0.546 

0.48 

02-ln 

14.316 

14.316 

14.316 

14.316 

14.32 

14.322 

14.327 

NOx-ln CO-In THC-In 

26.433 51 .774 1.327 

26.52 52.101 1.41 

26.826 50.003 1.059 

26.829 49.395 0.828 

26.433 53.395 1.542 

26.508 52.933 1.285 

26.534 52.248 1.235 

14.339 26.591 51.725 1.008 

14.342 26.309 53.934 1.439 

14.341 26.276 54.979 1.644 

14.342 26.361 53.97 1.467 

14.34. 26.484 53.72 1.804 

14.342 26.413 53.267 1.608 

14.34 26.459 53.09 1.473 

14.33 26.618 52.512 1.29 

14.317 27.021 48.737 0.868 

14.317 27.104 47.989 0.788 

14.316 27.181 47.472 0.759 

14.316 27.064 48.423 0.931 

14.315 26.918 49.046 0.945 

14.316 27.133 47.779 0.724 

14.314 27.281 46.688 0.696 

14.316 26.966 49.114 0.871 

14.315 26.92 49.886 0.999 

14.317 26.778 50.266 1.131 

14.317 26.732 51.159 1.162 

14.317 26.819 50.565 1.03 

14.315 26.965 49.802 0.894 

14.317 26.832 49.73 0.949 

14.316 26.814 50.224 0.934 

14.314 26.859 49.818 0.952 

14.309 26.945 48.684 0.782 

14.311 26.875 49.839 0.909 

14.311 26.838 49.709 0.921 

14.297 26.944 49.17 0.869 

14.297 26.896 49.659 0.961 

14.298 26.799 50.309 0.915 

14.292 26.952 49.718 0.979 

14.291 27.019 48.931 0.851 

14.296 26.843 49.592 0.866 

14.293 26.899 49.881 0.911 

14.294 27.036 49.03 0.766 

14.314 26.783 50.338 1.078 

14.314 26.664 51.466 1,151 

14.304 26.845 50.625 0.945 

14.294 27.011 49.689 0.874 

14.305 26.887 50.163 0.85 

14.314 26.765 50.8 0.95 

14.314 26.664 52.528 1.148 

14.314 26.673 52.979 1.351 

14.32 26.78 50.58 

Sentinel Unit 4 50% NOx-NH3-ROG Compliance.xls 

2/15/2013 

1:54PM 
Appendix C.2.3 One Minute Data Logger Data 

R041 0688 C-6 
Date Time 

0, 

% 

CO, 

% 

2/11/2013 7:31:00AM 19.788 0.489 

2/11/2013 7:32:00AM 19.755 0.488 

NO, 

PPM 

CO 

PPM 

0, 

% 

NO, 

PPM 

0.011 -0.346 16.94 -0.003 

0.011 -0.336 16.92 -0.008 

CO 

PPM 

0.028 

0.046 

THC 

PPM 

0.427 N2/NOx Mode 

0.478 

2/11/2013 7:33:00 AM 19.741 0.486 0.012 -0.335 16.898 -0.011 0.043 0.533 N2INO Mode 

211112013 U4:00AM 19.726 0.487 2.008 -0.331 16.892 1.824 0.046 0.433 

211112013 7:35:00 AM 19.711 0.488 4.822 -0.333 16.861 4.654 0.041 0.517 NO/NOx Mode 

211 112013 7:36:00 AM 19.708 0.488 4.631 -0.336 16.66 4.644 0.089 1.323 

2111/2013 7:37:00 AM 19.706 0.489 4.623 -0.337 16.878 4.645 0.065 .0.005 NO/NO Mode 

2111/2013 7:38:00 AM 19.697 0.489 2.217 -0.322 16.871 2.319 0.104 -0.005 ITHC Zero 

2111/2013 7:39:00AM 19.726 0.488 0.021 -0.337 16.868 0.002 0.139 -0.004 N02/NOMode 

2111/2013 7:40:00AM 19.799 0.486 3.186 -0.332 16.874 3.289 0.077 61.553 

2/11/2013 7:41 :00 AM 19.316 0.484 3.666 -0.335 16.893 3.686 0.071 78.003 N02lNOx Mode 

211112013 7:42:00 AM 9.121 0.484 2.095 -0.327 16.951 2.207 0.067 80.356 

2111/2013 7:43:00 AM 5.273 0.486 0.131 -0.348 16.99 0.117 0.035 85.136 ITHC Cal H;gh 

211 1/2013 7:44:00 AM 5.639 0.488 0.131 -0.353 16.963 0.059 0.03 85.45 

2111/2013 7:45:00 AM 5.996 0.485 0.102 -0.342 16.985 0.043 0.032 73.552 

2111/2013 7:46:00 AM 6.452 0.485 0.088 -0.337 16.989 0.043 0.033 46.836 

2/11/2013 7:47:00 AM 6.879 0.487 0.11 -0.348 17.032 0.042 -0.015 46.682 ITHC M;d 

2/11/2013 7:48:00 AM 5.192 0.47 0.083 -0.378 12.834 0.029 0.002 47.118 

2/11/2013 7:49:00AM 0.131 0.428 0.018 -0.423 0.084 -0.003 -0.118 31.233 

2/11/2013 7:50:00 AM 0.108 0.049 0.014 -0.016 0.033 -0.006 0.124 25.337 THC Low 

2111/2013 7:51 :00 AM L-,0:;'.;:10;;,7,---::-0'i.0;,;1;-7 __ 0;.;.0;,1;.:1~--i-0:,:.0;.:1~1_-:0:::'::,03,"3,--:-O;,;.006;,:::._-:0'=',,;;12:;7:;-1 24.507 Cat Zero 

2111/2013 7:52:ooAM 15.205 8.041 3.543 -0.021 12.427 24.75 51 .957 3.807 

2111/2013 7:53:oo AM 18.736 9.698 4.792 -0.016 19.047 48.728 238.759 0.838 

2111/2013 7:54:00 AM 18.829 9.701 4.789 .0.01 19.044 48.752 242.562 0.6 12 

211112013 7:55:00 AM 1r.1~8~.8~62i:-~9;";.7:ii05:i--::'4'i.7'"9"" -0.007 L.,1;.;9.:;.0,.2;;.4_.;;48;;;.;;784;,;..~2,;:42;;;.9;;;84;.;,J1 0.685 Cal H;gh 

2/1112013 7:56:00 AM --,1.;;2':.;1i'-24--'--i6,-:.1.;;63;-_3;;;.5~7:-i1..., 9.42 14.376 33.068 232.594 0.692 

2/11/2013 7:57:00 AM ILr...,.,1;.:O;.,.-_.::5:;.1,;:07:,......;2;;;.:;.54;.:2'-1 9.591 L.,1;,:;0,;;.0;,:;8;,.1_.;:2;;;5',;;.07;.:1...;..,1.,;.41;,;.6.:;.1,"2;.J1 0.796 M;d 

211112013 7:58:00AM 18.04 1.224 0.914 9.511 16.459 12.149 101 .171 0.79 

2111/2013 7:59:00AM 20.873 0.049 0.Q35 9.512 21.091 0.199 2.619 0.661 

211112013 8:00:00 AM 20.894 0.048 

211112013 8:01:00AM 20.896 0.046 

2111/2013 8:02:00 AM 20.909 0.044 

2111/2013 8:03:00 AM 20.922 0.044 

2/11/2013 8:04:00 AM 20.918 0.046 

2/1112013 8:05:00 AM 20.917 0.046 

2/11/2013 8:06:00 AM 20.916 0.046 

2/11/2013 8:07:00 AM 20.919 0.046 

2/11/2013 8:08:00 AM 20.925 0.045 

2111/2013 8:09:00 AM 20.94 0.044 

211112013 8:10:00 AM 20.946 0.048 

2111/2013 8:11 :00AM 20.957 0.051 

2/1 1/2013 8:12:00 AM 20.969 0.047 

2/11/2013 6:13:00AM 20.97 0.052 

2/11/2013 8:14:00AM 21 .117 0.048 

2111/2013 8:15:00 AM 21.246 0.047 

0.035 

0.04 

0.035 

0.04 

0.035 

0.022 

0.024 

0.029 

0.027 

0.034 

0.038 

0.037 

0.041 

0.037 

0.035 

0.051 

9.511 21.098 0.139 

8.999 21.116 0.123 

4.697 21.119 0.122 

4.522 21.14 0.127 

1.947 21 .162 0.102 

0.196 21.136 0.086 

0.374 

0.301 

0.327 

0.401 

0.375 

0.277 

0.634 CO Cat High 

0.617 

0.799 

0.697 CO Mid 

0.688 

0.69 

0.186 21 .149 0.097 0.355 0.542 

0.183 21.221 0.095 0.423 0.676 

0.184 15.488 23.254 8.878 0.738 

0.193 13.252 34.884 33.301 2.131 

0. 183 13.267 35.189 30.641 1.592 

0.204 13.262 35.828 29.259 0.926 

0.203 13.265 36.16 29.099 0.949 

0.195 13.318 34.37 34.446 1.928 

0.204 13.328 33.57 57.377 7.646 

0.213 13.324 33.804 84.046 9.623 

2111/2013 8:16:00AM 21 .099 0.047 0.056 0.213 13.269 35.258 41.922 3.134 

0.319 

0.469 

2111/2013 8:17:00 AM 21 .021 0.048 0.032 0.221 13.254 36.692 25.703 

211112013 8:16:00 AM 20.624 0.298 0.024 0.224 12.208 26.347 27.269 

2111/2013 8:19:00 AM 1...-i1';; 0.'i34~5:i---i5;:;.0~5i-1 --:0;;;.0;;;0~7"" -0.254 10.1 19 0.692 5.651 -0.009 02lC02 bias 

2111/2013 8:20:00AM 6.549 3.071 0.623 -0.338 4.466 27.164 1.01 

2111/2013 8:21 :00 AM 1r--:0;;;i-17:i4-~0;:;.0~18:;-""'2;;;.4~9:i3""'--i-0:':.0::;4';;6--:0i-~05ii7"-"";;'48;'8;'4;;;9~-On.'i35;;;9"" -0.011 

-0.01 NOx bias 

2/11/2013 8:22:00 AM 0.156 0.008 1.941 0.849 0.058 26.878 38.467 -0.009 

2111/2013 8:23:00AM 0.129 0.004 0.019 8.881 0.032 0.42 234.891 -0.001 

2111/2013 8:24:00AM 0.129 0.001 0.013 9.5 0.032 0.329 1242.6521 o CO bias 

2111/2013 8:25:00 AM 3.326 1.317 0.703 8.694 8.032 19.829 189.483 0.185 

2111/2013 8:26:00 AM 13.087 4.543 3.146 1.326 13.256 35.501 35.333 1.264 

2111/2013 8:27:ooAM 13.125 4.559 3.341 0.679 13.3 35.517 32.133 1.26 

21 11 /2013 8:28:ooAM 13.1 26 4.567 3.381 0.684 13.304 35.571 32.493 1.325 

2111/2013 8:29:oo AM 13.1 41 4.559 3.11 0.655 13.287 35.58 32.588 1.467 

2/11 /2013 8:30:00 AM 13.146 4.558 3.12 0.617 13.29 35.554 31.988 1.266 

2111/20 13 8:31:00AM 13.15 4.558 3.145 0.598 13.286 35.673 31.482 1.259 
Date 

2111/2013 

2/11/2013 

Time 

8:32:00 AM 

8033000 AM 

2111/2013 8:34:00 AM 

2111 /2013 8:35:00 AM 

2111 /2013 8:36:00 AM 

2/11 /2013 8:37:00 AM 

2/ 11 /2013 8:38:00 AM 

211112013 8039000 AM 

2111/2013 8:40:00 AM 

2111 /2013 8:41 :00AM 

211112013 8042000 AM 

211112013 8043000 AM 

2/11/2013 8:44:00 AM 

2111 /2013 8:45:ooAM 

2111 /2013 8:46:00 AM 

2/11 /2013 8:47:00AM 

2111 /2013 8:46:00 AM 

211112013 8049000 AM 

2/11 /2013 8:50:00 AM 

2/11/2013 8:51:00 AM 

2/11/2013 8:52:00 AM 

2/1112013 6:53:00 AM 

211112013 6:54:00 AM 

2111 /2013 6:55:00 AM 

2111 /2013 8:56:00 AM 

211112013 8:57:00 AM 

211112013 8058000 AM 

211 112013 8059000 AM 

211112013 9000000 AM 

211112013 9001000 AM 

211112013 9002000 AM 

2111 /2013 9:03:00 AM 

211112013 9004000 AM 

211112013 9 005000 AM 

2111 /2013 9:06:00 AM 

2111 /2013 9:07:00 AM 

2111/2013 9:08:00 AM 

2/11/2013 9:09:00 AM 

2/11/2013 9:10:00 AM 

2111/2013 9:11:00 AM 

2111 /2013 9:12:00 AM 

2111 12013 9:13:00 AM 

211112013 9:14:00 AM 

2/1 1/2013 9:15:00AM 

2/11/2013 9:16:ooAM 

2/11/2013 9:17:00AM 

2/11/2013 9:18:00 AM 

2111/2013 9:19:00AM 

211112013 9020000 AM 

2111 /2013 9:21 :00 AM 

211 112013 9022000 AM 

211112013 9:23:00 AM 

2/11 /2013 9:24:00 AM 

2/1112013 9025000 AM 

2/11/2013 9:26:00 AM 

2111/2013 9:27:00 AM 

2111/2013 9:28:00 AM 

211112013 9029000 AM 

211112013 9:30:00 AM 

211 112013 9031000AM 

211112013 9:32:00 AM 

2111 /2013 9:33:00 AM 

211112013 9:34:00 AM 

0 , 

% 

13.147 

13.151 

13.155 

13.158 

13.157 

13.156 

13.159 

13.158 

13.151 

13.148 

13.139 

13.141 

13.143 

13.146 

13.153 

13.153 

13.155 

13.148 

13.15 

13.156 

13.176 

13.178 

13.176 

13.168 

13. 189 

13.193 

13.191 

13.186 

13.188 

13.18 

13.187 

13.182 

13.199 

13.182 

13.156 

13.128 

13.111 

15.583 

15.526 

13.169 

13.152 

13.176 

13.191 

13.163 

13.188 

13.152 

13.853 

15.494 

13.186 

13. 193 

13.183 

13.189 

13.183 

13.182 

13.163 

13.176 

16.19 

13.199 

13.2 

13.204 

13.207 

13.224 

13.219 

CO, 

% 

4.562 

4.562 

4.564 

4 .565 

4 .566 

4.567 

4.565 

4.566 

4.566 

4.57 

4.574 

4.574 

4.574 

4.572 

4.572 

4.573 

4.571 

4.574 

4.574 

4.568 

4 .557 

4.557 

4.556 

4.559 

4.54 

4.541 

4.542 

4.552 

4.546 

4.552 

4.55 

4.556 

4.544 

4.561 

4.572 

4.588 

4.6 

3.032 

3.358 

4.568 

4.576 

4.558 

4.55 

4.556 

4.556 

4.583 

4.068 

3.342 

4.565 

4.554 

4.567 

4.557 

4.561 

4.558 

4.567 

4.56 

2.81 

4.549 

4.544 

4.543 

4.544 

4.533 

4.538 

NO, 

PPM 

3.167 

3.125 

3.097 

3.052 

3.171 

3.115 

3.157 

3.162 

3.103 

3.083 

3.148 

3.056 

3.141 

3.211 

3.171 

3.063 

3.1 15 

3.066 

3. 163 

3.206 

3.633 

3.228 

2.895 

2.953 

2.998 

3.123 

3.076 

3.1 99 

3.059 

3.196 

3.1 04 

3.143 

3.001 

3.024 

2.99 

3.026 

3.09 

2.161 

2.033 

3.051 

3.15 

3.01 

3.008 

2.936 

2.756 

3.01 

2.926 

2.154 

3.461 

3.28 

3.433 

3.296 

3.303 

3.275 

3.294 

3.111 

2.084 

3.358 

3.264 

3.322 

3.383 

3.427 

3.523 

CO 

PPM 

0.572 

0.609 

0 .703 

1.121 

1.126 

1.254 

1.237 

1.19 

1.217 

1.319 

1.527 

1.71 

1.888 

1.839 

1.656 

1.766 

2.06 

2.406 

2.369 

2.221 

1661 

0. 185 

0.391 

1.045 

1.549 

1.537 

1.487 

1.383 

1.467 

1.414 

1.574 

1.499 

1.739 

1.885 

1.757 

1.841 

1.994 

1.746 

1.019 

2.058 

2.032 

2.276 

2.752 

2.319 

2.514 

2.598 

2.277 

1.887 

3.008 

3.113 

2.863 

2.982 

2.951 

2.81 

2.661 

2.691 

1.87 

2.509 

2.786 

3.014 

2.987 

2.724 

2.767 

0, 

% 

13.278 

13.275 

13.273 

13.27 

13.241 

13.226 

13.227 

13.217 

13.225 

13.219 

13.21 

13.203 

13.212 

13.219 

13.236 

13.234 

13.223 

13.219 

13.227 

13.22 

13.231 

13.234 

13.272 

13.266 

13.295 

13.297 

13.29 

13.254 

13.279 

13.322 

13.296 

13.299 

13.308 

13.281 

13.271 

13.277 

13.269 

13.269 

13.294 

13.337 

13.342 

13.367 

13.288 

13.307 

13.301 

13.259 

13.272 

13.312 

13.308 

13.333 

13.296 

13.323 

13.292 

13.285 

13.329 

13.339 

13.318 

13.333 

13.351 

13.34 

13.326 

13.364 

13.31 

NO, 

PPM 

35.781 

35.724 

35.298 

34.914 

34.882 

34.748 

34.921 

34.954 

34.712 

34.422 

34.135 

33.777 

33.781 

34.125 

34.309 

33.723 

33.378 

33.073 

33.4 

33.244 

38.227 

37.954 

35.792 

34.575 

33.695 

33.875 

34.143 

34.405 

34.403 

34.08 

34.343 

33.824 

33.326 

33.535 

33.594 

33.093 

33.382 

33.371 

33.277 

33.384 

33.425 

32.128 

32.28 

32.663 

31.838 

32.774 

32.835 

32.34 

32.685 

32.525 

32.593 

32.228 

32.61 

32.651 

33.097 

32.604 

33.184 

32.793 

32.403 

32.556 

32.901 

33.039 

33.077 

CO 

PPM 

31 .157 

31.754 

36.171 

49.491 

49.262 

55.167 

51 .489 

49.893 

52.282 

59.893 

67.779 

76.571 

82.795 

77.163 

73.009 

62.217 

94.551 

102.716 

99.684 

95.02 

51.291 

17.606 

26.264 

45.949 

62.617 

57.991 

54.915 

49.741 

55.795 

54.062 

59.172 

59.526 

70.379 

75.088 

76.456 

80.618 

81 .343 

78.882 

83.598 

84.807 

83.447 

104.54 

121 .947 

112.449 

137.19 

132.093 

118.911 

126.354 

121.049 

127.662 

116.87 

123.484 

118.714 

117.671 

107.71 

117.572 

109.783 

106.907 

117.813 

123.327 

116.094 

107.271 

107.669 

THC 

PPM 

1.313 

1.421 

1.984 

5.078 

4.842 

6. 39 

5.245 

5.07 

5.716 

7.789 

9.826 

12.372 

14.547 

12.652 

11.521 

14.795 

18.355 

18.303 

17.206 

16.34 

7.082 

-0.007 

1.027 

4.051 

7.574 

6.575 

5.755 

4.644 

6.013 

5.622 

6.458 

6.554 

9.277 

10.329 

10.546 

12.019 

11.835 

11.524 

13. 161 

13.389 

12.69 1 

20.344 

29.134 

25.277 

35.372 

32.548 

27.523 

31 .27 

28.189 

31 .791 

27.334 

30.1 2 

27.951 

27.268 

23.335 

27.757 

24.41 

23.376 

27.402 

29.889 

27.539 

24.219 

24.066 
0, CO, 

% 

NO. CO O2 NO. CO THe 

Dale Time % PPM PPM % PPM PPM PPM 

2111/2013 9:35:00 AM 13.21 4.542 3.495 2.832 13.316 32.837 111.128 25.358 

2/11/2013 9;36;OQ AM 13.215 4.54 3.422 3.033 13.315 32.255 121 

2111/2013 9:37:00AM 5.694 1.734 1.477 5.454 1.305 5.797 187.373 

211112013 9:38:00 AM 0.167 0.046 0.034 9.403 0.059 0.978 1 242.65 1 

2111/2013 9:39:00 AM r-:i'0.i;-74::i3:-....;0i50iii-6_-:i-0'ii0~39~ 9.374 5.076 0.925 202.052 

2111/2013 9:40:00 AM LI-:;;9.:;88,.,3;..........,;;;5.;,09::,..._;;0.;;02;:9;,..J 1.544 r.1~0:i:066~--;0:;;7;;;2~6-,1 8.511 

2111 /2013 9:41 :00 AM 8.786 4.334 0.254 -0.359 5.217 20.715 -0.09 

2111/2013 9:42:00 AM rl-:i-0.-:;24~4:---;O;':.0~58+--;;2.~50~5;-.....,-o:;;0~8::i8,....-:i-0.'ii05i1,........;4;;;8,:.;5-;1'-~0;,;.2ii22::-, 

2/1112013 9:43:00AM 0.126 0.019 1.1 0.011 0.034 29.269 0.249 

2111/2013 9:44:00 AM 0.105 0.009 0.026 0.007 0.031 0.162 0.111 

2/1112013 9:45:00 AM rl-:i-0.~10~4:--i0;':.0;;0:::8--:i-0'ii02~6:--i0:;;.0~1';5--:i-0.'ii0"'31:--i0::-.1:;2;;;5-.....:;0;-'.1"1'--, 

2/11/2013 9:46:00 AM 8.533 4.528 3.736 4.944 7.376 32.059 66.852 

2/11 /2013 9:47:00 AM rl...,1~0:i:.0::i3;.7--:5i".1i':1;;8-, 4.584 9.474 10.135 48.663 240.9391 

2111 /2013 9:48:00AM 7.067 1.039 2.582 5.42 12.062 39.337 179.542 

2/ 11 /2013 9:49:00 AM 20.852 0.078 2.513 0.278 13.338 33.924 71 .114 

2/1112013 9:50:00 AM 20.954 0.066 0.497 0.153 13.333 34.266 61.765 

2111/2013 9:51 :00 AM 20.966 0.065 0.03 0.143 13.347 34.378 50.024 

2111/2013 9:52:00 AM 20.972 0.065 0.035 0.137 13.32 34.202 55.886 

2/11/2013 9:53:00 AM 

2/11/2013 9:54:00 AM 

2/11/2013 9:55:00 AM 

211 1/2013 9:56:00 AM 

2111 /2013 9:57:00 AM 

211 112013 9:58:00 AM 

2111/2013 9:59:00 AM 

211 1/2013 10:00:00 AM 

2111/201310:01:00AM 

2/11/2013 10:02:00AM 

2/11/2013 10:03:00 AM 

2111/2013 10:04:00 AM 

2I11/201310:05:00AM 

2I11 /201310:06:ooAM 

2111 /201310:07:ooAM 

2111 /2013 10:08:ooAM 

211 1/2013 10:09:00 AM 

2/11/2013 10:10:00 AM 

2/11/201310:11:00AM 

2/11/201310:12:00AM 

2/11/201310:13:00AM 

2111/2013 10:14:00 AM 

2111/201310:15:ooAM 

211112013 10:16:00 AM 

2I11/201310:17:00AM 

2111/2013 10:18:00 AM 

2/1112013 10:19:00 AM 

2111/2013 10:20:00 AM 

2111/2013 10:21 :00 AM 

2/11/2013 10:22:00 AM 

2111 /2013 10:23:00 AM 

2111 /2013 10:24:ooAM 

211112013 10:25:00 AM 

2111/2013 10:26:00AM 

2111 /2013 10:27:00AM 

2111/2013 10:28:00AM 

2/1112013 10:29:00 AM 

2/11/2013 10:30:00 AM 

2111/2013 10:31:00 AM 

2111 /2013 10:32:00 AM 

211112013 10:33:00 AM 

211112013 10:34:00 AM 

2111 /2013 10:35:00 AM 

2/1112013 10:36:00 AM 

20.979 

20.983 

20.989 

20.993 

20.997 

17.673 

13.221 

13.207 

13.216 

13.21 5 

13.225 

13.234 

13.25 

13.234 

13.223 

13.222 

13.227 

13.222 

13.219 

13.219 

13.211 

13.227 

13.218 

13.205 

13.222 

13.252 

13.231 

13.254 

13.255 

13.26 

16.098 

13.215 

13.212 

13.232 

13.224 

13.211 

13.216 

13.233 

13.211 

13.201 

13.209 

13.208 

13.215 

13.21 

0.064 0.03 0.178 13.3 34.346 64.216 

0.063 0.028 0.166 13.305 34.76 56.504 

0.063 0.05 0.157 13.221 35.135 47.33 

0.063 0.037 0.156 13.308 34.836 50.414 

0.063 0.035 0.155 13.297 35.131 44.855 

2.145 1.275 0.357 13.287 35.055 45.96 

4.519 3.245 1.141 13.275 35.165 42.413 

4.527 3.175 1.236 13.294 34.716 47.396 

4.524 3.119 1.442 13.312 34.426 54.289 

4.526 3.267 1.617 13.293 34.403 58.571 

4.523 3.253 1.676 13.317 33.428 70.803 

4.521 3.125 2.383 13.328 32.282 104.215 

4.513 3.1 52 3.07 13.312 32.678 109.86 

4.519 3.307 2.922 13.313 32.899 107.018 

4.527 3.256 2.867 13.291 32.887 109.561 

4.528 3.16 3.113 13.31 32.468 120.845 

4.526 3.218 3.325 13.313 32.49 122.197 

4.528 3.178 3.414 13.353 32.191 130.989 

4.532 3.287 3.405 13.352 32.527 121.007 

4.528 3.183 3.355 13.311 32.81 119.008 

4.533 3.343 3.073 13.327 32.397 114.493 

4.524 3.131 3.236 13.32 32.349 117.88 

4.531 3.244 3.102 13.301 32.946 106.015 

4.543 3.25 2.902 13.298 32.878 107.629 

4.529 3.224 2.893 13.359 32.279 108.441 

4.514 3.266 3.196 13.34 32.576 111.424 

4.523 3.422 3.037 13.35 32.287 111.772 

4.512 3.234 3.418 13.358 32.005 123.935 

4.512 3.279 3.463 13.366 31.854 124.21 

4.509 3.273 3.448 13.343 31 .868 124.372 

2.875 1.964 2.291 13.342 32.151 123.371 

4.531 3.352 2.975 13.332 32.773 101 .839 

4.529 3.103 2.969 13.345 32.302 111 .863 

4.519 3.114 3.133 13.349 31 .901 119.414 

4.522 3.079 3.261 13.324 32.231 119.052 

4.528 3.222 3.17 13.366 31.798 118.291 

4.521 3.098 3.358 13.364 31.26 129.429 

4.515 3.069 3.506 13.339 31.782 128.403 

4.524 3.12 3.241 13.327 32.087 119.159 

4.531 3.122 2.986 13.348 32.033 112.072 

4.524 3.051 3.11 13.337 32.055 115.475 

4.523 3.054 3.017 13.329 31.84 117.541 

4.517 3.027 3.188 13.324 31 .952 122.26 

4.52 3.034 3.232 13.348 31.814 123.56 

28.618 

14.08 

0.001 CO bias 

0.028 

-0.01 02/C02 bias 

-0.01 

-0.009 NOx bias 

-0.005 

11 .541 

18.33 Oirect Zero 

22.978 

15.313 Direct Span 

14.045 

10.48 NOx Direct Span 

8.231 

4.687 

6.929 

8.76 

6.598 

4.452 

5.21 

3.558 

3.868 

3.031 

4.278 

6.216 

7.071 

12.073 

24.597 

25.573 

24.968 Start 100% Compliance Test 1 & RATA 1 

25.926 

30.51 

30.369 

34.33 

29.921 

28.312 

28.213 

28.821 

23.609 

24.429 

25.239 

25.847 

26.14 

31.175 

31.588 

32.171 

31 .784 

21 .963 

27.04 

30.518 

30.009 

29.871 

34.451 

34.008 

30.587 

27.1 94 

28.534 

29.67 

32.126 

32.049 
Date Time 

2111/2013 10:37:00 AM 

2111 /2013 10:38:00 AM 

2111 /2013 10:39:00 AM 

211112013 10:40:00 AM 

21111201310:41:00AM 

211112013 10:42:00 AM 

0, 

% 

13.207 

13.203 

13.207 

13.197 

13.191 

13.192 

2111/2013 10:43:00 AM 15.938 

2111 /2013 10:44:00 AM 13.208 

2I11/201310:45:00AM 13.193 

2I11/201310:46:00AM 13.187 

2111/201310:47:00AM 13.194 

2111/2013 10:48:00 AM 13.197 

2111/201310:49:ooAM 13.199 

2111 /2013 10:50:00 AM 13.196 

2111 /201310:51:00AM 13.208 

2111/201310:52:00AM 13.192 

2111/201310:53:00AM 13.185 

2111/201310:54:00AM 13.182 

2111/2013 10:55:00 AM 13.179 

211112013 10:56:00 AM 

211112013 10:57:00 AM 

2111/201310:58:00AM 

2/11/201310:59:00 AM 

2111/2013 , 1 :00:00 AM 

211112013 11 :01 :00AM 

2111 /201311:02:00AM 

2111/2013 11 :03:00 AM 

21111201311:04:00AM 

13.177 

13.162 

13.171 

13.163 

13.162 

17.735 

13.194 

13.179 

13.175 

2111/2013 11 :05:00 AM 13.178 

21111201311:06:00AM 13.163 

2111/201311 :07:00AM 13.166 

211112013 11:08:00 AM 13.178 

2I111201311:09:00AM 13.164 

2/11/201311:10:00AM 13.172 

2/11/2013 11 :11 :00 AM 13.173 

2111/201311 :12:00AM 13.179 

2111/201311 :13:00AM 13.166 

2I11/201311 :14:00AM 13.171 

2I11/201311:15:00AM 13.152 

2111/201311:16:00AM 13.166 

21111201311:17:00AM 

2111/2013 11:18:00AM 

211112013 11:19:00 AM 

21111201311:20:00AM 

211112013 11:21:00 AM 

2111/201311 :22:00AM 

211112013 11 :23:00 AM 

2111/201311:24:00AM 

211112013 11:25:00 AM 

211112013 11 :26:00 AM 

2111/2013 11:27:ooAM 

2/11/2013 11:28:00AM 

2111/201311:29:00AM 

2111/2013 11 :30:00 AM 

211112013 11:31:00 AM 

2I111201311:32:00AM 

2111/2013 11 :33:00 AM 

2111/201311:34:00AM 

211112013 11 :35:00 AM 

2111/201311:36:ooAM 

2111/2013 11 :37:00 AM 

2111/2013 11 :38:00 AM 

2111/2013 11 :39:00 AM 

13.164 

13.169 

13.172 

13.149 

5.232 

0.185 

0.167 

0.157 

9.036 

10.041 

8.736 

0.26 

0.155 

0.457 

0.605 

0.209 

0.104 

8.659 

10.027 

10.034 

11 .434 

13.155 

13.141 

CO2 NOx CO 

% PPM PPM 

4.521 3.036 3.207 

4.526 3.05 2.99 

4.524 2.984 3.101 

4.528 2.967 3.034 

4.529 3.063 2.986 

4.53 3.002 2.946 

2.948 1.905 1.967 

4.521 2.908 2.72 

4.531 2.972 2.757 

4.534 2.938 2.571 

4.529 2.901 2.829 

4.528 2.952 2.704 

4.525 2.901 2.91 

4.529 2.899 2.71 

4.521 2.748 2.933 

4.533 2.868 2.737 

4.542 2.911 2.488 

4.548 2.922 2.263 

4.549 2.847 2.284 

0, 

% 

13.329 

13.319 

13.31 

13.294 

13.284 

13.296 

13.293 

13.288 

13.271 

13.294 

13.292 

13.306 

13.298 

13.314 

13.294 

13.28 

13.273 

13.266 

NO, 

PPM 

32.363 

32.214 

32.097 

32.109 

32.203 

32.242 

32.236 

32.36 

32.966 

32.542 

32.715 

32.341 

32.672 

32.21 

32.606 

32.946 

33.559 

33.587 

CO 

PPM 

115 

115.394 

119.689 

118.514 

115.748 

114.07 

117.193 

112.733 

104.941 

107.106 

111.473 

111.962 

116.533 

117.075 

120.056 

109.534 

97.155 

93.202 

THC 

PPM 

28.618 

29.228 

30.744 

30.264 

28.756 

27.777 

29.335 

27.485 

23.977 

24.941 

26.68 

27.449 

29.236 

29.709 

30.544 

26.069 

20.701 

19.247 

13.269 33.391 95.262 20.096 

4.551 2.786 2.225 13.264 33.456 95.135 19.961 

4.558 2.768 2.105 13.252 33.482 95.05 20.132 

4.554 2.772 2.132 13.26 33.497 94.64 19.743 

4.56 2.859 1.986 13.268 33.762 85.923 16.176 

4.561 2.734 1.884 13.258 34.221 81.039 14.124 

1.919 1.171 0.881 13.254 34.164 78.271 13.302 

4.541 2.955 1.572 13.263 34.24 77.263 13.145 

4.548 2.998 1.767 13.258 34.272 78.154 13.327 

4.548 2.963 1.772 13.257 34.193 79.875 14.517 

4.547 2.928 1.831 13.23 34.42 75.082 12.258 

4.552 2.953 1.734 13.24 34.168 77.609 13.297 

4.55 2.947 1.776 13.241 34.341 73.927 11.896 

4.543 2.937 1.6 13.21 34.581 69.496 10.652 

4.551 2.925 1.603 13.215 34.682 68.261 10.159 

4.546 2.938 1.589 13.215 34.519 69.653 10.712 

4.544 2.974 1.602 13.229 34.442 66.699 9.539 

4.538 2.817 1.652 13.256 33.775 78.538 13.744 

4.548 2.858 1.656 13.271 33.668 77.911 13.587 

4.541 2.811 1.681 13.256 34.201 77.147 13.035 

4.55 3 1.551 13.277 33.367 82.687 15.449 

4.541 2.814 1.99 13.284 33.04 94.278 19.753 

4.543 2.775 2.155 13.287 32.78 104.788 24.681 

4.54 2.73 2.179 13.278 33.115 98.171 21.529 

4.54 2.651 2.034 13.274 33.053 101.122 22.878 

4.554 2.963 2.1 11.696 32.592 91.549 18.72 

1.477 1.3 4.149 0.158 1.884 193.71 3.9 

0.03 0.044 9.286 0.056 0.868 242.691 0.002 

0.021 0.036 9.503 0.033 0.732 I 242.8451 0.002 CO bias 

0.017 0.033 9.513 5.869 4.088 198.816 2.154 

4.788 0.034 3.095 10.105 0.62 8.491 0.011 

5.079 0.037 -0.317 10.117 0.537 -0.116 -0.01 02lC02 bias 

4.252 0.266 -0.349 4.143 25.67 -0.054 -O.Q1 

0.047 2.522 -0.098 0.047 48.556 0.267 -0.009 

L..::0.~0::26~_~2'i.5~3::-_::0.~0~15~_~0~0:;;31~_4,:,8:i'.5~8:i'5_-::0.;;:2.,:42;:-._-::-O;:.0::1i-1INOX bias, THC Zero 

0.036 2.384 0.006 0.03 12.82 0.323 2.306 

0.046 1.529 0.023 0.03 0.422 0.518 32.223 

0.002 0. 117 0.011 0.044 0.182 0.327 47.512 

L..-O.;::,:.0:;:0:;.8_....,;0;;:.0:,;3;,-_;;0.;;0;;09;...._:,0.::;0;;31:..---:;;0.~1;,23::,....--:;:,0.;.:1;:,05:::-_4;;7,;;.9;::6;;3..JID irect Zero; THe Mid 

4.537 2.008 7.861 7.65 32.341 54.172 48.012 

5.102 2.532 9.72 10.087 48.815 239.701 48.099 

5.1 2.522 9.537 10.093 48.78 243.01 I 47.198 Direct Span 

4.542 2.773 5.929 8.321 37.734 144.759 35.846 

4.521 3.096 2.379 13.248 32.936 96.056 22.227 

4.537 2.945 2.173 13.26 32.686 100.24 22.528 
Dale Time 

2I11/201311:40:00AM 

2I11/201311:41:00AM 

2/11/201311:42:00AM 

2/1 1/2013 11 :43:00 AM 

2I1 1/201311 :44:00AM 

2I11 /201311 :45:00AM 

2I1 1/201311 :46:00 AM 

211112013 11 :47:00 AM 

2111/2013 11 :48:00 AM 

2I1 1/201311 :49:00AM 

2I11/201311:50:00AM 

2/111201311:51 :00 AM 

2I11/2013":52:00AM 

2/11/2013 1':53:oo AM 

2I11120131 1:54:oo AM 

2111 /201311 :55:00AM 

2111 /201311 :56:ooAM 

2111 /201311 :57:00AM 

211112013 11:58:00 AM 

2/11/2013 11:59:00 AM 

2111/2013 12:00:00 PM 

2111/2013 12:01 :00 PM 

2111 /2013 12:02:00 PM 

2111/2013 12:03:00 PM 

2111 /2013 12:04:00 PM 

21111201 3 12:05:00 PM 

2/11/2013 12:06:00 PM 

2/11/2013 12:07:00 PM 

2/11/2013 12:08:00 PM 

2/11/2013 12:09:00 PM 

2111/2013 12:10:00 PM 

21111201312:11:00 PM 

2I111201312: 12:oo PM 

2111 /2013 12:13:00 PM 

2111 /2013 12:14:00 PM 

2/11 /2013 12:15:00 PM 

2/11/2013 12:16:00 PM 

2/11/2013 12:17:00 PM 

2/11/2013 12;18:00 PM 

2111/2013 12:19:00 PM 

211 1/2013 12:20:00 PM 

211112013 12:21 :00 PM 

211112013 12:22:00 PM 

2111/2013 12:23:00 PM 

2/11/2013 12:24:00 PM 

2/11/2013 12:25:00 PM 

2/11/2013 12:26;00 PM 

211112013 12:27:00 PM 

2111/20 13 12:28:00 PM 

2111/2013 12:29:00 PM 

0, 

% 

13.164 

13.163 

13.151 

13.184 

13.202 

13.1 87 

13.188 

13.16 

13.159 

13.16 

13.173 

13.185 

13.153 

13.135 

13.149 

13.111 

13.1 24 

16.839 

13.186 

13.161 

13.174 

13.174 

13.196 

13.185 

13.187 

13.172 

13.177 

13.179 

13.173 

13.177 

13.192 

13.187 

13.198 

13. 191 

13.184 

13.188 

13.184 

16.441 

13.212 

13.187 

13.179 

13.174 

13.162 

13.159 

13.156 

13.155 

13.157 

13.156 

13.164 

13.178 

21111201312:30:00 PM 13.174 

2111 /2013 12:31 :00 PM 13.172 

211112013 12:32:00 PM 13.168 

21111201312:33:00 PM 13.178 

2/11/2013 12:34:00 PM 13.174 

2111/2013 12:35:00 PM 13.176 

2I11/201312:36:00PM 13.181 

2111/2013 12:37:00 PM 16.821 

211112013 12:38:00 PM 13.191 

2111 /201312:39:00PM 13. 173 

211 11201312:40;OOPM 13.176 

211 1/2013 12:41 :00 PM 13.169 

21111201312:42:00PM 13.165 

co, 

% 

4.523 

4.523 

4.529 

4.505 

4.494 

4.508 

4.505 

4.526 

4.528 

4.529 

4.519 

4.512 

4.536 

4.548 

4.543 

4.568 

4.56 

2.421 

4.525 

4.54 

4.535 

4.534 

4.515 

4.522 

4.523 

4.537 

4.534 

4.532 

4.537 

4.535 

4.521 

4.525 

4.518 

4.525 

4.533 

4.528 

4.529 

2.648 

4.512 

4.524 

4.53 

4.533 

4.54 

4.541 

4.543 

4.544 

4.542 

4.542 

4.537 

4.528 

4.531 

4.531 

4.534 

4.528 

4.531 

4.531 

4.524 

2.428 

4.514 

4.527 

4.527 

4.531 

4.533 

NO, 

PPM 

2.815 

2.85 

2.779 

3.696 

3.055 

2.779 

2.525 

2.632 

2.776 

3.08 

3.651 

3.012 

3.012 

3.006 

2.645 

2.965 

2.947 

1.632 

3.024 

3.116 

2.964 

3.915 

3.099 

2.777 

2.701 

2.887 

2.854 

2.819 

2.848 

2.784 

2.805 

2.839 

2.71 

2.664 

2.721 

2.621 

2.583 

1.529 

2.786 

2.84 

2.95 

3.003 

2.97 

3.007 

3.021 

2.969 

2.9 

2.867 

2.811 

2.795 

2.829 

2.759 

2.682 

2.681 

2.728 

2.653 

2.712 

1.452 

2.868 

2.848 

2.785 

2.808 

2.825 

CO 

PPM 

2.357 

2.467 

3 

0.865 

0.148 

0.19 

0.51 

2.259 

2.811 

3.226 

1.528 

0.265 

0.257 

0.415 

1.361 

2.305 

2.692 

1.709 

3.039 

3.315 

3.474 

2.333 

0.488 

0.502 

0.936 

1.29 

1.891 

2.126 

1.899 

2.127 

2.234 

2.223 

2.206 

1.954 

1.625 

1.351 

1.396 

0.916 

1.421 

1.786 

1.847 

1.866 

1.835 

1.642 

1.596 

1.664 

1.938 

2.283 

2.678 

2.647 

2.713 

2.817 

2.723 

2.914 

2.646 

2.696 

2.808 

1.758 

2.473 

2.544 

2.55 

2.42 

2.503 

0, 

% 

13.279 

13.274 

13.288 

13.314 

13.303 

13.294 

13.296 

13.263 

13.284 

13.292 

13.296 

13.291 

13.306 

13.284 

13.265 

13.27 

13.282 

13.284 

13.274 

13.279 

13.28 

13.287 

13.277 

13.297 

13.269 

13.278 

13.289 

13.261 

13.272 

13.297 

13.291 

13.303 

13.285 

13.272 

13.268 

13.282 

13.279 

13.27 

13.255 

13.245 

13.223 

13.213 

13.208 

13.213 

13.22 

13.218 

13.205 

13.234 

13.241 

13.268 

13.246 

13.22 

13.259 

13.247 

13.249 

13.242 

13.25 

13.224 

13.223 

13.224 

13.228 

13.234 

13.22 

NO, 

PPM 

32.534 

31.741 

37.77 

39.121 

36.449 

36.096 

32.668 

32.181 

31 .356 

34.657 

37.015 

37.042 

36.656 

33.857 

32.755 

32.366 

32.346 

32.251 

32.124 

31.836 

34.993 

36.34 

37.143 

34.852 

34.635 

33.679 

33.2 

33.864 

33.271 

33.153 

33.2 

33.126 

33.309 

33.723 

33.984 

33.581 

33.627 

33.679 

33.503 

33.648 

33.798 

33.887 

34.226 

34.029 

33.936 

33.584 

33.139 

32.739 

32.696 

32.296 

32.264 

32.28 

31.815 

32.507 

32.397 

32.186 

31 .863 

32.421 

32.578 

32.522 

32.837 

32.835 

32.599 

CO 

PPM 

108.847 

123.685 

86.846 

13.841 

14.528 

23.496 

73.698 

124.009 

142.823 

115.755 

23.988 

22.16 

23.474 

49.377 

102.665 

122.938 

126.243 

125.419 

134.732 

131.926 

122.866 

19.737 

19.699 

35.267 

48.973 

69.809 

88.112 

81.728 

85.912 

92.354 

95.837 

90.993 

92.261 

79.013 

54.498 

66.664 

62.868 

64.17 

70.782 

76.168 

75.739 

76.19 

71 .447 

68.483 

69.025 

72.957 

89.128 

98.762 

103.782 

108.94 

111.631 

114.703 

124.366 

116.334 

112.498 

119.216 

123.854 

117.435 

109.746 

107.573 

102.615 

101 .848 

110.113 

THe 

PPM 

26.179 

31.977 

20.282 

-0.009 

-0.009 

0. 17 

14.808 

32.295 

39.716 

29.76 

0.129 

-0.01 

-0.01 

6.034 

24.465 

30.993 

33.113 

32.511 

36.466 

34.74 

33.474 

0. 166 

-0.01 

1.674 

4.7 

11 .331 

17.957 

15.329 

17.188 

19.461 

21 .312 

19.761 

20.283 

14.654 

9.185 

10.523 

8.897 

9.292 

11.519 

13.249 

13.336 

13.489 

11 .836 

10.788 

11.444 

12.7 

18.661 

22.513 

24.951 

27.405 

28.44 

29.072 

34.533 

29.706 

28.257 

31.125 

33.981 

30.452 

26.883 

26.17 

24.02 

24.144 

26.967 
O2 CO2 NOx CO 

Date Time % % PPM PPM 

0, 

% 

2/11/2013 12:43:00 PM 13.157 4.534 2.79 2.745 13.217 

2/11/2013 12:44:00 PM 13.164 4.527 2.793 2.926 13.21 

2/11/201312:45:00PM 13.145 4.536 2.86 2.823 13.202 

2/111201312:46:00 PM 13.134 4.538 2.801 2.75 13.189 

2111/2013 12:47:00 PM 13.143 4.531 2.685 2.711 13.185 

2111/2013 12:48:00 PM 13.139 4.534 2.783 2.621 13.179 

2111/201312:49:00 PM 13.13 4.54 2.79 2.512 13.174 

2111/2013 12:50:00 PM 13.119 4.547 2.9 2.54 13.189 

2111/2013 12:51:00 PM 13.128 4.544 2.849 2.551 13.197 

211112013 12:52:00 PM 13.124 4.549 2.909 2.496 13.199 

211112013 12:53:00 PM 13.127 4.548 2.841 2.476 13.201 

211112013 12:54:00 PM 13.129 4.548 2.908 2.433 13.198 

2111/2013 12:55:00 PM 13.128 4.551 2.877 2.33 9.22 

2/11/2013 12:56:00 PM 5.274 1.658 1.355 4.291 0.074 

2/11 /20 13 12:57:00 PM 0.191 0.034 0.04 9.182 0.044 

2/11 /20 13 12:58:00 PM 0.178 0.023 0.032 9.49 0.031 

2111/201312:59:00 PM 0.172 0.019 0.035 9.505 4.258 

2111/2013 1:00:00 PM ....,5::,;.:;;52:,:9;,........;2;;;.9;,;';;,3_...;;.0.;;,03:;:5;..., 6.494 10.01 

2/11/2013 1:01:00 PM LI-":::0;:;.0~'6::.........:5~.0:::6~6_~0.~03:::6:...J -0.003 10.029 

211112013 1:02:00 PM 9.728 4.895 0.065 -0.351 10.038 

NO, 

PPM 

32.113 

32.276 

32.199 

32.124 

32.304 

32.516 

32.545 

32.549 

32.607 

32.595 

32.644 

32.814 

26.5 

1.137 

0.868 

0.739 

0.917 

0.595 

0.523 

0.47 

CO 

PPM 

120.677 

119.395 

121.694 

119.433 

117.908 

113.128 

111.953 

111 .11 

111.052 

106.728 

107.829 

105.663 

109.314 

219.094 

242.752 

1 243.0791 

217.041 

15.1 

-0.127 

-0.199 

2/1112013 1:03:00 PM .... ;;.0.:::4~66::...._;;.0.;:;0;;.8;' _....;;2;;;.4.;2;' __ -:;:0;,;.':;2.:.7_...;'.;;.5;:8;,........;38~.2:.;'.;2_..;-:;:0~.0:;:0~5.., 

211112013 1:04:00 PM LI_0;:.,:,17;:4;,.......;0::,.0;:;2;;,5_....;;2.;;.53:;:2;.-....;0::,.0:;:0;;4_....;;0.;;,03:;:5:........::48;:.;;.66,,2:.........,::,0.:;;2::;38:,..J 

2/1112013 1:05:00 PM 8.821 4.545 2.535 4.302 5.898 48.285 68.717 

2/1112013 1:06:00 PM .... ':.::0~.0:::3::.7_....::5.;:;0;:96:;...._.;2:.::.5:;:34;:...._;9.;;;4;;.65:;...._':.::0~.0:.::5::.7_..:4:.::8:;:.8:.;'.::4_.;2:.4';'.;:'5;::5:..., 

2111/2013 1 :07:00 PM LI ,.;':::0;,::.0;::44:.........:5:;:.0:;9;;,5_....;2.:;;52:-,;7_.....:9:;:;.5:;5.::,3 __ ':,::0:;:;.0;:;64:....-,;48::,;.;;.67:,:9;,....:;2;::43::,;.:;;39::4:.J1 

2/1112013 1:08:00 PM 4.046 1.425 0.86 4.861 4.69 24.647 126.85 

211112013 1 :09:00 PM ..... 0;:,,;;' 0;;7,.......,;-0;:.0.,1;:;6_....;;0.;;.02:;:7,........;0;:.0;;7;;.6_....;:0".0,;;3:-....;0;;,.1:;6;;.8_....;;0.;:;30:;:2;-, 

211112013 1: 1 0:00 PM LI_::;0.~1 0:::2:.........::-0:::,.0;':;:8;,......;;.0.;:;0;:28::.......,;0:;;.0;,;:;:8_...;;.0.:;:02;:7;,......,;0:,;..':.:2;::,2_...::0..:.1::.01~ 2/11/2013 1:11:00 PM 11.068 0.575 0.668 0.106 8.906 19.144 26.915 

2/11/2013 1:12:00 PM 13.236 4.49 2.726 1.904 13.213 32.479 104.739 

2/11/2013 1:13:00 PM 13.156 4.521 2.771 2.504 13.219 32.63 105.728 

2/11/2013 1:14:00 PM 13.155 4.525 2.791 2.466 13.22 32.836 103.139 

2/11/2013 1:15:00 PM 13.155 4.53 2.823 2.453 13.219 32.747 105.117 

2/11/2013 1:16:00 PM 13.154 4.531 2.877 2.501 13.222 32.601 105.85 

2111/2013 1:17:00 PM 13.156 4.528 2.721 2.455 13.219 32.706 105.167 

2111/2013 1:18:00 PM 13.139 4.537 2.862 2.376 13.212 32.686 102.603 

2111/2013 1:19:00PM 13.146 4.532 2.733 2.344 13.205 32.645 103.1 

211112013 1:20:00PM 13.135 4.534 2.875 2.364 13.211 32.888 100.109 

2111/2013 1:21:00 PM 13.115 4.546 2.628 2.116 13.205 33.142 96.68 

2/11/2013 1:22:00PM 13.102 4.554 2.705 2.071 13.194 33.034 96.546 

2/1 1/2013 1:23:00 PM 13.102 4.551 2.722 2.061 13.197 33.005 93.301 

2/11/2013 1:24:00 PM 17.436 2.045 1.233 1.254 13.196 32.932 93.28 

211112013 1:25:00 PM 13.166 4.519 2.816 2.082 13.194 32.993 92.038 

2/11/2013 1:26:00 PM 13.134 4.531 2.854 2.435 13.2 33.045 92.133 

2/11/2013 1:27:00 PM 13.129 4.537 2.834 2.395 13.2 33.099 92.574 

2111/2013 1:28:00 PM 13.132 4.538 2.798 2.392 13.215 32.691 95.116 

2111/2013 1:29:00PM 13.145 4.535 2.797 2.417 13.214 32.563 99.751 

2111/2013 1:30:00PM 13.142 4.539 2.901 2.499 13.212 32.413 98.137 

2/11/2013 1:31:00 PM 13.15 4.538 2.76 2.514 13.206 32.715 100.078 

2111/2013 1:32:00 PM 13.148 4.544 2.855 2.445 13.207 33.032 92.964 

2111/2013 1:33:00 PM 13.139 4.554 2.909 2.232 13.195 33.235 86.712 

2/11/2013 1:34:00 PM 13.13 4.563 2.974 2.155 13.194 33.158 88.059 

2/11/2013 1:35:00 PM 13.135 4.563 2.973 2.171 13.193 33.434 82.497 

2/11/2013 1:36:00 PM 16.506 2.62 1.646 1.25 13.193 33.482 82.111 

2111/2013 1:37:00 PM 13.163 4.554 3.035 1.913 13.2 33.519 77.211 

2111/2013 1:38:00 PM 13.154 4.56 3.025 1.974 13.203 33.41 78.995 

2111/2013 1:39:00PM 13.149 4.565 3.002 2.13 13.211 33.286 79.969 

211112013 1:40:00 PM 13.157 4.56 2.978 2.198 13.227 33.234 83.468 

2/11/2013 1:41:00 PM 13.157 4.563 3.065 2.121 13.233 33.125 84.066 

211112013 1:42:00 PM 13.152 4.567 2.903 2.152 13.22 33.368 82.666 

2111/2013 1:43:00 PM 13.155 4.565 2.91 1.991 13.22 33.386 78.742 

2/11/2013 1:44:00 PM 13.158 4.569 2.766 2.01 13.203 33.896 79.232 

2/11/2013 1:45:00 PM 13.128 4.584 2.792 1.738 13.213 33.627 77.433 

THC 

PPM 

31.935 

30.964 

32.46 

31.011 

30.282 

28.043 

27.751 

27.027 

27.552 

25.04 

26.085 

25.002 

24.947 

1.144 

° 

0.137 ° 

-0.01 

-0.011 

-0.011 

-0.011 

CO bias 

02lC02 bias 

-0.011 NOx bias 

4.199 

25.911 

26.316 Direct Span 

24.361 

26.006 

22.739 Direct Zero 

24.715 

25.648 

25.181 

23.757 

24.848 

25.196 

24.664 

23.708 

23.861 

22.561 

21.093 

21.274 

19.423 

19.457 

19.167 

19.115 

19.38 

20.936 

22.753 

21.995 

22.172 

19.268 

16.888 

17.586 

14.837 

14.954 

13.41 

14.054 

13.944 

15.595 

15.989 

15.247 

13.884 

14.19 

13.37 
Date 

2/11/2013 

211112013 

Time 

1:46:00 PM 

1:47:00 PM 

O2 CO2 NO~ CO O2 NOx CO 

% % PPM PPM % PPM PPM 

13.155 4.57 2.68 1.9 13.222 33.221 87.183 

13.398 4.376 2.731 1.994 13.218 33.334 84.285 

2111/2013 1:48:00 PM 16.192 2.872 1.743 1.183 13.218 33.321 80.311 

2/11/2013 1:49:00 PM 13.166 4.562 2.896 1.945 13.205 33.19 84.202 

2/11/2013 1:50:00 PM 13.168 4.559 2.901 2.079 13.207 32.998 89.244 

2/11/2013 1:51:00 PM 13.157 4.562 2.851 2.168 13.204 33.363 86.514 

2111/2013 1:52:00 PM 13.154 4.565 2.862 2.043 13.215 33.087 86.066 

2111/2013 1:53:00 PM 13.151 4.567 2.756 2.155 13.211 33.109 89.795 

2111/2013 1:54:00 PM 13.133 4.576 2.781 2.1 13.211 33.061 89.544 

2111/2013 1:55:00 PM 13.131 4.578 2.884 2.098 13.225 32.91 91 .84 

2111/2013 1 :56:00 PM 13.128 4.58 2.863 2.112 13.211 33.465 87.037 

2111/2013 1 :57:00 PM 13.13 4.58 2.834 1.819 13.204 33.803 78.06 

2/11/2013 1:58:00 PM 13.11 4.592 2.87 1.589 13.192 34.002 75.297 

2/11/2013 1:59:00 PM 13.101 4.599 2.757 1.432 8.574 26.293 75.352 

2/11/2013 2:00:00 PM 2.935 0.827 0.902 5.079 0.069 1.098 222.924 

211112013 2:01:00 PM 0.199 0.056 0.034 9.392 0.043 0.869 1242.8031 

THe 

PPM 

17.38 

15.854 

14.392 

15.655 

17.526 

16.81 

16.656 

18.139 

18.07 

19.041 

17.072 

14.006 

12.938 

9.357 

0.154 

-0.001 CO bias 

2111/2013 2:02:00 PM 0.177 0.047 0.031 9.512 4.112 0.938 215.791 -0.002 CO bias 

2111/2013 2:03:00 PM 0.252 0.159 0.026 9.484 10.029 0.685 14.09 -0.012 

2/11/2013 2:04:00 PM ....,9;.6::,;4:::3;..........::5:;:.0:;;3~7_..:;0 . .:;:02;;9:...., 2.353 10.038 0.597 -0.131 -0.013 02 bias 

2111/2013 2:05:00 PM LI...;1.;;0.;;.0;:23;;...."""'"5...;.1,,0;;.5_...;:;0 . .;;03;1;,...J -0.318 6.992 11.743 -0.128 -0.013 02/C02 bias 

2/11/2013 2:06:00 PM 10.032 5.112 0.033 -0.339 0.06 48.222 0.183 -0.013 

2111/2013 2:07:00 PM r-6;;;.2;;8;;8~"""'"3:;;.0;;:0;;.5_...;:;0 . .;87:::2:-.....:-0;;.2;;;9;;;2-+....:;;0 . .:;02:;;8~....;:48;;.5:;;2;;:9~...;:;0.;23;;;2;,...J -0.013 NOx bias 

2111/2013 2:08:00 PM L..,;0;; ..:;19:::8~.....:;0:;;.0:;;6;2_...;2 . .:;:52;:4;.........:;-0::;.0::;1:;;3.J 0.03 11.555 0.129 -0.014 NOx bias 

2111/2013 2:09:00 PM -0.014 ,....0;;; ..;,11:;,;4,...."""'"0:;;.0;,;1;;.9 _...;:;0 . .;;80::;2:-"""'"0:;;.0:;:2.;.7_...;:;0."02,,8;,.......,0::;.,;.;17:,,...._;0.,,1 0;;,1:-, 

211112013 2:10:00 PM I 0.102 0.009 0.026 0.021 0.028 0.143 0.097 -0.014 Direct Zero 

2111/2013 2:11:00 PM 

2/11/2013 2:12:00 PM 

2111/2013 2:13:00 PM 1 

2/11/2013 2:14:00 PM 

2/11/2013 2:15:00 PM 

2/1112013 2:16:00 PM 

2/1112013 2: 17:00 PM 

2/11/2013 2:18:00 PM 

2/11/2013 2:19:00PM 

2/11/2013 2:20:00 PM 

2111/20132:21:00PM 

2/11/2013 2:22:00 PM 

2111/2013 2:23:00 PM 

2111/2013 2:24:00 PM 

2111/2013 2:25:00 PM 

2111/2013 2:26:00 PM 

2111/2013 2:27:00 PM 

2111/2013 2:28:00 PM 

2111/2013 2:29:00 PM 

2/11/2013 2:30:00 PM 

2/11/20132:31:00PM 

2111/2013 2:32:00 PM 

2111/2013 2:33:00 PM 

2111/2013 2:34:00 PM 

2/11/2013 2:35:00 PM 

2111/2013 2:36:00 PM 

2111/2013 2:37:00 PM 

2/11/2013 2:38:00 PM 

2111/2013 2:39:00 PM 

2/11/2013 2:40:00 PM 

2111/2013 2:41:00 PM 

2111/2013 2:42:00 PM 

2111/2013 2:43:00 PM 

2/11/2013 2:44:00 PM 

2111/2013 2:45:00 PM 

2/11/2013 2:46:00 PM 

2/11/2013 2:47:00 PM 

5.453 

10.037 

10.043 

12.962 

20.865 

20.899 

20.893 

20.895 

20.881 

15.494 

13.834 

13.834 

13.819 

13.83 

13.825 

13.828 

13.812 

13.809 

13.811 

13.815 

13.826 

13.322 

13.539 

13.814 

13.825 

13.808 

7.033 

5.839 

13.775 

13.793 

13.794 

13.799 

13.807 

13.821 

13.824 

13.81 

13.806 

2.93 1.194 2.237 4.352 17.538 

5.116 2.545 9.224 10.065 48.659 

5.114 2.539 9.561 10.074 48.877 

1.08 1.277 5.89 12.296 39.968 

0.086 0.034 0.363 13.914 32.098 

0.075 0.029 0.142 13.908 32.002 

0.078 0.035 0.146 13.893 31.735 

0.078 0.035 0.149 13.888 31.899 

0.086 0.D38 0.148 13.886 32.007 

3.324 1.245 0.151 13.867 32.173 

4.142 1.679 0.262 13.87 31.851 

4.146 1.671 0.278 13.853 31.886 

4.156 1.712 0.32 13.873 31.319 

4.155 1.678 0.372 13.877 31.121 

4.16 1.725 0.35 13.875 30.996 

4.159 1.737 0.358 13.876 31.007 

4.163 1.755 0.335 13.861 30.899 

4.165 1.721 0.369 13.86 30.14 

4.166 1.709 0.428 13.864 30.022 

4.167 1.763 0.416 13.854 30.429 

4.162 1.843 0.415 13.876 30.214 

3.953 1.876 0.424 13.878 30.318 

4.122 1.901 0.392 13.864 30.45 

4.162 1.823 0.443 13.861 30.659 

4.162 1.858 0.403 13.859 30.464 

4.168 1.866 0.446 13.838 30.254 

1.968 0.977 0.3 13.832 30.221 

1.897 0.801 0.069 13.847 30.068 

4.154 1.923 0.437 13.843 29.993 

4.165 2.009 0.451 13.841 29.963 

4.168 1.944 0.446 13.858 29.9 

4.168 1.879 0.425 13.847 29.914 

4.164 2.025 0.464 13.844 29.762 

4.157 1.967 0.497 13.864 29.594 

4.157 1.907 0.479 13.868 29.743 

4.16 1.98 0.468 13.848 29.878 

4.165 2.042 0.497 13.831 30.125 

15.27 -0.013 

222.123 -0.003 

243.274 1 -0.002 

167.997 -0.007 

26.654 -0.014 

25.51 -0.013 

26.354 -0.012 

25.797 -0.013 

25.317 -0.01 2 

24.855 

25.69 

26.371 

28.198 

29.112 

29.304 

29.242 

28.912 

31.828 

33.554 

32.63 

32.814 

32.52 

33.174 

31.577 

31.929 

32.643 

33.103 

33.061 

34.207 

34.645 

34.638 

34.623 

35.35 

37.052 

36.79 

35.758 

34.923 

-0.012 

-0.012 

-0.011 

-0.011 

-0.011 

-0.011 

-0.011 

-0.011 

-0.011 

-0.01 

-0.01 

-0.01 

-0.011 

-0.011 

-0.01 

0.001 

0.001 

-0.002 

-0.005 

-0.004 

-0.001 

-0.009 

-0.009 

0.002 

0.056 

-0.009 

0.014 

0.028 

Direct Span 
Dale Time 

2/11/20132:48:00PM 

2111/2013 2:49:00 PM 

2111/20132:50:00PM 

2111/20132:51:ooPM 

211112013 2:52:00PM 

2111/2013 2:53:00 PM 

2111/2013 2:54:00 PM 

2/11/2013 2:55:00 PM 

2/11/2013 2:56:00 PM 

2111/2013 2:57:00 PM 

211112013 2:58:00 PM 

2/11/2013 2:59:00 PM 

211112013 3:00:00 PM 

2/11/20133:01:ooPM 

2/11/2013 3:02:00 PM 

2/11/2013 3:03:00 PM 

211112013 3:04:00 PM 

211112013 3:05:00 PM 

211112013 3:06:00 PM 

211112013 3:07:00 PM 

2111/2013 3:08:00 PM 

211112013 3:09:00 PM 

2111/2013 3: 10:00 PM 

2/11/2013 3:11:00PM 

211112013 3:12:00 PM 

211112013 3:13:00 PM 

2111/2013 3:14:00 PM 

2111/2013 3:15:00 PM 

2/1112013 3:16:00 PM 

2/11/2013 3:17:00 PM 

2/11/2013 3:18:00 PM 

2111/2013 3:19:00 PM 

2111/2013 3:20:00 PM 

2111/2013 3:21 :00 PM 

211112013 3:22:00 PM 

211112013 3:23:00 PM 

2/11/2013 3:24:00 PM 

211112013 3:25:00 PM 

211112013 3:26:00 PM 

2111/2013 3:27:00 PM 

2111/2013 3:28:00 PM 

2111/2013 3:29:00 PM 

2111/2013 3:30:00 PM 

2111/20133:31:00PM 

211112013 3:32:00 PM 

2111/2013 3:33:00 PM 

2111/2013 3:34:00 PM 

2111/2013 3:35:00 PM 

2/11/2013 3:36:00 PM 

2111/2013 3:37:00 PM 

211112013 3:38:00 PM 

211112013 3:39:00 PM 

2/11/20133:40:00PM 

2/11/2013 3:41:00 PM 

2/11/2013 3:42:00 PM 

211112013 3:43:00 PM 

211112013 3:44:00 PM 

2/11/2013 3:45:00 PM 

211112013 3:46;00 PM 

2/1112013 3:47:00 PM 

2111/2013 3:48:00 PM 

2111/2013 3:49;00 PM 

2/11/2013 3:50:00 PM 

0, 

% 

13.808 

13.822 

13.822 

13.822 

13.821 

13.803 

13.806 

13.811 

13.809 

13.807 

13.808 

13.809 

13.819 

13.824 

13.832 

13.83 

13.833 

13.832 

13.832 

13.836 

13.837 

13.837 

13.836 

13.835 

13.837 

13.829 

13.831 

13.832 

13.84 

13.82 

13.826 

13.818 

13.801 

13.798 

13.806 

13.795 

13.79 

13.802 

13.803 

13.807 

13.817 

13.8 

13.806 

13.806 

13.808 

13.816 

13.825 

13.828 

13.829 

13.83 

13.825 

13.829 

13.83 

13.823 

13.832 

13.833 

13.832 

13.829 

13.827 

13.829 

13.824 

13.83 

13.833 

co, 

% 

4.163 

4.157 

4.157 

4.156 

4.158 

4.168 

4.168 

4.169 

4.17 

4.172 

4.17 

4.17 

4.166 

4.166 

4.16 

4.166 

4.16 

4.163 

4.164 

4.16 

4.16 

4.161 

4.159 

4.1 55 

4.15 

4.154 

4.153 

4.15 

4.144 

4.155 

4.152 

4.159 

4.167 

4.166 

4.165 

4.167 

4.169 

4.165 

4.167 

4.165 

4.16 

4.169 

4.166 

4.162 

4.16 

4.161 

4.168 

4.169 

4.171 

4.171 

4.177 

4.177 

4.176 

4.179 

4.175 

4.176 

4.18 

4.185 

4.187 

4.187 

4.188 

4.183 

4.18 

NO, 

PPM 

2.074 

1.994 

2.107 

2.077 

2.082 

2.199 

2.218 

2.098 

2.119 

2.157 

2.104 

2.115 

2.165 

2.232 

2.208 

2.172 

2.157 

2.234 

2.259 

2.164 

2.283 

2.187 

2.198 

2.162 

2.136 

2.262 

2.263 

2.337 

2.178 

1.898 

1.938 

2.216 

2.326 

2.209 

2.221 

2.291 

2.295 

2.281 

2.273 

2.297 

2.266 

2.284 

2.38 

2.191 

2.16 

2.176 

2.319 

2.29 

2.312 

2.293 

2.349 

2.285 

2.274 

2.287 

2.199 

2.181 

2.261 

2.259 

2.286 

2.229 

2.305 

2.219 

2.133 

CO 

PPM 

0.469 

0.473 

0.488 

0.497 

0.509 

0.475 

0.505 

0.54 

0.508 

0.556 

0.503 

0.508 

0.531 

0.552 

0.591 

0.56 

0.57 

0.561 

0.558 

0.583 

0.612 

0.601 

0.605 

0.595 

0.597 

0.591 

0.562 

0.542 

0.598 

1.146 

2.047 

2.045 

1.568 

1.651 

1.583 

1.645 

1.657 

1.621 

1.721 

1.816 

2.102 

2.163 

1.917 

2.065 

2.406 

2.56 

2.353 

2.219 

2.221 

2.23 

1.965 

1.725 

1.787 

1.626 

1.762 

1.828 

1.62 

1.615 

1.55 

1.671 

1.529 

1.473 

1.721 

0, 

% 

13.865 

13.864 

13.867 

13.872 

13.857 

13.879 

13.886 

13.88 

13.879 

13.882 

13.884 

13.877 

13.904 

13.906 

13.894 

13.902 

13.914 

13.89 

13.914 

13.917 

13.91 

13.909 

13.917 

13.92 

13.914 

13.912 

13.895 

13.914 

13.895 

13.906 

13.915 

13.891 

13.894 

13.884 

13.882 

13.892 

13.878 

13.885 

13.873 

13.892 

13.897 

13.868 

13.861 

13.883 

13.883 

13.861 

13.867 

13.883 

13.879 

13.868 

13.853 

13.862 

13.838 

13.854 

13.867 

13.849 

13.86 

13.851 

13.845 

13.844 

13.846 

13.854 

13.862 

NO, 

PPM 

29.601 

29.533 

29.749 

29.335 

29.654 

29.55 

29.313 

29.369 

29.412 

29.317 

29.202 

29.289 

28.807 

28.733 

28.845 

28.778 

28.587 

28.949 

28.673 

28.579 

28.999 

28.839 

28.817 

28.809 

28.645 

28.758 

28.847 

28.591 

27.8 

25.507 

25.123 

25.927 

25.912 

26.115 

25.929 

25.833 

25.97 

25.851 

25.962 

25.393 

25.206 

25.814 

25.543 

24.888 

24.762 

24.915 

25.327 

25.273 

25.273 

25.588 

26.012 

25.689 

25.984 

25.897 

25.548 

25.993 

26.141 

26.198 

26.189 

26.207 

26.366 

26.001 

25.511 

CO 

PPM 

35.199 

35.914 

35.573 

36.825 

35.854 

35.922 

37.436 

37.883 

37.547 

37.473 

37.698 

37.063 

39.798 

40.142 

40.409 

39.995 

40.854 

40.242 

40.117 

42.485 

41.461 

41.96 

41.883 

41 .139 

42.411 

41 .441 

41 .147 

41.275 

45.876 

90.174 

124.417 

108.692 

92.53 

94.206 

95.986 

97.067 

94.923 

95.298 

97.614 

110.634 

124.89 

113.548 

108.781 

131 .073 

139.831 

147.471 

128.077 

129.264 

125.935 

122.807 

104.072 

99.11 

99.729 

93.938 

104.943 

100.569 

91.967 

93.037 

92.085 

99.379 

87.895 

91.769 

107.669 

THe 

PPM 

0.23 

0.109 

0.07 

0.199 

-0.001 

-0.008 

0.225 

0.023 

0.06 

0.132 

0.072 

0.008 

0.193 

0.214 

0.093 

0.139 

0.298 

0.241 

0.165 

0.35 

0.374 

0.523 

0.569 

0.194 

0.364 

0.322 

0.204 

0.291 

1.025 

15.432 

30.358 

21.576 

14.578 

15.545 

15.554 

16.917 

15.265 

15.336 

16.53 

23.353 

31 .759 

24.627 

22.293 

36.453 

40.978 

46.222 

33.545 

34.439 

32.491 

31.235 

19.624 

17.192 

17.953 

15.42 

19.887 

17.463 

13.962 

14.71 

14.417 

18.71 

12.693 

14.313 

21.741 
Date 

2/11/2013 

211112013 

Time 

3:51:00 PM 

3,52,00 PM 

2/11/2013 3:53:00 PM 

2111/2013 3:54:00 PM 

2/11 /2013 3:55:00 PM 

2111 /2013 3:56:00 PM 

2/11 /2013 3:57:00 PM 

2I1112{)13 3,58,00 PM 

2111/2013 3:59:00 PM 

211112013 4,00,00 PM 

2I11/20134:01:00PM 

211112013 4,02,00 PM 

2111/2013 4:03:00 PM 

2111/2013 4:04:00 PM 

211 1/2013 4:05:00 PM 

211112013 4:06:00 PM 

211112013 4:07:00 PM 

2/11/2013 4:08:00 PM 

2/11/2013 4:09:00 PM 

2111/2013 4"0,00 PM 

2111/2013 4:11 :00 PM 

211112013 4:12:00 PM 

2111 /2013 4:13:00 PM 

2111 /2013 4:14:00 PM 

2111 /2013 4:15:00 PM 

2111 /2013 4:16:oo PM 

2111/2013 4:17:00 PM 

211112013 4,18,00PM 

2111/2013 4:19:00PM 

211112013 4,20,00 PM 

2/ 11 /2013 4:21 :00PM 

211112013 4:22:00 PM 

2111/2013 4:23:00 PM 

211112013 4:24:00 PM 

2111 /2013 4:25:00 PM 

2/11/2013 4:26:00 PM 

2111/2013 4:27:00 PM 

2111/2013 4:28:00 PM 

2111/2013 4:29:00 PM 

211 1/2013 4:30:00 PM 

211112013 4:31 :00 PM 

211 112013 4:32:00 PM 

2111 /2013 4:33:00 PM 

2111/2013 4:34:00 PM 

211112013 4,35,00 PM 

211112013 4,36,00 PM 

2111/2013 4:37:00 PM 

211112013 4,38,00 PM 

211112013 4,39,00 PM 

211112013 4,40,00 PM 

211112013 4:41 :00 PM 

211112013 4,42,00 PM 

2/11 /2013 4:43:00 PM 

2/11/2013 4:44:00 PM 

2/11/2013 4:45:00 PM 

2111/2013 4:46:00 PM 

2111/2013 4:47:00 PM 

211112013 4:48:00 PM 

211112013 4:49:00 PM 

211112013 4,SO,00 PM 

211112013 4,51 ,00 PM 

211112013 4:52:00 PM 

2111/2013 4:53:00 PM 

0 , 

% 

13.824 

13.829 

13.821 

13.817 

13.81 

13.804 

13.772 

13.773 

13.776 

13.774 

14.724 

15.743 

13.832 

13.831 

13.832 

13.834 

13.833 

13.831 

13.824 

13.83 

13.827 

13.83 

13.818 

13.805 

13.799 

13.802 

13.804 

13.806 

14.67 

15.36 

13.823 

13.814 

13.8 11 

13.817 

13.819 

13.835 

13.832 

13.831 

13.829 

13.831 

13.823 

13.796 

13.797 

13.807 

13.819 

15.403 

15.01 

13.839 

13.843 

13.831 

13.829 

13.83 

13.825 

13.801 

13.799 

13.801 

13.794 

13.806 

13.756 

13.761 

13.765 

13.769 

13.787 

co, 

% 

4.187 

4.186 

4.191 

4.196 

4.202 

4.208 

4.225 

4.226 

4.228 

4.227 

3.62 

3.154 

4.193 

4.2 

4.196 

4.192 

4.194 

4.201 

4.202 

4.197 

4.193 

4.186 

4.191 

4.197 

4.201 

4.201 

4.201 

4.202 

3.65 

3.367 

4.192 

4.1 95 

4.198 

4.196 

4.195 

4.188 

4.187 

4.19 

4.194 

4.192 

4.1 94 

4.212 

4.21 

4.207 

4.2 

3.225 

3.582 

4.183 

4.181 

4.19 

4.189 

4.192 

4.193 

4.207 

4.21 

4.21 

4.215 

4.209 

4.236 

4.236 

4.236 

4.24 

4.231 

NO, 

PPM 

2.243 

2.184 

2.313 

2.253 

2.364 

2.319 

2.185 

2.28 

2.15 

2.163 

1.996 

1.527 

2.322 

2.288 

2.316 

2.451 

2.347 

2.26 

2.193 

2.163 

2.1 

2.152 

2.223 

2.234 

2.229 

2.059 

2.084 

2.077 

1.9 

1.683 

2.362 

2.439 

2.558 

2.642 

3.151 

3.152 

3.143 

3.106 

3.017 

3.06 

2.833 

2.538 

2.681 

2.532 

2.578 

2.14 

2.12 

2.76 

2.676 

2.769 

2.782 

2.72 

2.579 

2.629 

2.738 

2.585 

2.799 

2.583 

2.761 

2.717 

2.739 

2.699 

2.491 

co 

PPM 

1.911 

1.861 

1.794 

1.979 

1.799 

1.604 

1.436 

1.279 

1.231 

1.228 

1.265 

1.062 

1.628 

1.55 

1.569 

1.322 

1.174 

1.258 

1.333 

1.344 

1.469 

1.489 

1.575 

1.4 

1.39 

1.285 

1.324 

1.374 

1.526 

1.161 

1.4 

1.335 

1.229 

1.145 

1.089 

1.037 

1.053 

1.043 

1.03 

1.014 

1.044 

1.058 

0.949 

0.915 

0.934 

0.928 

0.684 

1.013 

0.977 

0.886 

0.922 

0.842 

0.864 

0.788 

0.688 

0.68 

0.68 

0.705 

0.68 

0.675 

0.711 

0.738 

0.727 

0, 

% 

13.872 

13.872 

13.877 

13.865 

13.883 

13.875 

13.86 

13.876 

13.863 

13.86 

13.878 

13.88 

13.888 

13.894 

13.904 

13.885 

13.886 

13.877 

13.859 

13.877 

13.873 

13.879 

13.854 

13.854 

13.842 

13.846 

13.866 

13.854 

13.852 

13.86 

13.855 

13.851 

13.849 

13.842 

13.855 

13.867 

13.862 

13.861 

13.87 

13.869 

13.861 

13.85 

13.853 

13.858 

13.873 

13.879 

13.884 

13.875 

13.881 

13.85 

13.852 

13.871 

13.872 

13.871 

13.884 

13.872 

13.887 

13.868 

13.869 

13.885 

13.889 

13.908 

13.943 

NO, 

PPM 

25.2 

25.025 

25.072 

25.16 

25.263 

25.82 

25.969 

26.137 

26.32 

26.086 

25.647 

25.779 

26.179 

26.241 

26.249 

27.017 

26.764 

26.58 

26.876 

26.335 

26.312 

25.799 

26.301 

26.254 

26.533 

26.46 

26.426 

26.492 

25.916 

26.394 

26.667 

26.815 

26.918 

27.104 

27.32 

27.121 

27.19 

27.327 

27.411 

27.445 

26.996 

27.1 5 

27.371 

27.263 

27.203 

27.171 

27.168 

27.102 

27.376 

27.197 

27.381 

27.386 

27.549 

27.66 

27.73 

27.673 

27.674 

27.563 

27.598 

27.33 

27.536 

27.517 

27.052 

CO 

PPM 

121.053 

127.066 

125.007 

137.838 

129.776 

108.662 

104.595 

92.304 

87.058 

90.055 

94.382 

95.181 

88.665 

64.851 

86.049 

71.316 

68.261 

74.345 

75.039 

77.949 

81.901 

87.147 

84.435 

80.409 

77.234 

76.394 

78.046 

79.314 

94.202 

89.248 

76.664 

72.161 

67.277 

64.487 

59.029 

59.785 

60.119 

58.687 

57.24 

56.467 

61 .277 

62.89 

57.425 

56.889 

57.513 

59.171 

60.234 

60.482 

58.904 

56.918 

55.924 

54.231 

53.914 

54.112 

51.273 

52.769 

51.004 

52.745 

52.048 

54.034 

53.316 

53.S02 

56.682 

THe 

PPM 

29.526 

32.946 

32.352 

40.409 

35.757 

21.458 

20.844 

14.216 

11 .92 

13.338 

14.893 

14.846 

12.531 

11 .209 

11.419 

6.732 

6.081 

7.853 

7.946 

9.005 

10.211 

12.107 

11 .179 

9.846 

8.872 

8.551 

8.954 

9.392 

15.948 

13.496 

8.668 

7.198 

5.933 

5.104 

3.588 

3.613 

3.672 

3.426 

3.1 

2.957 

4.141 

4.416 

3.023 

3.051 

2.954 

3.367 

3.786 

3.688 

3.494 

3.119 

2.944 

2. 478 

2.467 

2.629 

2.034 

2.371 

1.773 

2.435 

2.204 

2.548 

2.351 

2.359 

2.696 
O2 CO2 NO. CO O2 NO. CO THC 

Date Time % % PPM PPM % PPM PPM PPM 

2111 /2013 4:54:00 PM 13.797 4.226 2.662 0.917 9.055 20.754 73.305 4.443 

211112013 4:55:00 PM 1.666 0.383 0.414 5.411 0.071 0.829 220.819 0.013 

211112013 4:56:00 PM 0.216 0.073 0.035 9.352 0.043 0.65 1 242.9431 -0.002 CO bias 

2111 /2013 4:57:00 PM 0.201 0.068 0.039 9.5 2.775 0.633 233.797 -0.002 CO bias 

21 1112013 4:58:00 PM 8.594 4.522 0.03 3.831 10.007 0.516 31 .99 -0.011 

211112013 4:59:00 PM 1"1-:'~0'i;04'::9;-.5"';'-;33;-~0:f;;;03;'2" -0.225 10.014 0.463 -0.175 -0.013 0 2lC02 bias 

211 1/2013 5:00:00 PM 6.566 3.242 0.81 -0.297 3.522 28.324 -0.082 -0.013 

2111 /2013 5:01 :00 PM LI..;;;0.:;2.;;'8;-_,;:0.:;;08;;,3;-_,;:2.:;;5,;:'3;-_-O,;;;;.0:;;38;-_:,0.;;;0;:,39;.-....,4:;;8,;;.2;;;8:;;8 __ 0,;: . .,.20;;,7,-_-O';;;; '0:i:':;-3.JINOX bias; THC Zero 

2/11/2013 5:02:00 PM 0. 143 0.046 0.693 0.013 0.03 16.909 0.142 0.039 

2/11/2013 5:03:00 PM I 0.102 0.032 0.023 0.028 0.028 0.175 0.103 8.901 Direct Zero 

2/11/2013 5:04:00 PM 7.691 4.081 1.591 3.514 5.639 21 .846 26.29 10.78 

211112013 5:05:00 PM r-:':i;0;i0.,48;---;5...;'-:-49i;-_2:;;~53;;4;---i9:'i.3~6;;-4_.,';;;0:'i0:;-73;-_48;;7:'i6;,;9_-;2.;;3';,.2:;i5,..', 10.058 

2111 /2013 5:06:00 PM 1 10.063 5.149 2.533 9.549 10.072 48.8 243.2661 8.248 Direct Span 

2111 /2013 5:07:00 PM 4.646 1.169 2.302 6.351 12.094 37.474 175.721 7.655 

211112013 5:08:00 PM 19.473 0.963 0.456 0.474 13.831 26.632 72.595 6.78 

2111 12013 5:09:00 PM 

2111/2013 5:10:00 PM 

2/11/2013 5:11:00 PM 

2/11/2013 5:12:00 PM 

2/11/20135:13:00PM 

2/11/2013 5:14:00 PM 

2111 /20135:15:00PM 

211112013 5:16:00 PM 

2/1112013 5:17:00 PM 

2111 /2013 5:18:00 PM 

2111 12013 5:19:00 PM 

211112013 5:20:00 PM 

2111/20135:21 :00PM 

211112013 5:22:00 PM 

211112013 5:23:00 PM 

211 112013 5:24:00 PM 

21 1112013 5:25:00 PM 

211112013 5:26:00 PM 

2/11 /2013 5:27:00 PM 

2111/2013 5:28:00 PM 

211112013 5:29:00 PM 

2/11/2013 5:30:00 PM 

2/11/2013 5:31:00 PM 

211112013 5:32:00 PM 

2111 /2013 5:33:00 PM 

2111 /2013 5:34:00 PM 

2111 /2013 5:35:00 PM 

2111 /2013 5:36:00 PM 

2111 /2013 5:37:00 PM 

2111/2013 5:38:00 PM 

2/11/2013 5:42:00 PM 

2/11/2013 5:43:00 PM 

2111 /2013 5:44:00 PM 

2111 /2013 5:45:00 PM 

2111 /2013 5:46:00 PM 

2111 /2013 5:47:00 PM 

2/11 /2013 5:48:00 PM 

2/1 1/2013 5:49:00 PM 

2111/2013 5:50:00 PM 

2I11/20135:51:00PM 

2/11/2013 5:52:00 PM 

211112013 5:53:00 PM 

2/1 112013 5:54:00 PM 

211112013 5:55:00 PM 

211112013 5:56:00 PM 

21 11 /2013 5:57:00 PM 

211112013 5:58:00 PM 

13.844 

13.798 

13.79 

13.789 

13.794 

13.799 

13.802 

13.81 

13.786 

13.783 

13.785 

13.775 

13.765 

13.74 

13.753 

13.756 

13.754 

13.847 

16.925 

13.829 

13.803 

13.804 

13.827 

13.822 

13.832 

13.803 

13.799 

13.785 

13.788 

13.778 

13.755 

13.757 

13.806 

16.399 

13.821 

13.825 

13.822 

13.817 

13.808 

13.809 

13.806 

13.818 

13.821 

13.814 

13.814 

13.804 

13.793 

4.168 2.786 1.013 13.839 

4.187 2.81 1.172 13.822 

4.192 2.924 1.121 13.805 

4.193 2.918 1.117 13.819 

4.193 2.886 1.121 13.84 

4.193 2.769 1.102 13.835 

4.191 2.864 1.107 13.889 

4.189 2.595 1.044 13.868 

4.201 2.691 0.89 13.872 

4.204 2.712 0.806 13.831 

4.205 2.642 0.837 13.845 

4.211 2.841 0.821 13.922 

4.219 2.511 0.808 13.843 

4.23 2.677 0.842 13.84 

4.228 2.463 0.884 8.842 

4.225 2.613 0.817 0.07 

4.226 2.759 0.868 0.043 

4.141 2.619 0.912 3.78 

2.433 1.506 0.612 13.824 

4.187 2.625 1.102 13.885 

4.204 2.674 1.077 13.881 

4.205 2.574 1.067 13.928 

4.194 2.593 1.146 13.942 

4.197 2.692 1.164 13.96 

4.191 2.47 1.29 13.961 

4.211 2.819 1.254 13.936 

4.21 2.712 1.135 13.954 

4.218 2.957 1.143 13.954 

4.218 2.875 1.178 13.918 

4.225 2.884 1.061 13.918 

4.245 3 0.988 13.903 

4.248 2.928 0.971 13.921 

4.199 2.739 0.964 13.966 

2.74 1.69 0.765 13.961 

4.204 2.826 1.334 13.947 

4.201 2.617 1.313 13.943 

4.198 2.951 1.353 13.933 

4.199 3.066 1.391 13.929 

4.197 3.133 1.379 13.949 

4.195 2.992 1.372 13.94 

4.19 2.863 1.388 13.977 

4.184 2.741 1.478 13.958 

4.179 2.66 1.585 13.941 

4.185 2.704 1.624 13.927 

4.186 2.754 1.58 13.914 

4. 194 2.817 1.455 13.905 

4.201 2.633 1.356 13.918 

26.557 

26.552 

26.714 

26.73 

26.925 

26.953 

26.926 

27.039 

27.295 

27.272 

27.221 

27.223 

27.22 

27.065 

18.686 

0.749 

0.589 

6.326 

26. 199 

26.578 

26.844 

26.584 

26.529 

26.283 

26. 122 

26.328 

26.186 

25.945 

26.341 

26.509 

26.706 

26.636 

26.746 

26.074 

26.614 

26.271 

26.235 

26.201 

26.31 

26.37 

25.904 

25.597 

25.633 

25.779 

26.105 

26.298 

26.204 

74.853 

71.41 

69.369 

68.916 

67.541 

68.591 

64.714 

63.889 

59.876 

58.603 

58.149 

57.217 

58.783 

60.019 

56.853 

5.84 

0.106 

2.711 

59.1'4 

68.403 

63.866 

67.747 

71 .76 

72.58 

78.769 

80.09 

81.977 

83.571 

80.178 

72.653 

74.177 

71 .262 

69.458 

76.696 

72.483 

75.02 

76.539 

78.564 

76.641 

75.359 

80.29 

86.009 

91.446 

88.955 

85.967 

79.37 

78.669 

7.728 

6.879 

6.265 

6.149 

6.014 

6.25 

4.854 

4.869 

3.994 

3.501 

3.327 

3.159 

3.526 

3.853 

8.784 

45.244 

46.703 ITHe Mid 

44.462 

8.265 

5.2 

5.201 

5.201 

5.201 

5.201 

5.201 

5.201 

5.201 

5.2 

5.2 

5.2 

5.201 

5.201 

5.2 

5.2 

5.199 

5.199 

5.199 

5.199 

5.199 

5.199 

5.2 

5.2 

5.2 

5.201 

5.201 

5.2 

5.2 
Date 

2/11/2013 

2/11/2013 

Time 

5:59:00 PM 

6:00:00 PM 

O2 CO2 NOx CO O2 NOx CO 

% % PPM PPM % PPM PPM 

13.797 4.201 2.542 1.352 13.927 25.928 83.189 

13.805 4.193 2.46 1.464 13.915 25.666 88.673 

2111/2013 6:01:00 PM 13.805 4.193 2.458 1.516 13.939 25.487 91.334 

2/1112013 6:02:00 PM 14.256 3.832 2.28 1.571 13.946 25.415 95.349 

2/11/2013 6:03:00 PM 17.999 1.877 1.085 0.736 13.93 25.824 91.385 

2111/2013 6:04:00 PM 13.821 4.18 2.785 1.352 13.923 26.339 78.327 

2/11/2013 6:05:00 PM 13.806 4.187 2.596 1.389 13.929 25.955 80.377 

2111/2013 6:06:00 PM 13.805 4.189 2.72 1.434 13.93 26.029 79.319 

2111/2013 6:07:00 PM 13.807 4.19 2.653 1.41 13.939 25.966 82.075 

2111/2013 6:08:00 PM 13.816 4.187 2.741 1.431 13.935 26.059 81.721 

2111/2013 6:09:00 PM 13.814 4.19 2.712 1.432 13.94 26.118 81.625 

211112013 6:10:00PM 13.807 4.195 2.55 1.418 13.938 26.198 78.111 

2111/2013 6:11:00PM 13.812 4.197 2.492 1.366 13.939 26.463 74.791 

2/11/2013 6:12:00PM 13.809 4.197 2.98 1.333 13.946 26.292 76.712 

2/11/2013 6:13:00 PM 13.807 4.201 3.243 1.293 13.94 26.439 73.232 

2/11/2013 6:14:00 PM 13.812 4.199 3.073 1.326 13.939 26.004 77.954 

2/11/2013 6:15:00 PM 13.81 4.202 2.952 1.416 13.949 25.965 80.262 

2/11/2013 6:16:00 PM 13.803 4.207 2.837 1.35 13.955 25.822 81.957 

2/11/2013 6:17:00 PM 13.804 4.208 2.881 1.38 13.936 26.09 80.462 

2/11/2013 6:18:00 PM 13.808 4.21 2.796 1.338 13.948 26.126 80.755 

2111/2013 6:19:00 PM 13.81 4.212 2.622 1.36 13.962 25.962 83.375 

2111/2013 6:20:00 PM 12.808 3.755 2.567 1.415 5.162 13.051 118.33 

2111/2013 6:21:00 PM 0.426 0. 103 0.126 6.942 0.058 0.767 240.049 

2111/2013 6:22:00 PM 0.219 0.079 0.032 9.389 0.038 0.623 1 242.9371 

2111/2013 6:23:00 PM 0.2 0.072 0.027 9.486 7.002 0.623 161 .578 

2111/2013 6:24:00 PM 0.2 0.07 0.028 9.5 10.097 0.49 1.735 

2111/2013 6:25:00 PM 0.2 0.068 0.028 9.48 10.098 0.445 -0.167 

2111/2013 6:26:00 PM 0.199 0.068 0.018 9.483 3.588 28.674 0.03 

2111/2013 6:27:00 PM ~:::8 . .::38:::8:........:4:;.:.5~1::. 4_~0.~02;;4:...., 3.872 0.042 48.327 0.218 

2111/2013 6:28:00 PM LI_1:;:0;:;.0::;25::.........;5:;..1:;:3.:.1_....:;;0.~02;;7,...J -0. 194 1.393 47.274 0.478 

2111/2013 6:29:00 PM 10.044 5.141 0.026 -0.33 13.9 25.864 62.944 

211112013 6:30:00 PM 5.083 2.405 1.237 -0.263 14.015 25.379 89.617 

2/11/2013 6:31:00 PM rl....:;;0.;;20;;;7;.........;0;;;.0:;:8;;.8-....,;;2.;;.5;:;19:-....;-0".0;;;1;;;7~ 14.018 25.333 93.616 

2111/2013 6:32:00 PM 0.125 0.048 0.539 0.034 5.311 12.407 79.266 

2/11/2013 6:33:00 PM 0.102 0.04 0.023 0.032 0.032 0.204 4.136 

2/11/2013 6:34:00 PM rl ~0 . .;:10::;2:........;0::;.0;3;,.9-....:;;0.;;02;;3;.........;0;;;.0;.;1:;5-...;0.;02;;:8;.........;0;::.1:.::54:::....-;0 .;:10:;:4:-. 

2/11/2013 6:35:00 PM 7.422 3.959 1.646 5.528 6.357 1.449 101.974 

2/11/2013 6:36:00 PM .-1:;:0;:;.0:;44;.........;5:;:.1;5:;,8_....;.2,;;.5;;:3,.......,;9::;.4;;9;9_....,.:; 10::;.0:;:9;,..., 2.615 243.153 

2/11/2013 6:37:00 PM 1 10.052 5.158 2.531 9.562 10.097 4.865 1243.2461 

211112013 6:38:00 PM 7.696 2.781 2.607 5.364 10.102 48.409 243.713 

2/11/2013 6:39:00 PM 13.788 4.174 2.853 1.744 10.098 48.813 243.62 

211112013 6:40:00 PM 13.818 4.192 3.037 1.662 10.918 48.954 1241.913 

2111/2013 6:41:00 PM 13.83 4.193 2.908 1.7 ,....;1:;9;.;.1.;;12:......!:28;:;..9::2::9~ 191.179 

2/11/2013 6:42:00 PM 13.83 4.196 2.882 1.676 19.214 24.89 129.29 

2111/2013 6:43:00 PM 13.831 4.198 2.753 1.672 19.182 9.587 139.132 

2/11/2013 6:44:00PM 13.827 4.201 2.776 1.719 19.133 0.401 114.055 

2111/2013 6:45:00 PM 13.823 4.204 2.693 1.638 19.137 0.331 24.391 

2/11/2013 6:46:00 PM 13.816 4.206 2.654 1.545 19.128 0.289 4.245 

2/1112013 6:47:00 PM 13.813 4.207 2.464 1.632 19.13 0.275 1.21 

2111/2013 6:48:00 PM 13.804 4.212 2.456 1.487 19.117 0.263 0.757 

211112013 6:49:00 PM 13.804 4.208 2.318 1.512 19.077 0.247 0.685 

2111/2013 6:50:00 PM 13.806 4.208 2.295 1.616 19.064 0.24 0.708 

2111/2013 6:51:00 PM 16.464 2.661 1.562 1.339 19.129 0.228 0.705 

2111/2013 6:52:00 PM 13.875 4.173 3.007 1.503 19.101 0.217 0.707 

2/11f2013 6:53:00 PM 13.832 4.19 3.011 1.679 19.101 0.224 0.706 

2/11/2013 6:54:00 PM 13.835 4.191 2.868 1.682 19.097 0.205 0.657 

2/11/2013 6:55:00 PM 13.841 4.189 2.932 1.729 19.097 0. 195 0.684 

2/1112013 6:56:00PM 13.848 4.185 2.692 2.006 19.082 0.186 0.581 

2/11/2013 6:57:00PM 13.847 4.186 2.797 1.891 19.091 0.186 0.563 

2/11/2013 6:58:00 PM 13.842 4.189 2.723 1.866 19.084 0.178 0.587 

2111/2013 6:59:00 PM 13.641 4.189 2.659 1.904 19.082 0.177 0.562 

211112013 7:00;00 PM 13.834 4.193 2.634 1.855 19.071 0.171 0.609 

THe 

PPM 

5.2 

5.201 

5.201 

5.202 

5.201 

5.2 

5.2 

5.2 

5.201 

5.202 

5.202 

5.202 

5.202 

5.201 

5.201 

5.2 

5.2 

5.201 

5.201 

5.201 

5.201 

5.203 

5.208 

5.208 

5.204 

5.197 

5.197 

5.196 

5.197 

5.196 

5.199 

5.2 

5.2 

5.2 

5.197 

5.197 

5.202 

5.208 

5.209 

5.209 

5.208 

5.209 

5.206 

5.203 

5.203 

5.202 

5.198 

5.197 

5.197 

5.198 

5.197 

5.197 

5.197 

5.197 

5.197 

5.197 

5.196 

5.196 

5.196 

5.197 

5.196 

5.196 

CO bias 

CO bias 

02 bias 

NOx bias 

02fC02 bias 

NOx bias 

Direct Zero 

Direct Span 

NOx Direct 

02 High, NOx Mid 

CO Mid 
Date 

2/11/2013 

211112013 

Time 

7:01 :00 PM 

7:02:00 PM 

2/11/2013 7:03:00 PM 

2/11 /2013 7:04:00 PM 

2111 /2013 7:05:00 PM 

2111 /2013 7:06:00 PM 

211112013 7:07:00 PM 

2/11 /2013 7:08:00 PM 

2111 /2013 7:09:00 PM 

2/11/2013 7:10:00 PM 

2/11/2013 7: 11 :00 PM 

211112013 7:12:00 PM 

211112013 7: 13:00 PM 

2111 /2013 7:14:00 PM 

211112013 7:15:00 PM 

2/11 /2013 7:16:00 PM 

2111 /2013 7:17:00 PM 

2/11/20137:18:00PM 

2I11/20137:19:00PM 

2/11/2013 7:20:00 PM 

2111/2013 7:21 :00 PM 

2111/2013 7:22:00 PM 

2111 /2013 7:23:00 PM 

2111 /2013 7:24:00 PM 

2111 /2013 7:25:00 PM 

2111 /2013 7:26:00 PM 

0, 

% 

13.832 

13.825 

17.316 

13.873 

13.841 

13.836 

13.835 

13.837 

13.83 

13.827 

13.817 

13.8 

13.775 

13.759 

16.889 

13.839 

13.829 

13.828 

13.832 

13.837 

13.84 

13.829 

13.811 

13.776 

13.789 

13.786 

CO, 

% 

NOs. CO 

PPM PPM 

4.193 2.471 1.767 

4.199 2.527 1.709 

2.18 1.294 1.128 

4.167 2.787 1.442 

4.175 2.758 1.753 

4.176 2.66 1.72 

4.175 2.561 1.793 

4.171 2.574 1.831 

4.176 2.667 1.884 

4.178 2.725 1.869 

4.185 2.725 1.638 

4.194 2.654 1.379 

4.208 2.649 1.248 

4.221 2.653 1.288 

2.421 1.699 0.8 

4.178 2.705 1.236 

4.186 2.756 1.33 

4.19 2.628 1.373 

4.183 2.656 1.307 

4.178 2.508 1.386 

4.177 2.55 1.396 

4.186 2.543 1.359 

4.198 2.233 1.359 

4.219 2.435 1.29 

4.216 2.338 1.184 

4.216 2.125 1.258 

2/11/2013 7:27:00 PM 13.803 4.211 1.887 1.424 

2111/2013 7:28:00 PM 14.809 2.614 1.753 1.237 

2111/2013 7:29:00 PM 11.357 4.251 0.154 0.027 

211112013 7:30:00 PM 1'"1-:1:::0;;; 0~84:--~5'i1':'16:--~0i:'.~03~5"'" -0.313 

2111 /2013 7:31 :00 PM 10.07 5.118 0.049 -0.352 

2111 /2013 7:32:00 PM 10.081 5.116 0.106 ..().314 

21 11 /2013 7:33:00 PM 10.064 5.115 0.085 -0.337 

2111 /2013 7:34:00 PM 8.812 3.527 0.518 -0.295 

211112013 7:35:00 PM 1'"1 i:-:;;30"'9~--;O~.0"'7;--;"2;;5:----;-O;;.0;';1;i;6' 

2111/2013 7:36:00 PM 0.152 0.059 2.525 0.034 

2111/2013 7:37:00 PM 0.152 0.057 2.298 0.249 

2/11/2013 7:38:00 PM 0.13 0.054 0.035 7.919 

2/11/2013 7:39:00 PM 0.127 0.052 0.033 9.514 

2111 /2013 7:40:00 PM 0.109 0.032 0.023 5.728 

2111 /2013 7:41 :00 PM 1'"1 ~0i:':-:10:i2~--;;0"0"'26;-~0i:'.0;':2:i2~--;;0:':1~1;;-6' 

2111 /2013 7:42:00 PM 0.102 0.024 0.025 0.036 

2111 /2013 7:43:00 PM 0.134 0.04 0.018 0.038 

211 112013 7:44:00 PM 9.53 5.112 2.228 6.055 

2/11/2013 7:45:00 PM .. 1..,1"0"0:;,49,.........:;5;.;.1.,;37:;--2;;.;;52;;8~....:;9;;;.5:.:;1;.9..., 

2/11/2013 7:46:00 PM 10.061 5.136 2.528 9.568 

2111/2013 7:47:00 PM 10.068 5.133 2.524 9.56 

2/11/2013 7:48:00 PM 16.802 8.83 3.896 9.535 

2/11 /2013 7:49:00 PM 19.09 9.733 4.839 6.544 

2111 /2013 7:50:00 PM 11'"-:1;;9."0;,:94:---;;9".7"'33:;--4.;.8;.:2;;7;-.....:;4;;.6,;0.;.1..., 

211112013 7:51 :00 PM 19.043 9.744 4.765 4.533 

2111 /2013 7:52:00 PM 18.997 9.752 2.162 4.515 

2/1112013 7:53:00 PM 18.985 9.751 0.417 4.5 

2111/2013 7:54:00 PM 18.985 9.75 0.206 4.464 

2111/2013 7:55:00 PM 18.985 9.745 0.135 4.437 

0, 

% 

19.05 

19.022 

19.025 

19.015 

18.995 

18.986 

18.978 

18.966 

18.959 

18.95 

18.944 

18.939 

18.944 

18.954 

18.954 

18.95 

18.968 

18.967 

18.963 

18.957 

18.938 

18.943 

18.947 

18.951 

18.951 

18.951 

18.956 

18.953 

18.95 

18.934 

18.909 

18.901 

18.913 

18.912 

18.914 

18.913 

18.92 

18.928 

18.917 

18.912 

18.899 

18.882 

18.886 

18.882 

18.872 

18.871 

18.86 

18.847 

18.844 

18.847 

18.84 

18.839 

18.83 

18.823 

18.818 

NO, 

PPM 

0.166 

0.165 

0.164 

0.151 

0.147 

0.143 

0.142 

0.144 

0. 142 

0.144 

0.14 

0.141 

0.134 

0.126 

0.141 

0.134 

0.126 

0.139 

0.128 

0.128 

0.127 

0. 133 

0. 133 

0.1 27 

0.125 

0.122 

0.12 

0.113 

0.106 

0. 111 

0. 106 

0.108 

0.109 

0.109 

0. 109 

0.11 

0.109 

0.101 

0.105 

0.108 

0.105 

0.101 

0.106 

0.101 

0.099 

0.103 

0.101 

0.096 

0.097 

0.092 

0.095 

0.096 

0.094 

0.088 

0.084 

CO 

PPM 

0.589 

0.565 

0.564 

0.561 

0.56 

0.564 

0.566 

0.565 

0.565 

0.564 

0.565 

0.563 

0.564 

0.565 

0.564 

0.565 

0.564 

0.562 

0.536 

0.536 

0.561 

0.567 

0.515 

0.565 

0.564 

0.558 

0.561 

0.479 

0.486 

0.468 

0.538 

0.482 

0.517 

0.558 

0.559 

0.488 

0.512 

0.513 

0.563 

0.538 

0.561 

0.512 

0.415 

0.435 

0.413 

0.412 

0.413 

0.412 

0.44 

0.437 

0.413 

0.413 

0.413 

0.439 

0.414 

THC 

PPM 

5.196 

5.197 

5.197 

5.197 

5.198 

5.197 

5.197 

5.197 

5.197 

5.197 

5.197 

5.197 

5.197 

5.196 

5.196 

5.196 

5.196 

5.196 

5.196 

5.196 

5.197 

5.197 

5.197 

5.197 

5.197 

5.197 

5.197 

5.197 

5.197 

5.197 02/C02 bias 

5.198 

5.198 

5.1 97 

5.1 96 

5.196 

5.196 

5.197 

5.198 

5.197 

5.196 

5.196 

5.196 

5.196 

5.197 

5.196 

5.197 

5.198 

5.197 

5.197 

5.198 

5.198 

5.198 

5.197 

5.197 

5.197 

NOx bias 

CO bias 

Direct Zero 

Direct Span 

Direct High 
~ ~ N~ ro ~ ~ ro THC 

Date Time % % PPM PPM % PPM PPM PPM 

2/12/2013 7:47:00AM 0.393 6.13 0.007 0.42 17.933 L..;;;0 . .;;01;;6~ 0.792 

2/12/2013 7:48:00 AM 0.138 0.111 0.01 0.21 6.812 0.012 0.712 

5.212 Zero/NOx Mode 

5.211 

2/12/2013 7:49:00 AM 1r-0';;';;11;';6~"""'"0;;'.0;';0";'2-""';0:';;0;';07:--0;'.;;;08":'3""""""'"0;;;0;';6':;4-"";;0;;;.0';;11;--0';;"'25;;8;-' 5.21 Cal Zero; Zero/NO Mode 

2/12/2013 7:50:00AM 13.913 7.231 2.141 3.852 5.744 1.144 0.916 5.209 

2/12/2013 7:51 :00AM 1905 9773 48 9814 19604 4853 179524 5.216 

2/12/2013 7:52:00 AM 

2112/2013 7:53:00 AM 

2/12/2013 7:54:00 AM 

18.972 

I 18.971 

11 .725 

9.771 4.812 9.625 

9.663 4.816 9.617 

5.841 4.828 9.627 

2/12/2013 7:55:00 AM 10.03 5.092 4.826 9.581 

2/12/2013 7:56:00 AM r-:1.;,;0:.;;.0;,;27:,---=5;;;.;,;09,;;...., 1.524 7.3 

2112/2013 7:57:00 AM 16.698 1.071 0.025 4.829 

2/12/2013 7:58:00 AM 20.89 0.068 3.325 4.605 

2/12/2013 7:59:00AM 20.925 0.063 3.856 3.113 

2/1212013 8:00:00 AM 20.934 0.061 1.201 0.675 

2112/2013 8:01 :00 AM 20.94 0.06 0.019 0.309 

2/1212013 8:02:00 AM 20.919 0.079 3.278 0.257 

2/12/2013 8:03:00 AM 20.939 0.065 4.805 0.266 

2/12/2013 8:04:00 AM 

2/12/2013 8:05:00 AM 

2/12/2013 8:06:00 AM 

2/1212013 8:07:00 AM 

2/1212013 8:08:00 AM 

2/1212013 8:09:00 AM 

2/12/2013 8:10:00 AM 

2/12/2013 8:11 :00AM 

2/12/2013 8:12:00 AM 

2/12/2013 8:13:00 AM 

2/12/2013 8:14:00 AM 

2/12/2013 8:15:00AM 

2/12/2013 8:16:00 AM 

2/12/2013 8:17:00 AM 

2/12/2013 8:18:00 AM 

2/1212013 8:19:00 AM 

2/12/2013 8:20:00 AM 

20.931 

20.933 

20.932 

20.928 

20.925 

20.923 

20.917 

20.916 

20.913 

20.907 

20.903 

20.899 

20.9 

20.902 

20.932 

20.955 

20.955 

0.064 4.809 0.255 

0.065 4.013 0.236 

0.068 3.828 0.249 

0.071 2.609 0.24 

0.074 2.521 0.246 

0.076 1.49 0.254 

0.077 0.031 0.254 

0.079 0.033 0.247 

0.084 0.034 0.241 

0.084 0.028 0.258 

0.085 0.026 0.26 

0.087 0.025 0.258 

0.089 0.026 0.258 

0.091 0.032 0.249 

0.092 0.072 0.264 

0.091 0.031 0.262 

0.093 0.028 0.245 

2/12/2013 8:21:00AM 18.633 0.764 0.028 0.43 

2/12/2013 8:22:00 AM 1.--:1.;:0;;;.0.:;75,...."""'"5;;;0"8"'9-....;;0.;:0~13~ 0.193 

211212013 8:23:00AM 10.039 5.113 0.015 -0.295 

2/1212013 8:24:00AM 8.968 4.41 0.193 -0.298 

2/1212013 8:25:00 AM 0.274 0.09 2.496 -0.021 

2/12/2013 8:26:00 AM 1~0::-~154;-::---;0;-;.0i::7':-1--::2-;5~15;--0;i-;i:08;;6,..., 

2/1212013 8:27:00AM 0.139 0.069 1.579 2.401 

2/12/2013 8:28:00 AM 0.129 0.069 0.013 9.435 

2/12/2013 8:29:00 AM 0.129 0.D7 0.006 9.607 

2/12/2013 8:30:00 AM 6.646 0.735 0.145 8.083 

2/12/2013 8:31 :00 AM 13.852 4.153 1.629 1.542 

2/12/2013 8:32:00AM 13.832 4.167 1.577 1.481 

2112/2013 8:33:00AM 13.831 4.174 1.633 1.555 

2112/2013 8:34:00 AM 13.833 4.175 1.581 1.668 

2112/2013 8:35:00 AM 13.821 4.192 1.648 1.459 

2/12/2013 8:36:00 AM 13.818 4.197 1.717 1.154 

2/12/2013 8:37:00 AM 13.829 4.194 1.638 1.23 

2/12/2013 8:38:00 AM 13.812 4.212 1.701 1.109 

2/12/2013 8:39:00 AM 13.814 4.213 1.868 1.115 

2/12/2013 8:40:00 AM 13.832 4.204 1.747 1.197 

2/12/2013 8:41 :00AM 13.925 4.11 1.809 1.23 

2/12/2013 8:42:00 AM 17.91 1.988 0.778 0.624 

2/12/2013 8:43:00 AM 13.858 4.198 1.907 1.542 

19.026 4.866 244.456 

18.996 4.877 244.417 I 

12.422 4.886 226.315 

10.03 4.885 101.868 

10.012 1.629 139.913 

15.072 0.02 140.39 

16.814 3.301 140.364 

16.811 3.905 124.784 

16.803 1.373 99.245 

16.744 0.019 98.963 

15.599 28.268 53.304 

4.721 48.615 53.456 

0.D76 

0.057 

0.052 

0.805 

0.126 

0.033 

0.031 

0.032 

0.3 

0.036 

0.03 

0.526 

0.035 

0.03 

6.375 

13.818 

13.848 

48.352 

28.957 

24.664 

7.378 

0.78 

0.498 

0.453 

0.408 

0.926 

0.343 

0.302 

1.346 

0.265 

0.235 

10.222 

24.255 

24.303 

1.13 

0.336 

0.326 

1.194 

7.836 

0.249 

0.276 

0.22 

0.904 

1.401 

0.187 

2.117 

2.474 

0.187 

12.04 

84.176 

92.58 

13.85 24.526 92.331 

13.852 24.618 92.25 

13.852 24.58 100.21 

13.848 25.255 82.696 

13.849 25.088 81.148 

13.855 24.978 82.072 

13.872 24.645 92.05 

13.883 24.564 98.108 

13.892 24.822 95.413 

5.218 NO/NOx Mode 

5.218 Cal Hi9h 

5.215 NOINO Mode 

5.209 

5.211 02/C02 Mid 

5.211 N02/NO Mode 

5.211 CO Mid 

5.21 N02/NOx Mode 

5.871 

6.588 NOx Cal Zero 

1.822 

4.733 

-0.007 NOx Cal Hi9h 

-0.007 

-0.006 INOx Mid;THC Zero 

0.031 

72.455 NOx Mid 

89.371 

85.036 

85.133 ITHC Cal Hi9h 

85.469 

50.078 

46.953 ITHC Mid 

46.274 

26.83 

25.995 ITHC Low 

21 .625 

9.582 

10.638 

10.611 

10.772 02/C02 bias 

13.69 

8.102 

7.753 

7.916 NOxbias 

11.005 

12.926 

12.133 CObias 

13.884 25.148 89.024 10.386 

13.884 24.962 87.429 9.66 Start RATA Run 7 

13.881 24.85 93.193 11.762 

13.879 24 .752 97.439 13.31 

13.877 24.735 99.308 13.922 

13.862 25.214 85.452 9.236 

13.866 25.247 83.221 8.532 

13.881 25.242 86.698 9.867 

13.886 25.315 80.761 7.855 

13.903 25.132 87.099 9.734 

13.917 24.903 96.209 12.744 

13.912 25.132 90.233 10.793 

13.902 25.194 90.087 11 .171 

13.901 25.079 92.277 11.804 
O2 CO2 NO. CO 

Oate Time % % PPM PPM 

2/12/2013 8:44:00 AM 13.837 4.208 1.925 1.525 

2/12/2013 8:45:00 AM 13.836 4.207 1.897 1.554 

2/12/2013 8:46:00AM 13.832 4.211 1.958 1.469 

2/12/2013 8:47:00 AM 13.828 4.219 2.08 1.349 

2/12/2013 8:48:00 AM 13.832 4.217 1.824 1.352 

2112/2013 8:49:00 AM 13.831 4.225 1.896 1.406 

2112/2013 8:50:00 AM 13.832 4.227 1.943 1.285 

2112/2013 8:51 :00 AM 13.833 4.232 1.855 1.256 

2112/2013 8:52:00 AM 13.828 4.24 1.891 1.207 

2/12/2013 8:53:00 AM 14.55 3.679 1.89 0.973 

2/12/2013 8:54:00 AM 14.324 4.098 2.177 0.916 

2/12/2013 8:55:00AM 13.832 4.232 2.493 1.062 

2/12/2013 8:56:00 AM 13.833 4.233 2.469 1.086 

2/12/2013 8:57:00 AM 13.833 4.234 2.431 1.126 

2/12/2013 8:58:00 AM 13.832 4.238 2.481 1.1 49 

2112/2013 8:59:00 AM 13.75 4.238 2.32 1.195 

2/12/2013 9:00:00AM 13.747 4.25 2.232 1.176 

2/12/2013 9:01 :00 AM 13.801 4.26 2.292 1.191 

2/12/2013 9:02:00 AM 13.815 4.25 2.39 1.156 

2/12/2013 9:03:00 AM 13.826 4.244 2.475 1.052 

2/12/2013 9:04:00AM 13.838 4.235 2.561 1.148 

2/12/2013 9:05:00 AM 13.834 4.233 2.53 1.13 

2/12/2013 9:06:00 AM 13.833 4.229 2.553 1.183 

2/12/2013 9:07:00 AM 13.825 4.228 2.607 1.112 

2/12/2013 9:08:00 AM 13.824 4.224 2.518 1.103 

2/12/2013 9:09:00 AM 13.828 4.216 2.162 1.147 

2/12/2013 9:10:00 AM 13.829 4.211 2.054 1.183 

2/12/2013 9:11:00 AM 13.83 4.209 2.036 1.277 

2/12/2013 9:12:00 AM 14.167 3.902 2.037 1.312 

2/12/2013 9:13:00 AM 16.339 2.885 1.346 0.891 

2/1212013 9:14:00AM 13.867 4.186 2.141 1.316 

2/1212013 9:15:00 AM 13.865 4.189 2.101 1.383 

2/12/2013 9:16:00AM 13.875 4.186 2.057 1.484 

2/12/2013 9:17:00 AM 13.874 4.186 2.224 1.49 

2/12/2013 9:18:00 AM 13.869 4.192 2.199 1.649 

2/12/2013 9:19:00 AM 13.847 4.207 2.434 1.529 

2/12/2013 9:20:00 AM 13.86 4.201 2.56 1.313 

2/1212013 9:21 :00AM 13.878 4.194 2.346 1.416 

2/12/2013 9:22:00 AM 13.875 4.196 2.42 1.338 

2/1212013 9:23:00 AM 10.541 2.979 1.887 2.115 

2/12/2013 9:24:00 AM 0.193 0.113 0.021 8.926 

2/12/2013 9:25:00 AM 0.13 0.104 0.011 9.575 

2/12/2013 9:26:00 AM 4.504 2.6 0.012 7.255 

2/12/2013 9:27:00 AM 1...-:1.;;0.;, .0:,;14:---:5,;;.1"'6..,.4-....:,0".0,::1:....., -0.074 

2/12/2013 9:28:00 AM ...,4,;;.:,;70:;;3;-~2;;:2;:2::;2_ ...... 1.:;;2;,;75;.--,-"'0."'19;;2;-, 

2/12/2013 9:29:00 AM IL-O,;:.,;;13;.:7,.----:O:,;. .1:,;1;;.3_....;;2.;;;5;::08;.-_0,;:.;::05:.;7,.-J 

2/12/2013 9:30:00 AM 6.346 2.18 2.478 0.375 

2112/2013 9:31 :00 AM 13.831 4.202 2.371 1.381 

2112/2013 9:32:00 AM 

2112/2013 9:33:00 AM 

2/12/2013 9:34:00 AM 

2/1 2/2013 9:35:00 AM 

2/12/2013 9:36:00 AM 

2/12/20 13 9:37:00 AM 

2/12/2013 9:38:00 AM 

2/12/2013 9:39:00 AM 

2/12/2013 9:40:00 AM 

2/12/2013 9:41 :00AM 

13.846 

13.869 

13.873 

13.872 

13.888 

13.876 

13.876 

13.864 

13.861 

13.942 

4.213 2.505 1.376 

4.205 2.321 1.525 

4.205 2.472 1.477 

4.203 2.459 1.514 

4.193 2.503 1.681 

4.195 2.613 1.763 

4.192 2.631 1.695 

4.198 2.687 1.511 

4.197 2.653 1.505 

4.108 2.622 1.514 

0 , 

% 

13.897 

13.897 

13.889 

13.882 

13.897 

13.891 

13.892 

13.899 

13.882 

13.875 

13.879 

13.873 

13.883 

13.887 

13.91 

13.92 

13.917 

13.9 

13.878 

13.9 

13.897 

13.904 

13.894 

13.881 

13.894 

13.896 

13.896 

13.901 

13.908 

13.902 

13.907 

13.919 

13.922 

13.921 

13.909 

13.887 

13.901 

13.903 

13.918 

13.92 

13.924 

13.937 

13.909 

13.906 

13.915 

13.907 

13.908 

13.915 

13.928 

13.934 

13.929 

13.937 

13.94 

13.917 

13.91 

13.898 

13.902 

13.901 

NO, 

PPM 

25.225 

25.142 

25.325 

25.646 

25.286 

25.665 

25.79 

25.832 

26.315 

26.501 

26.347 

26.234 

26.115 

26.026 

25.899 

25.695 

25.675 

26.183 

26.641 

26.267 

26.344 

26.141 

26.22 

26.645 

26.335 

26.156 

26.026 

25.763 

25.632 

25.869 

25.885 

25.846 

25.475 

25.399 

25.332 

25.938 

25.898 

25.626 

25.551 

25.734 

25.798 

25.305 

25.779 

25.804 

25.486 

25.652 

25.58 

25.604 

25.49 

25.407 

25.573 

25.317 

25.042 

25.364 

25.434 

25.558 

25.425 

25.506 

CO 

PPM 

85.669 

88.29 

82.405 

75.774 

80.977 

76.525 

73.842 

73.012 

67.2 

60.327 

59.613 

60.255 

60.993 

63.345 

63.994 

67.33 

64.994 

62.043 

57.927 

58.369 

60.864 

63.473 

64.701 

58.642 

59.946 

63.119 

64.823 

70.026 

72.75 

70.889 

68.947 

69.343 

78.929 

76.694 

85.339 

71.694 

66.436 

74.058 

72.822 

74.577 

69.038 

78.41 

75.578 

70.579 

72.654 

71.686 

75.745 

72 .8 

73.293 

80.138 

76.138 

80.233 

87.696 

86.996 

84.275 

77.73 

79.796 

80.878 

THC 

PPM 

9.277 

10.5 

8.631 

6.464 

7.958 

6.907 

6.229 

5.956 

4.559 

3.112 

3.152 

3.123 

3.191 

3.628 

3.52 

4.3 

3.858 

3.293 

2.796 

2.799 

3.23 

3.611 

3.985 

2.957 

3.177 

3.652 

3.926 

5.206 

6.169 

5.504 

4.972 

4.902 

7.669 

6.741 

9.465 

5.683 

4.723 

5.961 

5.665 

6.049 

4.766 

7.024 CO bias 

6.767 

5.301 02/C02 bias 

5.572 

5.471 NOx bias 

6.603 

5.553 Start RATA Run 8 

5.553 

7.379 

6.348 

6.937 

9.175 

9.791 

8.834 

7.116 

7.668 

8.173 
0, CO, NO. CO 

Date Time % % PPM PPM 

2/12/2013 9:42:00 AM 16.484 2.745 1.577 1.003 

2/12/2013 9:43:00 AM 13.827 4.228 2.652 1.484 

2/12/2013 9:44:00 AM 13.827 4.228 2.428 1.55 

2/12/2013 9:45:00 AM 13.827 4.233 2.35 1.532 

2/12/2013 9:46:00 AM 13.83 4.232 2.329 1.592 

2/1 2/2013 9:47:00 AM 13.832 4.234 2.266 1.621 

2/12/2013 9:48:00 AM 13.832 4.237 2.281 1.68 

2112/2013 9:49:00AM 13.833 4.238 2.184 1.705 

2/12/2013 9:50:00 AM 13.831 4.248 2.275 1.602 

2/12/2013 9:51 :00 AM 13.832 4.25 2.379 1.327 

2/12/2013 9:52:00 AM 14.852 3.508 2.18 1.161 

2/12/2013 9:53:00AM 16.038 3.153 1.418 0.714 

2/12/2013 9:54:00 AM 13.842 4.245 2.146 1.247 

2/12/2013 9:55:00 AM 13.834 4.253 2.271 1.184 

211212013 9:56:00 AM 13.832 4.255 2.178 1.11 

2/12/2013 9:57:00 AM 13.836 4.251 2.116 1.177 

2/12/2013 9:58:00 AM 13.831 4.26 2.092 1.131 

2/12/2013 9:59:00 AM 13.832 4.26 2.072 1.082 

2/12/2013 10:00:00AM 13.831 4.265 1.999 1.1 

2/12/2013 10:01 :00AM 13.831 4.265 1.883 1.225 

2/12/201310:02:00AM 13.831 4.266 1.923 1.154 

2112/201310:03:00AM 15.311 3.25 1.629 1.039 

2112/2013 10:04:00 AM 14.489 4.06 2.019 0.746 

2112/2013 10:05:00 AM 13.836 4.263 2.321 0.877 

2/1212013 10:06:00 AM 13.845 4.257 2.201 0.932 

2/12/2013 10:07:00 AM 13.842 4.258 2.241 0.964 

2/12/2013 10:08:00 AM 13.83 4.269 2.386 0.918 

2/12/2013 10:09:00 AM 13.829 4.272 2.285 0.851 

2/1212013 10:10:00 AM 13.822 4.276 2.315 0.817 

2/12/2013 10:11 :00 AM 13.787 4.297 2.42 0.796 

2/1212013 10:12:00 AM 13.79 4.294 2.33 0.824 

2/1212013 10:13:00 AM 12.612 4.158 2.305 0.845 

2/1212013 10:14:00 AM 1'-:1"0".0"'33:---:5"".1"9""9-"""0"".0"'32::-"1 -0.148 

2/1212013 10:15:00 AM 4.367 2.071 1.372 -0.187 

2/12/2013 10: 16:00 AM 1r-:0;;-~14:-::7""'--;O~.1;-:;4-:;-1--:;2-;;5;;:05~-'i:0-;:.0~5"" 

2/12/2013 10:17:00AM 0.131 0.134 0.794 4.72 

2/1212013 10: 18:00 AM 0.129 0.13 0.016 9.533 

2/12/2013 10:19:00AM 0.129 0.127 0.01 9.58 

21121201310:20:00AM 0.129 0.125 0.016 9.592 

2/121201310:21 :00AM 3.438 1.329 0.48 8.831 

2/12/201310:22:00AM 13.79 4.232 2.192 1.662 

2/12/2013 10:23:00 AM 13.835 4.245 2.168 1.039 

2/12/2013 10:24:00AM 13.835 4.252 2.156 1.103 

2/12/2013 10:25:00 AM 13.838 4.255 2.136 1.086 

2/12/2013 10:26:00 AM 13.835 4.258 2.146 0.984 

2/12/2013 10:27:00 AM 13.829 4.263 2.038 0.971 

2/12/2013 10:28:00 AM 13.832 4.262 1.957 0.927 

2/12/2013 10:29:00 AM 13.833 4.26 2.083 0.907 

2/12/2013 10:30:00 AM 13.794 4.286 2.053 0.927 

2/12/2013 10:31 :00 AM 13.775 4.295 2.281 0.963 

2/12/2013 10:32:00AM 14.536 3.705 1.896 0.911 

2/12/2013 10:33:00 AM 15.851 

2/12/2013 10:34:00 AM 13.835 

2/1212013 10:35:00 AM 13.831 

211212013 10:36:00 AM 13.83 

2/1212013 10:37:00 AM 13.819 

2/12/2013 10:38:00 AM 13.832 

2/12/2013 10:39:00 AM 13.834 

3.252 1.393 0.742 

4.253 2.088 1.161 

4.261 2.127 1.176 

4.261 2.098 1.107 

4.265 2.188 1.054 

4.248 2.122 1.085 

4.243 2.042 1.159 

0, 

% 

13.903 

13.896 

13.901 

13.909 

13.918 

13.929 

13.922 

13.929 

13.914 

13.913 

13.902 

13.912 

13.914 

13.903 

13.904 

13.904 

13.903 

13.901 

13.912 

13.916 

13.915 

13.908 

13.898 

13.906 

13.914 

13.914 

13.907 

13.9 

13.892 

13.897 

13.907 

13.918 

13.91 

13.919 

13.927 

13.926 

13.908 

13.915 

13.909 

13.92 

13.919 

13.923 

13.918 

13.898 

13.899 

13.918 

13.916 

13.913 

13.913 

13.906 

13.906 

13.902 

13.899 

13.894 

13.888 

13.879 

13.901 

13.903 

NO. 

PPM 

25.322 

25.529 

25.519 

25.399 

25.299 

25.164 

25.133 

25.042 

25.907 

26.079 

26.491 

26 .303 

26.08 

26.406 

26.35 

26.327 

26.6 

26.5 

26.367 

26.236 

26.366 

26.467 

26.924 

26.893 

26.607 

26.538 

26.569 

26.537 

26.731 

26.554 

26.322 

26.382 

26.422 

26.255 

26.161 

26.03 

26.297 

26.158 

26.477 

26.462 

26.408 

26.159 

26.032 

26.413 

26.376 

26.13 

26.192 

26.361 

26.16 

26.183 

26.109 

CO 

PPM 

82.666 

79.427 

82.578 

81 .659 

87.251 

87.222 

89.949 

93.323 

78.289 

71 .686 

62.172 

64.225 

67.756 

60.731 

60.236 

62.525 

57.341 

58.127 

58.792 

61.938 

59.944 

57.867 

54.477 

54.129 

56.838 

58.422 

56.568 

58.145 

55.357 

56.332 

58.057 

58.286 

58.389 

59.584 

60.079 

62.511 

60.233 

63.327 

61 .797 

59.064 

59.71 

59.408 

62.389 

61 .384 

58.595 

59.957 

60.783 

60.207 

62.474 

61.029 

61.771 

26.132 62.13 

26.071 62.32 

26.327 60.798 

26.317 59.724 

26.592 56.74 

26.078 59.628 

25.975 62.429 

THC 

PPM 

8.373 

7.633 

8.565 

7.965 

9.906 

10.099 

10.665 

11 .86 

7.652 

5.65 

3.53 

4.044 

4.778 

3.329 

3.187 

3.745 

2.617 

2.645 

2.726 

3.281 

3.05 

2.656 

2.116 

2 

2.36 

2.613 

2.433 

2.743 

2.166 

2.473 

2.766 

2.55 

2.647 

2.725 

2.744 

3.337 

3.008 

3.632 

3.392 

2.807 

2.952 

2.864 

3.397 

3.332 

2.78 

3.02 

3.161 

3.15 

3.338 

3.079 

3.347 

3.205 

3.361 

2.977 

2.814 

2.485 

2.856 

3.326 

02/C02 bias 

NOx bias 

CO bias 

Start RATA Run 9 
Date Time 

0, 

% 

2/12/2013 10:40:00 AM 13.832 

2/12/2013 10:41 :00 AM 13.835 

2/12/2013 10:42:00 AM 13.834 

2/12/2013 10:43:00 AM 13.833 

2/12/2013 10:44:00 AM 13.833 

2/1212013 10:45:00 AM 15.164 

2/12/2013 10:46:00 AM 14.22 

2/12/2013 10:47:00 AM 13.827 

2/12/2013 10:48:00 AM 13.828 

2/12/2013 10:49:00 AM 13.825 

2/1212013 10:50:00 AM 13.831 

2/12/201310:51:00AM 13.833 

2/12/2013 10:52:00 AM 13.841 

211212013 10:53:00 AM 13.832 

2/1212013 10:54:00 AM 13.822 

2/12/2013 10:55:00 AM 17.214 

2/12/2013 10:56:00 AM 13.866 

2/12/2013 10:57:00 AM 13.838 

2/12/2013 10:58:00 AM 13.841 

2/12/2013 10:59:00 AM 13.84 

2/12/2013 11 :00:00 AM 13.839 

2/12/2013 11 :01 :00AM 13.843 

2/12/2013 11 :02:00 AM 13.836 

2/12/2013 11 :03:00 AM 13.843 

2/12/201311 :04 :00AM 13.834 

2/12/2013 11 :05:00 AM 13.795 

CO, 

% 

NO, CO 0, NO, CO 

PPM PPM % PPM PPM 

4.244 2.078 1.197 13.902 26.14 62.244 

4.238 2.11 1.114 13.91 26.027 61 .365 

4.237 2.103 1.188 13.901 26.074 63.683 

4.235 1.987 1.2 13.911 25.941 64.45 

4.237 1.924 1.13 13.904 26.212 61 .861 

3.312 1.582 1.098 13.903 25.905 64.462 

4.161 2.279 1.008 13.891 26.046 65.092 

4.235 2.628 1.209 13.895 26.1 61 .927 

4.236 2.594 1.173 13.897 26.288 60.888 

4.238 2.628 1.151 13.902 26.465 58.67 

4.233 2.479 1.16 13.912 26.082 61 .884 

4.23 2.436 1.201 13.936 25.914 63.866 

4.227 2.35 1.248 13.943 25.793 66.898 

4.238 2.444 1.189 13.923 26.221 63.329 

4.245 2.65 1.055 13.915 26.599 57.354 

2.301 1.317 0.649 13.94 26.219 58.755 

4.227 2.325 0.971 13.926 26.288 60.434 

4.237 2.297 0.996 13.914 26.599 57.747 

4.236 2.16 0.956 13.937 26.256 58.975 

4.238 2.246 0.977 13.927 26.404 58.708 

4.242 2.174 1.028 13.932 26.257 59.402 

4.241 2.166 1.021 13.947 25.973 63.145 

4.247 2.319 0.915 13.947 25.971 62.726 

4.243 2.247 0.952 13.948 25.995 64.192 

4.252 2.35 0.934 13.938 26.21 61.938 

4.281 2.507 0.867 13.933 26.335 59.075 

2/12/2013 11 :06:00 AM 13.796 4.282 2.43 0.857 13.937 26.351 58.772 

2/12/2013 11 :07:00 AM 13.802 4.278 2.356 0.859 13.935 26.341 58.952 

2/1212013 11 :08:00 AM 4.791 1.311 0.953 4.539 13.928 26.468 57.138 

2112/2013 11 :09:00AM 0.147 0.12 0.021 9.522 13.915 26.679 55.734 

2112/201311 :10:00AM 0.13 0.115 0.013 9.58 13.938 26.538 54.078 

2112/2013 11:11 :00AM ..... :4;::5:::92~_.:;2;:6;::6.;.7_....;0::;0::,1:,......, 7.161 11 .342 12.872 44.482 

2/12/2013 11 :12:00 AMLI_1~0;:0:::2.::.9_..;5::,1:,:7;::6_~0;:0~19::....J -0.105 10.051 0.723 0.607 

2/12/2013 11 :13:00AM 7.852 3.846 0.503 -0.281 5.083 21.913 0.264 

2/12/2013 11: 14:00 AM ..... ::,0 . .;.17:.;6:.....--...:0;;,.1:.;3;::5_....::2,;.; .5;::0.;.1 _....;0 . .:;.00:;,1:.....--...:0::;;.0;:5;::8:.........:,4 7~. 9;1:;:6:.........;0 .:;.3::,81:...., 

2/12/2013 11 :15:00 AM LI_0::, . .;;12:;:9:.....--...:0::,.1:,:2:..:1_-..::2,;: .5:;:03::...._::,0.;:.07:..:2;.....--...:0::;;.0:::3:;:6:.........:,47:..:8::,9:,:1_....::.0.;:;24::;4:....J 

2/1212013 11 :16:00 AM 0.12 0.098 0.702 0.072 1.235 20.862 11 .939 

211 212013 11 : 17:00 AM ..... 0:,:; . .,::1 0;:3:.....--...:0::;;0;:9::;4_....::0,;.;0.:;.09::-_;.0;..06:,::,..._..;.:.0:::03;..._..:;0..;1~7::,9 _....:;2 .,::1 0;;;2:...., 

211212013 11 :18:00 AM LI_0::, . .,::1 0:::3:.....--...:0::;;0:::9:;:5_~0,;:0:;:06::...._::,0 . .:::06:::4:.....--...:0::;;0:::2;.:9_~0..;1:::2:4_....,..::0..;1:..:1.....J 2/1212013 11 :19:00 AM 7.218 3.946 1.598 5.202 6.279 26.154 94.841 

2/12/2013 11 :20:00 AM ,....;1.:;.0:;;.0::4;,2 _....,..::5:.;2;"..._.;2,;.;.5;09::...._:,:;9 . .:;.58;:6:.........:1.:;.0 . .:;.04:;:4;........:,4 7~.9:::7:,:1,.....;2.;.43;.;:82;;8;., 

2/1212013 11 :21 :00 AM 1 10.046 5.199 2.511 9.615 10.052 48.008 243.676 1 

2/12/2013 11:22:00 AM 12.104 1.096 1.393 6.487 11.861 39.235 193.475 

2/12/2013 11:23:00 AM 20.912 0.168 0.027 0.412 14.364 27.363 49.895 

2/12/2013 11 :24:00 AM 20.961 0.157 0.018 0.197 9.882 22.592 51 .528 

2/12/2013 11:25:00AM 20.97 0.153 0.01 0.195 0.077 0.778 215.8 

2/12/201311 :26:00AM 20.007 0.817 0.373 0.191 0.047 0.592 1243.6871 

2/12/201311 :27:00AM 

2/12/2013 11 :28:00 AM 

2/12/2013 11 :29:00 AM 

2/12/2013 11 :30:00 AM 

2/12/2013 11:31 :00AM 

2/1212013 11 :32:00 AM 

2/12/2013 11 :33:00 AM 

2/1212013 11 :34:00 AM 

2112/2013 11 :35:00 AM 

2112/2013 11 :36:00 AM 

2/12/2013 11 :37:00 AM 

14.364 

14.317 

14.307 

14.305 

9.692 

14.184 

14.291 

14.289 

14.287 

14.285 

14.283 

3.939 3.389 0.196 0.032 0.509 244 .608 

3.951 3.195 0.297 7.081 11.882 209.376 

3.955 3 0.312 14.35 26.666 56.289 

3.957 2.965 0.308 14.367 26.717 50.519 

2.693 2.198 0.257 14.366 26.578 50.757 

3.948 2.825 0.256 14.365 26.648 50.798 

3.963 2.877 0.314 14.355 26.751 50.141 

3.97 2.867 0.324 14.342 26.849 49.025 

3.972 2.798 0.3 14.343 26.762 49.755 

3.973 2.798 0.294 14.34 26.742 50.272 

3.979 2.872 0.323 14.339 26.75 49.855 

THC 

PPM 

3.322 

3.143 

3.533 

3.514 

3.242 

3.617 

3.769 

3.019 

3.171 

2.702 

3.076 

3.497 

3.981 

3.418 

2.327 

2.535 

2.937 

2.362 

2.563 

2.634 

2.75 

3.335 

3.345 

3.398 

3.05 

2.697 

2.571 

2.558 

2.281 

2.083 

1.784 

1.855 

-0.011 

-0.011 

-0.011 

-0.011 

6.333 

37.083 

2.014 

2.014 

2.404 

1.922 

1.007 

0.718 

0.429 

-0.001 

0.001 

o 

0.074 

1.251 

1.348 

1.313 

1.329 

1.221 

1.028 

1.085 

1.159 

1.049 

CO bias 

02/C02 bias 

NOx bias 

Direct Zero 

Direct Span 

CO bias 
Date Time 

0, 

% 

2/12/201311:38:00AM 14.284 

211212013 11 :39:00 AM 14.283 

2/12/201311 :40:00AM 14.283 

2/12/2013 11 :41:00 AM 14.284 

2/12/2013 11 :42:00 AM 14.275 

2/12/201311 :43:00AM 14.271 

2/1212013 11:44:00 AM 14.282 

2/1212013 11 :45:00AM 14.278 

2/12/2013 11 :46:00AM 14.268 

2/12/2013 11 :47:00 AM 

2/12/2013 11:48:00 AM 

2/12/201311 :49:00AM 

211212013 11 :50:00 AM 

2/12/2013 11 :51 :00 AM 

2/12/2013 11 :52:00 AM 

2/1212013 11 :53:00 AM 

211212013 11 :54:00 AM 

2/12/2013 11 :55:00AM 

2112/2013 11 :56:00AM 

2/12/2013 11 :57:00AM 

2/12/2013 11 :58:00 AM 

2/12/2013 11:59:00AM 

2112/2013 12:00:00 PM 

2/12/2013 12:01 :00 PM 

2/12/2013 12:02:00 PM 

2/12/2013 12:03:00 PM 

2/12/2013 12:04:00 PM 

2/12/2013 12:05:00 PM 

2/1212013 12:06:00 PM 

2/1212013 12:07:00 PM 

2/12/2013 12:08:00 PM 

2/12/2013 12:09:00 PM 

2/12/2013 12:10:00 PM 

2112/2013 12:11 :00 PM 

211212013 12:12:00 PM 

211212013 12: 13:00 PM 

2/12/2013 12:14:00 PM 

2/1212013 12:15:00 PM 

2/12/2013 12:16:00 PM 

211212013 12:17:00 PM 

211212013 12:18:00 PM 

2/12/2013 12:19:00 PM 

2/12/2013 12:20:00 PM 

2112/2013 12:21:00 PM 

2/12/2013 12:22:00 PM 

211212013 12:23:00 PM 

2112/2013 12:24:00 PM 

2/12/2013 12:25:00 PM 

2/12/2013 12:26:00 PM 

2/1212013 12:27:00 PM 

2112/2013 12:28:00 PM 

2112/2013 12:29:00 PM 

2/12/2013 12:30:00 PM 

2/12/2013 12:31:00 PM 

2/12/2013 12:32:00 PM 

2/1212013 12:33:00 PM 

2/1212013 12:34:00 PM 

211212013 12:35:00 PM 

2/12/2013 12:36:00 PM 

14.285 

14.278 

14.268 

14.265 

14.255 

14.244 

14.257 

14.275 

14.27 

14.266 

14.267 

14.27 

14.269 

14.268 

14.27 

14.283 

14.279 

14.277 

14.242 

14.263 

14.263 

14.246 

14.241 

14.204 

14.204 

14.204 

14.198 

14.197 

16.57 

14.612 

14.286 

14.285 

14.277 

14.278 

14.268 

14.274 

14.271 

14.266 

14.265 

14.264 

14.268 

14.266 

14.259 

14.264 

14.261 

14.262 

16.207 

14.249 

14.241 

14.252 

co, 

% 

3.979 

3.982 

3.98 

3.983 

3.988 

3.983 

3.983 

3.983 

3.977 

3.977 

3.987 

3.991 

3.997 

3.999 

3.996 

3.994 

3.997 

3.999 

4.001 

4.002 

4.001 

4.003 

4.002 

4.001 

3.994 

3.998 

4 

4.017 

4.005 

4.007 

4.015 

4.021 

4.047 

4.048 

4.05 

4.049 

4.052 

2.571 

3.927 

3.995 

3.994 

3.997 

3.995 

3.999 

3.996 

3.996 

3.994 

3.993 

3.991 

3.988 

3.989 

3.992 

3.989 

3.99 

3.989 

2.874 

3.996 

3.999 

3.993 

NO, 

PPM 

2.728 

2.854 

2.799 

2.69 

2.714 

2.595 

2.741 

2.718 

2.677 

2.571 

2.732 

2.715 

2.623 

2.496 

2:422 

1.961 

1.669 

1.682 

1.771 

1.665 

1.658 

1.739 

1.765 

1.705 

1.683 

1.818 

1.785 

2.245 

2.268 

2.255 

2.32 

2.111 

2.246 

2.178 

2.273 

2.293 

2:402 

1.696 

1.664 

1.871 

1.87 

1.888 

1.932 

2.004 

1.841 

1.851 

1.812 

1.914 

1.825 

1.849 

1.886 

1.788 

1.798 

1.897 

1.901 

1.773 

2.665 

2.798 

2.637 

CO 

PPM 

0.319 

0.319 

0.341 

0.31 

0.332 

0.317 

0.313 

0.295 

0.323 

0.344 

0.316 

0.301 

0.317 

0.34 

0.339 

0.344 

0.355 

0.334 

0.325 

0.325 

0.307 

0.345 

0.329 

0.35 

0.353 

0.362 

0.344 

0.288 

0.263 

0.235 

0.237 

0.231 

0.308 

0.336 

0.365 

0.334 

0.327 

0.311 

0.386 

0.508 

0.553 

0.535 

0.556 

0.542 

0.542 

0.567 

0.564 

0.525 

0.577 

0.537 

0.579 

0.517 

0.542 

0.528 

0.527 

0.323 

0.375 

0.385 

0:407 

0, 

% 

14.338 

14.337 

14.32 

14.327 

14.338 

NO, 

PPM 

CO 

PPM 

26.682 50.816 

26.742 51 .17 

26.944 49.922 

27.04 49.207 

26.987 48.638 

14.338 26.98 49.501 

14.345 26.899 49.171 

14.354 26.775 50.425 

14.351 26.557 52 .259 

14.34 

14.343 

14.343 

14.331 

14.328 

14.337 

14.332 

14.329 

14.325 

14.318 

14.319 

14.322 

14.323 

14.337 

14.338 

14.34 

14.342 

14.34 

14.343 

14.343 

14.342 

14.342 

14.343 

14.344 

14.347 

14.345 

14.342 

14.342 

14.342 

14.335 

14.338 

14.332 

14.319 

14.318 

14.317 

14.317 

14.317 

14.317 

14.317 

14.317 

14.318 

14.317 

14.317 

14.317 

14.317 

14.317 

14.317 

14.318 

14.317 

14.317 

27.017 

27.014 

26.94 

27.051 

26.771 

26.761 

26.89 

26.863 

26.972 

27.002 

26.963 

26.72 

26.852 

26.781 

26.731 

26.731 

26.562 

26.692 

26:497 

26.678 

27.012 

27.046 

26.859 

26.806 

26.595 

26.713 

26.821 

27.055 

26.809 

26.802 

26:468 

26:463 

26:47 

26:404 

26.414 

26.364 

26.391 

26.392 

26.347 

26.212 

26.164 

26.353 

26.195 

26.235 

26.354 

26:411 

26.45 1 

26.577 

26.388 

26.327 

50.391 

48:441 

49.573 

48.967 

50.394 

50.797 

50.136 

50.251 

49.865 

48.907 

49:456 

50.876 

50.558 

50.621 

51.083 

51.714 

51.892 

51.607 

53.01 

51 .98 

49.591 

48:418 

49.444 

49.908 

51 .292 

51 .26 

50.506 

49.354 

50.867 

50.977 

52.756 

53.195 

52.917 

53.891 

53.217 

53.887 

53.529 

54.084 

53.774 

54.987 

55.822 

54.852 

55.237 

55.727 

54:492 

53.839 

53.268 

52.627 

53.085 

54.767 

THe 

PPM 

1.153 

1.284 

1.141 

1.136 

1.031 

1.122 

1.155 

1.285 Start PM 50% 

1.45 

1.152 

1.047 

0.979 

1.016 

1.371 

1.365 

1.321 

1.089 

1.14 

1.121 

1.193 

1.307 

1.33 

1.263 

1.238 

1.3 

1.469 

1:44 

1.535 

1.524 

1.124 

0.968 

1.172 

1.249 

1.322 

1.337 

1.156 

0.914 

1.204 

1.229 

1.485 

1.665 

1.59 

1.62 

1.591 

1.697 

1.623 

1.628 

1.587 

1.753 

1.678 

1.568 

1.738 

1.864 

1.713 

1.541 

1.47 

1.38 

1.434 

1.648 

Start 50% Compliance 1 
Date Time 

0 , 

% 

CO, 

% 

NO, CO 0, NO, CO THC 

PPM PPM % PPM PPM PPM 

2/12/2013 12:37:00 PM 14.238 4 2.947 0.388 14.317 26.499 53.048 1.419 

2/12/2013 12:38:00 PM 14.242 3.999 2.776 0.369 14.317 26.25 55.11 1.613 

2/12/2013 12:39:00 PM 14.251 3.995 2.698 0.373 14.317 26.181 56.07 1.763 

2/12/2013 12:40:00 PM 14.23 4.007 3.103 0.349 14.317 26.496 53.822 1.467 

2/12/2013 12:41 :00 PM 14.207 4.018 3.322 0.266 14.335 26.251 54.292 1.586 

2/12/2013 12:42:00 PM 14.257 3.991 3.063 0.263 14.34 26.086 56.39 1.927 

2/12/2013 12:43:00 PM 14.259 3.994 3.034 0.274 14.335 26.36 55.162 1.797 

2/12/2013 12:44:00 PM 14.255 3.995 2.952 0.267 14.34 26.237 54.94 1.638 

2/12/2013 12:45:00 PM 14.255 3.996 2.991 0.275 14.341 26.189 55.55 1.788 

2/12/2013 12.46:00 PM 14.191 4.035 3.004 0.379 14.338 26.382 54.88 1.724 

2/12/2013 12:47:00 PM 14.176 4.041 3.117 0.354 14.332 26.491 52.693 1.402 

2/12/2013 12:48:00 PM 14.18 4.04 2.916 0.35 14.333 26.385 53.528 1.449 

2/12/2013 12:49:00 PM 14.19 4.033 2.804 0.344 14.33 26.396 53.554 1.544 

2112/2013 12:50:00 PM 14.195 4.032 2.774 0.374 14.339 26.189 55.243 1.779 

2112/2013 12:51 :00 PM 16.756 2.556 1.759 0.316 14.336 26.201 55.021 1.711 

2112/2013 12:52:00 PM 14.308 3.972 2.875 0.523 14.339 25.998 57.214 2.024 

2/12/2013 12:53:00 PM 14.286 3.981 3.228 0.542 14.337 26.219 55.276 1.757 

2/12/2013 12:54:00 PM 14.288 3.978 3.192 0.553 14.342 26.084 56.717 1.931 

2/12/2013 12:55:00 PM 14.283 3.982 3.13 0.543 14.338 26.251 54.649 1.57 

2/1212013 12:56:00 PM 14.277 3.983 3.101 0.535 14.339 26.522 53.049 1.483 

2/12/2013 12:57:00 PM 14.277 3.984 3.022 0.507 14.341 26.367 53.619 1.531 

2/1212013 12:58:00 PM 14.28 3.983 2.907 0.549 14.341 26.271 53.949 1.637 

211212013 12:59:00 PM 14.286 3.978 2.648 0.526 14.339 26 .428 53.688 1.548 

2/1212013 1 :00:00 PM 14.282 3.982 2.817 0.524 14.337 26.399 53.634 1.496 

2/12/2013 1:01 :00 PM 14.279 3.983 2.696 0.503 14.328 26.661 51 .413 1.258 

2/12/2013 1:02:00 PM 14.279 3.983 2.561 0.533 14.332 26.628 51.871 1.185 

2/12/2013 1:03:00 PM 14.264 3.992 2.571 0.492 14.326 26.803 50.053 1.01 

2/12/2013 1004:00 PM 14.262 3.991 2.506 0.479 14.321 26.921 49.355 0.815 

2/12/2013 1005:00 PM 14.257 3.995 2.449 0.456 14.317 26.912 48.919 0.935 

2/12/2013 1:06:00 PM 14.259 3.992 2.333 0.492 14.317 26.901 49.249 0.933 

2/1212013 1:07:00 PM 14.256 3.996 2.403 0.467 14.317 27.027 48.319 0.791 

2/12/2013 1008:00 PM 14.25 3.999 2.311 0.446 14.317 27.244 46.977 0.599 

2/12/2013 1:09:00 PM 19.845 0.675 0.506 0.268 4.477 10.186 32.451 18.167 

2/12/2013 1010:00 PM 20.934 0.185 0.027 0.187 0.06 0.666 0.585 45.229 

2/12/2013 1:11:00 PM 20.943 0.177 0.023 0.197 0.048 0.561 0.173 46.105 ITHC Mid 

2/12/2013 1:12:00 PM 10.229 0.185 0.041 2.444 0.123 0.661 31 .525 42.45 

2/12/2013 1:13:00 PM 0.183 0.13 0.009 9.378 0.033 0.446 233.266 1.07 

2/1212013 1:14:00 PM 0.154 0.127 0.012 9.582 0.033 0.398 1 243.2551 0 CO bias 

2112/2013 1:15:00 PM 1.771 1.162 0.012 9.076 6.204 0.835 177.872 -0.004 

2112/2013 1016:00 PM 9.93 5.171 0.013 0.852 9.948 0.336 3.329 -0.012 

2/12/2013 1:17:00 PM 1 9.996 5.196 0.017 -0.309 9.949 0.304 -0.106 -0.012 02/C02 bias 

2112/2013 1:18:00 PM 9.996 5.204 0.01 -0.308 L..-=7;.;: .1.,:.98:;-.....,1;;;0.:,.1;;;3;,.1 oJ -0.085 -0.012 

2/12/2013 1:19:00 PM 3.736 1.814 1.491 -0.194 0.065 47.3 0.221 -0.012 

2/12/2013 1 :20:00 PM LI....::;o;,; . 1;44:....._~0~14;:6;..-_!.2;49'=-_..:0;;0~5;..-_;.0:;::.0:,:3:----;4.:,.7 .::;4,:,:75;..-.....:0:;: .2;,:,7""5 __ -:;0~0:.:.12;,..JINOX bias; THC Zero 

2/12/2013 1:21 :00 PM 0.121 0.115 1.075 0.07 0.031 26.999 0.23 -0.011 

2/12/2013 1:22:00 PM 0.103 0.105 0.015 0.061 0.029 0.151 0.115 1.092 

2/1212013 1 :23:00 PM LI...::;o.;,;:l 0::3:........:0::;, ..:,:1 0;,;:5....:.....:0:;:.0;,;:0::,8 _...::;0.;:;06::;2,--_;:;0.;:;0;:,3 _.....:0:;.1~0::.4_...:::0;.,: . 1.;.17:.....J 

2/1212013 1:24 :00 PM 6.967 3.798 1.513 3.599 5.739 23.36 31 .707 

2/12/2013 1:25:00 PM ..... 1:,:0:;:.0::..1:,:2;,......,::5:;: .2;.,:1.,:.1_....::2;;;.5;;0::;3_.....:9:;;.4;.:8:::9....:_.,.1::;0:,.,.._..;:4.;.7;.,:.7.;8.::.9_.;;2;:;34;.;61;.:9:..., 

2/12/2013 1 :26:00 PM LI_l.:,:0:;;.0;::2;.,:1_...::;5.:,21.:,:3:........:2;;:.5;::0;,;:5_.....::9,;;: .5;,;:8,:.1 __ 1~0,;;:.0;,;:0.;.1_..;:4,:.7.;,;:8:;:23:......:2~4.::3;.;.7.:,82;..J1 

2/12/2013 1:27:00 PM 7.021 3.19 2.494 8.648 10.778 45.557 233.318 

2/12/2013 1:28:00 PM 14.133 3.95 2.218 1.081 14.304 26.498 72.186 

2/1212013 1:29:00 PM 14.218 3.996 1.831 0.384 14.316 26.402 52.384 

2112/2013 1:30:00 PM 14.219 3.997 1.835 0.363 14.316 26.655 51.483 

2/12/2013 1:31 :00 PM 14.213 3.999 2.009 0.34 14.316 26.433 51.774 

2/1212013 1:32:00 PM 14.227 3.992 1.816 0.378 14.316 26.52 52.101 

2112/2013 1:33:00 PM 14.214 3.997 1.974 0.36 14.316 26.826 50.003 

2/12/2013 1:34:00 PM 14.208 4.001 2.014 0.291 14.316 26.829 49.395 

1.487 

1.396 

1.126 

1.185 

1.218 

1.27 

1.457 

1.3 

1.327 

1.41 

1.059 

0.828 

Direct Zero 

Direct Span 

Start Compliance 2 
Date Time 

2112/2013 1 :35:00 PM 

2112/2013 1 :36:00 PM 

2/12/2013 1 :37:00 PM 

2/1212013 1 :38:00 PM 

2112/2013 1 :39:00 PM 

2/12/2013 1:40:00 PM 

2/12/2013 1 :41 :00 PM 

2/12/2013 1 :42:00 PM 

2/12/2013 1 :43:00 PM 

2/12/2013 1 :44:00 PM 

2/12/2013 1 :45:00 PM 

2/12/2013 1 :46:00 PM 

2/12/2013 1:47:00PM 

2/12/2013 1 :48:00 PM 

2/12/2013 1 :49:00 PM 

211212013 1:50:00 PM 

2112/2013 1:51:00 PM 

2112/2013 1:52:00 PM 

2112/2013 1:53:00 PM 

2/12/2013 1:54:00 PM 

2/12/2013 1:55:00 PM 

2/12/2013 1:56:00 PM 

2/12/2013 1:57:00 PM 

2/12/2013 1:58:00 PM 

2/12/2013 1:59:00 PM 

2/12/2013 2:00:00 PM 

2/12/2013 2:01 :00 PM 

2/12/2013 2:02:00 PM 

2/12/2013 2:03:00 PM 

2/12/2013 2:04:00 PM 

2/12/2013 2:05:00 PM 

2/12/2013 2:06:00 PM 

2112/2013 2:07:00 PM 

2112/2013 2:08:00 PM 

2/1212013 2:09:00 PM 

2/1212013 2:10:00 PM 

2/1212013 2:11:00 PM 

2/1212013 2:12:00 PM 

2/12/2013 2:13:00 PM 

2/12/2013 2:14:00 PM 

2/12/2013 2:15:00 PM 

2/12/2013 2:16:00 PM 

2/12/2013 2:17:00 PM 

2/12/2013 2:18:00 PM 

2/12/2013 2:19:00 PM 

2/12/2013 2:20:00 PM 

2/12/2013 2:21 :00 PM 

2/12/2013 2:22:00 PM 

2/12/2013 2:23:00 PM 

2/12/2013 2:24:00 PM 

2112/2013 2:25:00 PM 

2112/2013 2:26:00 PM 

2112/2013 2:27:00 PM 

211212013 2:28:00 PM 

2/1212013 2:29:00 PM 

2/12/2013 2:30:00 PM 

2/12/2013 2:31 :00 PM 

2/1212013 2:32:00 PM 

2/12/2013 2:33:00 PM 

0, 

% 

14.221 

14.229 

14.201 

14.205 

14.203 

14.202 

14.203 

14.171 

14.162 

14.171 

14.171 

14.168 

17.642 

14.429 

14.259 

14.25 

14.252 

14.251 

14.239 

14.25 

14.235 

14.232 

14.232 

14.228 

14.226 

14.233 

14.231 

14.224 

14.217 

14.212 

19.004 

14.302 

14.203 

14.203 

14.2 

14.203 

14.203 

14.203 

14.201 

14.203 

14.203 

14.203 

14.197 

14.2 

14.203 

14.203 

14.199 

14.196 

16.858 

14.724 

14.226 

14.227 

14.225 

14.224 

14.216 

14.224 

14.225 

14.232 

14.237 

co, 

% 

3.997 

3.995 

4.016 

4.01 

4.015 

4.016 

4.018 

4.037 

4.038 

4.033 

4.036 

4.039 

1.97 

3.963 

3.988 

3.995 

3.995 

3.996 

4.003 

3.999 

4.007 

4.008 

4.009 

4.014 

4.016 

4.012 

4.014 

4.018 

4.022 

4.025 

1.238 

4.022 

4.037 

4.036 

4.041 

4.038 

4.041 

4.042 

4.045 

4.041 

4.041 

4.045 

4.048 

4.049 

4.047 

4.047 

4.051 

4.052 

2.388 

3.873 

4.03 

4.028 

4.031 

4.035 

4.035 

4.032 

4.032 

4.028 

4.027 

NO, 

PPM 

1.971 

1.775 

2.35 

2.228 

2.263 

2.368 

2.372 

2.418 

2.466 

2.312 

2.482 

2.541 

1.216 

1.833 

1.919 

2.075 

1.993 

1.896 

2.07 

1.941 

2.009 

1.797 

1.653 

1.72 

1.727 

1.665 

1.721 

1.663 

1.708 

1.675 

0.52 

2.217 

2.374 

2.308 

2.347 

2.304 

2.394 

2.401 

2.366 

2.013 

1.927 

1.969 

2.049 

1.871 

1.798 

1.97 

2.028 

2.103 

1.307 

1.734 

2.027 

1.941 

1.908 

1.934 

2.008 

2.044 

2.07 

2.082 

2.182 

CO 

PPM 

0.352 

0.374 

0.288 

0.252 

0.25 

0.24 

0.235 

0.249 

0.292 

0.299 

0.329 

0.318 

0.494 

0.568 

0.73 

0.705 

0.686 

0.632 

0.573 

0.588 

0.549 

0.527 

0.509 

0.484 

0.502 

0.526 

0.494 

0.495 

0.479 

0.439 

0.286 

0.399 

0.525 

0.559 

0.544 

0.561 

0.595 

0.541 

0.513 

0.559 

0.53 

0.534 

0.558 

0.514 

0.503 

0.533 

0.49 

0.518 

0.412 

0.367 

0.506 

0.538 

0.496 

0.492 

0.501 

0.516 

0.51 

0.518 

0.563 

0, 

% 

14.316 

14.317 

14.32 

14.322 

14.327 

14.332 

14.331 

14.339 

14.342 

14.341 

14.342 

14.343 

14.342 

14.342 

14.34 

14.342 

14.34 

14.33 

14.331 

14.32 

14.317 

14.317 

14.316 

14.316 

14.316 

14.316 

14.315 

14.316 

14.314 

14.307 

14.302 

14.315 

14.316 

14.315 

14.317 

14.317 

14.317 

14.315 

14.317 

14.316 

14.314 

14.306 

14.3 

14.309 

14.311 

14.311 

14.297 

14.296 

14.296 

14.3 

14.297 

14.298 

14.292 

14.291 

14.296 

14.293 

14.294 

14.314 

14.314 

NO, 

PPM 

26.565 

26.252 

26.433 

26.508 

26.534 

26.539 

26.599 

26.591 

26.309 

26.276 

26.361 

26.191 

26.275 

26.369 

26.484 

26.413 

26.459 

26.618 

26.664 

26.834 

27.021 

27.104 

27.181 

27.242 

27.032 

27.064 

26.918 

27.133 

27.281 

27.276 

27.341 

27.086 

26.966 

26.92 

26.778 

26.732 

26.819 

26.965 

26.832 

26.814 

26.859 

26.78 

26.994 

26.945 

26.875 

26.838 

26.944 

27.027 

26.885 

26.862 

26.896 

26.799 

26.952 

27.019 

26.843 

26.899 

27.036 

26.783 

26.664 

CO 

PPM 

50.932 

54.499 

53.395 

52.933 

52.248 

52.69 

51.821 

51.725 

53.934 

54.979 

53.97 

55.576 

54.932 

53.833 

53.72 

53.267 

53.09 

52.512 

51 .148 

50.689 

48.737 

47.989 

47.472 

46.738 

47.75 

48.423 

49.046 

47.779 

46.688 

47.046 

46.179 

47.782 

49.11 4 

49.886 

50.266 

51 .159 

50.565 

49.802 

49.73 

50.224 

49.818 

50.526 

49.109 

48.684 

49.839 

49.709 

49.17 

48.332 

49.782 

49.586 

49.659 

50.309 

49.718 

48.931 

49.592 

49.881 

49.03 

50.338 

51.466 

THe 

PPM 

1.116 

1.57 

1.542 

1.285 

1.235 

1.249 

1.021 

1.008 

1.439 

1.644 

1.467 

1.72 

1.638 

1.577 

1.804 

1.608 

1.473 

1.29 

1.109 

1.049 

0.868 

0.788 

0.759 

0.585 

0.731 

0.931 

0.945 

0.724 

0.696 

0.6 

0.46 

0.616 

0.871 

0.999 

1.131 

1.162 

1.03 

0.894 

0.949 

0.934 

0.952 

1.073 

0.832 

0.782 

0.909 

0.921 

0.869 

0.752 

1.066 

1.037 

0.961 

0.915 

0.979 

0.851 

0.866 

0.911 

0.766 

1.078 

1.151 
0, CO, NO, CO 0, NO, CO THe 

Date Time % % PPM PPM % PPM PPM PPM 

211212013 2:34:00 PM 14.234 4.029 2.178 0.566 14.304 26.845 50.625 0.945 

211212013 2:35:00 PM 14.229 4.032 2.275 0.553 14.294 27.011 49.689 0.874 

211212013 2:36:00 PM 14.225 4.033 2.233 0.531 14.305 26.887 50.163 0.85 

211212013 2:37:00 PM 14.232 4.029 2.279 0.511 14.314 26.765 50.8 0.95 

211212013 2:38:00PM 14.234 4.027 2.236 0.544 14.314 26.664 52.528 1.148 

211212013 2:39:00 PM 14.236 4.027 2.343 0.546 14.314 26.673 52.979 1.351 

211212013 2:40:00 PM 14.233 4.028 2.288 0.524 12.948 23.666 50.778 1.054 

211212013 2:41 :00PM 11.032 4.475 1.113 0.265 9.977 0.906 7.75 -0.009 

211212013 2:42:00 PM '"1-9""."99"'5:-:-5"'.2"'4"'3---:0"'.0"'2"'5"" -0.27 9.971 0.642 -0.196 -0.014 021e02 bias 

211212013 2:43:00 PM '-9~.~46;"7;-:-4~.8:::6~7---;O:;.0:;;6:;'8"" -0.305 4.56 22.194 0.155 -0.014 

211212013 2:44:00 PM 0.353 0.213 2.424 -0.061 0.054 47.522 0.263 -0.014 

211212013 2:45:00 PM '"I ~0;;1;;39;;"""-';:0;';1;';7;;6-"""'"2;;'4~9;';6---:0;';.04;;;"3~--:O;;'0:;;3;':4-"";4;'7;;.5,:;9;;....-0"';;28:;;8~ -0.014 NOx bias 

211212013 2:46:00PM 0.126 0.168 2.502 0.046 0.031 36.211 13.629 -0.013 

211212013 2:47:00 PM 0.126 0.164 0.894 4.332 0.029 0.596 220.739 -0.004 

211212013 2:48:00 PM 0.125 0.16 0.011 9.487 0.03 0.423 243.372 -0.002 

211212013 2:49:00 PM 0.126 0.158 0.006 9.585 0.029 0.361 243.5051 -0.003 leo bias 

211212013 2:50:00 PM 8.246 4.51 1.795 9.586 7.002 1.667 239.683 0.193 

211212013 2:51 :00 PM 1 9.995 5.245 2.495 9.599 10.003 2.526 243.418 1 0.965 Direct Span 

211212013 2:52:00 PM 2.261 1.17 0.844 5.912 4.618 1.5 178.702 0.968 

211212013 2:53:00 PM 0.101 0.134 0.005 0.15 0.028 0.102 2.45 

211212013 2:54:00 PM "1-0:':'~1 0~1~--:0"1;':3"'3---:-0~0~0~1--i0.-::05:':3;---:0"0:;;2~7"""--;O:';0:;;8::-8 --i0":1~09::-11 

211212013 2:55:00 PM 

211212013 2:56:00 PM 

211212013 2:57:00 PM 

211212013 2:58:00 PM 

211212013 2:59:00 PM 

0.151 

8.471 

20.66 

20.778 

20.835 

211212013 3:00:00 PM 18.695 

211212013 3:01:00 PM 14.257 

211212013 3:02:00 PM 14.241 

211212013 3:03:00 PM 14.24 

211212013 3:04:00 PM 14.234 

211212013 3:05:00 PM 14.23 

211212013 3:06:00 PM 14.224 

211212013 3:07:00 PM 

211212013 3:08:00 PM 

211212013 3:09:00 PM 

211212013 3:10:00 PM 

211212013 3:11 :00 PM 

211212013 3:12:00 PM 

211212013 3:13:00 PM 

211212013 3:14:00 PM 

211212013 3:15:00 PM 

211212013 3:16:00 PM 

211212013 3:17:00 PM 

211212013 3:18:00 PM 

211212013 3:19:00 PM 

211212013 3:20:00 PM 

211212013 3:21 :00 PM 

211212013 3:22:00 PM 

211212013 3:23:00 PM 

211212013 3:24:00 PM 

211212013 3:25:00 PM 

211212013 3:26:00 PM 

211212013 3:27:00 PM 

211212013 3:28:00 PM 

211212013 3:29:00 PM 

211212013 3:30:00 PM 

211212013 3:31 :00PM 

14.228 

14.225 

14.223 

14.208 

14.213 

14.22 

14.212 

14.222 

14.225 

14.23 

14.229 

14.233 

14.227 

14.223 

14.216 

14.216 

14.21 

14.207 

14.207 

14.213 

14.219 

14.222 

14.217 

14.218 

14.221 

0.164 0 1.597 5.57 5.15 

0.198 1.194 7.239 18.96 24 .701 

0.221 4.756 7.558 19.008 24.296 

0.209 19.009 24.302 

0.209 18.992 38.164 

1.6 

4.007 

4.012 

4.017 

4.02 

4.019 

4.024 

4.025 

4.026 

4.027 

4.032 

4.03 

4.025 

4.028 

4.028 

4.026 

4.023 

4.026 

4.023 

4.027 

4.028 

4.032 

4.031 

4.032 

4.031 

4.03 

4.028 

4.025 

4.025 

4.03 

4.029 

4.027 

0.585 

2.151 

2.04 

2.107 

2.114 

2.182 

2.219 

2.149 

2.122 

2.149 

2.213 

2.086 

1.896 

1.957 

1.977 

1.926 

1.966 

1.97 

1.968 

1.982 

1.987 

2.032 

2.011 

2.026 

2.009 

2.023 

2.015 

2.063 

1.992 

2.162 

2.102 

2.112 

3.517 

1.12 

0.481 

0.395 

0.405 

0.377 

0.354 

0.351 

0.387 

0.37 

0.372 

0.369 

0.377 

0.357 

0.369 

0.361 

0.372 

0.384 

0.36 

0.33 

0.336 

0.369 

0.348 

0.347 

0.341 

0.357 

0.346 

0.387 

0.364 

0.328 

0.354 

0.349 

18.983 47.473 

18.963 47.859 

18.959 11 .286 

18.952 0.362 

18.952 0.293 

18.942 0.267 

18.933 0.253 

18.916 

18.91 

18.909 

18.896 

18.907 

18.895 

18.895 

18.887 

18.885 

18.885 

18.885 

18.885 

18.885 

18.882 

18.87 

18.866 

18.86 

18.859 

18.843 

18.835 

18.835 

18.836 

18.837 

18.835 

18.834 

0.241 

0.236 

0.232 

0.227 

0.212 

0.201 

0.199 

0.19 

0.192 

0.18 

0.178 

0.18 

0.181 

0.177 

0.174 

0.176 

0.165 

0.165 

0.157 

0.156 

0.156 

0.155 

0.157 

0.155 

0.154 

0.746 

123.117 

135.434 

139.779 

118.696 

27.177 

4.879 

1.384 

0.845 

0.718 

0.715 

0.715 

0.669 

0.719 

0.719 

0.691 

0.694 

0.669 

0.669 

0.646 

0.619 

0.619 

0.615 

0.569 

0.57 

0.573 

0.593 

0.595 

0.57 

0.572 

0.597 

0.575 

0.573 

0.573 

0.578 

0.574 

0.569 

0.846 

0.758 

0.96 

1.1 

1.115 

1.014 

1.326 

1.466 

Direct Zero 

NOxl02 High, CO Mid 

CO Mid 

1.295 NOx Direct 

1.704 

1.611 

1.526 

1.115 

1.285 

1.46 

1.274 

0.793 

0.407 

0.407 

0.407 

DA08 

DA08 

DA08 

0.407 

0.407 

0.407 

0.407 

0.407 

0.408 

0.408 

0.407 

0.407 

0.407 

0.407 

DA08 

DA08 

DA08 

DA08 

DA08 
Date Time 

2/12/2013 3:32:00 PM 

2/12/2013 3:33:00 PM 

2112/2013 3:34:00 PM 

2/12/2013 3:35:00 PM 

2/12/2013 3:36:00 PM 

2/12/2013 3:37:00 PM 

2/12/2013 3:38:00 PM 

2/12/2013 3:39:00 PM 

2/12/2013 3:40:00 PM 

2/12/2013 3:41 :00 PM 

2/12/2013 3:42:00 PM 

2/12/2013 3:43:00 PM 

2/12/2013 3:44:00 PM 

2/12/2013 3:45:00 PM 

2/12/2013 3:46:00 PM 

2/1212013 3:47:00 PM 

2/1212013 3:48:00 PM 

2/12/2013 3:49:00 PM 

2/12/2013 3:50:00 PM 

2/12/2013 3:51:00 PM 

2/1212013 3:52:00 PM 

2/12/2013 3:53:00 PM 

2/12/2013 3:54:00 PM 

2/12/2013 3:55:00 PM 

2/12/2013 3:56:00 PM 

2/12/2013 3:57:00 PM 

2/12/2013 3:58:00 PM 

2/12/2013 3:59:00 PM 

2/12/2013 4:00:00 PM 

2/12/2013 4:01 :00 PM 

2/12/2013 4:02:00 PM 

2/12/2013 4:03:00 PM 

2/12/2013 4:04:00 PM 

2/1212013 4:05:00 PM 

2/12/2013 4:06:00 PM 

2/12/2013 4:07:00 PM 

2/12/2013 4:08:00 PM 

2/12/2013 4:09:00 PM 

2/12/2013 4:10:00 PM 

2/12/2013 4:11 :00 PM 

2/12/2013 4:12:00 PM 

2/12/2013 4:13:00 PM 

2112/2013 4:14:00 PM 

2/12/2013 4:15:00 PM 

2/12/2013 4:16:00 PM 

2/12/2013 4:17:00 PM 

2/1212013 4:18:00 PM 

2/12/2013 4:19:00 PM 

2/12/2013 4:20:00 PM 

2/12/2013 4:21:00 PM 

2/12/2013 4:22:00 PM 

2/12/2013 4:23:00 PM 

2/12/2013 4:24:00 PM 

2112/2013 4:25:00 PM 

2/12/2013 4:26:00 PM 

2/12/2013 4:27:00 PM 

2/12/2013 4:28:00 PM 

2/12/2013 4:29:00 PM 

0, 

% 

CO, 

% 

NO, 

PPM 

14.229 4.024 2.077 

14.225 4.026 2.125 

14.225 4.026 2.153 

14.23 4.025 2.208 

14.229 4.024 2.12 

14.217 4.031 2.232 

14.218 4.033 2.241 

14.238 4.023 2.107 

14.237 4.023 2.238 

14.24 4.022 2.123 

14.237 4.025 2.03 

14.224 4.028 2.123 

14.232 4.025 2.026 

14.236 4.022 2.123 

14.232 4.026 2.204 

14.23 4.027 2.158 

11 .687 4.287 1.213 

10.019 5.229 0.025 

10.019 5.235 0.021 

10.019 5.239 0.027 

6.433 3.212 0.028 

0.164 0.182 0.019 

0.127 0.167 0.017 

3.699 1.094 0.834 

0.105 0.132 0.022 

7.46 4.079 0.016 

10. 038 1-;5.;:;24;;6;........;0;0:;:2~3:...J 

18.123 ..... ;9.:;4:;:92;:..........;0;.;01:.,:7...., 

19.008 1-.::.9.;::6::;62::..........;0::;.::;01:;:4:...J 

20.006 7.187 0.024 

20.952 5.157 0.015 

20.953 0.646 0.019 

20.953 0.192 0.015 

20.952 0.193 0.014 

20.875 0.213 0.023 

20.785 0.228 0.054 

20.765 0.23 0.074 

20.756 0.235 0.052 

20.741 0.235 0.05 

20.736 0.234 0.042 

20.722 0.234 0.047 

20.711 0.237 0.047 

20.698 0.243 0.057 

20.683 0.249 0.053 

20.681 0.259 0.059 

20.672 0.27 0.059 

20.657 0.283 0.052 

20.646 0.296 0.052 

20.642 0.311 0.046 

20.641 0.327 0.047 

20.637 0.342 0.047 

20.631 0.357 0.048 

20.618 0.375 0.046 

20.607 0.39 0.041 

20.606 0.406 0.047 

20.598 0.422 0.053 

20.592 0.437 0.047 

20.588 0.452 0.043 

CO 

PPM 

0.382 

0.38 

0.365 

0.373 

0.38 

0.356 

0.344 

0.389 

0.404 

0.409 

0.402 

0.358 

0.381 

0.369 

0.372 

0.368 

0.784 

-0.21 

-0.299 

-0.306 

-0.27 

0.019 

0.058 

0.118 

0.192 

0.192 

0.199 

0.201 

0.199 

0.196 

0.192 

0.206 

0.199 

0.196 

0.212 

0.206 

0.219 

0.207 

0.201 

0.194 

0.195 

0.202 

0.206 

0.207 

0.218 

0.217 

0.224 

0.212 

0.215 

0.207 

0.215 

0.215 

0.219 

0.225 

0.216 

0.224 

0.215 

0.228 

0, 

% 

18.834 

18.834 

18.834 

18.834 

18.834 

18.834 

18.834 

18.835 

18.835 

18.83 

18.809 

18.809 

18.803 

18.8 

18.784 

18.784 

18.784 

18.781 

18.78 

18.782 

18.781 

18.782 

18.781 

18.783 

18.771 

18.763 

18.76 

18.755 

18.756 

18.738 

18.733 

18.733 

18.733 

18.733 

18.733 

18.73 

18.715 

18.709 

18.71 

18.709 

18.708 

18.689 

18.685 

18.672 

18.659 

18.65 

18.648 

18.659 

18.661 

18.662 

18.658 

18.637 

18.636 

18.637 

18.636 

18.624 

18.623 

18.615 

NO, 

PPM 

0.147 

0.15 

0.142 

0.139 

0.141 

0.138 

0.131 

0.143 

0.14 

0.129 

0.126 

0.131 

0.132 

0.119 

0.122 

0.116 

0.121 

0.12 

0.121 

0.111 

0.112 

0.111 

0.118 

0.11 

0.111 

0.11 

0.111 

0.107 

0.107 

0.1 

0.107 

0.098 

0.109 

0.11 

0.11 

0.109 

0.113 

0.109 

0.097 

0.098 

0.096 

0.103 

0.099 

0.093 

0.098 

0.096 

0.093 

0.09 

0.095 

0.096 

0.095 

0.093 

0.091 

0.093 

0.093 

0.089 

0.094 

0.086 

CO 

PPM 

0.571 

0.567 

0.564 

0.564 

0.563 

0.567 

0.569 

0.573 

0.543 

0.571 

0.57 

0.568 

0.538 

0.562 

0.514 

0.568 

0.542 

0.569 

0.568 

0.567 

0.564 

0.561 

0.564 

0.563 

0.562 

0.561 

0.56 

0.564 

0.561 

0.538 

0.563 

0.536 

0.511 

0.537 

0.535 

0.559 

0.541 

0.541 

0.442 

0.419 

0.42 

0.416 

0.44 

0.415 

0.414 

0.443 

0.442 

0.442 

0.418 

0.448 

0.421 

0.417 

0.443 

0.418 

0.418 

0.471 

0.523 

0.449 

THC 

PPM 

0.407 

0.406 

0.407 

0.408 

0.408 

0.408 

0.408 

0.409 

0.409 

0.409 

0.408 

0.408 

0.408 

0.407 

0.407 

0.406 

0.408 

0.407 02/C02 bias 

0.407 

0.407 

0.407 

OA07 Zero bias 

0.408 

0.407 

0.407 Direct Zero 

0.407 

0.407 Direct Span 

0.407 

0.407 02/C02 High 

0.407 

0.407 C02 Mid 

0.407 

0.408 

0.408 

0.408 

0.408 

0.408 

0.408 

0.408 

0.408 

0.408 

0.408 

0.407 

0.408 

0.408 

0.407 

0.408 

0.408 

0.408 

0.408 

0.408 

0.407 

0.407 

0.408 

0.408 

0.408 

0.408 

0.408 
Date Time 

2/12/2013 4:30:00 PM 

2/1212013 4:31 :00 PM 

2/1212013 4:32:00 PM 

2/12/2013 4:33:00 PM 

2/12/2013 4:34:00 PM 

2/12/2013 4:35:00 PM 

2/1212013 4:36:00 PM 

2/12/2013 4:37:00 PM 

2/12/2013 4:36:00 PM 

2/12/2013 4:39:00 PM 

2/1212013 4:40:00 PM 

2/12/2013 4:41 :00 PM 

2/12/2013 4:42:00 PM 

2/12/2013 4:43:00 PM 

2/12/2013 4.44:00 PM 

2/12/2013 4:45:00 PM 

2/12/2013 4:46:00 PM 

211212013 4:47:00 PM 

2/12/2013 4:46:00 PM 

2/12/2013 4:49:00 PM 

2/12/2013 4:50:00 PM 

0 , 

% 

20.576 

20.564 

20.546 

20.537 

20.522 

20.512 

20.505 

20.494 

15.672 

14.445 

14.474 

14.465 

14.462 

14.463 

14.461 

14.46 

14.453 

14.451 

14.451 

14.451 

14.446 

2/12/2013 4:51:00 PM 14.443 

2/12/2013 4:52:00 PM 14.441 

2/1212013 4:53:00 PM 14.443 

2/1212013 4:54:00 PM 14.443 

2/12/2013 4:55:00 PM 14.44 

2/12/2013 4:56:00 PM 14.436 

2/12/2013 4:57:00 PM 

2/12/2013 4:56:00 PM 

2/12/2013 4:59:00 PM 

2/12/2013 5:00:00 PM 

2/12/2013 5:01 :00 PM 

2/12/2013 5:02:00 PM 

14.427 

14.422 

14.416 

14.412 

14.412 

14.409 

2/1212013 5:03:00 PM 14.41 

2/12/2013 5:04:00 PM 14.41 

2/12/2013 5:05:00 PM 14.403 

2/12/2013 5:06:00 PM 14.401 

2/12/2013 5:07:00 PM 14.401 

2/1212013 5:06:00 PM 14.402 

2/12/2013 5:09:00 PM 

2/1212013 5:10:00 PM 

2/12/2013 5:11:00 PM 

2/12/2013 5:12:00 PM 

2/12/2013 5:13:00 PM 

2/1212013 5:14:00 PM 

2/1212013 5:15:00 PM 

2/1212013 5:16:00 PM 

2/12/2013 5:17:00 PM 

2/12/2013 5:16:00 PM 

2/12/2013 5:19:00 PM 

2/1212013 5:20:00 PM 

2/1212013 5:21 :00 PM 

14.409 

14.411 

14.417 

14.425 

14.436 

14.446 

14.451 

14.451 

14.451 

14.451 

14.452 

14.451 

14.455 

2/12/2013 5:22:00 PM 14.462 

2/12/2013 5:23:00 PM 14.46 

2/12/2013 5:24:00 PM 14.46 

2112/2013 5:25:00 PM 14.463 

2/1212013 5:26:00 PM 14.467 

2/12/2013 5:27:00 PM 14.465 

co, 

% 

0.466 

0.463 

0.496 

0.51 2 

0.526 

0.539 

0.552 

0.564 

0.574 

0.562 

0.59 

0.597 

0.604 

0.611 

0.616 

0.624 

0.63 

0.636 

0.642 

0.646 

0.656 

0.663 

0.669 

0.676 

0.663 

0.669 

0.694 

0.699 

0.706 

0.712 

0.719 

0.723 

0.73 

0.735 

0.741 

0.746 

0.751 

0.759 

0.765 

0.771 

0.777 

0.763 

0.769 

0.794 

0.796 

0.604 

0.609 

0.615 

0.621 

0.627 

0.633 

0.637 

0.643 

0.646 

0.653 

0.659 

0.663 

0.67 

NO, 

PPM 

0.042 

0.043 

0.042 

0.047 

0.042 

0.041 

0.046 

0.046 

1.26 

1.96 

2.16 

2.006 

2.09 

1.261 

0.196 

0.093 

0.065 

0.064 

0.074 

0.062 

0.05 

0.045 

0.045 

0.045 

0.045 

0.044 

0.051 

0.047 

0.056 

0.044 

0.046 

0.044 

0.04 

0.042 

0.047 

0.047 

0.049 

0.051 

0.046 

0.042 

0.056 

0.059 

0.046 

0.05 

0.05 

0.054 

0.057 

0.051 

0.049 

0.051 

0.052 

0.045 

0.046 

0.046 

0.043 

0.046 

0.043 

0.041 

CO 

PPM 

0.232 

0.227 

0.231 

0.232 

0.227 

0.476 

0.534 

0.553 

0.254 

0.066 

1.712 

4.51 

4.565 

5.561 

3.135 

3.951 

4.65 

4.716 

4.766 

4.659 

4.661 

4.922 

4.695 

4.906 

4.917 

4.954 

4.971 

4.915 

4.951 

4.94 

4.993 

4.957 

4.961 

4.999 

5.004 

5.02 

4.973 

4.975 

4.969 

4.992 

4.964 

5.011 

4.94 

4.919 

4.966 

4.967 

5.014 

5.017 

4.991 

4.02 

0.29 

0.066 

0.064 

2.679 

4.561 

4.566 

5.252 

5.406 

0, 

% 

16.611 

16.595 

16.569 

16.562 

16.576 

16.574 

16.565 

16.564 

16.563 

16.562 

16.563 

16.564 

16.564 

16.565 

16.563 

16.562 

16.561 

16.541 

16.541 

16.536 

18.537 

16.536 

16.541 

16.55 

18.541 

16.545 

16.536 

16.533 

16.521 

16.512 

16.513 

16.506 

16.501 

16.496 

16.466 

16.46 

16.479 

16.46 

16.46 

16.472 

16.479 

16.467 

16.469 

16.489 

16.495 

16.503 

16.507 

16.511 

16.506 

16.506 

16.501 

16.499 

16.499 

16.506 

16.513 

16.513 

16.513 

16.507 

NO, 

PPM 

0.067 

0.069 

0.09 

0.063 

0.063 

0.06 

0.076 

0.072 

0.062 

0.076 

0.061 

0.077 

0.073 

0.069 

0.074 

0.066 

0.076 

0.076 

0.07 

0.076 

0.076 

0.065 

0.076 

0.081 

0.075 

0.067 

0.069 

0.065 

0.06 

0.056 

0.056 

0.066 

0.066 

0.06 

0.054 

0.064 

0.059 

0.057 

0.06 

0.064 

0.06 

0.053 

0.054 

0.055 

0.053 

0.053 

0.053 

0.049 

0.055 

0.054 

0.054 

0.053 

0.053 

0.053 

0.053 

0.051 

0.056 

0.056 

CO 

PPM 

0.423 

0.42 

0.421 

0.446 

0.469 

0.422 

0.495 

0.419 

0.42 

0.419 

0.416 

0.395 

0.391 

0.416 

0.416 

0.367 

0.366 

0.42 

0.416 

0.422 

0.42 

0.417 

0.415 

0.415 

0.414 

0.415 

0.414 

0.413 

0.418 

0.416 

0.395 

0.416 

0.416 

0.393 

0.392 

0.42 

0.419 

0.417 

0.393 

0.414 

0.366 

0.343 

0.394 

0.419 

0.395 

0.42 

0.42 

0.417 

0.395 

0.422 

0.397 

0.417 

0.419 

0.422 

0.422 

0.42 

0.544 

0.719 

THe 

PPM 

0.407 

0.407 

DA06 

0.406 

DA06 

0.406 

0.409 

0.406 Unspiked background CO 

0.406 

0.406 System Zero 

0.406 

0.409 

0.409 System bias 

0.409 

0.409 

0.409 

0.409 

0.41 

0.409 Start CO Spiking RATA Run 1 

DA06 

0.406 

0.406 

DA06 

0.406 

0.406 

DA06 

0.406 

0.406 

0.406 Start 2 

0.406 

D.406 

0.406 

0.406 

0.409 

0.409 

0.409 

0.409 

D.406 

0.406 Start 3 

0.409 

0.409 

0.409 

0.409 

0.409 

0.41 

0.409 

0.409 

0.409 

0.409 

0.409 

0.41 

0.409 

0.409 Zero bias 

0.406 

0.408 

OA06 Span bias 

0.407 

0.407 
Date Time 

2/12/2013 5:28:00 PM 

2/12/2013 5:29:00 PM 

2/12/2013 5:30:00 PM 

2/12/2013 5:31:00 PM 

211212013 5:32:00 PM 

2/12/2013 5:33:00 PM 

2/12120 13 5:34:00 PM 

2/12/2013 5:35:00 PM 

2/12/2013 5:36:00 PM 

2/12/2013 5:37:00 PM 

2/12/2013 5:38:00 PM 

2/12/2013 5:39:00 PM 

2/12/2013 5:40:00 PM 

2/12/2013 5:41 :00 PM 

211212013 5:42:00 PM 

2/1212013 5:43:00 PM 

2/12/2013 5:44:00 PM 

2/12/2013 5:45:00 PM 

2/12/2013 5:46:00 PM 

2/12/2013 5:47:00 PM 

2/12/2013 5:48:00 PM 

2112/2013 5:49:00 PM 

2112/2013 5:50:00 PM 

2112/2013 5:51 :00 PM 

2/12/2013 5:52:00 PM 

0 , 

% 

14.463 

14.459 

14.461 

14.461 

14.452 

14.45 

14.45 

14.45 

14.442 

14.427 

14.418 

14.411 

14.411 

14.413 

14.414 

14.419 

14.42 

14.422 

14.424 

14.425 

14.43 

14.435 

14.443 

14.45 

14.45 

2/12/2013 5:53:00 PM 14.45 

2/12/2013 5:54:00 PM 14.453 

2/12/2013 5:55:00 PM 14.459 

2/12/2013 5:56:00 PM 14.459 

2/12/2013 5:57:00 PM 14.46 

2/12/2013 5:58:00 PM 

2/12/2013 5:59:00 PM 

2/12/2013 6:00:00 PM 

2/12/2013 6:01 :00 PM 

2/12/2013 6:02:00 PM 

2/12/2013 6:03:00 PM 

2/12/2013 6:04:00 PM 

2/12/20 13 6:05:00 PM 

2/12/2013 6:06:00 PM 

2/12/2013 6:07:00 PM 

2/1212013 6:08:00 PM 

2/12/2013 6:09:00 PM 

2/12/2013 6:10:00 PM 

2/12/2013 6:11 :00 PM 

14.458 

14.46 

14.461 

14.466 

14.469 

14.466 

14.466 

14.464 

14.464 

14.463 

14.461 

14.465 

14.465 

14.468 

2/12/2013 6:12:00 PM 14.471 

2/1212013 6:13:00 PM 14.474 

2112/2013 6:14:00 PM 14.476 

2/1212013 6:15:00 PM 

2/1212013 6:16:00 PM 

2/12/2013 6:17:00 PM 

2/12/2013 6:18:00 PM 

2/12/2013 6:19:00 PM 

2/12/2013 6:20:00 PM 

2/12/2013 6:21 :00 PM 

2/1212013 6:22:00 PM 

2/1212013 6:23:00 PM 

2/12/2013 6:24:00 PM 

2/12/2013 6:25:00 PM 

14.477 

14.48 

14.486 

14.491 

14.5 

14.502 

14.51 

14.51 

14.511 

14.513 

14.521 

co, 

% 

0.874 

0.879 

0.883 

0.889 

0.892 

0.897 

0.901 

0.906 

0.909 

0.913 

0.918 

0.922 

0.927 

0.931 

0.934 

0.939 

0.942 

0.946 

0.949 

0.952 

0.955 

0.957 

0.96 

0.963 

0.966 

0.969 

0.973 

0.977 

0.98 

0.983 

0.985 

0.987 

0.991 

0.993 

0.995 

0.999 

1.002 

1.004 

1.007 

1.008 

1.009 

1.011 

1.013 

1.014 

1.016 

1.019 

1.02 

1.023 

1.025 

1.028 

1.03 

1.032 

1.033 

1.035 

1.037 

1.037 

1.039 

1.04 

NO, 

PPM 

0.044 

0.047 

0.047 

0.05 

0.054 

0.051 

0.052 

0.047 

0.043 

0.05 

0.05 

0.047 

0.045 

0.048 

0.051 

0.048 

0.043 

0.042 

0.048 

0.047 

0.044 

0.046 

0.049 

0.042 

0.056 

0.042 

0.Q35 

0.036 

0.039 

0.041 

0.04 

0.043 

0.043 

0.032 

0.037 

0.037 

0.034 

0.037 

0.Q35 

0.042 

0.046 

0.046 

0.041 

0.033 

0.037 

0.037 

0.04 

0.039 

0.039 

0.043 

0.041 

0.036 

0.04 

0.045 

0.038 

0.037 

0.04 

0.04 

CO 

PPM 

5.175 

5.149 

5.112 

5.156 

5.157 

5.168 

5.206 

5.14 

5.178 

5.172 

5.203 

5.21 

5.213 

5.219 

5.196 

5.171 

5.193 

5.145 

5.144 

5.171 

5.121 

5.116 

5.149 

5.158 

5.201 

5.279 

5.203 

5.262 

5.283 

5.191 

5.308 

2.565 

0.087 

0.06 

2.69 

4.558 

5.267 

5.54 

5.293 

5.281 

5.271 

5.324 

5.277 

5.263 

5.281 

5.291 

5.298 

5.292 

5.283 

5.247 

5.305 

5.249 

5.246 

5.217 

5.178 

5.216 

5.231 

5.183 

0, 

% 

18.498 

18.488 

18.477 

18.466 

18.458 

18.454 

18.438 

18.438 

18.419 

18.413 

18.41 

18.411 

18.413 

18.412 

18.411 

18.412 

18.41 2 

18.412 

18.406 

18.402 

18.403 

18.41 

18.413 

18.411 

18.412 

18.411 

18.41 

18.412 

18.406 

18.394 

18.398 

18.401 

18.405 

18.41 

18.4 

18.39 

18.369 

18.366 

18.365 

18.362 

18.341 

18.34 

18.34 

18.34 

18.34 

18.335 

18.315 

18.315 

18.316 

18.328 

18.341 

18.341 

18.341 

18.341 

18.341 

18.341 

18.328 

18.316 

NO, 

PPM 

0.064 

0.057 

0.058 

0.052 

0.053 

0.061 

0.051 

0.053 

0.052 

0.048 

0.05 

0.055 

0.056 

0.05 

0.045 

0.039 

0.046 

0.Q41 

0.041 

0.047 

0.043 

0.046 

0.043 

0.038 

0.035 

0.034 

0.035 

0.034 

0.038 

0.035 

0.036 

0.037 

0.038 

0.041 

0.038 

0.04 

0.048 

0.047 

0.046 

0.043 

0.053 

0.041 

0.036 

0.038 

0.043 

0.037 

0.038 

0.039 

0.048 

0.039 

0.04 

0.041 

0.041 

0.038 

0.026 

0.03 

0.029 

0.025 

CO 

PPM 

0.675 

0.573 

0.572 

0.494 

0.419 

0.417 

0.413 

0.416 

0.416 

0.412 

0.41 

0.415 

0.415 

0.415 

0.417 

0.415 

0.411 

0.413 

0.415 

0.416 

0.414 

0.411 

0.413 

0.414 

0.414 

0.415 

0.414 

0.411 

0.432 

0.409 

0.411 

0.408 

0.409 

0.408 

0.411 

0.412 

0.412 

0.417 

0.413 

0.413 

0.417 

0.416 

0.421 

0.423 

0.418 

0.422 

0.423 

0.419 

0.422 

0.418 

0.418 

0.421 

0.42 

0.419 

0.42 

0.392 

0.389 

0.419 

THe 

PPM 

0.407 Start 4 

Q.408 

0.407 

0.407 

0.407 

0.407 

0.408 

0.407 

0.407 

0.407 

0.407 Start 5 

0.407 

Q.408 

Q.408 

Q.408 

0.409 

Q.408 

Q.408 

Q.408 

Q.408 

0.408 Start 6 

Q.408 

0.407 

Q.408 

Q.408 

0.409 

0.409 

Q.408 

0.407 

0.408 

0.408 

0.408 

0.408 

0.409 Zero bias 

0.408 

0.408 CO bias 

0.409 

0.409 

0.408 Start 7 

0.409 

0.409 

0.41 

0.41 

0.41 

0.41 

0.41 

0.41 

0.41 

0.41 Start 8 

0.41 

0.41 

0.41 

0.411 

0.411 

0.411 

0.41 

0.411 

0.41 
0, CO, NO, CO 0, NO, CO THC 

Date Time % % PPM PPM % PPM PPM PPM 

2/12/2013 6:26:00 PM 14.519 1.042 0.033 5.214 18.315 0.031 0.42 0.41 Start 9 

2/12/2013 6:27:00 PM 14.524 1.043 0.036 5.207 18.315 0.033 0.419 0.41 

2/12/2013 6:28:00 PM 14.556 1.06 0.034 5.252 18.314 0.028 0.393 0.409 

2/12/2013 6:29:00 PM 15.656 1.097 0.031 5.265 18.293 0.026 0.394 0.409 

2/12/2013 6:30:00 PM 18.467 1.014 0.256 5.261 18.29 0.031 0.389 0.409 

2/1212013 6:31 :00 PM 20.026 0.842 0.461 5.194 18.29 0.034 0.561 0.409 

2/12/2013 6:32:00 PM 20.55 0.687 0.465 5.202 18.29 0.027 0.977 0.409 

2112/2013 6:33:00 PM 20.723 0.582 0.463 5.244 18.295 0.041 0.911 0.409 

2/12/2013 6:34:00 PM 20.792 0.515 0.458 5.24 18.315 0.028 0.792 0.409 

2/12/2013 6:35:00 PM 20.826 0.468 0.325 5.278 18.315 0.031 0.593 0.408 

2/12/2013 6:36:00 PM 20.852 0.438 0.177 5.28 18.316 0.033 0.543 0.408 

2/12/2013 6:37:00 PM 20.862 0.417 0.101 2.346 18.315 0.032 0.414 0.409 

2/12/2013 6:38:00 PM 20.916 0.496 0.068 0.145 18.326 0.029 0.421 0.409 Zero bias 

2/1212013 6:39:00 PM 20.967 0.183 0.023 0.557 18.338 0.027 0.418 0.409 

2/12/2013 6:40:00 PM 20.941 0.163 0.014 4.321 18.34 0.023 0.419 0.41 

2/12/2013 6:41 :00 PM 20.953 0.155 0.013 4.566 18.34 0.029 0.417 0.41 CO bias 

2/12/2013 6:42:00 PM 20.971 0.144 0.019 2.657 18.34 0.035 0.416 0.41 

2/12/2013 6:43:00 PM 20.991 0.138 0.01 0.146 18.34 0.031 0.417 0.409 Cal Zero 

2/12/2013 6:44:00 PM 21.013 0.134 0.019 6.595 18.341 0.026 0.42 0.41 

2/12/2013 6:45:00 PM 21 .014 0.131 0.02 9.877 18.342 0.03 0.42 0.41 

2/12/2013 6:46:00 PM 21 .026 0.129 0.014 9.625 18.342 0.032 0.418 0.41 

2/12/2013 6:47:00 PM 21 .047 0.127 0.011 9.619 18.342 0.03 0.396 0.41 Cal High 

2/12/2013 6:48:00 PM 21 .056 0.127 0.019 6.765 18.352 0.035 0.369 0.409 

2/12/2013 6:49:00 PM 21 .063 0.127 0.011 4.599 18.363 0.036 0.417 0.409 

2/12/2013 6:50:00 PM 21 .062 0.127 0.011 4.581 18.352 0.035 0.414 0.409 CO Mid 

2/12/2013 6:51 :00 PM 21.055 0.129 0.014 2.264 18.34 0.032 0.418 0.409 
Appendix C.3 Ammonia Data by SCAQMD Method 207.1 

R041 0688 C-7 
AMMONIA TEST RESULTS SUMMARY 

Client Gemma Parameter 

location CPV Sentinel Fuel 

Unit 4 Oata By 

Test Number CPV Senlinel-4-NH3-106-1 CPV Sentinel-4-NH3-107-2 

Reference T emperalure, F 60 60 

Test Date 2/11 /2013 2/11/2013 

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 (sq tt) 143.14 143.14 

Sample Time (Min) 60 60 

Barometric Pressure (in Hg) 29.64 29.64 

Start Time 10:06 11 :40 

Stop Time 11:19 12:54 

Meter Volume (act) 45.341 48.446 

Meter Temperature (F) 59.1 59.5 

Meter Pressure (iwg) 1.50 1.50 

Liquid Volume (m!) 113.3 96.0 

Stack 02 (%) 13.29 13.15 

Slack NOx (ppm)@ 15% 02 2.34 2.18 

Unit load MW 106 107 

Fuel Flow Rate, hscfh 8,830 8,854 

Standard Sample Volume (SCF) 44.795 47.828 

Moisture Fraction 0.105 0.085 

Stack Flow Rate (dscfm, 60 of) 383,018 357,556 

Stack Flow Rate (dscfm, 70 of) nla nla 

Gas Constant (ft-Ibflltrmole-R) 1545.33 1545.33 

Standard Pressure (lbfIft2) 2116.224 2116.224 

Molecular Weight NH3 (Ib/ltrmole) 17 17 

SpecifiC Molar Volume (ft3/Ib-mole) 379.50 379.50 

Mass Conversion (lb/ug) 2.20E-09 2.20E-09 

02 Correction Factor (%) 15 15 

Mass NH3 (ug/sample) 2229.534 2432.571 

Mass NH3 (mg) 2.230 2.433 

Mass NH3 (Ib) 4.91E-06 5.36E-06 

PPM NH31flue gas) 2.4 2,5 

PPM NH3 @ 02 Correction 1,9 1,9 

Ib/hr 2.52 2.40 

IblMMscf fuel 2.85 2.72 

NH3 EQUATIONS, 

ppm NH3 = (mass NH3* Gas Const * Ref Temp * 106 )/(Sample vol. • Press· MW) 

ppm NH3 @ 02 correction = ppm * (20.9-02 Corr)/(20.9-%02) 

NH3 

natural gas 

AA, SS, RM, JM 

CPV Senlinel-4-NH3--3 Average Umit 

13.22 

2.26 

2.5 

1,9 5 

2.46 

2.7854 
AMMONIA TEST RESULTS SUMMARY 

Client Gemma Parameter 

location CPV Sentinel Fuel 

Unit 4 Data By 

Test Number CPV SentineI4·NH3·81·1 CPV Sentinel-4·NH3·80·2 

Reference Temperature, F 60 60 

Test Date 211112013 211112013 

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 (sq tt) 143.14 143.14 

Sample Time (Min) 60 60 

Barometric Pressure (in Hal 29.64 29.64 

Start Time 15:45 17:10 

Stop Time 1652 18:19 

Meter Volume (act) 37.865 39.500 

Meter Temperature (F) 58.6 57.6 

Meter Pressure (iwg) 1.50 1.50 

Liquid Volume (mil 83.1 661 

Stack 02 (%) 13.81 13.80 

Stack NOx (ppm)@ 15% 02 2,07 2,30 

Unit Load MW 81 80 

Fuel Flow Rate hscfh 7018 6961 

Standard Sample Volume (SCF) 37.445 39.138 

Moisture Fraction 0.094 0.073 

Stack Flow Rate (dscfm, 60 of) 304,102 311 ,648 

Stack Flow Rate (dscfm 70 of) nla nla 

Gas Constant (ft-Ibfllb-mole-R) 1545.33 1545.33 

Standard Pressure (lbf/ft2) 2116.224 2116.224 

Molecular Weight NH3 (Ibllb-mole) 17 17 

Specific Molar Volume (ft3/Ib-mole) 379.50 379,50 

Mass Conversion (Ib/ug) 2.20E-09 2.20E-09 

02 Correction Factor (%) 15 15 

Mass NH3 (ug/sample) 931 .021 777.1 18 

Mass NH3 (mg) 0.931 0.777 

Mass NH3 (I b) 2.05E-06 1,71E-06 

PPM NH3 (flue oas) 1.2 1,0 

PPM NH3 @ 02 Correction 1,0 0,8 

Iblhr 1.00 0.82 

Ib/MMscf fuel 1.42 1.18 

NH3 EQUATIONS: 

ppm NH3 = (mass NH3* Gas Canst * Ref Temp * 106 )/(Sample vol . • Press' MW) 

ppm NH3@02correction= ppm' (20.9-02 Corr)/(20.9-%02) 

NH3 

natural gas 

AA, SP, 55 JM 

AveraQe Limit 

13.81 

2.18 

1.1 

0,9 5 

0.91 

1,3002 
AMMONIA TEST RESULTS SUMMARY 

Client Gemma Parameter 

location CPV Sentinel Fuel 

Unit 4 Oata By 

Test Number CPV Sentinel-4-NH3·55·1 CPV Sentinel-4-NH3-55-2 

Reference Temperature, F 60 60 

Test Date 2/1212013 2/12/2013 

Test Method SCAQMD 207.1 SCAQMD 207.1 

Sample Train 9-P&M 9-P&M 

Meter Calibration Factor 0.992 0992 

Slack Area (sq ftl 143.14 143.14 

Sample Time (Min) 60 60 

Barometric Pressure in Hql 29.74 29.74 

Start Time 11 :58 13:30 

Stop Time 13:07 14:39 

Meter Volume (act) 45.874 41 .937 

Meter Temperature (F) 77.6 69.6 

Meter Pressure (iwg) 150 1.50 

Liquid Volume (ml) 89.2 78.6 

Stack 02 (%) 14.27 14.26 

Stack NOx (ppm) @ 15% 02 2.16 1.86 

Unit load MW 55 55 

Fuel Flow Rate, hscfh 5,337 5,341 

Standard Sample Volume (SCF) 43.909 40.747 

Moisture Fraction 0.086 0.082 

Stack Flow Rate (dscfm, 60 of) 270,908 267,286 

Stack Flow Rate (dscfm, 70 of) nla nla 

Gas Constant (ft-Ibfllb-mole-R) 1545.33 1545.33 

Standard Pressure (lbfIft2) 2116.224 2116.224 

Molecular Weight NH3 (Ib/lb-mole) 17 17 

Specific Molar Volume (ft3/1b-mole) 379.50 379.50 

Mass Conversion (Ib/ug) 2.20E-09 2.20E-09 

02 Correction Factor (%) 15 15 

Mass NH3 (ug/sample) 786.041 813.625 

Mass NH3 (mg) 0.786 0.814 

Mass NH3 (Ib) 1.73E-06 1.79E-06 

PPM NH3 (flue oas) 0.9 1.0 

PPM NH3 t8l: 02 Correction 0.8 0.9 

Iblhr 0.64 0.71 

Ib/MMscf fuel 1.20 1.32 

NH3 EQUATIONS: 

ppm NH3 = (mass NH3* Gas Const " Ref Temp" 106 )/(Sample vol. .. Press· MW) 

ppm NH3@02correction= ppm" (20.9-02 Corr)/(20.9-%02) 

NH3 

natural gas 

AA MC RM, JM 

Averaqe Limit 

14.26 

2.01 

0.9 

0.8 5 

0.67 

1.2616 
WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: C--1eMMCt, 

LOCATION: ":>eN;! ' >V, I 

DATE: -zlll [13... 

RUN NO: :; - 'I )(iF IV 1-1; - \PO \ F-"\-,,, \ OPERATOR ~ . .J.)--,;M;;>-,~ ____ _ METER BOX NO: "I PM 

METER toH@:·-;\- ."=S':!J-',c::, '--------

METER Yd: Q .",,,, 2-

STACK AREA, FT': \'\, ... \'\ 

TRAVERSE POINT;':S!'-, ~M""IN-cI"'PO::07:1 N"'T:- ' ;;""-7/ 1--:2=--

toH; p'/Pr X toP: j Probe Condition, prelpost test . ...-"J'---_ _ _ 

Silica Gel Expanded, ""rJ~ ___ _ 

Filter Condition ft:?"est:.-,-",--,---,~,--__ _ Check Weight_-'-____ ___ _ 

Meter toP 

Point Time Volume, ft' in. H,O 

.;J ~ 1001..> .,~, ;J"l6 ~ I. '3 

2- ivi I 11 /. </ 

1 

'" I '" .'2... i, Go 

LI 102.1 "\~ QI'" f.j 

I\J , \ 10 l-<., '>'1.1',:;,1,\ l'f ", ,"1 L 

2, iO'" h ,c.; '''' 

I 10"'" I', i . , V 1<> l< I ) ') "tlZ 'i II I . .:. 

It ? i<J 4" 'I) L2,,\ II O. '\ '" 

7. h~q I ', I" 

I 10,)'"1 ?. I . \ 

0 \:)<;,q ' Y"h ~~ I I" 

1'-, '3 . If)" \" 70 ,(0, .. .1" l).tI\ .;;-

~, l\O q I·, I '" 

I \ \\ l.f. ?-. \ 1 

0 Ulq <::;37, ill II I . (r. 

Average: 

AMBIENT TEMPERATURE: A 1.d 

BAROMETRIC PRESSURE :_ -~'l,_6'i~~"1'l~-=--=--=--=--=--=--=--=--=--=--= ASSUMED MOISTURE ::_"""....-_:..:~"'<f."'I0'--____ _ 

PITOTTUBE COEFF, Cp: 0.'\"" 

PROBE 10 NO/MATERIAL-: ~"""cc:;;l;).-'-':--. -c:>i=-- ----

PROBE LENGTH: 3 ' NOZZLEIDNO M-A-T-E R-IA L- M-Z'~---- ----

NOZZLE DIAMETER:_---'/V=-I 4"-_____ _ _ _ _ 

F I L TER NOfTYPE :=="-iV."'v:,::-'l-o----:--===--.-:::o----c,-----:-:--

PRE-TEST LEAK RATE: : 0 .002.. CFM@ \S- in. Hg. 

POST-TEST LEAK RATE: :'-0 ",,:> CFM@ ':' in. Hg. 

PITOT LEAK CHECK - PRE: ,...-- POST: 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN '4"-""---

SAMPLER J-'» SAMPLEC~U~S~TO~D IA -:-4:- --

toH Stack Probe Filter Imp. Out 

in. H,Q Temp, OF TemD, OF TemD, OF TemD, OF 

\ ' :::. 7" -; ",(f> foI/~ 5"-

'/v ~ , 76t, 

7 (., (., 

\> -'/.,? 5'( 

7'''( 

10,0 

1k;'ZI, '" 

'7 t, '2. 5) 

h<; 

'10'" 

1.8 

\. '5 ·1,,0 )7 

1<;7 

?f~ 

1,,0 \. 

II II 

'\ 

Imp. # Contents Post-Test - Pre-Test; Difference 

/ C'. / AI /125!-(/ 1, n J i, --'==-- C' :...;,5"---__ 

L tJ/'1//!2lf-lobb,166?~ 

...1-64"-7 5'fi I ,L£ -,-5 -,5'/...:..: , '-,- _ _ _ 

L &r 1M "I ,0 8'19 "''---_ 

U. til- 11'1 (} l C? 0 __ 

Total: ____________ _ 

Meter Temp, OF Vacuum 0, P. static 

In Out in. Ha. % in. H,O 

C~ '>7 if' ['7 7 ,;], 

'f 

G'z. ,6 (f 

h\ <;., (j 

CS '" L/ 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 1/25/2013 Page __ of _ _ Master Document StoragelFormsl Datashee. 
DeHa~ ""'-""""--

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: G1:?VV\MPr 

LOCATION: 5§T' ''ViM--

DATE: ;2! " \ 

RUN NO: ', ' 4 £-N'lh-/o) - 't- f'G\,",, '1, 

OPERATOR: Q <IV\. .) ""-

METER BOX NO :_--l5~f,-;"";:...... ____ _ 

METER Ll.H@:._-:i:"';',..J'1"., ~I!-"J,--____ _ 

METER Yd: 0 9<;:1-

STACK AREA, FT': i ·0 .' 't 

TRAVERSE POINT~S-, -'M-'INco/P-'O--'-IN-T-: ~11-;LLl.H= rV (),- X Ll.P: .,/ 

Probe Condition, pre/post test-:;../ ___ _ 

Silica Gel Expanded, YIN: ;J 

Filter Condition after T est----'j;M:-..---

Check Weioht ~ 

/ 

AMBIENT TEMPERATURE: 

-Lil' 

BAROMETRIC PRESSURE-: ---"J."l"", /;-e7:' 1 ------

ASSUMED MOISTURE :._-:=9~1&. r--------- PITOT TUBE COEFF, Cp: - ,~'i PROBE 10 NO/MA TERIAL-: - ,j\::-'-'o-'o-,8,,--;:;-:':-:D-------

PROBE LENGTH: l' NOZZLEIDNO/M-;A-:T~E-R-IA-L-: -~0-~--------

NOZZLE DIAMETER: _ __ -':''\.J~Ac_------_ 

FILTER NOfTYPE: IV "" 

PRE-TEST LEAK RATE: : .0· col.- CFM@ l )- in. Hg. 

POST-TEST LEAK RATE: : CFM@ in. Hg. 

PITOT LEAK CHECK· PRE: ~ POST: 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN -;;4--;J\-c--

SAMPLER C'''''-

SAMPLE CUSTODIAN F\ '" 

Imp. # Contents Post-Test· Pre·Test = Difference 

O,'r.J~i 1l7~,) (",,\0.\ 

~~~---

'2 " , N \\,-W b hi. ~ (",l.,u 5 

3 v\A.\ 5'1,2,) S'OIZ __ _ 

~ S; if ''[q I ,~ '1 /':,0,0, __ 

i>:J.. Ih.o L,.'J e [Z"" 517 - 100. '"'CJ 

Total: ____ _________ _ 

Meter Ll.P Ll.H Stack Probe Filter Imp. Out Meter Temp, OF Vacuum 02 P. static 

Point Time Volume, ft' in. H20 in. H20 Temp, OF Temp, OF Temp, OF Temp, OF In Out in. Hg. % in. H20 

1-::. 3 1\"1'" s:n)·"11 "10 .. t? I·) ((.,',1 I" .." 10 ~ :,0 1.-( <'7 V I \,0 ·5'/0 1-;1. .'-1 

2. II'" .:;, 11 /~ 7~{, 

, \I ",,-, 1. o.c 1'-1 '1 (. G 

o "D )'\"\·11! I d,'1')" "I&~ ' 

.,-; 3 r Zo,., "'\'1·71, .\ C, '1 v , I ~ 7", ~ ') -{ r .. ) \x '-/ 

a 11.V' ." () n 71.> 1 

\ nlo 'L D,9'7 7~ ') 

o I'Z-I')- bO,,·(:;>'(L- I /).>(<1 -J('/ 

N , l1.lo GOI. "17_ lj u 9''/ I·"" 76 ~ :5 7 61 a ", '2. 1,-1-.,- 5 h ,'I Z- 7 to Co 

I \ ,-,>0 ·z .'I/ ·7M .. 

o \1--'>:\" If Iq .(-Z." i flO 7(.,5 

vJ 3 IM''I l i:,tl.tZq '1 · 1 / (.'5"" /66 <;.7 (:,0 ')~ 'i 

'Z l'l.-I.{'1 '3'17 /6 7 

.J. 11).(11 '2- iI.f/o 761 

I 

v (1,.)i 611.1<1" \ 1J,'67_ 7D"-

Averaqe: 'I- .J-.-

Comments: __________________________________________ ~----------------------------------------------__________________ ___ 

Date of last revision 1/25/2013 PageL-ofl 

DS834049 

Master Document StoragelFormslDatasheets\Field Datasheets 
Della/),. ~ 

... ~--

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: (--. ~A!\.I'.f\!'t 

LOCATIOk ) ,::: '~,., I A ( 

DATE: hI "I tI 

RUN NO: IS ' 'i (Oi-, 11-41- 1S:, I i2ffTltl-'1 

OPER6Tr"'R: (2..(VI. ).M.~ ____ _ 

METER BOX NO: • .....,,'1.J..7-l'V'''-'-_____ _ 

METER l>H@:..,-_' -"i\,,-~,-," ______ _ 

METER Yd:=-=-, ::; , q:7"'-'1--"::;--..,-_____ _ 

STACK AREA, FT2~ 

TRAVERSE POINTS, MIN/POINT: \/11_ 

l>H= ~ X liP: // 

Probe Condition, pre/pJst :es!:""vi+'" __ _ Silica Gel Expanded. YIN: N 

Filter Condition after Test: ( / 

Check Weigh!: _____ -';?O-

~ Point I I Meter l>P 

Time Volume, fe in. H,O 

\< ~ I"S"I.-\ ~ "c; > --: ilL , Ill'') 

1- \~'> o \ X, 

i {-r<\" > H+'\ 

,0 t bOO 611{ 't~ . 1l--

-: . ." , h')~ n~·qlq • 0 11';-

2- k.,3 1!L 11''-\ , 11.<; , 9:11<01 

{) ,10 1,Y \:>)/'/. 'J~.5 ' Ol>r 

J 1 1.'2.0 Gy~')~ ~- ~ O:'\f" 

2- 16'l.' ) tdVi 

\ . \, \0 , 0.' '7.-

0 ' {,'IS -i'\ <.(. a,lS' I n. ., 

y..J 1 11·;1 if 1.,1'{·'Q., ~ ( " l:t 

1. II:. 'l~ ) (' .~2-

. \ b" is' ~ l ;1) 

0 I(,.n '101, .(,11 l · Thl.0 

I Average: 

I 

!\MBIENT TEMPERATURE:,--_')2-" _______ _ 

aAROMETRIC PRESSURE: 

ASSUMED MOISTURE: 1 '.--1.--------- PITOT TUBE COEFF. Cp: ~II 

PROBE ID NO/MATERIAL-':"' .... -'--';;--'O~-;;-2::-------

PROBE LENG: H::-:-::l :=·=-:-_--:c _______ _ 

r.OZZLE ID NOI MATERIAL :~ 

NOZZLE DIA ETER:_-;' /f("-----------_ 

F I L TE R NOfTYPE :==-~NI.:,-=-;:;;=;;o--;-:::----,--;-;-:-_ PRE-TEST LEAK RATE:: L, .,,-'" CFM@ \ (' in. Hg. 

POST-TEST LEAK RATE: :;." ".'7.- CFM@ i~ in. Hg. 

PITOT LEAK CHECK - PRE: ,,/ POST: L.--'" 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN,-"A",,,,,-__ 

SAMPLER t '" ,-

SAMPLE CUSTODIAN_.L(}"'"L-__ 

l>H I St8ck Probe Filter Imp. Out 

io. H,O Tenlp, OF Temp. ' F Temp. ' F Temp, ' F 

1-"> '\ ,-'" ,/I .... tvl-"" /)5 

" ., 7..-. 

7 ~ '1 

'1 ('0 

I -:-, -1 S' ]... 1:)0 

J ,;} / 

Hq I I - 1~ A" I 

I . .,,-- In I S If 

1,;; / 

1 .\0 

./ "II! 

IY 1''1'' ')6 

1:>1.- - 15'i 

1~-1.-

- bl II 

:mp. # Contents "ost-Test - Pre-Teet = Difference 

...L Of }JfI,0.t 1;~;~;7 -=,,-, J''1c.... ' '--- ( __ 

~ Dlt.JH/f!q M:::t:> IJ (.,?-51 __ 

.L~ 4'67, q 'i6/, ~ __ 

£ L?t- "'jet" b CjS95 __ 

'J5t- 100 - -

Tot" l: ____________ _ 

Meter Temp, ' F Vacuum 0, P. static 

In Out in. Hg. % in. H2O 

;..., 'f 7 ~ t... . '"'\.. 

ho .;-, 

b", ') ' 

(O.? ~&. 

. J./ 

Comments: ________________________________________________ . __________________________________________ ___ 

Date of last revision 1/25/2013 Page __ of __ 

05834049 

Master Document 5toragel FormslOatasheetslFieid Oatasheets 
Della;). 

... 0.-,. ...... ,-

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: C:I.~M, .... ALOCATION: ~"'r,'VA \ 

DATE: l-i" II ." 

RUN NO ';~ j ISfl'- - Nfl> ' 7)- 'l- iL<;1-" S 

OPERATOR: ILlY' j ."" 

METER BOX NO:,'?\~g.:..: ",-,--_____ _ 

METER LlH@:~ 

METE R Y d :~"'=:='3~~i'--':' 1.--;-;:-,-_ ___ _ STACK AREA, FT~ i~i-Ij TRAVERSE POI NT~S~, ¥M"'IN+I=P:::O""I N7.:T:-/ 7';:;=;7r-::2--

LlH= IV I /l- X LlP: './ 

Probe Condition, prelpost test: 

Silica Gel Expanded, YIN: N ( 

Filter Condition after Test:_---c,;<{:...-__ _ 

Check Weight: 7 

Meter LlP 

Point Time Volume, ft3 in. H2O 

S 'i 1110 loL.V1l-5 11/0"72-

7 111; 'J I, )!-o 

I 11P l AO· &~ 

v l-r~\ ·11'j.170 Ie· d'~ 

If .) 11 z.~ ~,'i . 77,( ill I ~:1 

1..- \'1;" ." 0 ,( 

( 11~8 [;z. _£;<j <:r" 

(.) 11 'I" 12.-"\, b11.{ ( (},l/, :J,. 

tJ 'j n~0 1'2-0.{ . ("1'1 <I ~~ 

? 11,1 .? 0 • '\'3 

I ' 1~<. 1'2 \J. 

0 I gO, , z,'I • (,1-'-1 , Q. no 

'" ~ l ()~ /~,{··(;2-i II 0. 1 

1 \ 0 q ·z H;-

{ ( II{ 2_ 1>1<:l 

0 I, . 1"1 ll.tl.(·'1L" , D.p,o 

Average: ____ - -

<I 

AMBIENT TEMPERATURE: 5'~ Imp. # Contents Post-Test - Pre· Test = Difference 

BAROMETRIC PRESSURE: __ ..<Z,,'l-::;;it,'-i.:-_____ _ ASSUMED MOISTURE:_-:-;:-;;---II"'-..:f""'--____ _ \ 

~ 

OINH-J"'i '3?7,L S~2,7 

PITOT TUBE COE FF, Cp:-",,- :..: ·1l.C"Ic...,.,-,-::-,,------

PROBE ID NOIMATERIAL:--'C#',-""'", ' ,-"o'iI_ '>"'r...,QL-____ _ PROBE LENGTH:==, :=· ::-:-o_-:--;-_______ _ 

NOZZLE ID NOI MATERIAL :~ 

NOZZLE DIAMETER:_-'i/V~/4C::---------

FI L TER NOITYPE :=~,-('-jf.-' a--:;---:::~-;=:--,--::::--:---,-.,-_ PRE-TEST LEAK RATE:: '0·.' l- CFM@ '> in. Hg. 

POST-TEST LEAK RATE: Ul.O">?.. CFM@ \.s;- in. Hg. 

PITOT LEAK CHECK - PRE: V- POST: ic:= 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN-" ( _ _ 

SAMPLER /ZM \-""-

SAMPLE CUSTODIAN--,Y'",L~ __ 

LlH Stack Probe Filter Imp. Out 

in. H,O Temp, OF Temp, OF Temp, OF Temp, OF 

\. ") '7 'f/ 'Y rJ/'+- IV/;\- r) 

7,S v ' J 

I';> ( 

7Ju / 

I .... ,; 7'> I <:,> 

75'2. 

7S'2-

'7 ~ CJ 

\ . <:) -1 -;-.0 )1 

-'7,,( 

I'll(' 

'-'<0 

l'S '/ "-1.- sy 

-JS"i 

7';Z. 

~ 'it( 

, \ 

~ 

;, 

'1 

LR.. 

c.l:\I 111 S(:Jc, 1:5'0 7 

~"" fj.1 5'1; \, b 

~ .l;,. "6 G/'i ,:r 

D~ 1\ .. 0 

!.o5q,, ><-b __ 

5 <£;0, -,--_ 4

Lb33.) 

--

\00 __ 

Total: _____________ _ 

Meter Temp, OF Vacuum 0, P. static 

In Out in. HQ. % in. H,O 

1.,0 ::r> ;--2. '1 

1 

1 

t.l 5'X 

-' "\ <,5 

,>1> )) 

\ , ) 

Comments: ____________________________________________________________________________________________________________ ___ 

Date of last revision 1/25/2013 Page __ of __ 

D5834049 

Master Document 5toragelFormslDatasheetslFieid Datasheets 
Delta/). ... 0..-.. _ ........... 

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

f~~~~~1£;;~~ "\ 

DATE: "2-1" 1' 5 

RUN NO:S:J {S'-I'- 'AIWI ' SO - \ 

OPERATOR: 0-"" ~"" METERBOX 0~:~7\~e~~~-------------

METER IIH@:..."... ' ''' 1 ".. ''-..1= ______ _ 

METERYd: O';J5 

STACK AREA, FT: ,'{".\, 

TRAVERSE POINT'"'S'-,""' M"',N-cI"'P""O"' IN-:::To-:--::S-=/T,"::" LIIH= ."-' I ,,, X liP: r " 

probecOr1ciition, prel post test: <!. 

Silica Gel Expanded, YIN: N . Filter Condition after Test: // 

Check Weight ___________ 7"-

Meter liP 

Point Time Volume, ft3 in. H2O 

:> 'S ,l') 8 5l'U'. )'')0 q • '" 7 

L- ,'Lo'3 .< r , ', 2-

l 1'2.0$ " " .") " " '1. \ '"'> j(~'t.1S~4 · "7 'I 

t:" > i"2-\('" 1, S"\ $~,,\ '" • "" 1"/ 

?,.. \ 7_ 1.-\ . .<16-

\ 111. "J..l> ~ 

~ , "7 ( 

'" ,'2.", 't7(' \ 3 L.. I 77 

IJ ~ I )-t" '1/ I ~.l..- I.., . '12.-

'l-- \ 1.-~ · -{ 7 

\ 11. ~.' . 

or ~ '/ 

" I -z,.\.( ~ ?,gL .l'i3 I · I": j IVJ "7 II '2-Y7- ~n. '}·n <.I 7 I 

1.- 1\'1.:)1 , · Ie , I ~(j <- . , ~ £) 

D \~o·-' )('14. 4?A I • .:;,"1-

Average: 

AMBIENT TEMPERATURE: (.21) 

BAROMETRIC PRESSURE-: --'"-:·z;;;'1"'1"'L/ ,,-------

ASSUMED MOISTURE: ~11J'7< 

PITOT TUBE COEFF, C-p-: -:(::-)."''\-;;''',---"'-'''--- ----

PROBE 10 NOIMATERIAL: !!:CUD$. "o,Y"'2 

PROBE LENGTH:,.,-::1'"='=-:---:-= ____________ ___ 

NOZZLE 

NOZZLE DIAMETER

10 NOI MATERIAL:

: ___ f'-- ':-"-!(

~ 

'-', ·, _____________ _ 

FILTER NOrTYPE: NH 

PRE -TEST LEAK R=-A:-:T==Eo-: -': --' .,>-c"'o"'·/..--C"'F"'MC:-@-:::-:-:-:' S-- =-~in-. HC:-g- .-

POST-TEST LEAK RATE: :t, r "- CFM@ " in. Hg. 

PITOT LEAK CHECK, PRE: ! --= POST: I-----

CHAIN OF CUSTODY: SAMPLE CUSTODIAN~ 

SAMPLER f,-IA ,\1'" 

SAMPLE CUSTODIAN 10.( 

IIH Stack Probe Filter Imp. Out 

in. H2O Temp, OF Te "p, OF Tem , oF Temp, OF 

\' ') 7'11 .M .;r !VI, 5"" 0 

./ .. I 

7¥L 

7J" 0 

t· ~ 7fl '\1 "7 ~ 2.... 

NJ 

.,( I 

1,'- •• <0 5"" \ 

7 S" Z 

7J 2-

'7" / 

\. ') -; h 2- <;2..... 

7 \ L. 

-;1 3 . 

7 of 1 

-_ .. _- - _t*' 'l. 

Imp. # Contents Post-Test - Pre-Test = Difference 

I),IV It Y)'1 ~(,2, b £:''87,3 

.3:.. 0 \ IJ 111 '11,/ Cd? ~ ,1) bbl. / 

:> e q1'"'-1 ~<6'V , ~ Y "67, ?::> 

I C{(t(, ,5" .'::L <C/), '10<0, 2 

1:3- DSltz.,U \ () \) 

Total: ___________ _ 

Meter Temp, OF Vacuum 0 2 P. static I 

In Out in. Hg. % in. H2O 

'1l'1 1 -1 i 2 L/ 

f 

12- -N 

6'5 .'Y " ) 

~x I, '\ 

"-

V 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 112512013 Page __ of __ 

DS834049 

Master Document Storagel Formsl Datasheetsl Field Datasheets 
Della;). 

~-

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: C:::ltM"'ALOCATION: <-.Ervr,,JA \ Ll 

DATE: '"-1,2..1 \<, 

RUN NO: ;, - '-\ 7\11--1\/tf-1 " -...;) .2-

OPERATOR: f-M. .\ "" METERBOX~N~O~:~~~~~~------

METER t.H@:.~1 iI,,,,-\'f 'l ------ METER Yd: 0 .• \~ 1-

STACK AREA, FT': 1'1'-, '1 

TRAVERSE POI NT"'S'-J, '"'M::-:I N7./=PO=1 N"'TC": =-r./ "";z..-

t.H= 111- X t.P: ' 

Probe ondition, pre/post test: /,/ 

Silica Gel Expanded, YIN: (VI'.--

Filter Condition after Test: ¥ 

Check Weight: ______ _ 

Meter t.P 

Point Time Volume, ft3 in. H2O 

S ') i~ 3 ( J 3''l~ ~C\' , .J , 

2- ~' ,. , (P' '', 

\ I, y o • (., <%, 0 nt)- Cl,1J1.>.1.1 1 • t; ..... 

~ ." \ 1, '-''6 'Iq, '2..'13 ' c.~",'f" 

2- \ "> <;" , S·L. 

I ,,\ ''is , , S '-f ~ I 'l ~ '\\(. ,~i1 ' S 2-

" 5 ,'<. (, '\ \1. , 51) . ,-1' 

, ....... v 

? \ 't, I ; ,<; 0 

( 14 ! {' ). ':- c! 

u j 4- 7. 1 '11.:T II'1 I . '(-: 

'" 2, ,ct'). c( "'f 2:1 · i 1 y.. (if 

L i '-iZ,q · So) 

\ Ii.( 2,-.i ~ 0, 

V ,(~"i " '> 1-"X'3(. I ' I c.., 

AveraQe: 

AMBIENT TEMPERATURE: (.,-D BAROM ETRIC PRESSURE :---''''"''1T- Z , ""14"' · -------

ASSUMED MOISTURE: lif4 

PITOT TUBE COEFF, C:-p-: - 0::-:";;' " "".----------

PROBE ID NO/MATERIAL:#S", · ,-,,,-,-- ,,-,-",Q ______ _ 

PROBE LENGTH: '7' NOZZLEIDNO M~A~T=E~R~IA -: --------

NOZZLE DIAMETER:---,;-';-: C';t-r'f-'--________ _ 

FILTER NO/TYPE: "-! 4,-

PRE· TEST LEAK R=-CA"'T==E"': "': '-;~ ' '2- ,......,C"'F=:M7 @;O:-I"'.,=----,ic--n--: . H-;-g-. 

POST·TEST LEAK RATE: : Lo.o''L CFM@ IS- in. Hg. 

PITOT LEAK CHECK· PRE: L.--- POST: __ J_ 

Imp. # Contents Post·Test· Pre·Test = Difference 

I V IN ff k 5fJ'f 'bY ~ ,1- (Q "bOo 'b 

t 6. /1\1 H,5ii'v; 65"5. D 0SF3 

') f'-(24t 5 '3 {i, 1 5'1.;C,,) 

vi 5·G-1. 1>5'6, j 'B Ytj,) 

LA ... III \/0 () [0 CI 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN,-:-':-A...;: '-'--__ 

SAMPLER (Z..M .)-IV' 

SAMPLE CUSTODIAN,-.:M.:.:L==--_ _ Total: _____________ _ 

t.H Stack Probe Filter Imp, Out Meter Temp, OF Vacuum 0 , P. static 

in. H2O Temp, OF Temp, OF Temp, OF Temp, OF In Out in. Hg. % in. H2O 

L'i 7 '6' rJ( j),- !VIA .:sS- 7') '7/ 7" 1"2. '1 

'7 , 0 

~'?~ 

7 e1 v 

j,) 7 <i , 5(' ",,\ 1>&\ '-t '7 '1 'I' 

7 <1 '> 

7"( "2-

\' ) -/ c: ~ S-q ~ (, ~ cj ....... '·1 (;. 

.', (;, 

";,;" J 

S '7 ,oJ ') (;0 '1 0 (,,", '-\ 

7"; ) 

7 '7(, 

'1' « 

I II ~ 

l\I . I 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 1/25/2013 Page __ of __ 

DS834049 

Master Document StoragelFormsl DatasheetslField Datasheets 
WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: C:::1f{ll\V\/T' 

LOCATION: XN\L'" ~\ 

DATE:?. !..L:?- Iy 

RUN NO: S ~ '1 !)I It.. - ful_\) Q,1,'kA'~L. - NH:<, 

OPERATOR:=,-,,-,.,.. _____ _ 

METER BOX NO:_ "'? "Vc..:"' 2-____ _ 

~~i~~ ~~@-,~\ . .:,-;'!';:"~iCL;;.------- STACK AREA, FT': TRAVERSE POI NT~S::-, 7M"'1 N:7I

:-:: P"'O"'IN"'T;-:--

Ll.H= __ XLl.P: 

Probe Condition, prelpost tesl: ____ _ 

Silica Gel Expanded, YIN: ____ _ _ 

Filter Condition after T esl: _____ _ 

Check Weighl: _________ _ 

Meter Ll.P 

Point Time Volume, ft' in. H2O 

Average: - - -

AMBIENT TEMPERATURE: ':;-.0 BAROMETRIC PRESSURE:-: ----''-'''''------- -

ASSUMED MOISTURE: 

PITOT TUBE COEFF, C'-p-: -0:-.""""'1--------

PROBE ID NOIMATERIAL:r-'lSi;y.~?='8 ________ _ 

PROBE LENGTH: 1 

NOZZLE ID NOI M''''A'''T=E-=R'''IA'::-L- : -tJ"r"''I-:--- ------

NOZZLE DIAMETER:_,-;N-,\{It""-T_---------

FILTER NOfTYPE: NI'f' 

PRE-TEST LEAK R"'A"'T"'E"' : "': -i[.'::-e :-<o:1')...-:-;;C"' F .. Mc;;@::--"'I$'"~-ci::-n ...,HO:g:-. -

POST-TEST LEAK RATE: : <0. d2 __ CFM@ '''' in. Hg. 

PITOT LEAK CHECK - PRE: V POST: <.---

CHAIN OF CUSTODY: SAMPLE CUSTODIAN ML 

SAMPLER 

SAMPLE C<;-U"'S""T""O;:CDIC;;-A"'N-,,,,( :-:---

6H Stack Probe Filter Imp. Out 

in. H2O Temp, OF Temp, OF Temp, OF Temp. OF 

Imp. # Contents Post-Test - Pre-Test = Difference 

(j . \ .Iv HJ S0'1 7'b), 2. 1,'07.3:, 

'l.... 0 \ rv HJ 10,! bSq,) (';'5'<1, S-

') M1 571, "1 5 7'[,'1 -

.:L 5· 0i . qq 2./1 '11/,15 

l..vl Of 1-11. 0 10 () 

Total: _____________ _ 

Meter Temp, OF Vacuum 02 P. static 

In Out in. Hg. % in. H2O 

I 

Comments: ________________________________________ __________________ _ 

Date of last revision 112512013 Page __ of __ 

D8834049 

Master Document StoragelFormslDatasheetslField Datasheets 
AMMONIA ELECTRODE CALIBRATION CURVE 

"ample t<oom 

NH3 concentration log NH3 concentration Electrode potential Temperature Temperature 

(~g NH3 1 ml as N) (mV) (C) (C) 

t 0.000 90.8 23.2 23.2 

5 0.699 53.1 23.2 23.2 

20 1.301 18.6 23.2 23.2 

100 2.000 -22.2 23.2 23.2 

Ammonia Electrode Calibration Curve y = -56.5667< + 91 .6417 

2/13/2013 R' = 0.9996 

100.0 

;;- 80.0 

.§. 

.. 60.0 

'" I: 

" 40.0 -0 

11. 

" 20.0 "C 

0 

~ 

-... 0.0 

iii " -20.S' 00 0.500 1.000 1.500 ~OO 

-40.0 

logarithm of the concentration of ammonia (~g NH,I ml as N) 

slope 

V-intercept 

Concentration 

("9 NH31 ml as N) 

1 

5 

20 

100 

Calculation: 

-56.5667 

91 .6417 

Value LR line 

10349 

4.8012 

19.5546 

102.9250 

Regression Line: P=M'log("g of NH,I ml as N)+B 

Difference 

0.0349 

-0.1988 

-0.4454 

2.9250 

Measured Concentration of Ammonia (C) in "g 1 ml NH3 as N: C=10,P.8VM 

where P = electrode potential, M= slope (must be -57±3) and B= intercept 

% Difference 

3.4857 

-3.9760 

-2.2270 

2.9250 

All standards were prepared in 0.04N H2S04 and allowed to equilibrate to room temperature. 

2. 00 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS CALCULATION 

Client! Location: 

Sample Location: 

District Method: 

Sample Date: 

Analysis Date: 

Analyst's Initials: 

Calibration Curve: 

R' 

Sample 

Sentinel 

Unit 4 100% 

SCAQMD 207.1 

2/12/2013 

2/13/2013 

RF 

y= -56.5667 x+ 91 .6417 

0.9996 

P Conc. 

mV g NH3/ml as N 

28 ug NH3/ ml as N 10.4 

r~-"at 28 ug NH3/ml as N 10.6 

1-NH3 -100-1 64.2 

repeat 1- NH3-100-1 65.0 

2-NH3 - 100-1 619 

repeat 2- NH3 -100-1 62.2 

spike 2-NH3 100-1 15.6 

repeat spike 15.6 

28 NH3/ml as N 10.7 

repeat 28 UQ NH3/ml as N 10.7 

Reagent Blank 145.6 

repeat Reagent Blank 145.0 

Field Blank 125.8 

repeat Field Blank 126.1 

DI H20 Blank 147.5 

Repeat DI H20 Blank 146.9 

28 NH3/mt as N 11 .8 

r~at 28 ug NH3Iml as N 11.7 

Notes: 

Measured Concentration of Ammonia (C) in ~g NH3/ ml as N 

C= 1 O(P-8)/M 

P = electrode potential (mV), M=slope and B=intercept 

27.303 

27.082 

3.056 

2.958 

3.356 

3.315 

22.094 

22.094 

26.972 

26.972 

0.111 

0.114 

0.249 

0.246 

0.103 

0.105 

25.791 

25.896 

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 

~g NH3 1 sample = Cavg (~g NH,Iml as NH3) • TV 

Used 100 ml of samples and standards with 2 ml ISA and constant stirring rate. 

All solutions turned blue and remained blue with ISA unless otherwise indicated. 

Sample PH and Temperatures can be found on the laboratory datasheet. 

CavgasN 

27.192 

3.007 

3.335 

22.094 

26.972 

0.1126 

0.2475 

0.1042 

25.843 

Maximum samples (including blanks) between 28 ug/ml check standard is 5 samples 

analyzed in duplicate. 

TV C avg as NH3 ~9 NH,I 

(ml) sample 

NA 33 .054 NA 

610 3.655 2229 .534 

600 4.054 2432.571 

NA 26.857 NA 

NA 32 .786 NA 

NA 0.137 NA 

405 0.301 121 .823 

NA 0.127 NA 

NA 31.414 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 NH3 1 ml as N 

repeat 28 ug NH3/ml as N 

1-NH3 -100-1 

repeat 1- NH3 -100-1 

2-NH3 -100-1 

repeat 2- NH3 -100-1 

spike 2-NH3 100-1 

repeat spike 

28 NH3/ml as N 

repeat 28 ug NH3/ml as N 

Reagent Blank 

repeat Reagent Blank 

Field Blank 

repeat Field Blank 

DI H20 Blank 

Repeat DI H20 Blank 

28 NH3/ml as N 

repeat 28 ug NH3/ml as N 

Notes: 

Sentinel 

Unit4100% 

SCAQMD 207.1 

2/12/2013 

2/13/2013 

RF 

% recovery 

NA 

NA 

NA 

97.88 

NA 

NA 

NA 

NA 

NA 

spike: 100 ml sample + 2 ml (1000 fIg NH3 1 ml as N) 

Matrix Spike Percent Recovery (%R) 

%R = (C spike*O 104 - Csample*0.1 02)/2 *100 

Cspike = average result of matrix spike (fIg NH31 ml as N) 

RPD 

% 

0.81 

3.26 

1.22 

0.00 

0.00 

-2.44 

1.22 

-2.44 

-0.41 

RPA 

% 

-2.885 

NA 

NA 

NA 

-3.673 

NA 

NA 

NA 

-7.703 

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-theoretical value of standard)1 theoretical value of standard * 100 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project #: ______ District Method: SCAQMD 207.1 Sample Date: ?/12/13 

ClienllLocation: S(01.iOe. f Calibration Date: ~! /13 Analysis Date: Z./l3/13 

Sample Location: Una:; L.( Calibration Curve:V-~.~1 X ~ +9/. "'IN Analyst's Initials: R r 

-,rO/ 2 0 "-90 Test #'s: __ ++-""':::!..Lc.!?.2...-__ R : • 7 'f 

Sample Electrode TV Cone. Cavg fl9 NH31 Commentsl Temp/pH 

Potential (ml) fl9 NH3- (fl9 NH3 sample 

(mV) N Iml - N I mil 

Standard Check: Percent Recovery: 

28 J.Jg NH,Iml IO·V n. 303 

Repeat 28 1&.(, 21. Ml nJ'r. 2-

/- f/!/, - f(X:) - I (.'(.1. "3. os," 

&cct /JI/h /00 - \ (,5,-0 (Plo 2J1!:>""f :? ·coer 221. 1.!) pH <. 2. T:::23.L( 

2·#1/, - lro - I (,1-"( <. ~,,(. 

1f6Jl.d 2##, ICfJ - I {.. 2..J. Iboo 3·3/5" 3- 3~S- 2 '132. S; I "Ii <:. 2.. 7"='1.32. ( 

~ /),'Ile. 2.. il;, 1M - 1 I S.(,. 2. 7. ·01'1 

n. J _'5/)/1(, {S.c, 22.di'-/ 22.6'N re.. r rfl>etl/::'t,j' ,tt o 

2fUIL ID.1- 2('·171 

ro:·_~tV 2J. k'6~ to. 1 2~.111. Kent 

ne.a o.no./- p.~K. Iqs.~ 1'>.111 I A II ~oL t. i Crtt,5 

IJ: ~~ RfJ. 11./5.0 CJ. /J '{ o. ft2r: -k,·kJ c..C 

fi~ fd, n Ir.N>1<. 125-8' ().1'fC, 23.2- 0 

c.. 

!/2 'At',c ~ A /7.(,.( D.Nr. o. ),475 

IDlJ ;r-, A{c,y.,k.. I~T'S ID.l03 

I~ ~ //2,.:1: IY /1.0 t3 I K. 1"1 (,. ~ O·lb:> D ./OL{2... 

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: Cone. (fl9 NH3 - N 1 ml) = 10 (P-B)IM 

P = electrode potential, B = y·intercept and M = slope 

Cavg = average result of duplicate analyses (fl9 NH, - N I ml) = (C1 +C2)/2 

flg NH31 sample = Cavg* 17.03/14.01 * TV 

mg I sample = fl9 Isample -;- 1000 

ppm NH3 = mg NH,Isample x 1Nmstd x 1/454000 x SVI17 x 10· 

8e//a~ .-~- DS834059 

Date of last revision 12/5/2008 Master Document StoragelFormslDatasheetslLab Forms 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project#: _______ District Method: SCAQMD 207.1 Sample Date: .:? /lzJ/3 

Client/Location: Seat" 1\ e. ( Calibration Date: 2.1/3//'~ Analysis Date: 2/13 /13 

Sample Location: U()/t~1 Calibration Curve: _________ Analyst's Initials: R:lTest #'s: IDo /0 R2: ------

Sample Electrode TV Cone. Cavg g NH31 Commentsl Temp/pH 

Potential (ml) ~g NH3- ~g NH3 sample 

(mV) N I ml - N I ml-) 

Standard Check: Percent Recovery: 

28 ~g NH,Iml 

/I.~ ZS.11/ 

Repeat 28 Ji.1 2S .5Qt; 2s.N.? 

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. (~g NH3 - N I ml) = 10 (P·B)IM 

P = electrode potential, B = y-intercept and M = slope 

Cavg = average result of duplicate analyses (~g NH3 - N I ml) = (Cl+C2)/2 

~g NH3 1 sample = Cavg* 17.03/14.01 * TV 

mg I sample = ~g Isample .,. 1000 

ppm NH3 = mg NH,Isample x lNmstd x 1/454000 x SV/17 x 10· 

Del/a!'1 .......... - .- ..... 

Date of last revision 12/5/2008 

DS834059 

Master Document StoragelFormslDatasheetslLab Forms 
AMMONIA ELECTRODE CALIBRATION CURVE 

Sample Room 

NH3 concentration log NH3 concentration Electrode potential Temperature Temperature 

(~g NH3 1 ml as N) (mV) (C) (C) 

1 0.000 90.8 23.2 23.2 

5 0.699 53.1 23.2 23.2 

20 1.301 18.6 23.2 23.2 

100 2.000 -22.2 23.2 23.2 

Ammonia Electrode Calibration Curve y = -56.5667x + 91 .6417 

2113/2013 R' = 0.9996 

100.0 

S- 80.0 

.s 

n; 60.0 :;:; 

$ " 40.0 

0 

II. 

" 20.0 ." 

0 

- 0.0 ~ 

<) 

" iii -20.B - 00 0.500 1.000 1.500 000 2. 00 

-40.0 

logarithm of the concentration of ammonia (I'g NH31 ml as N) 

slope 

y-intercept 

Concentration 

(I'g NH31 ml as N) 

1 

5 

20 

100 

Calculation: 

-56.5667 

91.6417 

Value LR line 

1.0349 

4.8012 

19.5546 

102.9250 

Regression Line: P=M'log(~g of NH,t ml as N)+B 

Difference 

0.0349 

-0.1988 

-0.4454 

2.9250 

Measured Concentration of Ammonia (C) in ~g 1 ml NH3 as N: C=10(p·B)lM 

where P = electrode potential, M= slope (must be -57±3) and B= intercept 

% Difference 

3.4857 

-3.9760 

-2.2270 

2.9250 

All standards were prepared in 0.04N H2S04 and allowed to equilibrate to room temperature. 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS CALCULATION 

ClienV Location: 

Sample Location: 

District Method: 

Sample Date: 

Analysis Date: 

Analyst's Initials: 

Calibration Curve: 

R' 

Sample 

Sentinel 

Unit4 75% 

SCAQMD 207.1 

2/12/2013 

2/13/2013 

RF 

y= -56.5667 x+ 91.6417 

0.9996 

P Conc. 

mV ~g NH3/ml as N 

28 ug NH3 / ml as N 10.3 

reDeat 28 UQ NH3/ml as N 10.4 

l-NH3 -75-1 86.0 

repeat 1- NH3 -75-1 86.1 

2-NH3 -75-1 89.3 

repeat 2- NH3 -75-1 89.2 

spike 2-NH3 75-1 17.9 

repeat spike 18.0 

28 NH3/ml as N 10.4 

repeat 28 UQ NH3/ml as N 10.6 

Reagent Blank 145.6 

repeat Reagent Blank 145.0 

Field Blank 125.8 

repeat Field Blank 126.1 

DI H20 Blank 147.5 

Repeat 01 H20 Blank 146.9 

28 NH3/ml as N 11.8 

repeat 28 uq NH3/ml as N 11.7 

Notes: 

Measured Concentration of Ammonia (C) in )19 NH31 ml as N 

C= 1 O{P-B)IM 

P = electrode potential (mV), M=slope and B=intercept 

27.414 

27.303 

1.258 

1.253 

1.100 

1.104 

20.120 

20.038 

27.303 

27.082 

0.111 

0.114 

0.249 

0.246 

0.103 

0.105 

25.791 

25.896 

Average Measured Ammonia Concentration (Cavg) = (Cl + C2)/2 

where C1, C2 results from duplicate analyses (l1g NH3/ml as N) 

Cavg ("9 NH,Jml as NH3) = Cavg (~g NH31 ml as N) '17.03/14.01 

I1g NH3/ sample = Cavg (l1g NH:yml as NH3) ... TV 

Used 100 ml of samples and standards with 2 mllSA and constant stirring rate. 

All solutions turned blue and remained blue with ISA unless otherwise indicated. 

Sample PH and Temperatures can be found on the laboratory datasheet. 

CavgasN 

27.359 

1.256 

1.102 

20.079 

27.192 

0.1126 

0.2475 

0.1042 

25.843 

Maximum samples (including blanks) between 28 ug/ml check standard is 5 samples 

analyzed in duplicate. 

TV C avg as NH3 ~g NH31 

(ml) sample 

NA 33.256 NA 

610 1.526 931.021 

580 1.340 777.118 

NA 24.407 NA 

NA 33.054 NA 

NA 0.137 NA 

405 0.301 121.823 

NA 0.127 NA 

NA 31.414 NA 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS QUALITY CONTROL 

Client! Location: 

Sample Location: 

District Method: 

Sample Date: 

Analysis Date: 

Analyst's Initials: 

Sample 

28 ug NH3 1 ml as N 

repeat 28 ug NH3/ml as N 

1-NH3 -75-1 

repeat 1- NH3 -75-1 

2-NH3 -75-1 

repeat 2- NH3 -75-1 

spike 2-NH3 75-1 

repeat spike 

28 NH3/ml as N 

repeat 28 ug NH3/ml as N 

Reagent Blank 

repeat Reagent Blank 

Field Blank 

repeat Field Blank 

DI H20 Blank 

Repeat DI H20 Blank 

28 NH3/ml as N 

repeat 28 ug NH3/ml as N 

Notes: 

Sentinel 

Unit 4 75% 

SCAQMD 207.1 

2/12/2013 

2/13/2013 

RF 

% recovery 

NA 

NA 

NA 

98.79 

NA 

NA 

NA 

NA 

NA 

spike: 100 ml sample + 2 ml (1000 }1g 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 (}1g NH31 ml as N) 

RPD 

% 

0.41 

0.41 

-0.41 

0.41 

0.81 

-2.44 

1.22 

-2.44 

-0.41 

RPA 

% 

-2.290 

NA 

NA 

NA 

-2.885 

NA 

NA 

NA 

-7.703 

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-theoretical value of standard)1 theoretical value of standard * 100 
Oel/aJi 

AIr a....lity s.Mc.I. In«IrpGI'II!o1j 

AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project #: _______ District Method: SCAQMD 207.1 Sample Date: 2/;2./13 

ClientlLocation: Sf-oil oe. ( Calibration Date: ~ I!.Vi 3 Analysis Date: Z./l3/<3 

Sample Location: ul)a: (I Calibration Curve:y--.st::.6U7 X'+9/. t 111 Analyst's Initials: R r 

Test#·s ~50~ 2" Co : ___ .:...=7,..!../.::.e~ __ R: • 779£ 

Sample Electrode TV Cone. Cavg fig NH31 Commentsl Temp/pH 

Potential (ml) fig NH3- (fig NH3 sample 

(mV) N Iml - N I ml-) 

Standard Check: Percent Recovery: 

28 ~g NHsfml 

/0·3 27.'fN 

Repeat 28 ID.L.{ 2";1.303 71· 355-

1- .NI/, - 7':, - I g·o I· 26f 

~cci I N~ 75; - \ ~&'I (plo J.153 I. Zsc. <131. () pH < 2- T~23·1.. ( 

2,·111/, - tS- - I ~·3 /. Jot> 

1.Q~ct zN'4-t5-1 ~ft,2. Sfo J. /61.( I.J at pl./ <:. 1.. T=" 2n .. ( 

flp,'t(1!.. 2... A/II, 7[; - I li·9 20.llC 

f)~""A- ~IKI!.. Jf·o 2o·o3J- 2e>· 0"19 ieCCNeN =-77 ' 

2fAlI'/. lo.y n. 3(;>.1 

~ API'j' 2 f J/I/, JO.(; 27.oh. 2f./9l 

I?G ''.'If. pJ()vo.1( Il.Is.(. D. I \ I IA I { soLl.i 0>1.5 

~ ~d R/j I~S.o 6. II"! C>./IU u..st.c.J 6. tfie.ld P./fMK 125.g t; . 2. '/9 13-2.°(.. 

O.M,-i: F IJ J2~. I O,2.'IC 0,2'11.5 

lilll ~6 fj{CMK. l'ft.oS D·IO] 

IN '.,4;?G-f Ii /ho /j J K.. 1"I(."e, 0.10S' O./D'/Z. 

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 NH3 - N I ml) = 10 (p·81IM 

P = electrode potential. B = y-intercept and M = slope 

Cavg = average result of duplicate analyses (fig NH3 - N I ml) = (C1 +C2)/2 

fig NH31 sample = Cavg* 17.03/14.01 * TV 

mg I sample = fig Isample .,. 1000 

ppm NH3 = mg NHslsample x 1Nmstd x 1/454000 x SV/17 x 106 

Oe/lal'1 

---- DS834059 

Date of last revision 12/5/2008 Master Document StoragelFormslDatasheetslLab Forms 

~ 

° 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project #: _______ District Method: SCAQMD 207.1 Sample Date: 2. /12./13 

ClienVLocation: Seat,' 1\ e. t Calibration Date: 2. 1;3/13 Analysis Date: .2 /13 /13 

Sample Location: Un/I: 'I Calibration Curve: _________ ,Analyst's Initials: Rr 

'"::1r 010 ' Test #'s: I:::' t.:. R : 

------

Sample Electrode TV Cone. Cavg flg NH31 Commentsl Temp/pH 

Potential (ml) flg NH3- (fl9 NH3 sample 

(mV) N Iml - N I ml) 

Standard Check: Percent Recovery: 

28 ~g NH,tml 

I/.~ 25· 7"1/ 

Repeat 28 //.1 21>. H', 25. f't? 

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. (fl9 NH3 - N I ml) = 10 (p·S)IM 

P = electrode potential, B = y-intercept and M = slope 

Cavg = average result of duplicate analyses (fl9 NH3 - N I ml) = (C1+C2)/2 

fl9 NH3 1 sample = Cavg* 17.03/14.01 * TV 

mg I sample = flg Isample .. 1000 

ppm NH3 = mg NH,tsample x 1Nmstd x 1/454000 x SV/17 x 106 

Del/atl 

---- DS834059 

Date of last revision 12/5/2008 Master Document StoragelFormslDatasheetslLab Forms 
AMMONIA ELECTRODE CALIBRATION CURVE 

Sample Room 

NH3 concentration log NH, concentralion Electrode potential Temperature Temperature 

(~ g NH, I ml as N) (mV) (C) (C) 

1 0.000 90.8 23.2 23. 2 

5 0.699 53.1 23.2 23.2 

20 1.301 18.6 23.2 23.2 

100 2.000 -22.2 23.2 23.2 

Ammonia Electrode Calibration Curve y = -56.5667x + 91 .6417 

2/13/2013 R' = 0.9996 

100.0 

> 80.0 

.§. 

l! 60.0 

1: 

$ 

0 

40.0 

Il. 

., 20.0 "C 

0 

~ 

U 0.0 

1.500 ~OO ., 

iii -20.&( 00 0.500 1.000 

-40.0 

logarithm of the concentration of ammonia (I'g NH,' ml as N) 

slope 

y-inlercepl 

Can central ion 

(I'g NH, I ml as N) 

1 

5 

20 

100 

Calculation: 

-56.5667 

91 .6417 

Value LR line 

1.0349 

4.8012 

19.5546 

102.9250 

Regression Line: P=M'log ~g of NH,I ml as N)+B 

Difference 

0.0349 

-0.1988 

-0.4454 

2.9250 

Measured Concentration of Ammonia (C) in g 1 ml NH, as N: C=10IP-BlIM 

where P = electrode potential, M= slope (musl be -57±3) and B= inlercept 

% Difference 

3.4857 

-3.9760 

-2.2270 

2.9250 

All standards were prepared in 0.04N H2SO, and allowed 10 equilibrate 10 room temperature. 

2. 00 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS CALCULATION 

ClienV Location: 

Sample Location: 

District Method: 

Sample Date: 

Analysis Date: 

Analyst's Initials: 

Calibration Curve: 

R' 

Sample 

Sentinel 

Unit4 50% 

SCAQMD 207.1 

2/12/2013 

2/13/2013 

RF 

y= -56.5667x+ 91.6417 

0.9996 

p Conc. 

mV ).19 NH3/ml as N 

~ 

Measured Concentration of Ammonia (C) in ).19 NH3 1 ml as N 

C=10(P-8)1M 

P = electrode potential (mV), M=slope and B=intercept 

Average Measured Ammonia Concentration (Cavg) = (C1 + C2)12 

where C1 , C2 results from duplicate analyses (1-19 NH3/ml as N) 

Cavg (~g NH,iml as NH3) = Cavg (~g NH31 ml as N)' 17.03/14.01 

~g NH,I sample = Cavg (~g NH,iml as NH,) • TV 

Used 100 ml of samples and standards with 2 mllSA and constant stirring rate. 

All solutions turned blue and remained blue with ISA unless otherwise indicated. 

Sample PH and Temperatures can be found on the laboratory datasheet. 

C avg as N 

Maximum samples (including blanks) between 28 ug/ml check standard is 5 samples 

analyzed in duplicate. 

TV C avg as ~g NH,t 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS QUALITY CONTROL 

Client! 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-NH3 -50-1 

repeat 1- NH3 -50-1 

2-NH3 -50-1 

repeat 2- NH3 -50-1 

spike 2-NH3 50-1 

repeat spike 

28 NH3/ml as N 

repeat 28 ug NH3/ml as N 

Reagent Blank 

repeat Reagent Blank 

Field Blank 

repeat Field Blank 

01 H20 Blank 

Repeat 01 H20 Blank 

28 NH3/ml as N 

repeat 28 ug NH3/ml as N 

Notes: 

Sentinel 

Unit 4 50% 

SCAQMD 207.1 

2/12/2013 

2/13/2013 

RF 

% recovery 

NA 

NA 

NA 

99.28 

NA 

NA 

NA 

NA 

NA 

spike: 100 ml sample + 2 ml (1000 I1g 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 (l1g NH 31 ml as N) 

RPD 

% 

0.00 

3.26 

-4.07 

-041 

041 

-244 

1.22 

-244 

-041 

RPA 

% 

-0484 

NA 

NA 

NA 

-2.290 

NA 

NA 

NA 

-7.703 

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-theoretical value of standard)1 theoretical value of standard' 100 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project#: ______ District Method: SCAQMD 207.1 Sample Date: 21 /13 

Client/Location: SCD-/.ioe. ( Calibration Date: ;;;:! /13 Analysis Date: Z./13/13 

Sample Location: UI);';; J.( Calibration Curve:y:~.6U7X~+9/. ~fl1 Analyst's Initials: R7 

'-'0 o~, 2 0 9 Test #'s: .J /(., R : • 7'1'f 

Sample 

Standard Check: 

28 I1g NH,Iml 

Repeat 28 

/- .HI/, - So - I 

2.·N~ - So - I 

2CJI1) 

lieM, J>.. / t:N.1<. 

Electrode 

Potential 

(mV) 

11.f 

/O.'{ 

ILl5., 

/l{6 .0 

12(,. I 

TV 

(ml) 

S'lo 

Cone. 

~g NH3 -

N 1 ml 

Cavg 

(~g NH3 

- N 1 mil 

27. sr,</ 21. fC.({ 

I. JD'{ 

D~7 j,of.1 

/.ISc 

2e:> . 202. 

0. /11 

o.IN /I7.~ 

D, /OJ 

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. (~g NH3 - N 1 ml) = 10 (p.B)/M 

P = electrode potential, B = y-intercept and M = slope 

~g NH31 

sample 

pis . C 

Commentsl Temp/pH 

Percent Recovery: 

23 . 2... 0 L 

Cavg = average result of duplicate analyses (f!g NH3 - N 1 ml) = (C1 +C2)/2 

~g NH31 sample = Cavg' 17.03/14.01 • TV 

mg 1 sample = ~g Isample + 1000 

ppm NH3 = mg NH,Isample x 1Nmstd x 1/454000 x SV/17 x 106 

De/lab. 

----- DS834059 

Date of last revision 12/5/2008 Master Document StoragelFormslDatasheetslLab Forms 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project #: _______ District Method: SCAQMD 207.1 Sample Date: ;( /12./13 

ClienULocation: Seot,' 1\ e. ( Calibration Date .2./13/13 Analysis Date: 2/13/13 

Sample Location: U()/t J./ Calibration Curve: _________ ,Analyst's Initials: & 

S

' ,-0/0 Test#'s: (//' R': 

-------

Sample Electrode TV Cone. Cavg fig NH31 Commentsl Temp/pH 

Potential (ml) fig NH3- (fig NH3 sample 

(mV) N/ml - N 1 ml) 

Standard Check: Percent Recovery: 

28 ~g NH,Iml 11·8- 2S.1'1( 

Repeat 28 11.l- 2.~. 4'1~ 2S'1'i~ 

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 NH3 - N 1 ml) = 10 (P-B)IM 

P = electrode potential, B = y-intercept and M = slope 

Cavg = average result of duplicate analyses (fig NH3 - N 1 ml) = (C1 +C2)/2 

fig NH31 sample = Cavg" 17.03/ 14 .01 • TV 

mg 1 sample = fig Isample -<- 1000 

ppm NH3 = mg NH,Isample x 1Nmstd x 1/454000 x SV/17 x 106 

.. Della~ __ ........... 

Date of last revision 12/5/2008 

DS834059 

Master Document StoragelFormslDatasheetslLab Forms 
Appendix C.4 SOx by SCAQMD Method 307.91 

R041 0688 C-8 
Max 

Parameter Units Result Limit Rule 

Ib/MM8tu 0.00002 0.06 40 CFR 60 

Ib/MMsef 0.025 0.67 Rule 2011 

SO, grH2S/100sef 0.009 0.25 SCAQMD Permit 861.1 
Sentinel 4 Fuel Analysis and Sulfur Calcs 

Sulfur 

Client 

Facility 

Unit 

Gemma 

CPV Sentinel 

4 

CPV Sentinel-4 - - Fuel 1&2 

HHV 

Fuel Sulfur Content, (BTU/ft3 MW MW 

ppmv @60F) (H2S) (S02) 

Result < 0.15 1021.4 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 scI = ppmv lue1/10'6 x MW (H2S)/SV x 10'6 

Ib-S02/MMBtu = ppm lue1/10'6 x MW (S02)/SV/HHV x 10'6 

(Specific 

Molar 

Volume@ 

60F) 

379.5 

grllb 

7,000 

gr-H2S/100 

scI 

0.009 

0.25 

SCAQMD 

Permit, 

B61.1 

IbsH2S/MMscl 

0.013 

0.690 

Rule 2011 

IbS02/MMBtu 

0.00002 

0.06 

40 CFR 60 

3/1/20t3 

10:56 AM 
Client 

Facility 

Unit 

Load, 

MW 

106.5 

Gemma 

CPV Sentinel 

4 

Fuel Sulfur Content, 

ppm 

<1 0.15 

Sentinel 4 Fuel Analysis and Sulfur Cales 

SOx 

CPV Sentinel-4-Fuel-1 &2 

Specific 

Molar 

Volume Stack 

(SV), Flow Rate Fuel Flow 

dscf/lb- (Qsd19), Rate, 

mol dscfm hscfih 02 Ib/hr, S02 

379.5 350,311 8845 12.99 0.02237 

S02 Ib/hr = (sulfur ppmv)/1 0'6 x (MW S02)/SV x hscf/hr x 100 scf/hscf 

ppm S02 = Ib/hr x SV/MW x 1/Qsd19 x 10'6/60 

Stack flow rate, fuel flow and 02 in conjuction with PM tests at 100% load condition 

ppmv@ 

ppmv 15% 02 

0.006 0.005 

S02, 

Ib/MMscfFuel 

0.025 

3/1/2013 

1056 AM 
Client 

Facility 

Unit 

Carbons 

1 

2 

2 

3 

3 

4 

4 

4 

4 

4 

4 

4 

5 

5 

6 

Gemma 

CPV Sentinel 

4 

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-4-Fuel-1&2 

1 2 Average 

detect? I MOLE % detect? I MOLE % detect? I MOLE % 

< 0.001 < 0.001 < 0.001 

0.469 0.452 0.461 

< 0.001 < 0.001 < 0.001 

2.634 2.774 2.704 

0.038 0.048 0.043 

92.299 92.073 92.186 

< 0.001 < 0.001 < 0.001 

3.904 3.957 3.931 

0.513 0.531 0.522 

< 0.001 < 0.001 < 0.001 

0.032 0.038 0.035 

0.069 0.084 0.077 

< 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 

0.016 0.013 0.015 

0.014 0.015 0.015 

0.011 0.014 0.013 

detect? ppm detect? ppm detect? ppm 

< 0.1 < 0.2 < 0.15 
FUEL F-FACTOR CALCULATIONS 

Client Gemma Unit 4 

Facility CPV Sentinel 

CPV Sentinel-4-Fuel-1&2 

SPECIES MW MOLE % MW*% HHV BTU/SCF C H 0 

CO2 44 0.461 20.27 0.06 0.00 0.15 

CO 28 0.001 0.03 321.0 0.003 0.00 0.00 0.00 

N2 28 2.704 75.75 0.00 0.00 0.00 

O2 32 0.043 1.38 0.00 0.00 0.01 

C, 16 92.186 1478.9 1012.0 932.92 11.06 3.69 0.00 

C2 30 3.932 118.22 1773.0 69.71 0.94 0.24 0.00 

C3 44 0.523 23.06 2524.0 13.20 0.19 0.04 0.00 

C. 58 0.117 6.76 32710 3.81 0.06 0.01 0.00 

Cs 72 0.029 2.09 3998.0 1.16 0.02 000 0.00 

C6+ 86 0.013 1.08 4743.0 0.59 0.01 000 0.00 

Ave. / Total 100.01 1630.12 1021.39 12.28 3.98 0.00 

Weight, % 99.74 75.31 24.43 0.00 

GasMW 16.30 

Btu/sef= 1021 @60F 

Btu/sef= 1037 @68F 

Btu/lb.= 23,779 

Ib.lsef= 0.0430 

Fd"(60)= 8,455 (02 Based) 

Fd"(68)= 8,585 

Fe"(60)= 1 ,001 CO2 Based) 

Fe"(68)= 1 ,017 

Calculations: 

Fd"(68) = 10A6 * [3.64 * (H%) + 1.53 * (C%) + 0.14 * (N%) - 0.46 * (0%)]1 HHV, Btu/lb 

Fd"(60) = Fd"(68) * 520 R 1 528 R 

Fe"(68) = 1 OA6 * [0.321 * (C%)] 1 HHV, Btu/lb 

Fe"(60) = Fe"(68) * 520 R 1528 R 

N 

0.00 

000 

0.76 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

000 
Sentinel 4 Fuel Analysis and Sulfur Cales 

F-Summary 

Client 

Facility 

Unit 

Gemma 

CPV Sentinel 

4 

CPV Sentinel-4-Fuel-1&2 

GasMW 16.30 

Btu/scf= 1,021 

Btu/scf= 1,037 

Btullb.= 23,779 

Ib.lscf= 0.04295 

Fd"(60)= 8,455 

Fd"(68)= 8,585 

Fc"(60)= 1 ,001 

Fc"(68)= 1 ,017 

3/112013 

10:56AM 
·t 

Parameter 

Fixed Gases 

HHV 

Sulfur 

Method No. 

ASTM 01945/1946 

ASTM 03588 

ASTM D5504/SCAQMD METHOD 307-91 

Method Title 

Analysis of Natural Gas/Reformed Gas by Gas Chromatography 

Calculating Heat Value, Compressibility Factor, and Relative Density of Gaseous Fuels 

Determination of Sulfur Compounds in Natural Gas and Gaseous Fuels by Gas 

Chromatography and Chemiluminescence/Determination of Sulfur In A Gaseous Malrix 
Appendix C.5 ROG by Modified SCAQMD Method 25.3 

R041 0688 C-g 
Client/Location Gemma CPV Sentinel 

Unit 4 

Sample Location Stack 

Test No. S-4/STK-ROG-100-1A 

Date 2111 /2013 

Test Method Modified SCAQMD 25.3 

Sample Time (HH:MM) 1 :17 

Start Time 10:06 

Stop Time 11 :23 

Stack O2 (%) 13.29 

Results 

Canister NMNEOC (ppm) 0.85 

ROG, ppm' 0.85 

ROG, ppm @ 15% O2 0.66 

RPD2

, % - 1) Includes bias correction of 1.086 

2) Relative percent difference less than 20% 

3) Samples were collected simultaneously as a pair 

Results reported at PQL 

Reference Temp (F) 60 

Data By AA, SS, RM, JM 

S-4/STK-ROG-100-1 B Average 

2/11 /2013 

Modified SCAQMD 25.3 

1 :17 

10:06 

11 :23 

13.29 

0.65 

0.65 0.75 

0.50 0.58 

- 13.3% 
Client/Location Gemma CPV Sentinel 

Unit 4 

Sample Location Stack 

Test No. S-4/STK-ROG-75-1A 

Date 2111/2013 

Test Method Modified SCAQMD 25.3 

Sample Time (HH:MM) 1:20 

Start Time 15:45 

Stop Time 17:05 

Stack O2 (%) 13.81 

Results 

Canister NMNEOC (ppm) 0.65 

ROG, ppm' 0.65 

ROG, ppm@15%02 0.54 

RPD2

, % - 1) Includes bias correction of 1,086 

2) Relative percent difference less than 20% 

3) Samples were collected simultaneously as a pair 

Results reported at PQL 

Reference Temp (F) 60 

Data By AA, SP, SS, JM 

S-4/STK-ROG-75-1 B Average 

2/11 /2013 

Modified SCAQMD 25.3 

1:20 

15:45 

17:05 

13.81 

0.70 

0.70 0.68 

0.58 0.56 

- 3.7% 
ClientiLocation Gemma GPV Sentinel 

Unit 4 

Sample Location Stack 

Test No, S-4/STK-ROG-50-1A 

Date 2112/2013 

Test Method Modified SGAOMD 25.3 

Sample Time (HH:MM) 1 :22 

Start Time 11 :58 

Stop Time 13:20 

Stack O2 (%) 14.27 

Results 

Canister NMNEOC (ppm) 0.69 

ROG, ppm' 0.69 

ROG, ppm@15%02 0.61 

RPD2

, % - 1) Includes bias correction of 1.086 

2) Relative percent difference less than 20% 

3) Samples were collected simultaneously as a pair 

Results reported at PQL 

Reference Temp (F) 60 

Data By AA, MG, RM, JM 

S-4/STK-ROG-50-1 B Average 

2/12/2013 

Modified SGAOMD 25.3 

1:22 

11 :58 

13:20 

14.27 

0.55 

0.55 0.62 

0.49 0.55 

- 11 .3% 
SCAQMD METHOD 25.3 

EVACUATED CANISTER SAMPLING DATA 

ClientlFacility:LlErt\iY!!\- /5cNf/." A '- Oate: __ ;)' .l. 13",--______ _ 

UnitlLocation: If»!"! 4-( S~f\lTiNA'- Performed By: __ '<_fI'\-'--_____ _ 

S Probe Material _____ <' :;;.. . I ::> _____ Probe Length __ -",.J"--_____ _ 

Connecting Tubing Material-,-:..:f1..L/.",A ___ Connecting Tubing Length",:,f1.!....!....« g"---__ _ 

/f cUt.-1 &5° Barometric Pressure __ u----'"_ I ____ .Ambient Temperature ______ _ 

Test No. I" -L{ Ln I< - V6(. -I~- S -'1lsr¥---IC!c - tJo-I t 

Vial 10 f'll<- {lfiQ. 

Canister 10 000 '-Di (JOO 0 LD ~ 

Time Vacuum Time Vacuum ~ime Vacuum 

Pre-Test Leak Start :;t.~ ~ 2(1 " Check O~w .;, '620 I 

Pre-Test Leak Stop ,\ 1."\' Check \ (/'5,:00 'd-CI. DC030 

Sample Start , ' Z - // Collection \ k. l ' ,) (0 '2'; /0. ~ ? 

.5 1 0 2..<0 2 !r /D.2Cc, .f \ 

L(/ pscJ 41 Izl So II Ie; \ 

/(IZ /'0 jJ/;Z Ie;' I 

Il) -

j .. - F' 0 t' 112;> /& /(2-) lu \ 

\ 

\ 

Sample Stop II ;.?~ 16 112'3 /Q Collection \ 

Post -Test Leak Start 

/ /)U Check 16 II) v /{.J i 

Post-Test Leak Stop il L/v' I (, 11(/ J /U Check \ 

\ 

Line Rinse / / / ~ \ Volume 

Comments: ________________________ _ 

Date of last revision 11/13/08 

05834043 

Master Document StoragelFormslDatasheetslField Datasheets 
SCAQMD METHOD 25.3 

EVACUATED CANISTER SAMPLING DATA 

Client/Facility: G€(v Iva it5i. l-t-:""A....{Date: .2 11/ / I 3 , ; I 

r 4,1 If(' /f? , ..,- ' / c3 :? ,; UnitlLocation:J - :-r. \ - 0.(jf..r - / ~- k' Performed By ,co/-o:...c.. /'-,-7j -f7,--_ ____ _ 

~ ~ ~ // Probe Material .: - Probe Length --:,L..{:. ,<.......!,"-' ------

Connecting Tubing Material,.,-_____ --- Connecting Tubing Length _____ -- _ 

Barometric pressure._-=l _

Cr...:.._( _L,( ____ .Ambient Temperature .5 c/' 

Test No, LL ?I 1.;""7 

," -=t IS/ 

ViaiiD J..-/ (VIY- I... [Vlf 

Canister ID / \, f/~-Ku& -/~ <::<;I51>( ./GL- -lS -15 

Time Vacuum Time Vacuum ime Vacuum 

Pre-Test Leak Start I <10 V ZCJ IV C/ .J 29 Check 

Pre-Test Leak Stop 1110 2..1 (1/ /(./ 27 Check 

Sample Start 15'7)' -(;/' 2. '/ /-

Collection 1.\..1 L:- ,Y~jN It> I () 2 c

/ Ih !(~ ;2..5 \ 

L /t ,lu / cJ 11-;3(. 20 \ - ~5' 5 I Ll I,? .5'-.5 . ) / 5 \ 

Lit/I; 1705 /U /70 ) . II \ 

I I 

~ple \ 

Stop /t I' 

I. 

Collection IT er I+~ I ' 

Post -Test Leak Start 11- 20 / tJ I' , 

Check \ 1¥-2 .:; I / 

Post-Test Leak Stop / 1/ \ II;U ) Ii) qYf.l Check /(- II , 

// /' .- Line Rinse / V V .../" Volume 

Comments: _____________________ _ 

Date of last revision 11 /13/08 

DS834043 

Master Document StoragelFormslDatasheetslField Datasheets 
SCAQMD METHOD 25.3 

EVACUATED CANISTER SAMPLING DATA 

Client/Facility: (~..:: "" \ V'- I "J I >;",c Ll"" ( Oate:_..::2=-·_'_·? __ I_' -~d-_____ _ 

I 

Unit/Location: !/ .,s !-<, c. IS Performed BY:_--,,-/<' -.:<c..A.:.... ] ..,1. 7'---____ _ 

Probe Material ____ -,_- -"'S'---____ Probe Length _~/f'-'__ / _____ _ 

/ 

Connecting Tubing Material, ___ '"---- ___ Connecting Tubing Length, __ ·...: V'--__ _ 

Barometric Pressure 2-cr, 1 '-I Ambient Temperature_--'u:....·_<-.!.. I ___ _ 

Test No. 5 -4/>1/...- ~c,,,--j,,, -fA . > - 'fI,fl<-I(" v i" lf3 

Vial 10 "h~ f'lPr' 

Canister 10 #" 0'1/ p- It) -; 

Time Vacuum Time Vacuum Time Vacuum 

Pre-Test Leak Start 

/1/; - Check //i)- 29 2"7 

Pre-Test Leak Stop / r 2)- ... 'I //2- s- 'Z 7' 

Check ,-

Sample Start 115,:5 ;2.7 / / .5 c,/ '2 ;;- Collection ''-' () 

S I.) Ii .... 7'-/ I~ / (~ ?.1 

£" i ,;. .' .. / J /1 /0:.. 'l:J ;:' 0 

,J I l) I c' 1'1 / 1 / f.....' If 1 

ell:;; '3 2. J /v ' J. l :j )/ 

\ 

~ Sample Stop f) 2-~ Iu Collection f?, 20 1 

Post -Test Leak Start 

131.6- /)2J- Check /<J '7 

Post-Test Leak Stop 

Check In IR /0 I/J (, j 

Line Rinse 

~ / ------ Volume 

I--"' ~ 

---- ./ 

Comments: 

... 

Della~ O::::"SoM. ... ........... .... 

Date of last revision 11 /13/08 

DS834043 

Master Document StoragelFormslDatasheetslField Datasheets 
Atmospheric Analysis & Consulting, Inc. 

CLIENT 

PROJECT NAME 

AAC PROJECT NO. 

REPORT DATE 

Delta Air Quality Services, Inc. 

Gemma, Sentinel 4 

130160 

2115/2013 

On February 13, 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) 

S4/Stk-VOC-IOO-IA 130160-60984 345.7 

S4/Stk-VOC-IOO-IB 130160-60985 459.8 

S4/Stk-VOC-75-1 A 130160-60986 460.2 

S4/Stk-VOC-75-IB 130160-60987 437.2 

S4/Stk-VOC-50-IA 130160-60988 437.3 

S4/Stk-VOC-50-IB 130160-60989 543.5 

Upon receipt at the laboratory, the initial vacuum was recorded and the canister was pressurized to 900 

mmHg using dry UHP Helium. The PQL for this modified method was established at 0.10 pp·mV (as 

Propane) as dictated by the lowest point in the calibration curve. All results were detected below this level 

and therefore reported as <PQL. 

One Entech Flow Controller Gauge was damaged upon return. Canisters #000403 and #000411 were not 

returned with this batch. 

[ certify that this data is technically accurate, complete and in compliance with the terms and conditions 

of the 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 results, please contact the undersigned. 

-ffL 

Marcus Hueppe ~ Laboratory Director 

This report consists of 41 pages. 

Page 1 

1534 Eastman Ave., ste. A • Ventura, • CA 93003 @ www.aaclab.com. (80S) 650·1642 • FAX (805) 650-1644 
® h CC Atmospheric Analysis & Consulting, Inc. 

SAMPLE RECEIPT / LOG-IN REPORT 

AAe Proiect 130160 Received By: J. Zachman 

Sample Pro i eet Desc Clients 10 Matrix Sampling Samnled By Sample # 

Receipt Date Daterrime 

2/ 13 /2013 Delta Air Quality S4/Stk-VOC-IOO Summa 2111 /2013 Client 60984 

1330 -IA Canister 

Gemma, Sentinel 4 

2113/2013 Delta Air Quality S4/Stk-VOC-IOO Summa 2/ 11 /2013 Client 60985 

1330 -18 Canister 

Gemma, Sentinel 4 

2113 /2013 Delta Air Quality S4/Stk-VOC-75- Summa 2111 /2013 Client 60986 

1330 IA Canister 

Gemma, Sentinel 4 

2/13/2013 Delta Air Quality S4/Stk-VOC-75- Summa 2111 /2013 Client 60987 

1330 IE Canister 

Gemma, Sentinel 4 

211312013 Delta Air Quality S4/Stk-VOC-50- Summa 2112/2013 Client 60988 

1330 IA Canister 

Gemma, Sentinel 4 

2/ 13 /2013 Delta Air Quality S4/Stk-VOC-50- Summa 2/ 1212013 Client 60989 

1330 18 Canister 

Gemma, Sentinel 4 

TURN AROUND TIME: Nonnal (lOdays) 

Lab Due Date: 2/20/2013 

Total Samples: 

REMARKS: 

Client returned 6 x Summa canisters + 6 x Flows. One Entech Flow Controller Gauge was damaged upon return. 

"Note: Canister #000403 and #000411 were voided tests. Please do not analyze." Canisters #000403 and #000411 

were not returned with this batch. 

Analysis 

. Requested 

SCAQMD 25.3M 

SCAQMD 25.3M 

SCAQMD 25.3M 

SCAQMD 25.3M 

SCAQMD 25.3M 

SCAQMD 253M 

6 

Page 2 
Client: 

Date: 

Delta Air Quality 

2/13/2013 

Canister # 

201 

020 

129 

151 

041 

107 

Atmospheric Analysis & Consulting, Inc. 

CANISTER PRESSURE LOG 

Project No.: 130160 

Sample # Initial Pressure Final Pressure 

60984 345.7 906.1 

60985 459.8 913.6 

60986 460.2 912.4 

60987 437.2 940.6 

60988 437.3 919.8 

60989 543.5 909.7 

1 

Page 3 
/f//c# 1 30 / raO 

CHAIN OF CUSTODY 

-.:t 

CLIENT: Ser" url!::1 TEST DATE(S): 211112013 211212013 (l) 

00 • SAMPLER(S): RM OJ 

p.. 

LOCATION: 

SAMPLE LOCATION: ~ u\ PROJECT MANAGER: BF 

TEST METHOD(S): f' ......... A ...... ,.. ~ ... 

' ",I"\\ •• [lvn." ' '''' .-> DATE DUE: 212012013 

OUTSIDE LAB REQUIRED?: Y-- ____________________________ COMPLIANCE TEST? Yes 

'4- l DATE ; ()q f? ----- ---- _ I _fiM~ __ L ___ TEST# 

~ 6 9?!;.-

1>01 8 <1:, 

; 0<1 87 \ ,->og e "i.? 

;"0"1 8'9 

2/11/2013 S4/Stk-VC 

2112 20 ~ 

2112120' 

ot l Sa_l!lples 

) 25 

) 25. 

:anister #OC :anister; 

:anister i 

:anlster: 

;anister: 

"z..{ 

1""'1 

~ 

6 

RElEASED BY DATEmME --- --- FRECEfVErfS'Y - - --- f DATEfTIME 

3£iJV /l'~ 2.( 13ft3. to:d'" __ Z:b::: - 9 21'27 1 5 ( t. 5r\ ~ ~ ? - I 'Z<'//)//3 ·· I ; ~ • > " . "3-m1/3 / 33", IY _ ... i ~ 

Note: Canister #000403 and #000411 were voided tests. Please do not analyze. 

A 
Results 

Page 5 
Atmospheric Analysis & Consulting, Inc. 

LABORATORY ANALYSIS REPORT 

CLIENT 

PROJECT NO. 

MATRIX 

UNITS 

Client ID 

S4/Stk-VOC-IOO-IA 

S4lStk-VOC-lOO-1 B 

S4/Stk-VOC-75-IA 

S4lStk-VOC-75-1 B 

S4IStk-VOC-50-IA 

S4/Stk-VOC-50-IB 

Delta Air Quality Services,lnc. 

130160 

Air 

: ppmC 

Tank Vol Liters Lab ID # 

(VT"k) 

130160-60984 6.00 

130160-60985 6.00 

130160-60986 6.00 

130160-60987 6.00 

130160-60988 6.00 

130160-60989 6.00 

SCAQMD 25.3 Modified 

Initial Return Final 

Pressure Pressure Pressure 

mmHg(P;) mmHg (P,) mmHg (Pr) 

0.0 345 .7 906.1 

0.0 459.8 9 13.6 

0.0 460.2 912.4 

0.0 437.2 940.6 

0.0 437.3 919.8 

0.0 543.5 909.7 

* TNMNEOC Includes Bias Correction=1.086, as per method 

PQL = 0.10 ppmV Propane x 3.0 (carbon conversion) x Tank Dilution Factor x 1.086 (correction factor) 

EPA3C - --

PQL: 0.1 % Analvte 

Client ID Lab ID # Oxyeen CO 

S4/Stk-VOC-I OO-IA 130160-60984 12.8 <PQL 

S4lStk-VOC-100-1 B 130160-60985 13 .0 <PQL 

S4/Stk-VOC-75-IA 130160-60986 13.6 <PQL 

S4/Stk-VOC-75-IB 130160-60987 13.6 <PQL 

S4IStk-VOC-50-IA 130160-60988 14.1 <PQL 

S4/Stk-VOC-50-1 B 130160-60989 14.1 <PQL 

Fixed Gases have been normalized to 1000/0 on a dry weight basis 

Sample Vol. 

(L) (VS.mpl.) 

2.73 

3.63 

3.63 

3.45 

3.45 

4.29 

CO2 

6.0 

5.9 

5.4 

5.5 

5.2 

5.1 

Tank Dil 

Factor 

(DFT.,k) 

2.62 

1.99 

1.98 

2.15 

2.10 

1.67 

SAMPLING DATE : 2111 ,1212013 

RECEIVING DATE : 0211312013 

ANALYSIS DATE : 0211412013 

REPORT DATE : 02/1512013 

Total PQL NMNEOC* 

<PQL 0.85 

<PQL 0.65 

<PQL 0.65 

<PQL 0.70 

<PQL 0.69 

<PQL 0.55 

~L~ - . , Marcus Hueppe 

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 DFTank X 3.0 x 1.086 

Where: 

TNMNEOC = 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 (PdPr) 

3.0 = Conversion of result (as Propane) to (as Carbon) 

Per method section 4.11, the final concentration includes a 1.086 bias correction factor. 

Where: 

Pf= Final canister pressure after pressurization for analysis !from Sample Receiving Data Sheet) 

Pr = Return canister pressure upon sample receipt (from Sample Receiving Data Sheet) 

Page 7 
QA/QC 

Summary 

Page 8 
Atmospheric Analysis & Consulting, Inc. 

Quality ControVQuality Assurance Report 

Date Analyzed : 0211412013 

Analyst : ZG 

Units : % 

J - ODenin.e: Continu1n1! Calibration Verification· SeA MD25.125.3 

AACID Analyle 0, N, 

Spike Cone 5.18 14.4 

cev Result 5.15 15.70 

% Rec:-· 99.3 109.0 

0, 

MB Concentration II ND ND 

fiI-Laboratory Control Spike & Du liute - SCAQMD 25.1,25.3 

AACID Analyle N, CO, 

Sample Cone 0.0 0.0 

Spike Cone 14.4 10.3 

Lit b C(mtrol LCS Result 15.6 10.4 

Standards LCSD Result 15.4 10.7 

LCS % Rec· 108.1 101.7 

LCSD %Rec * 107.0 103.9 

G/o RPD *.* 1.0 2.2 

IV -Sample & Sample Duplicate - SCAQMD 25.1,25.3 

AACID An.lyle 0, N, 

Sample 6.4 39.7 

130160-60985 Sample Dup 6.3 39.2 

Mean 6.3 39.4 

%RPD ~** 1.4 1.4 

V -Matrix Spike & Duplicate - SCA( MD 25.125.3 

AAC1D Analyte N, CO, 

Sample Cone 19.7 1.4 

Spike Cone 9.2 10.3 

MSResult 29.5 12.0 

130160'60985 ·, ·MSDReSult 30.4 12.0 

MS % Rec ** 106.4 103.4 

MSD % Rec·· 115.7 103.3 

% RPD ••• 8.4 0.1 

VI - OOSiIU! Continuinl! Calibration Verification - SCAOMD 25.125.3 

I MCID I 

cev 

• MMstbe85-1l5% • 

•• Must be 75-125% 

•• tMustbe<25% 

ND - Not DeJected 

. Anatfl. 

Spike Conc 

Result 

%Rec· 

<RL "" less than Reporting Lima 

II 0, I N, 

5.1S 14.4 

5.04 15.S 

97.3 110.0 

co, 

10.3 

10.5 1 

102.5 

CO, 

ND 

CIf. 

0.0 

9.9 

9.9 

10.0 

99.8 

100.3 

0.5 

CO, 

2.9 

2.8 

2.9 

0.8 

CIf. 

0.0 

9.9 

10.3 

lOA 

104.0 

104.5 

0.5 

I CO, 

10.3 

10.S 

105.0 

I 

Instrument ID 

Calb Date 

TCD#1 

04113/2012 

Reporting Limit: 0.1 % 

CIf. CO 

9.9 10.3 

9.90 10.33 

99.6 99.8 

CO 

ND ND 

CO 

0.0 

10.3 

10.3 

lOA 

99.8 

100.5 

0.7 

CHt CO 

0.0 0.0 

0.0 0.0 

0.0 0.0 

0.0 0.0 

", CO 

0.0 

10.3 

10.8 

10.9 

104.3 

105.2 

0.9 

'CH. I CO 

9.9 10.3 

10.2 10.6 

102.5 102.6 

~~ Marcus Hueppe 

Laboratory Director 

I 

Page 9 

1534 Eastman Ave., Ste. A • Ventura, • CA 93003 www.aaclab.com • (805) 650-1642 • FAX (805) 650-1644 
I 

I 

Atmospheric Analysis & Consulting, Inc. 

SCAQMD Method 25.1,3 Quality ControVQuality Assurance Report 

Date Analyzed 

Analyst 

02/1412013 

ZG 

I ~ ODcning Calibration Verification Standard 

AAeID ' Analvte Concentration 

O-CV NMNEOC 0.27 

O-CV dp NMNEOC 0.27 

O-CV tp NMNEOC 0.27 

II -Method Blank 

AACID Analvte Result 

MB NMNEOC ND 

111- Matrix Spike & Duplicate 

AAC~ Analyte Sample 

Concentration 

4 NMNEOC I 0.00 

IV . I ppm Backflush Standards 

AAeID · I Analyte I Result 

Backflush 1 NMNEOC 0.980 

Backflush 2 NMNEOC 0.956 

Backflush 3 NMNEOC 1.027 

Result 

0.266 

0.274 

0.257 

Spike 

Added 

I S4.3S 

I % Recovery ," 

90.2 

87.9 

94.5 

V - Bracketed Closing Calibration Verification Standards 

AAelD I 

C-CV Low 

C-CV High 

• Must be 90-/10% 

•• Must be 80-/10% 

*** Must be 75-125% 

***'" Must be < 25% 

***** Must he < 10% 

AnalYte 

NMNEOC 

NMNEOC 

I Concentration I Result 

0.27 0.267 

2.72 2.48 

% Recovery -· 

97.9 

100.8 

94.6 

MS I 

Result 

I 46.92 I 

I 

I % Reeoveryt I 

98.3 

91.2 

MSD 

Result 

46.57 I 

Instrument !D: F!D#4 

Units: PPMV 

Calibration Date: 

MS MSD 

0/0 Ree "' •• % Ree ."'* 

86.3 I 85.7 

Marcus Hueppe . 

Laboratory Director 

1/1012013 

% RPO .... 

I 0.8 

Page 10 

1534 Eastman Ave., Ste. A • Ventura, • CA 93003 www.aaclab.com • (805) 650-1642 • FAX (805) 650-1644 

I 
Atmospheric Analysis & Consulting, Inc. 

SCAQMD Method 25.1,3 Quality Control/Quality Assurance Report 

Date Analyzed : 02114/2013 

Analyst: : ZG 

Sample Duplicate analysis RPD's 

I "'AACID 'i I ·-":" ResuU"< I ResultDu~ 

130160-60984 <PQL <PQL 

130160-60985 <PQL <PQL 

130160-60986 <PQL <PQL 

130160-60987 <PQL <PQL 

130160-60988 <PQL <PQL 

130160-60989 <PQL <PQL 

I Qualitl: Assurance Criteria 

Cone. (ppmv) %RPD 

1·3 ~20 

4·6 ~15 

7-12 <12 

13·30 <10 

31-50 <5 

I 

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Instrument ID: 

Units: 

FID#4 

PPMV 

Calibration Date: 1110/2013 

> %RPD > I 

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 
Chrom Perfect Chromatogram Report 

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Time - Minutes 

Sample Name ~ 130160·60984 

Instrument = TeO #1 

Raw File Name ~ C:ICPDATAltnst#01 12013102141 3.0006.RAW 

Method File Name ~ C:ICPDATAltnsI#01120131021413.0006.bnd 

Calibration Fite Name ~ C:ICPDATAlt nsI#01120131021413.0006.bnd 

Peak # Ret. Time Name Amount Amt% 

1 7.04 Oxygen.MS5A 3.977 12.792 

2 9.19 Nitrogen-MS5A 25.162 80.938 

3 9.54 C02-Q bond 1.949 6.270 

Total Area ~ 444611.3 Total Height ~ 71315.2 

Printed on 211412013 8:45:03 AM 

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Date Taken (end) ~ 211412013 7:40:46 AM 

Dilution Factor = 1 

Area Area % Type Width 

54492 12.256 BB 0.08 

366716 82.480 SBB 0.09 

23404 5.264 TBB 0.20 

Total Amount ~ 31 .08822 

24 

Page p1\le 1 of 1 
Chrom Perfect Chromatogram Report 

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Raw File Name = C:ICPDATAllnst#01120131021413.0007.RAW 

Method File Name = C:ICPDATAllnst#01120131021 413.0007.bnd 

Calibration File Name = C:ICPDATAllnst#01120131021413.0007.bnd 

Peak# Ret. Time Name Amount Amt % 

1 7.04 Oxygen-MS5A 4.382 12.801 

2 9.18 Nitrogen-MS5A 27.899 81 .505 

3 9.54 C02-Q bond 1.949 5.694 

Total Area = 490038.3 Total Height = 77284.88 

Printed on 2/14/2013 8:08:38 AM 

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Date Taken (end) = 2/14/2013 7:59:54 AM 

Dilution Factor = 1 

Area 

60041 

406598 

23399 

Area % Type W idth 

12.252 BB 0.08 

82.973 BV 0.10 

4.775 VB 0.19 

Total Amount = 34.22934 

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Instrument;: TCD #1 

Chrom Perfect Chromatogram Report 

130160-60965 

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Raw File Name = C:ICPDATAllnst#01120131021413.0010.raw Dale Taken (end) = 2/14/2013 9:19:41 AM 

Melhod File Name = C:ICpmelhodsllnsl #0112012IDI945-01946-3C.MET Oilulion Faclor = 1 

Calibration File Name = CICpmelhodsllnsl #0112012101945-01 946-3C-041312-standard.CAL 

Peak # Ret Time Name Amount Amt% Area Area % Type Width 

1 7.03 Oxygen·MS5A 6.385 13.043 87492 12.489 BB 0.09 

2 9.15 Nitrogen-MS5A 39.701 81 .097 578602 82.594 SBB 0.11 

3 9.54 C02-Q bond 2.869 5.861 34447 4.917 TBB 0.20 

Total Area = 700540.6 T olal Height = 100279.8 Total Amount = 48.95485 

24 

Printed on 2/14/2013 9:20.11 AM Page ~a1Je 1 of 1 
Chrom Perfect Chromatogram Report 

130160-60985 dp 

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Sample Name = 130160-60985 dp 

Instrument = TeO #1 

Raw File Name = C:ICPDATAllnst#01120131021413.0011.raw Date Taken (end) = 2/14/2013 93639 AM 

Method File Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C .MET Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #01 12012ID1945-D1946-3C-041312-standard.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 7.03 Oxygen-MS5A 6.297 13.038 86290 12.485 BB 0.09 

2 9.15 Nitrogen-MS5A 39.158 81 .072 570692 82572 SBB 0.11 

3 9.54 C02-Q bond 2.845 5.890 34159 4.942 TBB 0.19 

Total Area = 691141 .7 Total Height = 99449.89 Total Amount = 48.30048 

Printed on 2/14/2013 9:37:13 AM Page 16 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130160-60986 

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Time - Minutes 

Sample Name = 130160-60986 

Instrument = TCD #1 

Raw File Name = C:ICPDATAllnst#01120131021413.0014.raw Date Taken (end) = 21141201310:30:48 AM 

Melhod File Name = CICpmethodsllnst #0112012ID1945-D1946-3C.MET Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C-041312-standard .CAL 

Peak # Ret Time Name Amount Amt% Area Area % Type Width 

1 7.03 Oxygen-MS5A 6.694 13.622 91720 13.037 BB 0_09 

2 9.15 Nitrogen-MSSA 39.801 80.998 580059 82.451 SBB 0.11 

3 9.54 C02-Q bond 2.643 5.380 31737 4.511 TBB 0.20 

Total Area = 703516.4 Total Height = 100729 Total Amount = 49.13772 

Printed on 21141201310:33:40AM Page 17 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130160~0986dp 

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Sample Name = 130160-60986 dp 

• Instrument ;;: TeO #1 

Raw File Name = C:ICPDATAUnst#01120131021413.0015.raw Date Taken (end) = 21141201310:47:21 AM 

Method File Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C .MET Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C-041312-standard.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 7.03 Oxygen-MS5A 6.609 13.642 90565 13.058 BB 0.09 

2 9.15 Nitrogen~MS5A 39:200 80.911 571306 82.373 SBB 0.11 

3 9.54 C02-Q bond 2.639 5:447 31686 4.569 TBB 0.20 

Total Area = 693556.9 Total Height = 99957.52 Total Amount = 48:44856 

Printed on 21141201310:47:51 AM Page 18 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130160-60987 

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Time - Minutes 

Sample Name = 130160-60987 

Instrument = TeO #1 

Raw FIle Name = C:ICPDATAllnst#01120131021413.0016.raw Date Taken (end) = 2/14/2013 11 :04:54 AM 

Method File Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C.MET Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C-041312-standard.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 7.03 Oxygen-MS5A 6.058 13.634 83013 13.053 BB 0.09 

2 9.16 Nitrogen-MS5A 35.913 80.824 523399 82.298 SBB 0.11 

3 9.55 C02-Q bond 2.463 5.542 29568 4.649 TBB 0.21 

Total Area = 635980 1 Total Height = 93820.45 Total Amount = 44.43389 

Printed on 2/14/201311:06:04 AM Page 19 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130160-.60987 dp 

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Time - Minutes 

Sample Name = 130160-60987 dp 

Instrument = TeO #1 

Raw File Name = C:ICPDATAllnst#01120131021413.0017.raw Date Taken (end) = 21141201311:21:13AM 

Method File Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C.MET Dilution Factor = 1 

Calibration File Name = CICpmethodslinst #0112012ID1945-D1946-3C-041312-standard.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 7.03 Oxygen-MS5A 5.932 13.633 81283 13.049 BB 0.09 

2 9.16 Nitrogen-MS5A 35.217 80.938 513256 82.397 SBB 0.11 

3 9.55 C02-Q bond 2.362 5.429 28363 4.553 TBB 0.21 

Tolal Area = 622902.6 Total Height = 92448.69 Total Amount = 43.51136 

Printed on 211412013 11 :21 :39 AM Page 20 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130160-60988 

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Time - Minutes 

Sample Name = 130160·60988 

Instrument:;; TeO #1 

Raw File Name = C:ICPDATAllnst#01120131021413.0018.raw Date Taken (end) = 2/14/2013 11 :39 29 AM 

Method File Name = C:ICpmethodsllnst #01\2012ID1945-D1946-3C.MET Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #01 \2012ID1945-D1946-3C-041312-standard.CAL 

Peak # Ret Time Name Amount Amt% Area Area % Type Width 

1 703 Oxygen-MS5A 6.397 14.092 87659 13.485 BB 0.09 

2 916 Nitrogen-MS5A 36.675 80.788 534501 82.223 SBB 0.11 

3 9.54 C02-Q bond 2.324 5.120 27905 4.293 TBB 0.21 

Total Area = 6500646 Total Height = 95324.45 Total Amount:;; 45.39617 

Printed on 2/14/2013 11 :4042 AM Page 21 Page 1 of 1 
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Raw File Name = C:ICPDATA\lnst#01120131021413.0019.raw Date Taken (end) = 2/14/2013 11 :56:00 AM 

Method FIle Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C .MET Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0112012\D1945-D1946-3C-041312-standard.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 7.03 Oxygen-MS5A 6.399 14.093 87691 13.489 BB 0.09 

2 9.16 Nitrogen-MS5A 36.621 80.648 533712 82.1 00 SBB 0.11 

3 9.54 C02-Q bond 2.388 5.259 28670 4.410 TBB 0.20 

Total Area = 650072.5 Total Height = 95161.16 Total Amount = 45.40808 

Pnnted on 2/14/201311 :56:28 AM Page 22 Page 1 of 1 
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Instrument = TCD #1 

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Raw Fi le Name = C:ICPDATAllnst#01120131021413.0020.raw Date Taken (end) = 2/14/2013 12: 13:24 PM 

Method File Name = C:ICpmethodsllnst #01 \2012ID1945·D1946·3C.MET Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #01 \2012ID1945·D1946·3C·041312·standard.CAL 

Peak # Ret Time Name Amount Amt% Area Area % Type Width 

1 7.02 Oxygen-MS5A 8.217 14.143 112592 13.532 BB 009 

2 9.1 4 Nitrogen-MSSA 46.947 80.806 684204 82.233 SBB 0.12 

3 9.53 C02-Q bond 2.935 5.051 35232 4.234 TBB 0.26 

Total Area = 832028.5 Total Height = 113797.1 Total Amount = 58.09794 

Printed on 2/14/201312:13:50 PM Page 23 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130160-{}Q989 dp 

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Time - Minutes 

Sample Name = 130160-60989 dp 

Instrument = TeO #1 

Raw File Name = C:tCPDATA\lnst#01t2013t021413.0021.raw Date Taken (end) = 21141201312:30:20 PM 

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 7.02 Oxygen-MS5A 8.228 14.129 112749 13.519 BB 0.09 

2 9.14 Nitrogen-MS5A 47.064 80.817 685913 82.244 SBB 0.12 

3 9.53 C02-Q bond 2.943 5.053 35333 4.237 TBB 0.20 

Total Area = 833994.2 Total Height = 114081 .9 Total Amount = 58.23498 

Printed on 2114/201312:30:47 PM Page 24 Page 1 of 1 
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Raw File Name = C:ICPDATAllnst#04120131021413_0008.RAW Date Taken (end) = 2/14/2013 7:44:52 AM 

Method File Name = C:ICpmethodsllnst #04\2013IMethod25.1 ,3_low.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #04\2013IM251 ,3Iow-Oll013.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.85 Carbon Monoxide 25.998 1.244 368221 0.861 BV 0.20 

2 106 Methane 14.563 0.697 284421 0.665 W 0.17 

3 194 Carbon Dioxide 2049.641 98.058 42115948 98:469 VB 0.50 

4 5.53 NMNEOC 1 0.038 0.002 2043 0.005 BB N 0.13 

Total Area = 4.277064E+07 Total Height = 1130671 Total Amount = 2090.24-

Printed on 2/14/2013 7:59:39 AM Page 25 Page 1 of 1 
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Raw File Name = C:ICPDATAllnst#04120131021413.0009.RAW Date Taken (end) = 2/14/2013 7:57:24 AM 

Method File Name = C:\Cpmethods\lnst #04\2013\Method2S.1 ,3_low.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0412013IM25.1 ,310w-011 OnCAl 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.86 Carbon Monoxide 23. 130 1.121 327598 0.775 BV 0.20 

2 1.06 Methane 14.118 0.684 275718 0.653 W 0.17 

3 1.87 Carbon Dioxide 2026.839 98.194 41647420 98.569 VB 0.49 

4 5.75 NMNEOC 1 0.025 0.001 1362 0.003 BB N 0.23 

Total Area = 4.22521 E+07 Total Height = 1124763 Total Amount = 2064.112 

Printed on 2/14/2013 7:59:45 AM Page 26 Page 1 of 1 
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Raw File Name = C:ICPDATAllnst#04120131021413.0012.raw Date Taken (end) = 211412013 8:39:08 AM 

Method File Name = C:\Cpmethods\lnst #04\2013\Method25.1 ,3Jow.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0412013IM25.1 ,310w-011013.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.85 Carbon Monoxide 20.641 0.946 292346 0.654 BV 0.19 

2 1.06 Methane 15.728 0.721 307177 0.687 VB 0.17 

3 197 Carbon Dioxide 2146,404 98.333 44104240 98657 BB 0.52 

4 5.69 NMNEOC 1 0.020 0.001 1073 0.002 BB N 0.17 

Total Area = 4,470484E+07 Total Height = 1124409 Total Amount = 2182.793 

Printed on 211412013 85505 AM Page 27 Page 1 of 1 
1600 

1400 

1200 

1000 

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Instrument::; FID #4 

Chrom Perfect Chromatogram Report 

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Raw File Name = C:ICPDATAllnst#04120131021413.0013.raw Date Taken (end) = 2/14/2013 8:53:20 AM 

Method File Name = C:ICpmethodsllnst #0412013\Method25.1 ,3Jow.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodslln5t #0412013IM25.1.310w-011 onCAl 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.86 Carbon Monoxide 18.717 0.860 26510 1 0.595 BV 0.19 

2 1.06 Methane 15.616 0.718 304985 0.684 VB 0.18 

3 1.94 Carbon Dioxide 2142.022 98.422 44014208 98.720 BB 0.52 

4 5.69 NMNEOC 1 0.015 0.001 811 0.002 BB N 0.17 

Total Area = 4.45851E+07 Total Height = 11 21025 Total Amount = 2176.371 

Printed on 2/14/2013 855: 13 AM Page 28 Page 1 of 1 
1600 

1400 

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Sample Name = 130160-60986 

Instrument :: FlO #4 

Chrom Perfect Chromatogram Report 

3 0 

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4.0 

130160-60986 

5.0 

Time Minutes 

" o 

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" Z 

60 

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7 0 8.0 9.0 

Raw File Name = C:ICPDATAllnst#04120131021413.0014.raw Date Taken (end) = 2/14/2013 9:0659 AM 

Method File Name:: C:\Cpmethods\lnst #04\20 13\Method25.1 ,3Jow.met Dilution Factor:: 1 

Calibration File Name = C:ICpmethodsl lnst #04\2013IM25.1 ,310w-0 11 OnCAl 

Peak # Ret. Time Name Amount Amt% Area Area % Type W idth 

1 0.86 Carbon Monoxide 18.772 0.888 265879 0.614 BV 021 

2 1.05 Methane 9.448 0.447 184515 0.426 VB 0.1'6 

3 1.98 Carbon Dioxide 2084.729 98.664 42836936 98.958 BB 0.51 

4 5.51 NMNEOC 1 0.016 0.001 856 0.002 BB N 0.11 

Total Area = 4.328818E+07 Total Height = 1109342 Total Amount = 2112 .964 

Printed on 2/14/2013 9:29:50 AM Page 29 Page 1 of 1 
1600 

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Sample Name; 130160-60986 dp 

Instrument = FlO #4 

Chrom Perfect Chromatogram Report 

. 

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130160..{)0986dp 

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Time - Minutes 

" 0 

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60 

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" 0 

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70 8.0 9.0 

Raw File Name; C:ICPDATAllnst#04120131021413.0015.raw Date Taken (end); 2/14/2013 925:21 AM 

Method File Name = C:\Cpmethods\lnst #04\2013\Method25.1 ,3_low.met Dilution Factor = 1 

Calibration File Name; C:ICpmethodsllnst #0412013IM25.1 ,310w-011013.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 085 Carbon Monoxide 17.547 0.831 248531 0.575 BV 0.20 

2 1.06 Methane 9.150 0.434 178710 0.413 VB 0.17 

3 1.93 Carbon Dioxide 2084.110 98.734 42824216 99.010 BB 051 

4 5.52 NMNEOC 1 0.016 0.001 880 0.002 BB 0. 11 

Total Area; 4.325234E+07 Total Height; 1108594 Total Amount; 2110.823 

Printed on 2/14/2013 9:29:56 AM Page ,0' Page 1 of 1 
1400 ~l 

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Sample Name = 130160·60987 

Instrument;: FlO #4 

Chrom Perfect Chromatogram Report 

~ 

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30 4.0 

130 160.00987 

~ m 

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5.0 

Time Minutes 

° 0 

w 

z 

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Raw File Name = C:ICPDATAllnst#04120131021413.0016.raw Date Taken (end) = 2/14/2013 9:40:20 AM 

Method File Name = C:\Cpmethods\lnst #04\2013\Method25.1 ,3Jow.met Dilution Factor = 1 

Calibration File Name = CICpmethodsllnst #04\2013IM25.1 ,310w·011013.CAL 

Peak # Ret Time Name Amount Amt% Area 

1 0.86 Carbon Monoxide 16.236 0.788 229966 

2 1.05 Methane 8.154 0.396 159258 

3 1.96 Carbon Dioxide 2035.720 98.812 41829908 

5 5.53 NMNEOC 1 0.010 0.001 553 

6 6.72 NMNEOC 2 < 0.065 0003 3467 

-.-o,S 

Total Area = 4.222315E+07 Total Height = 1105057 

Pnnted on 2/14/2013 100043 AM 

Area % Type Width 

0.545 BV 0.20 

0.377 VB 0.16 

99.069 BB 0.49 

0.001 BB 0.08 

0.008 BB N 0:44 

Total Amount = 2060.186 

Page 31 Page 1 of 1 

liJ1-\ \~\I~ 
1600 

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Sample Name = 130160-60987 dp 

Instrument = FID #4 

Chrom Perfect Chromatogram Report 

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130160-60987 dp 

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Raw File Name = C:ICPDATAllnst#04120131021413.0017.raw Dale Taken (end) = 2/14/2013 9:53:44 AM 

Method File Name = C;\Cpmethods\lnst #04\2013\Method25.1 ,3Jow.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0412013IM25.1 ,310w-Oll013.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.85 Carbon Monoxide 15.297 0.746 216665 0.516 BV 0.20 

2 1.05 Methane 8.025 0.392 156731 0.373 VB 0.16 

3 1.94 Carbon Dioxide 2026.369 98858 41637756 99.101 BB 0:49 

5 5.53 NMNEOC 1 0.009 0.000 505 0.001 BB 0.08 

6 6.75 NMNEOC 2 • 0.075 0004 4019 0.010 BB N 0:43 

o -0'/)1-

Total Area = 4.201568E+07 Total Height = 1103646 Total Amount = 2049.775 

Printed on 2/14/2013 10:00:48 AM Page 32 Page 1 of 1 
1600 

1400 

1200 

1000 

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~ 

g 600 ~ 

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400 

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Sample Name = 130160-60988 

Instrument = FlO #4 

Chrom Perfect Chromatogram Report 

30 4.0 

130160-60988 

~ m 

£ 

w 

5.0 

Time - Minutes 

u 

0 

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Z 

" z 

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ro 

6.0 

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7.0 8.0 9.0 

Raw File Name = C:ICPDATAllnst#04120131021413_0020,raw Date Taken (end) = 21141201310:40:48 AM 

Method File Name = C:\Cpmethods\lnst #04\2013\Method2S.1 ,3Jow.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0412013IM25.1,310w-011 013.CAL 

Peak # Ret Time Name Amount Amt% Area Area % Type Width 

1 0.86 Carbon Monoxide 23.426 1.142 331802 0.790 BB 0.23 

2 1.96 Carbon Dioxide 2027.373 98.857 41658396 99.209 BB 0.49 

3 5.68 NMNEOC 1 0.010 0.000 533 0.001 BB N 0.16 

Total Area = 4.199073E+07 Total Height = 1092637 Total Amount = 2050.81 

Printed on 211412013 11 :00:40 AM Page 33 Page 1 of 1 
"0 

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600 

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Sample Name = 130160·60988 dp 

Instrument: FlO #4 

Chrom Perfect Chromatogram Report 

, 

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13Q160-6()988 dp 

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Time - Minutes 

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7.0 80 90 

Raw File Name = C:ICPDATAllnst#04120131021413.0021.raw Date Taken (end) = 2/14/201310:54:26 AM 

Method File Name = C:\Cpmelhods\lnst #04\2013\Method25.1 ,3_low.met Dilution Factor = 1 

Calibration File'Name = C:ICpmethodsllnst #0412013IM25.1 ,310w·011 013.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.86 Carbon Monoxide 21.857 1.074 309577 0.743 BB 0.25 

2 1.89 Carbon Dioxide 2013.586 98.926 41375100 99.256 BB 0,49 

3 5.52 NMNEOC 1 0.011 0.001 569 0.001 BB N 0.10 

Total Area = 4.168524E+07 Total Height = 1089396 Total Amount = 2035.454 

Printed on 2/14/2013 11 :00:45 AM Page 34 Page 1 of 1 
1600 

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Sample Name = 130160·60989 

Instrument = FlO #4 

Chrom Perfect Chromatogram Report 

• c 

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Raw File Name = C:ICPDATAllnst#04120131021413.0022.raw Date Taken (end) = 2/14/2013 11 : 1 0:43 AM 

Melhod File Name = C:ICpmelhodsllnsl #0412013IMethod25.1 .3Jow.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsl lnst #0412013IM25.1.310w·011 013.CAL 

Peak # Ret Time Name Amount Amt % Area Area % Type Width 

1 086 Carbon Monoxide 22.691 1.054 321381 0.729 SS 0.26 

2 1.92 Carbon Dioxide 2129.163 98.945 43749968 99.269 SS 0.52 

3 5.51 NMNEOC 1 0.Q16 0.001 877 0.002 SS 0.09 

Tolal Area = 4:407222E+07 Total Height = 1089665 Tolal Amount = 2151 .87 

Prinled on 2/14/2013 11 :2639 AM Page 35 Page 1 of 1 
1600 

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Sample Name = 130160-60989 dp 

Instrument = FlO #4 

Chrom Perfect Chromatogram Report 

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Raw File Name = C:ICPDATAllnst#04120131021413.0023.raw Date Taken (end) = 2/14/2013 11 :23:52 AM 

Method File Name = C:ICpmethodsllnst #0412013IMethod25.1 ,3_low.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0412013IM25.1 ,3Iow-Oll 013.CAL 

Peak # Ret. Time Name Amount Amt % Area Area % Type Width 

1 0.86 Carbon Monoxide 21 .575 1.010 305583 0.698 BB 0.27 

2 1.96 Carbon Dioxide 2114.615 98.989 43451044 99.300 BB 0.51 

3 5.52 NMNEOC 1 0.014 0.001 767 0.002 BB 0.08 

Total Area = 4.37574E+07 Total Height = 1087625 Total Amount = 2136.205 

Printed on 2/14/2013 1126:52 AM Page 36 Page 1 of 1 
Calibration 

Summary 

Page 37 
SCAQMD Method 25.1 125.3 Calibration Curve (GC/FID/TCA #4) 

ANALYTE: TNMNEOC (as Propane) Analysis Date: 1/10/2013 

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 14483 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 156327 5.4 6179.41 2.72 

5.44 6.84 282757 

5.44 6.84 280611 0.8 1517.45 5.44 

AvgRT 6.65 RTWindow +/- 0.20 min 

Calibration Verification Standards: 

CCV Retention Time Result (ppmv % Rec· 

2.5 ppmv 6.64 2.69 106.3 

2.5 oomv do 6.85 2.79 102.5 

'M ust be +/- 10 % of Theoretical Concenfration 

Analyst (Intitial & date)::i13 \ I \0113 Lab Director (Initial & date): ~I 

1m ~ 

Analyst: 

Response Area 

(mean) 

6536 

14388 

27611 

64019 

162697 

281684 

Calb. Type 

R2 value: 

Intercept (8) 

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+B 

Must be :> 0,990 

Included 

00 

M 

.., 

~ i:l.. 
'" '" ~ 

<C 

4.E+05 

3 .E+05 

3.E+05 

1',-

2.E+05 

2.E+05 

1.E+OS 

S.E+04 

O.E+OO 1/ 

0.00 

TNMNEOC (as Propane) Plot 

, 

, " 

, 

., 

y = 53584.6911x 

R2 = 0.9925 

./ 

! 

' ~, ' V , .' . ./ . 

V , 

* ........ 

f\r; 

V , 

V ., 

1.00 2.00 3.00 4.00 5.00 6.00 

Concentration (ppmv) 

0-

M 

p., 

~ 
Date: 0111012013 Analyst: ZG 

Analvte: Cone. MDL#1 

NMOC 0.050 0.058 

Analvte: Mean Std Dev 

NMOc 0.051 0.005 

FlO MOL Study per SCAQMO 25.1/25.3 

Instrument: GCIFID #4 Units: ppmV 

MDL#2 MDL#3 MDL#4 MDL#5 MDL#6 MDL#7 

0.050 0.054 0.043 0.051 0.056 0.047 

MDL " Method Detection Limit Study per USEPA Guidelines 

MDL MRL 

0.016 0.049 MOL (Method Detection Limit) (7 replicates) = Standard Deviation x 3.1 43 

MRL (Minim um Reporting Limit) = MOL x 3.0 

Is the spiked concentration < 10 times the calculated MDL0 N 

Defi/)ition: MDL- The minimum concentration of a substance that ca/J be Ide/Jtified, measured and reported wit" a 99% confidence interval, that 

the ana/yte concentration is greater than zero and is determined from the analysis of a sample in a given matrix containing the ana/yte. 

Definition: MRL - The smallest measured concentration of a substance that can be reliably measured by using a given analytical method. 

o 

"'" ., 

~ ~ 
Analvte: LOD LOa Conc./MDL 

NMOC 0,01 6 0,052 3 

Alternative Supporting Calculations 

M%Rec S:N Ratio 

103 9.8 3 

LOD {Limit of Detection) ;:,· Standard Deviation )( 3,Q 

LOQ (Limit of Quantitation)= Standard De .. 'lation)( 10,0 

Mean % Ree • (Mean Rest True Value) Y. 100% 

Is the Mean % Ree between 80% and 120% ?<Y) I N 

C: onc.lMDL - Concentration I MOL I?\ 

Is the Conc.lMDL between 2 to 5?1....!J1 N 

3ignal to Noise Ratio · (Mean/StdDev) 

Is the signal to Noise Ratio between 2.5 and 10'6>1 N 

Definition : LOD - The lowes t concentration that can be determined to be statistically different from a brank. 

Definition: LOO - The concentration above which quantitative results carl be obtained with a specific degree of confidence. 

Analyte: POL RL ~ 

NMOC 0.104 0.104 

Proposed POL and RL 

Practical Quantitat;on limit 

Is the PQL 2 to 5 times higher than the LOQt(Y)1 N 

Repolt ing Limit 

Is the Rl equal to or greater than the PQl QI N 

POL (Practical Quantitation Limit) = Established by the laboratory based on the above calculations 

RL (Reporting Limit)::o Establ i she(1 by the laboratory based on the PQl andfor mettlod, 

Definition,' PQL· The lowest level tllat can be reliably achieved wit/fin specified limits of precision and accuracy during routine laboratory 

operating conditions, In addition, if quatitating at this level, the lowest pOint of the calibration curve must be set at this point 

Comments: 

Analyst (sign & date): $3 \ \ \ 0 \ \ 5 Lab Director (sign & date): ;;&. _. ¢7.J 

-'<t 

p... 

~ 
Appendix C.6 PM by SCAQMD Method 5.1 

R041 0688 C-10 
SCAQMD METHOD 5.1 PARTICULATE TEST DATA SUMMARY 

ClientJlocatlon. 

Unit 

Sample location 

Test No. 

Test Method 

Date 

Start Time 

Stopnme 

Sample Train 

Pitot Factor 

Meter Cal Factor 

Stack. Area (sq ttl 

Sample Time (Min) 

Bar Press (in Hg) 

Nozzle Diam (in) 

Stack. Press (iwg) 

Stacll Temp (F) 

Vel Head (iwg) 

Stack. 02 (%) 

Stack C02 (%) 

Meter Vol (acf) 

Meter Temp (F) 

Meter Press (iwg) 

Liquid Vol (mil 

Sid Sample Vol (SCF) 

MOisture Fraction 

Slack Gas Mol Wt 

Stack Gas Velocity (It/sec) 

Stack Flow Rate (wacfm) 

Slack. Flow Rate (dscfm) 

Isoklnelic Ratio (%) 

Facility Average Gas Flow (hscfh) .. 

Facility Average Gas Flow (MMscfh) . 

Total Weight Gain, mg 

Particulate EmissIons 

Grain Loading. gr/dscf ... 

Grain Loading @3%02 

Grain Loading@ 15% 02 

Grain Loading@12%C02. 

Mass Emissions, Ib/hr' .• 

Emission Rate. IbfMMSCF 

1) 11 IbJhr per Rule 475 PM Limrt 

Gemma 

Sentinel 

4 

S-4!STK·PM·loo·1 

SCAQMOS.l 

211112013 

8:41 

12:55 

17-WCS 

0,84 

0.996 

143.14 

240 

29.64 

0.234 

2.40 

769.4 

1.5320 

12.99 

4.44 

183.160 

58,6 

175 

432.2 

181.978 

0.099 

28.11 

107.48 

923,058 

350,311 

103.70 

8845.2 

0.885 

17.2 

0.0015 

0.0033 

0.0011 

0.0039 

4,38 

4,95 

Reference Temp (F). 60 

Fuel Nat. Gas 

Data By AA 

Average Limits 

2.40 

769.4 

1.5320 

13.0 

4.4 

183,16 

58.6 

1.75 

432.2 

181 .978 

0.099 

28.11 

107.48 

923,058 

350,311 

103.70 

8845.2 

0,885 

17.2 

0.0015 

0,0033 

0,0011 

0,0039 

4.38 

4.95 

Limits 

0.01 

01 

11 

5.71 

Sentinel Un it 4 IOI ~'" PM 

S"n\JTW~ 

21111201J 

2:l 1 PM 
. I ; I 

; 

~ i '- :- - .~ 

~ - , 

~ , 

, 

~ 

Hit jl I t--

t--

. ~ 

.1, 

t-- l=j t-- R I . . 

I I

t--

- . ~ 

Page I 
SCAQMD METHOD 5,1 PARTICULATE TEST DATA SUMMARY 

Client/Location, 

Unit 

Sample Location 

Test No, 

Test Method 

Date 

Start Time 

Stop Time 

Sample Train 

Pitot Factor 

Meter Cal Factor 

Stack Area (sq ttl 

Sample Time (Min) 

Bar Press (in Hg) 

Nozzle Diam (in) 

Stack Press (iwg) 

Stack Temp (F) 

Vel Head (iwg) 

Stack 02 (%) 

Slack C02 (%) 

Meter Vol (act) 

Meter Temp (F) 

Meter Press (iwg) 

liquid Vol (mil 

Sid Sample Vol (SCF) 

MOisture Fraction 

Slacll Gas Mol Wt 

Stack Gas Velocity (flJsec) 

Stacll Flow Rate (wacfm) 

StaCk Flow Rate (dscfm) 

Iso kinetic Ratio !%) 

Facility Average Gas Flow (hscfh) .. 

Facility Average Gas Flow (MMscfh) 

Tolal Weight Gain, mq .. 

Particulate Emissions 

Grain Loading, gr/dscf... 

Grain Loading @ 3% 02 .. 

Grain Loading@ 15% 02 ... 

Grain Loading@ 12% C02 . 

Mass Emlssions, lblhr'

. 

Emission Rate, Ib/MMSCF 

1) 11 Iblhr per Rule 475 PM Limit 

Gemma 

Sentinel 

4 

S·4/STK·PM·75·1 

SCAQM0 5.1 

2111/2013 

14:48 

18:56 

17-wes 

0.84 

0.996 

143.14 

240 

29.64 

0.234 

2.40 

752.4 

1.3751 

13.83 

4.05 

174.630 

52.6 

1.52 

380.9 

175.437 

0.092 

28.17 

101.01 

867,518 

336,734 

104.01 

5:;74.0 

0.697 

44 

0.0004 

0.0010 

0.0003 

0.0011 

1.12 

1.60 

Reference Temp (F), 60 

Fuel Nat. Gas 

Data By 

AYerage 

2.40 

752.4 

1.3751 

13.8 

4.0 

174.63 

52.6 

1.52 

380.9 

175.437 

0.092 

28.17 

101.01 

867,518 

336,734 

104.01 

6974.0 

0.697 

4.4 

0.0004 

0.0010 

0.0003 

0.0011 

1.12 

1.60 

AA 

Limits 

Limits 

0.01 

0.1 

11 

5.71 

Senli"d Unil ~ 15% PM 

Su",n' ' 

21211200 

22~ PM 
I 

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Page I 
DeI/all ... <>-, .... ,.~ .... 

SCACMD METHOD 5.1 PARTICULATE TEST DATA SUMMARY 

Client/location. 

Unit 

Sample Locatkm 

Test No. 

Tes\ Mettlod 

Date 

Start Time 

SlOp Time 

Sample Train 

Pilot Factor 

Meier Cal Factor 

Stack Area (sq ttl 

Sample Time (Min) 

Bar Press (in Hg) 

Nozzle Diam (in) 

Stack Press (iwg) 

Stack Temp (F) 

Vel Head fiwg) 

Stack 02 (%) 

Stack C02 (%) 

Meter Vol (sct) 

Meter Temp (F) 

Meier Press (iwgl 

Liguid Vol (ml) 

SId Sample Vot (SCF) 

Moisture Fraction 

Slack Gas Mol IIV\ 

Slack Gas Velocity (ft/sec) 

S1aCk Flow Rate (wacfm) 

StadI: Flow Rate (dsdm) 

l50klnetlc Ratio ("to) 

Faollty Average Gas Flow (hsdh) .. 

Facility Average Gas Flow (MMsdh) .. 

Total Weight Gain m9 .. 

Particulate Emissions 

Grain Loading, gr/dscf .. 

Grain Loading tm 3% 02. 

Grain Loading tm 15% 02 ... 

Grain Loal1ing tm 12% C02 

Mass Emissions, Iblhrl. ...... . 

EmiSSion Rate, IblMMSCF 

1) 11 Ibl1"1r per Rule 475 PM Umit 

Gemma 

Sentinel 

4 

S-4!STK-PM-50-1 

SCAQMDS.l 

2112/2{113 

11 .45 

15:52 

H-wes 

084 

0.996 

143.14 

240 

2974 

0.234 

2.40 

785.6 

0.7075 

1423 

379 

134.830 

73.6 

078 

241 .5 

130.327 

0.079 

26.29 

73.17 

626,365 

241,434 

107.76 

5354. 1 

0.535 

" 

0.0007 

0.0018 

0,0006 

0,0022 

1,42 

2.65 

Reference Temp (F). 60 

Fuel Nat Gas 

Oatil By 

Average 

2.40 

785.6 

0.7075 

'" 3.8 

134.83 

73.6 

0.76 

2415 

130.327 

0.079 

28.29 

73.17 

628.365 

241,434 

107.76 

535-4.1 

0535 

5.8 

0.0007 

0.0016 

0.0006 

0.0022 

1.42 

2.65 

AA 

Limits 

Limits 

0.01 

0.1 

11 

5.71 

Sc:millci Unil4 ~O% PM 

Summa!)' 

212112013 

1:27 PM 
'.46 

~ ~~. . 

~ 

~ 

Page I 
CPV SENTINEL UNIT 4 

PARTICULATE TEST 

STACK 0" CO, DATA 

Test #: S-4/STK-PM-100-1 

Date: 2111/2013 

Time: 8:41 12:55 

Load: 107 MW 

O2 CO2 

Range 20 10 

Cal Gas 9.98 4.96 

Analyzer Zero 0.11 -0.02 

Analyzer Span 10.00 5.11 

Pre-Bias Zero 0.17 0.02 

Pre-Bias Span 10.35 505 

Post-Bias Zero 0.17 0.03 

Post-Bias Span 10.02 5.07 

Average Bias Zero 0.17 0.02 

Average Bias Span 10.18 5.06 

Pre-test zero bias 0.3% 0.4% 

Pre-test span bias 1.7% -0.6% 

Post-test zero bias 0.3% 0.4% 

Post-test span bias 0.1% -0.4% 

Zero Drift 0.0% 0.1% 

Span Drift -1.6% 0.1% 

Test Results (from data logger average) 

Average 13.20 4.53 

Cal Corrected 12.99 4.44 
O2 CO2 

Date Time % % 

2/11/2013 8:42:00 13.139 4.574 

2/11/2013 8:43:00 13.141 4.574 

2/11/2013 8:44:00 13.143 4.574 

2/11 /2013 8:45:00 13.146 4.572 

2/11/2013 8:46:00 13.153 4.572 

2/11 /2013 8:47:00 13.153 4.573 

2/11 /2013 8:48:00 13.155 4.571 

2/11/2013 8:49:00 13.148 4.574 

2/11/2013 8:50:00 13.15 4.574 

2/11/2013 8:51 :00 13.156 4.568 

2/11 /2013 8:52:00 13.176 4.557 

2/11/2013 8:53:00 13.178 4.557 

2/11/2013 8:54:00 13.176 4.556 

2/11 /2013 8:55:00 13.168 4.559 

2/11 /2013 8:56:00 13.189 4.54 

2/11/2013 8:57:00 13.193 4.541 

2/11/2013 8:58:00 13.191 4.542 

2/11 /2013 8:59:00 13.186 4.552 

2/11/2013 9:00:00 13.188 4.546 

2/11 /2013 9:01 :00 13.18 4.552 

2/11/2013 9:02:00 13.187 4.55 

2/11/2013 9:03:00 13.182 4.556 

2/11/2013 9:04:00 13.199 4.544 

2/11/2013 9:05:00 13.182 4.561 

2/11 /2013 9:06:00 13.156 4.572 

2/11 /2013 9:07:00 13.128 4.588 

2/11/2013 9:08:00 13.111 4.6 

2/11 /2013 9:11 :00 13.169 4.568 

2/11/2013 9:12:00 13.152 4.576 

2/11/2013 9:13:00 13.176 4.558 

2/11 /2013 9:14:00 13.191 4.55 

2/11 /2013 9:1500 13.183 4.556 

2/11/2013 9:16:00 13.188 4.556 

2/11/2013 9:17:00 13.152 4.583 

2/11/2013 9:20:00 13.186 4.565 

2/11/2013 9:21 :00 13.193 4.554 

2/11/2013 9:22:00 13.183 4.567 

2/11 /2013 9:23:00 13.189 4.557 

2/11 /2013 9:24:00 13.183 4.561 

2/11/2013 9:25:00 13.182 4.558 

2/11 /2013 9:26:00 13.163 4.567 

2/11 /2013 9:27:00 13.176 4.56 

2/11/2013 9:29:00 13.199 4.549 

2/11 /2013 9:30:00 13.2 4.544 

2/11/2013 9:31 :00 13.204 4.543 

2/11/2013 9:32:00 13.207 4.544 

2/11 /2013 9:33:00 13.224 4.533 

2/11 /2013 9:34:00 13.219 4.538 

2/11/2013 9:35:00 13.21 4.542 
2/11 /2013 9:36:00 13.215 4.54 

2/11/2013 9:59:00 13.221 4.519 

2/11/2013 10:00:00 13.207 4.527 

2/11 /2013 10:01 :00 13.216 4.524 

2/11 /2013 10:02:00 13.215 4.526 

2/11 /2013 10:03:00 13.225 4.523 

2/11/2013 10:04:00 13.234 4.521 

2/11/2013 10:05:00 13.25 4.513 

2/11/2013 10:06:00 13.234 4.519 

2/11/2013 10:07:00 13.223 4.527 

2/11/2013 10:08:00 13.222 4.528 

2/11/2013 10:09:00 13.227 4.526 

2/11/2013 10:10:00 13.222 4.528 

2/11/2013 10:11 :00 13.219 4.532 

2/11 /2013 10:12:00 13.219 4.528 

2/11 /2013 10:13:00 13.211 4.533 

2/11 /2013 10:14:00 13.227 4.524 

2/11 /2013 10:15:00 13.218 4.531 

2/11/2013 10:16:00 13.205 4.543 

2/11/2013 10:17:00 13.222 4.529 

2/11/2013 10:18:00 13.252 4.514 

2/11/2013 10:19:00 13.231 4.523 

2/11/2013 10:20:00 13.254 4.512 

2/11/2013 10:21 :00 13.255 4.512 

2/11/2013 10:22:00 13.26 4.509 

2/11/2013 10:24:00 13.215 4.531 

2/11 /2013 10:25:00 13.212 4.529 

2/11 /2013 10:26:00 13.232 4.519 

2/11 /2013 10:27:00 13.224 4.522 

2/11 /2013 10:28:00 13.211 4.528 

2/11/2013 10:29:00 13.216 4.521 

2/11/2013 10:30:00 13.233 4.515 

2/11 /2013 10:31 :00 13.211 4.524 

2/11 /2013 10:32:00 13.201 4.531 

2/11 /2013 10:33:00 13.209 4.524 

2/11/2013 10:34:00 13.208 4.523 

2/11/2013 10:35:00 13.215 4.517 

2/11/2013 10:36:00 13.21 4.52 

2/11/2013 10:37:00 13.207 4.521 

2/11/2013 10:38:00 13.203 4.526 

2/11 /2013 10:39:00 13207 4.524 

2/11/2013 10:40:00 13.197 4.528 

2/11 /2013 10:41 :00 13.191 4.529 

2/11/2013 10:42:00 13.192 4.53 

2/11/2013 10:44:00 13.208 4.521 

2/11/2013 10:45:00 13.193 4.531 

2/11 /2013 10:46:00 13.187 4.534 

2/11/2013 10:47:00 13.194 4.529 

2/11/2013 10:48:00 13.197 4.528 

2/11/2013 10:49:00 13.199 4.525 

2/11/2013 10:50:00 13.196 4.529 
2/11 /2013 10:51 :00 13.208 4.521 

2/11 /2013 10:52:00 13.192 4.533 

2/11/2013 10:53:00 13.185 4.542 

2/11/2013 10:54:00 13.182 4.548 

2/11/2013 1055:00 13.179 4.549 

2/11 /2013 10:56:00 13.177 4.551 

2/11 /2013 10:57:00 13.162 4.558 

2/11 /2013 10:58:00 13.171 4.554 

2/1112013 10:59:00 13.163 4.56 

2/11 /2013 11 :00:00 13.162 4.561 

2/11/2013 11 :02:00 13.194 4.541 

2/11 /2013 11 :03:00 13.179 4.548 

2/11 /2013 11 :04:00 13.175 4.548 

2/11/2013 11 :05:00 13.178 4.547 

2/11 /2013 11 :06:00 13.163 4.552 

2/11/2013 11 :07:00 13.166 4.55 

2/11/2013 11 :08:00 13.178 4.543 

2/11/2013 11 :09:00 13.164 4.551 

2/11/2013 11 :10:00 13.172 4.546 

2/11/2013 11 :11 :00 13.173 4.544 

2/11/2013 11 :12:00 13.179 4.538 

2/11 /2013 11 :13:00 13.166 4.548 

2/11 /2013 11 :14:00 13.171 4.541 

2/11/2013 11 :15:00 13.152 4.55 

2/11/2013 11 :16:00 13.166 4.541 

2/11/2013 11 :17:00 13.164 4.543 

2/11 /2013 11 :18:00 13.169 4.54 

2/11 /2013 11 :19:00 13.172 4.54 

2/11/2013 11 :20:00 13.149 4.554 

2/11/2013 11:38:00 13.155 4.521 

2/11/2013 11 :39:00 13.141 4.537 

2/11/2013 11 :40:00 13.164 4.523 

2/11 /2013 11 :41 :00 13.163 4.523 

2/11/2013 11 :42:00 13.151 4.529 

2/11/2013 11 :43:00 13.184 4.505 

2/11/2013 1144:00 13.202 4.494 

2/11/2013 1145:00 13.187 4.508 

2/11/2013 1146:00 13.188 4.505 

2/11/2013 11 :47:00 13.16 4.526 

2/11 /2013 11 :48:00 13.159 4.528 

2/11/2013 1149:00 13.16 4.529 

2/11/2013 11 :50:00 13.173 4.519 

2/11/2013 11 :51 :00 13.185 4.512 

2/11 /2013 11 :52:00 13.153 4.536 

2/11/2013 11 :53:00 13.135 4.548 

2/11/2013 11 :54:00 13.149 4.543 

2/11/2013 11 :55:00 13.111 4.568 

2/11 /2013 11 :56:00 13.124 4.56 

2/11/2013 11 :57:00 16.839 2.421 

2/11 /201 3 11 :58:00 13.186 4.525 

2/11 /2013 11 :59:00 13.161 4.54 

2/11/2013 12:0000 13.174 4.535 
2/11/2013 12:01 :00 13.174 4.534 

2/11/2013 12:02:00 13.196 4.515 

2/11/2013 12:03:00 13.185 4.522 

2/11/2013 12:04:00 13.187 4.523 

2/11/2013 12:05:00 13.172 4.537 

2/11/2013 12:06:00 13.177 4.534 

2/11 /2013 12:07:00 13.179 4.532 

2/11 /2013 12:08:00 13.173 4.537 

2/11/2013 12:09:00 13.177 4.535 

2/11/2013 12:10:00 13.192 4.521 

2/11/2013 12:11:00 13.187 4.525 

2/11/2013 12:12:00 13.198 4.518 

2/11/2013 12:13:00 13.191 4.525 

2/11 /2013 12:14:00 13.184 4.533 

2/11 /2013 12:15:00 13.188 4.528 

2/11/2013 12:16:00 13.184 4.529 

2/11/2013 12:18:00 13.212 4.512 

2/11/2013 12:19:00 13.187 4.524 

2/11/2013 12:20:00 13.179 4.53 

2/11 /2013 12:21 :00 13.174 4.533 

2/11/2013 12:22:00 13.162 4.54 

2/11/2013 12:23:00 13.159 4.541 

2/11/2013 12:24:00 13.156 4.543 

2/11/2013 12:25:00 13.155 4.544 

2/11/2013 12:26:00 13.157 4.542 

2/11/2013 12:27:00 13.156 4.542 

2/11/2013 12:28:00 13.164 4.537 

2/11 /2013 12:29:00 13.178 4.528 

2/11/2013 12:30:00 13.174 4.531 

2/11/2013 12:31 :00 13.172 4.531 

2/11 /2013 12:32:00 13.168 4.534 

2/11/2013 12:33:00 13.178 4.528 

2/11/2013 12:34:00 13.174 4.531 

2/11/2013 12:35:00 13.176 4.531 

2/11/2013 12:36:00 13.181 4.524 

2/1112013 1238:00 13.191 4.514 

2/11/2013 12:39:00 13.173 4.527 

2/11/2013 12:40:00 13.176 4.527 

2/11/2013 12:41:00 13.169 4.531 

2/11/2013 12:42:00 13.165 4.533 

2/11/2013 12:43:00 13.157 4.534 

2/11 /2013 12:44:00 13.164 4.527 

2/11 /2013 12:45:00 13.145 4.536 

2/11 /2013 12:46:00 13.134 4.538 

2/11/2013 12:47:00 13.143 4.531 

2/11/2013 12:48:00 13.139 4.534 

2/11 /2013 12:49:00 13.13 4.54 

2/11 /2013 12:50:00 13.119 4.547 

2/11/2013 12:51 :00 13.128 4.544 

2/11/2013 12:52:00 13.124 4.549 

2/11/2013 12:53:00 13.127 4.548 

2/11/2013 12:54:00 13.129 4.548 
2/11/2013 12:55:00 13.128 4.551 

Average 13.20 4.53 
Test #: 

Date: 

Time: 

Load: 

CPV SENTINEL UNIT 4 

PARTICULATE TEST 

STACK O2• CO2 DATA 

S-4/STK-PM-75-1 

2111/2013 

14:48 18:56 

81 MW 

O2 

Range 20 

Cal Gas 9.98 

Analyzer Zero 0.10 

Analyzer Span 10.04 

Pre-Bias Zero 0.20 

Pre-Bias Span 10.02 

Post-Bias Zero 0.21 

Post-Bias Span 10.03 

Average Bias Zero 0.20 

Average Bias Span 1002 

Pre-test zero bias 0.5% 

Pre-test span bias -0.1% 

Post-test zero bias 0.5% 

Post-test span bias -0.1% 

Zero Drift 0.0% 

Span Drift 0.0% 

CO2 

10 

4.96 

0.01 

5.11 

0.06 

5.11 

0.09 

5.13 

0.08 

5.12 

0.5% 

-0.1% 

0.8% 

0.2% 

0.3% 

0.3% 

Test Results (from data logger average) 

Average 13.81 4.19 

Cal Corrected 13.83 4.05 
O2 CO2 

Date Time % % 

2/11/2013 14:49:00 13.822 4.157 

2/11/2013 14:5000 13.822 4.157 

2/11/2013 14:51 :00 13.822 4.156 

2/11/2013 14:5200 13.821 4.158 

2/11/2013 14:53:00 13.803 4.168 

2/11/2013 14:5400 13.806 4.168 

2/11/2013 14:55:00 13.811 4.169 

2/11/2013 14:56:00 13.809 4.17 

2/11/2013 14:57:00 13.807 4.172 

2/11/2013 14:58:00 13.808 4.17 

2/11/2013 14:59:00 13.809 4.17 

2/11/2013 15:0000 13.819 4.166 

2/11/2013 15:01 :00 13.824 4.166 

2/11/2013 15:02:00 13.832 4.16 

2/11/2013 15:03:00 13.83 4.166 

2/11/2013 15:04:00 13.833 4.16 

2/11/2013 15:05:00 13.832 4.163 

2/11/2013 15:06:00 13.832 4.164 

2/11/2013 15:07:00 13.836 4.16 

2/11/2013 15:08:00 13.837 4.16 

2/11 /2013 15:09:00 13.837 4.161 

2/11/2013 15:10:00 13.836 4.159 

2/11/2013 15:11:00 13.835 4.155 

2/11/2013 15:12:00 13.837 4.15 

2/11/2013 15:13:00 13.829 4.154 

2/11 /2013 15:14:00 13.831 4.153 

2/11/2013 15:15:00 13.832 4.15 

2/11/2013 15:16:00 13.84 4.144 

2/11 /2013 15:17:00 13.82 4.155 

2/11/2013 15:18:00 13.826 4.152 

2/11/2013 15:19:00 13.818 4.159 

2/11/2013 15:20:00 13.801 4.167 

2/11/2013 15:2100 13.798 4.166 

2/11/2013 15:22:00 13.806 4.165 

2/11/2013 15:23:00 13.795 4.167 

2/11/2013 15:24:00 13.79 4.169 

2/11/2013 15:25:00 13.802 4.165 

2/11/2013 15:26:00 13.803 4.167 

2/11/2013 15:2700 13.807 4.165 

2/11 /2013 15:2800 13.817 4.16 

2/11 /2013 15:29:00 13.8 4.169 

2/11 /2013 15:30:00 13.806 4.166 

2/11/2013 15:31 :00 13.806 4.162 

2/11/2013 15:3200 13.808 4.16 

2/11/2013 15:33:00 13.816 4.161 

2/11/2013 15:34:00 13.825 4.168 

2/11/2013 15:35:00 13.828 4.169 

2/11 /2013 15:36:00 13.829 4.171 

2/11/2013 15:37:00 13.83 4.171 

2/11 /2013 15:38:00 13.825 4.177 

2/11/2013 15:39:00 13.829 4.177 

2/11/2013 15:40:00 13.83 4.176 
2/11 /2013 15:41 :00 13.823 4.179 

2/11 /2013 15:42:00 13.832 4.175 

2/11 /2013 15:43:00 13.833 4.176 

2/11/2013 15:44:00 13.832 4.18 

2/1 1/2013 15:45:00 13.829 4.185 

2/11 /2013 15:46:00 13.827 4.187 

2/11/2013 15:47:00 13.829 4.187 

2/11 /2013 15:48:00 13.824 4.188 

2/11/2013 15:49:00 13.83 4.183 

2/11/2013 15:50:00 13.833 4.18 

2/11/2013 155100 13.824 4.187 

2/11/2013 15:52:00 13.829 4.186 

2/11/2013 15:53:00 13.821 4.191 

2/11/2013 15:54:00 13.817 4.196 

2/11 /2013 15:55:00 13.81 4.202 

2/11 /2013 15:56:00 13.804 4.208 

2/11 /2013 15:57:00 13.772 4.225 

2/11 /2013 15:58:00 13.773 4.226 

2/11/2013 15:59:00 13.776 4.228 

2/11 /2013 16:00:00 13.774 4.227 

2/11 /2013 16:03:00 13.832 4.193 

2/11/2013 16:04:00 13.831 4.2 

2/11/2013 16:05:00 13.832 4.196 

2/11/2013 16:06:00 13.834 4.192 

2/11/2013 16:07:00 13.833 4.194 

2/11/2013 16:08:00 13.831 4.201 

2/11/2013 16:09:00 13.824 4.202 

2/11 /2013 16:10:00 13.83 4.197 

2/11 /2013 16: 11 :00 13.827 4.193 

2/11 /2013 16:12:00 13.83 4.186 

2/11 /2013 16:13:00 13.818 4.191 

2/11 /2013 16:14:00 13.805 4.197 

2/11 /2013 16: 15:00 13.799 4.201 

2/11/2013 16:16:00 13.802 4.201 

2/11/2013 16:1 7:00 13.804 4.201 

2/11 /2013 16:18:00 13.806 4.202 

2/11/2013 16.21 :00 13.823 4.192 

2/11/2013 16:22:00 13.814 4.195 

2/11/2013 16:23:00 13.811 4.198 

2/11/2013 16:24:00 13.817 4.196 

2/11/2013 16:25:00 13.819 4.195 

2/11 /2013 16.26:00 13.835 4.188 

2/11 /2013 16:27:00 13.832 4.187 

2/11/2013 16:28:00 13.831 4.19 

2/11 /2013 16:29:00 13.829 4.194 

2/11/2013 16:30:00 13.831 4.192 

2/11 /2013 16:31 :00 13.823 4.194 

2/11 /2013 16:32:00 13.796 4.212 

2/11 /2013 16:33:00 13.797 4.21 

2/11/2013 16:34:00 13.807 4.207 

2/11/2013 16:35:00 13.819 4.2 
2/11/2013 16:38:00 13.839 4.183 

2/11/2013 16:3900 13.843 4.181 

2/11/2013 16:40:00 13.831 4.19 

2/11/2013 16:4100 13.829 4.189 

2/11/2013 16:42:00 13.83 4.192 

2/11/2013 16:43:00 13.825 4.193 

2/11/2013 16:44:00 13.801 4.207 

2/11/2013 16:45:00 13.799 4.21 

2/11/2013 16:46:00 13.801 4.21 

2/11/2013 16:47:00 13.794 4.215 

2/11/2013 16:48:00 13.806 4.209 

2/11/2013 16:49:00 13.756 4.236 

2/11/2013 16:50:00 13.761 4.236 

2/11/2013 16:5100 13.765 4.236 

2/11/2013 16:52:00 13.769 4.24 

2/11/2013 16:53:00 13.787 4.231 

2/11/2013 16:5400 13.797 4.226 

2/11/2013 17:0900 13.844 4.168 

2/11/2013 17:10:00 13.798 4.187 

2/11/2013 17:11:00 13.79 4.192 

2/11/2013 17:12:00 13.789 4.193 

2/11/2013 17:13:00 13.794 4.193 

2/11/2013 17:14:00 13.799 4.193 

2/11/2013 17:15:00 13.802 4.191 

2/11/2013 17:16:00 13.81 4.189 

2/11/2013 17:17:00 13.786 4.201 

2/11/2013 17:18:00 13.783 4.204 

2/11/2013 17:19:00 13.785 4.205 

2/11/2013 17:20:00 13.775 4.211 

2/11/2013 17:21 :00 13.765 4.219 

2/11/2013 17:22:00 13.74 4.23 

2/11/2013 17:23:00 13.753 4.228 

2/11/2013 17:24:00 13.756 4.225 

2/11/2013 1725:00 13.754 4.226 

2/11/2013 1726:00 13.847 4.141 

2/11/2013 17:28:00 13.829 4.187 

2/11/2013 1729:00 13.803 4.204 

2/11/2013 17:30:00 13.804 4.205 

2/11/2013 1731 :00 13.827 4.194 

2/11/2013 17:32:00 13.822 4.197 

2/11/2013 17:33:00 13.832 4.191 

2/11/2013 17:34:00 13.803 4.211 

2/11/2013 17:35:00 13.799 4.21 

2/11/2013 17:36:00 13.785 4.218 

2/11/2013 17:37:00 13.788 4.218 

2/11/2013 17:38:00 13778 4.225 

2/11/2013 17:39:00 13773 4.23 

2/11/2013 17:40:00 13.747 4.245 

2/11/2013 17:41 :00 13.765 4.237 

.• 2/11/2013 17:42:00 13.755 4.245 

2/11/2013 17:43:00 13.757 4.248 
2/11 /2013 17:46:00 13.821 4.204 

2/11/2013 17:47:00 13.825 4.201 

2/11/2013 17:48:00 13.822 4.198 

2/11/2013 17:49:00 13.817 4.199 

2/11/2013 17:50:00 13.808 4.197 

2/11/2013 17:51 :00 13.809 4.195 

2/11/2013 17:52:00 13.806 4.19 

2/11/2013 17:53:00 13.818 4.184 

2/11/2013 17:54:00 13.821 4.179 

2/11/2013 17:5500 13.814 4.185 

2/11/2013 17:56:00 13.814 4.186 

2/11/2013 17:57:00 13.804 4.194 

2/11/2013 17:58:00 13.793 4.201 

2/11/2013 17:59:00 13.797 4.201 

2/11 /2013 18:00:00 13.805 4.193 

2/11/2013 18:01 :00 13.805 4.193 

2/11/2013 18:04:00 13.821 4.18 

2/11/2013 18:05:00 13.806 4.187 

2/11 /2013 18:06:00 13.805 4.189 

2/11 /2013 1807:00 13.807 4.19 

2/11/2013 18:08:00 13.816 4.187 

2/11/2013 18:09:00 13.814 4.19 

2/11 /2013 18:10:00 13.807 4.195 

2/11/2013 18:11:00 13.812 4.197 

2/11/2013 18:12:00 13.809 4.197 

2/11/2013 18:13:00 13.807 4.201 

2/11/2013 18:14:00 13.812 4.199 

2/11/2013 18:15:00 13.81 4.202 

2/11 /2013 18:16:00 13.803 4.207 

2/11/2013 18:17:00 13.804 4.208 

2/11/2013 18:1800 13.808 4.21 

2/11 /2013 18:19:00 13.81 4.212 

2/11 /2013 18:39:00 13.788 4.174 

2/11/2013 18:40:00 13.818 4.192 

2/11/2013 18:41 :00 13.83 4.193 

2/11/2013 18:42:00 13.83 4.196 

2/11/2013 18:43:00 13.831 4.198 

2/11/2013 18:44:00 13.827 4.201 

2/11/2013 18:45:00 13.823 4.204 

2/11 /2013 18:4600 13.816 4.206 

2/11/2013 18:47:00 13.813 4.207 

2/11 /2013 18:48:00 13.804 4.212 

2/11/2013 18:49:00 13.804 4.208 

2/11/2013 18:50:00 13.806 4.208 

2/11 /2013 18:52:00 13.875 4.173 

2/11/2013 18:53:00 13.832 4.19 

2/11/2013 18:54:00 13.835 4.191 

2/11 /2013 18:55:00 13.841 4.189 

2/11 /2013 18:56:00 13.848 4.185 
Average 13.81 4.19 
CPV SENTINEL UNIT 4 

PARTICULATE TEST 

STACK O2• CO2 DATA 

Test #: S-4/STK-PM-50-1 

Date: 2112/2013 

Time: 11:45 15:52 

Load: 55MW 

O2 CO2 

Range 20 10 

Cal Gas 9.98 4.96 

Analyzer Zero 0.10 0.10 

Analyzer Span 10.05 5.20 

Pre-Bias Zero 0.13 0.12 

Pre-Bias Span 10.03 5.18 

Post-Bias Zero 0.16 0.18 

Post-Bias Span 10.02 5.23 

Average Bias Zero 0.15 0.15 

Average Bias Span 10.02 5.20 

Pre-test zero bias 0.1% 0.3% 

Pre-test span bias -0.1% -0.2% 

Post-test zero bias 0.3% 0.9% 

Post-test span bias -0.1% 0.3% 

Zero Drift 0.2% 0.6% 

Span Drift 0.0% 0.5% 

Test Results (from data logger average) 

Average 14.23 4.01 

Ca I Corrected 14.23 3.79 
O2 CO2 

Date Time % % 

2/12/2013 11 :46:00 14.268 3.977 

2/12/2013 11:47:00 14.285 3.977 

2/12/2013 11 :48:00 14.278 3.987 

2/12/2013 11 :49:00 14.268 3.991 

2/12/2013 11 :50:00 14.265 3.997 

2/12/2013 11 :51:00 14.255 3.999 

2/12/2013 11 :52:00 14.244 3.996 

2/12/2013 11 :53:00 14.257 3.994 

2/12/2013 11 :54:00 14.275 3.997 

2/12/2013 11 :55:00 14.27 3.999 

2/12/2013 11 :56:00 14.266 4.001 

2/12/2013 11 :57:00 14.267 4.002 

2/12/2013 11 :58:00 14.27 4.001 

2/12/2013 11 :59:00 14.269 4.003 

2/12/2013 12:00:00 14.268 4.002 

2/12/2013 12:01 :00 14.27 4.001 

2/12/2013 12:02:00 14.283 3.994 

2/12/2013 12:03:00 14.279 3.998 

2/12/2013 12:04:00 14.277 4 

2/12/2013 12:05:00 14.242 4.017 

2/12/2013 12:06:00 14.263 4.005 

2/12/2013 12:07:00 14.263 4.007 

2/12/2013 12:08:00 14.246 4.015 

2/12/2013 12:09:00 14.241 4.021 

2/12/2013 12:10:00 14.204 4.047 

2/12/2013 12:11 :00 14.204 4.048 

2/12/2013 12:12:00 14.204 4.05 

2/12/2013 12:13:00 14.198 4049 

2/12/2013 12:14:00 14.197 4.052 

2/12/2013 12:17:00 14.286 3.995 

2/12/2013 12:18:00 14.285 3.994 

2/12/2013 12:19:00 14.277 3.997 

2/12/2013 12:20:00 14.278 3.995 

2/12/2013 12:21 :00 14.268 3.999 

2/12/2013 12:22:00 14.274 3.996 

2/12/2013 12:23:00 14.271 3.996 

2/12/2013 12:24:00 14.266 3.994 

2/12/2013 12:25:00 14.265 3.993 

2/12/2013 12:26:00 14.264 3.991 

2/12/2013 12:27:00 14.268 3.988 

2/12/2013 12:28:00 14.266 3.989 

2/12/2013 12:29:00 14.259 3.992 

2/12/2013 12:30:00 14.264 3.989 

2/12/2013 12:31 :00 14.261 3.99 

2/12/2013 12:32:00 14.262 3.989 

2/12/2013 12:34:00 14.249 3.996 

2/12/2013 12:35:00 14.241 3.999 

2/12/2013 12:36:00 14.252 3.993 
2/12/2013 12:37:00 14.238 4 

2/12/2013 12:38:00 14.242 3.999 

2/12/2013 12:39:00 14.251 3.995 

2/12/2013 12:40:00 14.23 4.007 

2/12/2013 12:41 :00 14.207 4.018 

2/12/2013 12:42:00 14.257 3.991 

2/12/2013 12:43:00 14.259 3.994 

2/12/2013 12:44:00 14.255 3.995 

2/12/2013 12:45:00 14.255 3.996 

2/12/2013 12:46:00 14.191 4.035 

2/12/2013 12:47:00 14.176 4.041 

2/12/2013 12:48:00 14.18 4.04 

2/12/2013 12:49:00 14.19 4.033 

2/12/2013 12:50:00 14.195 4.032 

2/12/2013 12:52:00 14.308 3.972 

2/12/2013 12:53:00 14.286 3.981 

2/12/2013 12:54:00 14.288 3.978 

2/12/2013 12:5500 14.283 3.982 

2/12/2013 12:56:00 14.277 3.983 

2/12/2013 12:57:00 14.277 3.984 

2/12/2013 12:58:00 14.28 3.983 

2/12/2013 12:59:00 14.286 3.978 

2/12/2013 13:00:00 14.282 3.982 

2/12/2013 13:01 :00 14.279 3.983 

2/12/2013 13:02:00 14.279 3.983 

2/12/2013 13:03:00 14.264 3.992 

2/12/2013 13:04:00 14.262 3.991 

2/12/2013 13:05:00 14.257 3.995 

2/12/2013 13:06:00 14.259 3.992 

2/12/2013 13:07:00 14.256 3.996 

2/12/2013 13:08:00 14.25 3.999 

2/12/2013 13:28:00 14.133 3.95 

2/12/2013 13:29:00 14.218 3.996 

2/12/2013 13:30:00 14.219 3.997 

2/12/2013 13:31 :00 14.213 3.999 

2/12/2013 13:32:00 14.227 3.992 

2/12/2013 13:33:00 14.214 3.997 

2/12/2013 13:34:00 14.208 4.001 

2/12/2013 13:35:00 14.221 3.997 

2/12/2013 13:36:00 14.229 3.995 

2/12/2013 13:37:00 14.201 4.016 

2/12/2013 13:38:00 14.205 4.01 

2/12/2013 13:39:00 14.203 4.015 

2/12/2013 13:4000 14.202 4.016 

2/12/2013 13:41:00 14.203 4.018 

2/12/2013 13:42:00 14.171 4.037 

2/12/2013 13:43:00 14.162 4.038 

2/12/2013 13:44:00 14.171 4.033 

2/12/2013 13:45:00 14.171 4.036 

2/12/2013 13:46:00 14.168 4.039 

2/12/2013 13:49:00 14.259 3.988 
2/12/2013 13:50:00 14.25 3.995 

2/12/2013 13:51 :00 14.252 3.995 

2/12/2013 13:52:00 14.251 3.996 

2/12/2013 13:53:00 14.239 4.003 

2/12/2013 13:54:00 14.25 3.999 

2/12/2013 13:5500 14.235 4.007 

2/12/2013 13:56:00 14.232 4.008 

2/12/2013 13:57:00 14.232 4.009 

2/12/2013 13:58:00 14.228 4014 

2/12/2013 13:59:00 14.226 4016 

2/12/2013 14:00:00 14.233 4012 

2/12/2013 14:01 :00 14.231 4014 

2/12/2013 14:02:00 14.224 4.018 

2/12/2013 14:03:00 14.217 4.022 

2/12/2013 14:04:00 14.212 4.025 

2/12/2013 14:06:00 14.302 4.022 

2/12/2013 14:07:00 14.203 4.037 

2/12/2013 14:08:00 14.203 4.036 

2/12/2013 14:09:00 14.2 4041 

2/12/2013 14:10:00 14.203 4.038 

2/12/2013 14:11 :00 14.203 4.041 

2/12/2013 14:12:00 14.203 4042 

2/12/2013 14:13:00 14.201 4045 

2/12/2013 14:14:00 14.203 4.041 

2/12/2013 14:15:00 14.203 4.041 

2/12/2013 14:16:00 14.203 4.045 

2/12/2013 14:17:00 14.197 4.048 

2/12/2013 14:18:00 14.2 4.049 

2/12/2013 14:19:00 14.203 4.047 

2/12/2013 14:20:00 14.203 4.047 

2/12/2013 14:21 :00 14.199 4.051 

2/12/2013 14:22:00 14.196 4.052 

2/12/2013 14:25:00 14.226 4.03 

2/12/2013 14:26:00 14.227 4.028 

2/12/2013 14:27:00 14.225 4.031 

2/12/2013 14:28:00 14.224 4.035 

2/12/2013 14:29:00 14.216 4.035 

2/12/2013 14:30:00 14.224 4.032 

2/12/2013 14:31 :00 14.225 4.032 

2/12/2013 14:32:00 14.232 4.028 

2/12/2013 14:33:00 14.237 4027 

2/12/2013 14:34:00 14.234 4.029 

2/12/2013 14:35:00 14.229 4.032 

2/12/2013 14:36:00 14.225 4.033 

2/12/2013 14:3700 14.232 4.029 

2/12/2013 1438:00 14.234 4.027 

2/12/2013 14:39:00 14.236 4027 

2/12/2013 14:40:00 14.233 4.028 

2/12/2013 15:0100 14.257 4.007 

2/12/2013 15:02:00 14.241 4.012 

2/12/2013 15:03:00 14.24 4.017 
2/12/2013 15:04:00 14.234 4.02 

2/12/2013 15:05:00 14.23 4.019 

2/12/2013 15:06:00 14.224 4.024 

2/12/2013 15:07:00 14.228 4.025 

2/12/2013 15:08:00 14.225 4.026 

2/12/2013 15:0900 14.223 4.027 

2/12/2013 151000 14.208 4.032 

2/12/2013 15:11:00 14.213 4.03 

2/12/2013 15:12:00 14.22 4.025 

2/12/2013 151300 14.212 4.028 

2/12/2013 15:14:00 14.222 4.028 

2/12/2013 15:15:00 14.225 4.026 

2/12/2013 15:16:00 14.23 4.023 

2/12/2013 15:17:00 14.229 4.026 

2/12/2013 15:1800 14.233 4.023 

2/12/2013 15:19:00 14.227 4.027 

2/12/2013 15:20:00 14.223 4.028 

2/12/2013 15:21 :00 14.216 4.032 

2/12/2013 15:22:00 14.216 4.031 

2/12/2013 15:23:00 14.21 4.032 

2/12/2013 15:24:00 14.207 4.031 

2/12/2013 15:25:00 14.207 4.03 

2/12/2013 15:26:00 14.213 4.028 

2/12/2013 15:27:00 14.219 4.025 

2/12/2013 15:28:00 14.222 4.025 

2/12/2013 15:29:00 14.217 4.03 

2/12/2013 15:30:00 14.218 4.029 

2/12/2013 15:31 :00 14.221 4.027 

2/12/2013 15:32:00 14.229 4.024 

2/12/2013 15:33:00 14.225 4.026 

2/12/2013 15:34:00 14.225 4.026 

2/12/2013 15:35:00 14.23 4.025 

2/12/2013 15:36:00 14.229 4.024 

2/12/2013 15:37:00 14.217 4.031 

2/12/2013 15:38:00 14.218 4.033 

2/12/2013 15:39:00 14.238 4.023 

2/12/2013 15:40:00 14.237 4.023 

2/12/2013 15:41 :00 14.24 4.022 

2/12/2013 15:42:00 14.237 4.025 

2/12/2013 15:43:00 14.224 4.028 

2/12/2013 15:44:00 14.232 4.025 

2/12/2013 15:45:00 14.236 4.022 

2/12/2013 15:46:00 14.232 4.026 

2/12/2013 15:47:00 14.23 4.027 
... De//a!J. 

__ ... - WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD ., 

CLIENT: c- G 1'4 I,-,t I>' 

LOCATION: -;e\;'\:'i""C\.... 

DATE: 2. 11- I'} 

RUN NO: 5- 1f611< - /'1>/ - I CC - I 

OPERATOR: K/.\~' 1'1 

METER BOX NO: / 7 - '--' "':' 

METER ~H@: ~ t 

METER Yd: 4~?- 1'2 htT f 

STACK AREA, FT : J :5. / 

TRAVERSE POINTS, MIN!POINT: if)/ 2 'f H= ; , I X~P: / 

Probe Condition, prelpost test: . / 

Silica Gel Expanded, YIN: ~, 

Filter Condition after Test: ~ 

Check Weight: 7 

Meter 

Point I Time I Volume, ft3 

{; I> I c>/'i:JfX161',75(i 

/. I IJ'bi; 1 1 77!5, 1:1 tfJ 

£/ I 0'lD I I 'l.r'i, 02. v 

:J I iJq I r 17'1'2 . '1-">.2 

;2. lo qJ-1 1/;101·8?O 

/ 10 '1 B I 1<o1/0 .{J ~ 5 

(' /IIJ"N I I <{,I</, ,'ill -'" I I · I ~" { I ". - .. (7 v/ (/I.../Lf (. t(: , i (./ ., (.ty l- I, 

'7 loq 5 1-1 1'1. ~ 'I, .).~ L 

1J l ie 0 l{ I 'j, 'h·" c,m.' .'. JI Ll I L/ 1-<;'(1<:;.;" I J 

;z ;o :~ '1 I ~SI , ~ <f u" 

TTi P1.'-¥----'----r;';[ t( \ '~I 

() I'ol.! l( I ~'j,j.. 1:'j 

Average: 

P 

in. H,O 

( . -:L, 

/. " 

I· <'< 

2. . ..1. 

2.. 2. 

--z , ,,",,, 

x. 

J. .-.L 

2. I 

'1... 1 1 

2. '" )- < 

I ,-.!L 

AMBIENT TEMPERATURE: S <'P 

BAROMETRIC PRESSURE :-~:""'"'tj,-, . ,,''1r------ ASSUMED MOISTURE: '" len 

PITOT TUBE COEFF, c -p:-"Cfo=--'-o'=-". <'B~1""------

~~g~~ :~~g~~TE ~~ t R?c,+; 5) 

NOZZLE 10 NO! MATERIAL: £d (!til') ~I - S5 

NOZZLE DIAMETER: Q,2..:;'1 

FILTER NOfTYPE: 'S~,- 11 G '1 'Sz::£L1I<:> 

PRE·TEST LEAK RATE: : <0 ct 2-CFM@ AU in. Hg. 

POST·TEST LEAK RATE: : CFM@ in. Hg. 

PITOT LEAK CHECK· PRE: C-<'O tJ POST:--,-, __ _ 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN 4·,,-__ 

H 

in. H, O 

I .. q 

2 . ...6.. 

2. c.;-

? ~ 

~ . ..J. 

, , <j. p-

"/-

2.."'> 

''7 '1.., 

1. . ') 

1 , 1 

2.,-1 

;2 . '-J 

Stack 

Temp, OF 

7& :; 

7c-. ~ 

7 tP '7 

772., 

'/21 

7 7 '--' 

x . "/C;-7 

110 

'/71 

17 ';L 

17 .?-

17 ; 

SAMPLER en 

SAMPLE C'""U~So;Ti;OD"'IC7A""N-A"~'-

Probe 

T e rllJ>., 0 F 

AI 

;.; 

x 

)< 

x 

x 

x 

x 

)\ 

')( 

A 

2'. 

Filter 

T erllJ>., 0 F 

') .... 

2<, 

)<. 

.;x 

;< 

)( 

L 

x. 

)( 

;A 

~ 

Imp. Out 

Temp, OF 

~s 

51 

S:2-

5 c > 

::52--

" .0 

;><. 

'5/ 

<:':; (";J 

"f'1 

~'i7 

L('C __ L ./ 

d0 

Imp. # Contents Posl·Test· Pre·Test = Difference 

; ~'2~;L <.J3b,b,,;pg2-

;( f!.A1V I';'-"/- cH'i.'l 7,lf;! __ _ 

2- t"';d! bbL (, (-r3sy __ 

~ S6- "65'0, J S!?:r __ 

_ ___ Ii 1:. - lot? H L-__ _ 

Total: ___ _________ _ 

Meter Temp, OF 

In lOut 

5?:: I <?'7 

r :.2- l s'? 

~.c; . ., I 2 

o{, '1 63 

2L 6~; 

.] 7 _ ~ j 

l' A 

'7/ 6-7 

?'7 c., 7 

(,.r'7 ,( " 0tJ c..o 

5-, 57 $"~ ? ~L 

Vacuum 

in. ti9., 

.3 

'" 5 

.s . :;. ~ ~-<-' 

s 

> 

s .- ~. J 

r. 

c-

..L . 

s 

0 , 

% 

P. static 

in. H, O 

T-.2 'IComments: _____________________________________________________________________________________________________________ ___ 

Date of last revision 1/25/2013 Page _\ _ of J- DS834049 

Master Document Storagel FormslDatasheetslField Dalasheets 
... 1Ie1/a~ 0.... __ 

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

(;,!;A/\ IVI ,'1 ) 

AMBIENT TEMPERATURE: ___ 5_- ...J.y..L, ______ _ Imp. # Contents Post-Test - Pre-Test = Difference 

BAROMETRIC PRESSURE: _________ _ 

ASSUMED MOISTURE: 

PITOTTUBE COEFF, C'""Cp'--: - ---------

PROBE 10 NO/MATERIAL: 5 teo; oq ~~~~CELI~N~~H~ATERIAL: ~ §f--

NOZZLE DIAMETER:. _______ ____ _ 

FILTER NO/TYPE: 

PRE-TEST LEAK RCo-A'""'T"'E'""": -: ---C"'F"'M:7@=-----,--in-c.Hc;-g-.-

Probe Condition, pre/post test: ____ _ 

Silica Gel Expanded, Y/N: _ _____ _ 

POST-TEST LEAK RATE: :<i 'L'oZ-CFM@ / <-;, in. Hg./} 

PITOT LEAK CHECK - PRE: POST: 0 " - { 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN-,·::.. J __ _ 

Filter Condition after T est: ______ _ 

Check Weight: _________ _ SAMPLER~~~:-oc;-___ _ 

SAMPLE CUSTODIAN. ___ _ Total: ____ _________ _ 

Meter t.P t.H Stack Probe Filter Imp. Out I Meter Temp, OF l VdeUUI 

Point I Time I Volume, ft3 in. H,O in. H,O Temp, OF Temp, OF Temjl, OF Temp, oL _ In lOut in, Hg. 

lIiU .'> l ieS / I '~7.'I ,} (p(f I. 5 / 77,;;, <::, I :XX I L/~ I ~v I") V- I .y 

5 111o( 1<'(10, 1.'101 I. t> I 17 776 'X )( 4-;, ~s C;</ V 

,v111 11 5ST,5t7::::1~7 1 /; -,;2.- -1 772- Y -;" -1 (/-7 "; ,,-I .c "':> I ) 

-;' 1111/ l:ffJ;;,'1{td I ~ I I "71r.:-rj I X x- !y,.~ £'3 <77, .J" .-

.21 If 31 ICIf '1. li;oI .;;. '12- I I· '.') I "7 7 v I 'X )\ 'Yi I '? <; I s:o", ":> 

I 

U 

IN & 1/(<;:> I ?1!( 79iti (/ 'if..' I '''/ r/ I 7/7 ',) I )" .A '-I'D I -;'1' I :; ::, I .-., .::5 i:):L5" q/~- , Dq":,l (/.] '7' J __ <;t,. -,; I 2&"~ 1 X A q;:.... )-5 "S .2 ~ 

SII ;,7- 1 \- I 'p.l(. 11~ 1 (). 7 0 7 ) 77 I 'x A Lf , I -:;i" I I .c: . 2 ;'" 

!.; I 17. l.. " G(, '1 'hJ I O· q .+- I I 0 11 ~ I X X </ r- I <;:!:. I S" ~ I 'y 

:21 ,7_ .3;- 11 3'7 ,)'iJ I /,S" I ' "1 7'i ( I X X ' 'I (,-- I (,'<1 I ,SJ I '7 ,? ~'.( 7.' (~ \ .~ 

0, 

% 

P. static 

in. H2Q 

l2~ 

Comments: ___________________ __________________________ ______ _ 

Date of last revision 1/25/2013 page ~of L 

DS834049 

Master Document StoragelFormslDatasheetslField Datasheets 
Oe/lafl. 

... ..-.,.--

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: G ~ \'\1\ ..1\ 

LOCATION: 5.ev"-

AMBIENT TEMPERATURE: ¥:. , 

BAROMETRIC PRESSURE: "if Imp. # Contents Post·Test - Pre-Test = Difference 

ASSUMED MOISTURE: /0 ' I C;TifrL", 'li"S.? "1fJ. 'Z-- DATE: 'L-- ' LC/ ,~ RUN NO: S34G pi"\3 )- OPERATOR :: ~~~~~ ____ ~ ____ __ 

PITOT TUBE COEFF, Cp: G,\{=! PROBE 10 NO/MA TERIAL-: --2::-:1"/ '10-"----;<;-, \,',--:~..,>------ ~ 'D]:: 1+ z.., 8'57, 2- 61i. Y 

METER BOX NO: \ " - ____ c \ PROBE LENGTH: G .J? \ NOZZLEIDNO ~A~T ~I L-:~TI- ~)-------------- L <{ ..., gf-: ~ J7. « r"nl 

I METER ilH@: j, 2"1 ~ METER Yd: 0, '2 <; 

STACK AREA, FT" ;If , Ji-L 

NOZZLE DIAMETER: 0, ).) '1 

FILTER NOITYPE: "':i""5';=,T17IT.q--'------------------

PRE,TEST LEAK RATE: :4 .oa 2..CFM@ 7 S in, Hg. :L Si.:r 1l'1.:> 'l)zp 

TRAVERj E POINTS, MIN/POINT:~ 

t.H= \' X t.P: 

Probe Condition, pre/post test:-----':::::: 

POST,TEST LEAK RATE:,;: ,) {Hz.. CFM@ in, Hg. 

PITOT LEAK CHECK - PRE: 1/ POST: L/ 

LI'\ - tuv r1 L 

Silica Gel Expanded, YIN: - CHAIN OF CUSTODY: SAMPLE CUSTODIAN~ 

Filter Condition after Test: ~ SAMPLER f'-. ""'" 

Check Weight: ----- SAMPLE CUSTODIAN I> I:;:: Total: _______________ _ 

Meter t.P t.H Stack Probe Filter Imp, Out Meter Temp, OF Vacuum 0, P. static 

Point Time Volume, ft' in, H,O in, H,O Temp, OF Temp, OF Temp, OF Temp, OF In Out in, HQ. % in, H,O 

fI/ It Il£ttj" <1>2. 'lei'" 1, U / , / '75(.. x: .A' 5'Q- ,,'2. <'I ',> T 2, Y 

'" t'<'$'r ")H.fdO t , I (:2. '75'7 V Y 5'/ 5? ", '/ '3 

lj,. 'i tfl>« ''7001 ( , 0 (, / 7.$ ..s {y ...r S I ::'>' 2' I "? 

t>'t i- '71/ , I" v ( , D / . I 7 S <,- "'" X s I >4 ., i :'> , /52-e, '177,S~v / . 2., / . j 7Si-- -' )ro, 5'u 5L( <'I _"t 

,57;), c,{i(,c.n j , '} j . 'f 75 V'\ X >0 <'LI s I ~ 

o IS Y l5 1"11, 2-'1 .L X A X. /\ X X X X ./< 

W '" ts50 q"l/, 2..'7 .. L _'3_ I sC' TS U v'\ X $" "" :;"J!-, ~ 

! //JdrJ 1' ?r ''td, f ' ;.J /,c/ ?S(-, X X i',?4 y );z.... '<{ 

l /1;1 C /0,,5, </2.0 ( . 5~ / 7:5" / X X' ~o :S-' ) S:z.. 't . SItkO tU/2.. 'l'l, 1-' / . 7S / X Y C;i ",u' 5>'> :s-

:, 1 j, ') '-' tJ SI-/ ,2..s u ( . 5' I 75 :2..x- -« 51 S '</ <; '2... > , ,,'fcJ to2.'6,r'fi... ( , '5 / ? ?.5 0 A A '5 2- '5) S-:; .::, 

( p$v {,;3~ 2-,;'Y 

Average: _ 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 1/25/2013 Page of ~ 

DS834049 

Master Document Storagel Formsl Datasheetsl Field Datasheets 
..... -= 

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: r:; E /y/ IV( /J LOCATION :~ -,pdf'" '---F 

DATE: L- /(- 2,,;( "2 

RUN NO: :5:-<f,I;~ 8 '-1 7;-- 7 

OPERATOR: / 'L f 1-'1 '" :::;z 

METER BOX NO: / 7 . , '. /' J 

METER llH@: /. <? ( (, 

METER Yd: V . r '7'r( / 

STACK AREA, FT'",: :-;-:===c-;-;:;~ TRAVERSE PON' S. MIN/POINT: (,?/ii- '/ 

6H= X6P: ' 7 

Probeeo;;d;tion. pre/post test: ____ _ 

Silica Gel Expanded. Y/N: _ ____ _ 

Filter Condition after T est: _____ _ 

Check Weight: _ _ _______ _ 

Meter 6P 

Point Time Volume, ft' in. H2O 

.1/ I., 1/, s -., '* ~.- j)'<;' I ' L I 

(. 17 0 -' o<{ ', '-I t.I ,,- I', ~ 

;1 11'11-., ~C,I·~"<?(· I , \' ,,,, I' ).. " DLj" ' r ) /. L--

'J t"1,'j O(p~ , CI /"";; / ~ 'J 'II' 71 07<;. ';P·(. ;..- 7 

(> 11 t , u':) { , ~4' i." "'- ~ f ,''7('- (.., Iv:< I <:, ¥ '" 1 -( 

<: / Ofp 105/", > 1 ( I <..J 

(I { , ({, ID '7> ,, 'f / { . .; 

'; /~ 'Lb , Io? 2.~.::: {, 7 , 

.", I i "fL' f iI rI II I L /. 7 

I f,c(i- I f/ ri.2::;:'-- I ' c...,. .. 

r 1,\ ') L > 112-7.u2'

/ ' 

AveraQe: 

AMBIENT TEMPERATURE: :7 c/ 

BAROMETRIC PRESSURE-: --"'-------- Imp. # Contents Post·Test· Pre-Test = Difference 

ASSUMED MOISTURE: ___________ _ 

PITOT TUBE COEFF, Cp: __________ _ 

PROBE 10 NO/MATERIAL: _________ -,,~ 

PROBE LENGTH: ~ 

NOZZLE 10 NO/ MATERIAL: ;;ee 

NOZZLE DIAMETER: FILTER NOfTYPE: '--;-1 ""7-' -:-1 ----::c'2 ;;,-=---

~j.J 

PRE·TEST LEAK RATE: : CFM@ in. Hg. 

POST·TEST LEAK RATE: '-_ u"Z.CFM@ 7;.., in. Hg. . 

~~~~ ~:~~~T~;Y~ PR~AMPLE CUST061~~T ) (, ,--,/' 

SAMPLER 

SAMPLE COC'U"'S"'TO"'"D""IC7A""N---- Total: __________ ___ _ 

6H Stack Probe Filter Imp. Out Meter Temp, of Vacuum 0 , P. static 

in. H2O Temp, of Temp, of Temp, of Temp, of In Out in. Hg. % in. H2O 

I, ") '75,-- X ./\ 5'/ <; • ....., 5/ '-'- , ' 2 L/ 

/ '7 7 "'- ( A "" St ... .:; ...--;. -t <; ? <-

i· '7 7 <; 2- " v' '7'2 c:: -'"7_ S I c: 

I C 7" / " t y. ~7 1 ,?q '";7 ("", .-::--

( , -) ( .? 7-, I'" ?< -c:<,< .---, 52 ","' , 

' r-' -, c;- L " >( <;~ :;oS r> ~ </ 

'- ,/ y- y' ...x/ -l \( V- I 

/ ' \ 7 _'> 'y / f :> '7. c.' i/ 5'1 'f "J 

t· -- 'I \ f ,\;' x' -;~L .-:. ''1.. ~L 't', yI L 7 1 7 'X X <:7' l:,. -- -7 ,'- 2- '-(, r 

L , <L 7:;;" \ X :> 'I ss '>5 5, <: 

i, '/ '/ -" .2- /\ X '7.7 .-:.~ r ('_ ~. '; -

/ , t ...,;- /e::: I " --" 7/ I'" ,,<- 'Sf S . t) 

I 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 1125/2013 .., ~ 

Page ~ of ..:::=... 

DS834049 

Master Document StoragelFormsl DatasheetslField Datasheets 
.... 

Del/a~ "..,..,.--

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: G E. rv\ f-\ I'" 

LOCATION: S - " \.-. _c_, \ 

DATE: :l- - 1 '" - ;......; \~ 

AMBIENT TEMPERATURE: ? (:' BAROMETRIC PRESSURE-: ---;z,z',r,Brr------ Imp, # Contents Post-Test - Pre-Test = Difference 

RUN NO: ~. ;-ii' ,+1.. - {('I - 5e- 1 

OPERA TOR:-,2'I .l.-'i '-'1'-c=o----,,,,---- METER BOX NO: 17 - ,-' ,-S 

METER AH@: ..; 7 V 

METER Yd: i' ·j" 'r 0:' 

STACK AREA, FT': . JJi", ' , TRAVERSE POINTS, MIN/POINT: " /;;1 

AH= I , I X AP: I 

Probe Condition, pre/post test ~ ./ 

Silica Gel Expanded, YIN: NI 

ASSUMED MOISTURE: ~I()"i', 

PITOT TUBE COEFF, C·-p-: ----'="':L:-. -c'-:, ,""/ ,.------

PROBE 10 NO/MATERIAL:7'i!~' d""",f£o:. · _' ______ _ 

PROBE LENGTH: /1" I' '/ 

NOZZLE 10 NOI M:-:A-=T=E:!R:': IA-:-L-: 7>'1-(,--,5"'5-----

NOZZLE DIAMETER: a Z'7'j 

FILTER NOfTYPE: Z 5'-If \ SPRE-TEST LEAK RA~T"'E'-::::': -':" "-'-',,'c';I.. --;C:;-;F=-;M-;:@;;-_""'/"'{~' ---ci

ccn""', H'g=-,-

POST-TEST LEAK RATE: : CFM@ in, Hg, 

PITOT LEAK CHECK - PRE: ;../" POST: 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN '-:-;<17

, - -

SAMPLER /;,,) 

~ I) 1- 11, tJ ~'b'T . ..s 

L 01'- 11, () n6, '1 

},. €MQ ~ b'i ), 4 

., >Cn. Q5'6/'I 

Ltt 01\11. 0 

,,-0, L 

lo"!b,. O __ 

('0 :s k. f:. --

q l6, '1 

-'--

\00 __ _ 

Filter Condition after T est_ -,LZ ___ _ 

Check Weight I SAMPLEC~U~S~T~O~D~IA~N~~~L-- Total: _____________ _ 

-.:, \:'.. -: .. . :;. '::;' ,t...-

'\., - Meter AP AH Stack Probe Filter 

Point I Tim"" Volume, ft' in, H20 in, H20 Temp, OF Temp, OF Temp, OF 

... 114";- 15 , --t' :; . ? 0 . ..., '7 77 v-x' X'_ 

Imp, Out 

Temp, OF 

(.; --,-. ..... 1 ,, 55 Ir"4i, [<,,,,' I . 7$- 1 ,¢' -? I -/:;7</ 1 X' -/ 5" -"; 

Meter Temp, OF 

In lout 

7)' ~ 

Vacuum 

i~ 

Z-

-=--. J( I n"s <{ I1' ~'-, "/~ 10 I 77"7-r ,.<.,-. - I A :;ic; I Br/ I 7, 1 '3 

. ~ ~ 

;; . ., .. f\.; ":; .r ~ 

/ I 12-"':; I (1/-',0" , &...;' ~'''o 1735 ~ )l <// I ~'-f' I -I '7 

1/ 1 Iii '1 i1 Il/, '1'7 2-1 'i l - ~ i x ~ _-I / I :/ " ~/ 

7 ,$(;; "/52-- , ?S 

r ~5f> ____ '7 ~ -; A - q 

Z-

.2-

/I I 13" 7 11g". tv ~ I & <j , 7 U,7 ,r;~.:> 1 %' -- I X -r-..,.r-& '? t> I 7' 7 

I ;3rl 11.'1& ). I S '/ '"" ' ::~, 7,\ / I \/ Z.: t,/I h I '7(.( I 7, ..6 

..2. ';;> 1~'2.7 /'i'~,1 /7 1-- 7--'; I ,'~r, ---r--7,C)<; ) I y '< I 'Ie 1 7'7 1 15 Cy 

-/ i?'~ 1 I 1'75 . <C 5 ';> I '/ '/ , "'" 7 '7 "'> '7 -..( V l "f 3;' - -17 172. ?' 

0 1(",t/7 1.,l°Z (I '/~ 

Average: 

02 

% 

p , static 

in, H20 

I::;; ..2 d 

1 

Comments: __________________________________________________________________________________________________________________ __ 

Date of last revision 1/25/2013 Page _of~ DS834049 Master Document StoragelFormslDatasheetslField Datasheet~ 
I 

DellalJ. """---

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: G7:. _"-,, ""-'{ CI 

LOCATION: S;;;~~ \-: ~c 

DATE: ;;be i 7 e , .." 

RUN NO: ~ - '~/s 1( - Pi''' - 60 ·- ( 

OPERATOR: r J"--ICf 

METER BOX NO: / 7 '-"-' c , 

METER 6H@: /' ;:: 7 (.., 

METERYd: o· q q c..,-

STACK AREA, FT'",: ~~=c=----,--,-=----c TRAVERSI;O POINTS, MIN/POINT: IV,! ,Cl. V 

6H= L-1- X 6P: 

Probe Condition, pre/post tesl: ____ _ 

Silica Gel Expanded, Y/N: _____ _ 

Filter Condition after Tesl: _____ _ 

Check Weighl: _________ _ 

Meter 6P 

Point Time Volume , ft3 in. H2O 

I; 1.1 !,; U ';<0 / N .2.. ~- , , .....; L/ 

5 i¢IJ O 2 01. <."r 'r , t;. ~ r . 

1/ 1'1 h;; "q S () , c..., C' 

• 0:: /'120 " i ('S. c:,., liJ , ;", '" 

;d-- /fl ?fl ':2 ; .1./1' . , p:'U 

/ / '.f Li'-' z zq·/c) f-~( L( 

0 Nju 2 35,/7).. X 

/'15 .2 ;7<-; 17 :2 ~ ~ ~/

, ! -5 tJ'2- ~:."2;.cl, "1/ I & "S 

i. 15/ L ,;. r.I..J • f"[ (, , (> c/ 

/ <. --: 7. I Z '1('1. cl / o < ~C-' 

I 'S '72- '2 x., , Jh, , C2 ~ 'i 

1 15'17_ 1-1 "-./. '; ,1, " , <j 

u ,S" 'J- 2t,1.SI(· 

Average: 

AMBIENT TEMPERATURE:,---_-"0"'-<..CL) _____ _ 

BAROMETRIC PRESSURE: __________ _ 

Imp. # Contents Post-Test - Pre-Test = Difference 

ASSUMED MOISTURE: 

PITOT TUBE COEFF, C-p-: - ----------

PROBE ID NO/MATERIAL: __________ _ 

PROBE LENGTH: NOZZLE ID NO/ M·"'Ac::T=E=RC"IA:-:-L-:----------

NOZZLE DIAMETER: ____________ _ 

~~~:,.~~~~EY::~ATE : : CFM@ in. Hg. ;;~C9j lPOST-TEST LEAK RATE: :,-,l « , 2.CFM@ / j, in. Hg. " 

PITOT LEAK CHECK - PRE: POST: C "A~ 

CHAIN OF CUSTODY: SAMPLE CUST09!AN.:::::/:-__ _ 

SAMPLER J <- /4 

SAMPLE CUSTODIAN. ___ _ Total: _ ____________ _ 

6H Stack Probe Filter Imp. Out Meter Temp, OF Vacuum 0 2 P. static 

in. H2O Temp, OF T el11J'. OF Temp, OF T el11J'. OF In Out in. I:!ll % in. H2O 

: 5~ \ ? !LI A /.. 5 / t:' <f t,.. I' J t- z , '/ . , C-:. G, 7 C . 7 .x X "'Ir 2L 6.::.. .. 

, '7 ;" 7 c; / y ~ ':/-; " 

-, , -:z..1. ..££:0. ~ ?C'- ../ )< A 0' 7 7 -.., 6-· ' . , (-- 7r. (,., L X (~'2 '7~ ..6.'2 J 

Y? 7 9<; /X· X C!/ .:;. "7_/ t:.C'j g .-

-"" A X /< .x ~ ../ 'y \ 

, ,<'i- 7 ;7 c5 '7 A ....-\ 9 C 7(' v...z. -z.- ..1 w'l / < '. "/ )( )( </l::j 7). 6 a <'""'- I 

·71 -; , ,> '7 X- X V S: 7-"1. .c,;, r . -=- I 

_p. c ' J C '\ )( X i/'I 7 --; ~'Z: ~- . , t:::..l . ,0/ , ?'~ C ; Y ;x. .r,.c Co, ~ ~ • <. c_ . ,q- ""C, -7 X /' L.J - (_ '7 :" ~ . (- , -

I 

Comments: ____________________________________________________________________________________________________________ ___ 

Date of last revision 1/25/2013 Page ~ of ,;;.--

DS834049 

Ma5ter Document StoragelFormslDatasheetslField Datasheets 
Oe/1a1J.. ."Ouo ...... ~ .... ..... _ .. 

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: C-S I/. / '/. i.L-\ . LOCATION: 'b7 k i ~ '- 1 &.~ 

DATE: ;:::L 2- - I""'> 

RUN NO: '; .. i;/,{tl{- 6 '://1 ;,9 / 111/\ 

OPERATOR: )-;.-1 c, 

METER BOX NO: I 7 0:. (V,' S 

METER 6H@: / ~ Iv 

METER Yd: ,'-p-/ (.; 

STACK AREA, FT': 

TRA VERSF POINT"'S;-, 7M"'1 N'"'/;;;P:;;O"'I N:;;T"": '/'-:;-'17.,,";; -;;>7 

6H= _'_. _1_ X 6P: 7 

Probe Condition, pre/post tesl:. ____ _ 

Silica Gel Expanded, Y/N.: ______ _ 

Filter Condition after T esl: _ ____ _ 

Check Weight..· ________ __ _ 

Meter 6P 

Point Time Volume, fe in. H2O 

Average: 

AMBIENT TEMPERATURE: ~C- BAROMETRIC PRESSURE-: - 2." "",-::: ·1.,.;'1"'------

ASSUMED MOISTURE: 

PITOT TUBE COEFF, C-p-: -.f2.-,- .,,-t::..=--------

PROBE ID NO/MATERIAL: #;;;2, ?L/I:;-J 

PROBELENGTH :· ~~~(#~ r: z=70-~ ------

NOZZLE ID NO/ MATERIAL: ~ 1- 5:' 

NOZZLE DIAMETER:.."xO;>.. ' 1.=,)",,.'-:. , .,-_ _ ______ _ 

FILTER NOrTYPE: 1:,; - 11 \ (, 

PRE-TEST LEAK ~A"' ::': -: -'. .>'-'.,)":',,'".)-:::""C=CF=M7@=---'""'('~'-i'-n-:. H

7g-.-

POST-TEST LEAK RATE,..,,,' 1{'2 CFM@ / ( in. Hg. 

PITOT LEAK CHECK - PRE: ,/ POST: v---

CHAIN OF CUSTODY: SAMPLE CUSTODIAN->.. . '0.:"'---__ 

SAMPLER (,M 

SAMPLEC~U~S~T~O~ IA M~C--

6H Stack Probe Filter Imp. Out 

in. H2O Temp, OF Temp, OF Temp, OF Temp, OF 

Imp. # Contents Post-Test - Pre-Test = Difference 

O~ !\ U Ib), ~ b <g.s-: So2 01 \13,0 13'l."i J33,.'1 

l fAi b)3,0 ('33, U 

~ sG, $3';,6 13 "/, 0 

...!:: 'l- \) I B 1...0 lOO 

Total: _____________ _ 

Meter Temp, of Vacuum 0 2 P. static 

In Out in. Hg. % in. H2O 

Comments: _______________________________ ___________________________ _ 

Date of last revision 1/25/2013 Page ofL 05834049 Master Document 5toragelFormslDatasheetslFieid Datasheets 
8811811 

PARTICULATE 

SCAQMD 5.1, WET IMPINGEMENT 

Project # 

Client/Location 5I!.ni.\'n~( 

Sample Location u/\; f '{ 

Test # S"!fitK.-ht/brr/ 

Item Number 

1. Glass Fiber Filter 5S- (Backup Filter) 

11'{o 

2. Insoluble Solids Filter 55'-

/fZ'! 

3. Impingers and Probe 

Catches 11367-

a. Water Fraction 

b. Organic Extraction /136(, 125 ml MeCI2 

(5 x 25 ml) 

Dellaf'1 

... ...-.....-,-.... 

Date of last revision 11/13/08 

Sample Date 

Water Blank mgfml (l,ooOO Analysis Date 

MeC" Blank mgfml 0, "00 0 Analyst Initials 

Final Tare Gain Aliquot Net Gain 

Weight Weight Weight Correction (mgfSample) 

(qj (qj (mol (mlfm/) 

0 ·((.20 0.((,/5 o·~ ---------------- OS 

0 ./53">' o./s3'( 01 0, ---------------- \ 

~'T.'P2)'i :l'1.ro'f- /&~ !tf2 

f'Jo /&(, 

~~,'2..nO 

f10 

'2..'U"" I. D,c) ~6 0,0 

Blank based 

on Total 

Volume (mql 

-----------------

----------------

Total Particulate = 1 7. 'Z.. mg --------------~~ 

Method of Sample Prep/Notes 

DS834012 

Master Document StoragelFormslDatasheetslLab Forms 
8011a/1 

PARTICULATE 

SCAQMD 5.1, WET IMPINGEMENT 

Project # 

ClienVLocation 5 ... "t.'-_ ... ( 

Sample Location Un: to 'i 

Test # S"¥lSt/(.""', 75-1 , 

Item Number 

1. Glass Fiber Filter SS-- (Backup Filter) {1t ( 

2. Insoluble Solids Filter £~-

1"n.3 

3. Impingers and Probe 

Catches 1130::> 

a. Water Fraction 

b. Organic Extraction 

125 ml MeCI2 /I 3D,,! 

(5 x 25 ml) 

Delfal'1 "'--,""-- Date of last revision 11/13/08 

Water Blank mg/ml O.CQ01:> 

Sample Date 

Analysis Date 

Analyst Initials 

:l/fl/13 

MeCl, Blank mg/ml 12.00<>0 

Final Tare Gain Aliquot Net Gain Blank based 

Weight Weight Weight Correction (mg/Sample) on Total 

(g) (g) (mg) (ml/ml) Volume (mg) 

O·IS<;.1 o./S':t( o·D 0·0 ---------------- -----------------

<J.15~1 D·/S~o 0.0 ---------------- 0.0 ------._--._-----

¥s;r 

b'l.)"I'Db 2'1.3<j</1. 4.'-( ..---- Ii .1..( D·D is r 

¥.5'8' O·c) ~'l.S'O'11 ~ '1.~'IJ O·c.) ......---- 00 &-Sf 

Total Particulate = __ '-fL ·_L..Lf ___ --'m:..;.9;L 

Method of Sample Prep/Notes 

DS834012 

Master Document StoragelFormslDatasheetslLab Forms 
Dclla~ 

PARTICULATE 

SCAQMD 5.1, WET IMPINGEMENT 

Project # 

ClienVLocation S .. "i: in ~( 

Sample Location UII. i e 'f 

Test # Sq,st!<. I'll( So-I 

Item Number 

1. Glass Fiber Filter 5S-- (Backup Filter) 

i1/~ 

2. Insoluble Solids Filter SS"-

/f22. 

3. Impingers and Probe 

Catches 1/3~3 

a. Water Fraction 

b. Organic Extraction 

125 ml MeCI2 /Ij(>l 

(5 x 25 ml) 

... De/tab. _ ......... -...... 

Date of last revision 11/13/08 

2/11/1.3 

Water Blank mgfml ". woO 

MeCl, Blank mgfml 0,0000 

Sample Date 

Analysis Date 

Analyst Initials 

1./137/3 

Final Tare Gain Aliquot Net Gain Blank based 

Weight Weight Weight Correction (mgfSample) on Total 

(g) (g) (mg) (mlfml) Volume (mg) 

O.((,'{V O.,.r,y/ ~ I f,'f- 0·0 

0·0 ---------------- -----------------

0'/S50; o./,sSS 0·0 ------------.--- 0 ,0 -----------._----

~'Y,12.17 2<j.~lset £r !!S- S.S- 0.0 :;').~ 

2~.S3't<=t U.I'31>1> 0·0 

"12 ,;; 

----.:: O · c) 0·0 7-2~ 

Total Particulate = __ 5_._g-_----'-m"'9OL. 

Method of Sample Prep/Notes 

DS834012 

Master Document StoragelFormslDatasheetslLab Forms 
Dclla~ 

PARTICULATE 

SCAQMD 5.1, WET IMPINGEMENT 

Project # 

ClienULocation Sczt) l,'ne! 

Sample Location Und_ q 

Test # Frdd &I_I<. 

Item Number 

1. Glass Fiber Filter 5f>'-

(Backup Filter) 17{~ 

2. Insoluble Solids Filter ~S-_ 

IlL/ 

3. Impingers and Probe 

Catches If 3D I 

a. Water Fraction 

b. Organic Extraction 

11300 125 ml MeCI2 

(5 x 25 ml) 

ClII{,-O Il.Lo-.(..( Illlt" 

~<Z. C I J.. 61 "'" (~ (ll'7'1 

Deltal1 .. _ .................... 

Date of last revision 11/13/08 

Water Blank mg/ml 6.0000 

MeCl, Blank mg/ml o· 00"0 

Final Tare Gain 

W~tt W~tt Weight 

(mil) 

o (&,/u o·It-V3 0.0 

O·/£S7.. O'/~3 C).V 

~ Z 1.352.1 0.8'" 

Z''T,H'3S' 

2<t·>.WI 2'i.S320 6 .c) 

2.'b .lfl7 '1 1. or. (/11,/ 6·Q 

~'l.%2S' 2.., ~,n D·c) 

Sample Date 

Analysis Date 

Analyst Initials 

Aliquot Net Gain 

2./11 /13 

R? 

Blank based 

Correction (mg/Sample) on Total 

(mllml) Volume (mol 

------------.--- 00 -------.---------

------._.------- 0 ·0 -----------------

ff3 W 0·9- 0 ·0 

~ li'.J ~ 0.0 0·0 '-/ ¥3 

z.z.l.. 

2]"t. 

2:;;0 

-----

ZbO 

Total Particulate = _---=o:... . ..:Y'---___ ........:.m"'9"--

Method of Sample Prep/Notes 

DS834012 

Master Document StoragelFormslDatasheetslLab Forms 
APPENDIX D GENERAL EMISSIONS CALCULATIONS 

R041 0688 D-1 
GENERAL EMISSION CALCULATIONS 

1) Stack Gas Velocity 

2) 

A. Stack gas molecular weight, Ib/lb-mole 

MW", = 0.44 * %CO, + 0.32 * %0, + 0 .28 * %N, 

MWwet = MWdry * (1-Bwo) + 18 * Bwo 

B. Absolute stack pressure, iwg 

Ps = Pbar + Psg 

13.6 

c. Stack gas velocity, ftlsec 

Vs = 2.9 * Cp * ..)!1P *.JT: * 

Moisture 

A. Sample gas volume, dscf 

Vmstd = 0.03342 * Vm * (Pb", + 

B. Water vapor volume, scf 

v = 0.0472 * V. * Tref 

wstd Ie 528 oR 

29.92 * 28.95 

Ps * MWwet 

!1H ) * T,ef * y 

13.6 Tm d 

c. Moisture content, dimensionless 

Bwn = (Vmstd + Vwstd ) 

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 

R041 0688 0-2 
Q 

sd 

= Q * (1-B wo ) * TT ,., *~ 2992 s . 

4) Gaseous Mass Emission Rates, Ib/hr 

M = ppm * MW, * QSd * 60 

SV * 106 

5) Emission Rates, Ib/MMBtu 

Ib ppm * MW, * F * 20.9 ~-=--= MMBtu SV*106 20.9-%02 

6) Emission Factor, Ib/MMSCF 

Ib Ib *HHV 

MMSCF MMBtu 

VI. Percent Isokinetic 

17.32 x T, (V" std ) 5280 R 

1= , x 

(1 - Bwo)O x V, x Ps x Dn T,',j 

VII. Particulate emissions 

a) Grain loadin9, gr/dscf 

C = 0.01543 (MnNm sid) 

b) Grain loading at 12% CO2, gr/dscf 

C,2% C02 = C (121% CO2) 

c) Grain loading at 3% O2, gr/dscf 

C3%02 = C' 17.9/(20 .9-%02 ) 

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 1 10 Btu = ex 7000gr x F x 20.9 _ % 0 , 

R041 0688 0-3 
Nomenclature: 

As 

Bwo 

C '2%C02 

C3%02 

C 

Cp 

On 

F 

H 

HHV 

I 

Mn 

M; 

MW 

M", 

o 

P 

Pbar 

Ps 

P Sg 

Q 

Q ws 

Qsd 

8V 

Tm 

Tref 

Ts 

Vs 

V ic 

Vm 

Vmstd 

VwStd 

Yd 

R041 0688 

= stack area, ff 

= flue gas moisture content, dimensionless 

= particulate grain loading, gr/dscf corrected to 12% CO2 

= particulate grain loading, gr/dscf corrected to 3% CO2 

= particulate grain loading, gr/dscf 

= pitot calibration factor, dimensionless 

= nozzle diameter, in. 

= fuel F-Factor, dscf/MMBtu @ 0% O2 

= orifice differential pressure, iwg 

= fuel higher heating value, Btu/8CF 

= % 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: 

802: 64 

NOx: 46 

CO: 28 

HC: 16 

= sample time, min. 

= average velocity head, iwg = (..,Jt;P)' 

= 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, 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 
APPENDIX E CHAIN OF CUSTODY 

R041 0688 E-1 
CHAIN OF CUSTODY 

CLIENT: Sentinel TEST DATE(S): 2111/2013 2112/2013 

LOCATION: 4 SAMPLER(S): "S"-S ___________ _ 

SAMPLE LOCATION: Stk PROJECT MANAGER: 

TEST METHOD(S): SCAQMD 207.1 DATE DUE: 

OUTSIDE LAB REQUIRED?: No COMPLIANCE TEST? 

15m 

ti'2i2ir 

__ Rea9e:r~t lot #'s:1 

~ 

S4fStk·1 

S4/Stk-1 

S4-,-Stk· 

;-2 

B Blank 

~ 

3110020 xt 

) 207. 

) 207. 

i20f 

-.l 

_be, line , 

_be. line, 

.be, line, 

.be. line, 

Probe, line 

Probe, line, 

),1 N H2SO4 

BF 

212012013 

Yes 

m:;47 ? Z 13-\3 10:1£ U2':f;tDck'!::: 2/6,h:3 (~:("zJ ~SED BY .. ---- DATEITIME I RECENED BY DATEITIME 

I __ I 

A 
CHAIN OF CUSTODY 

CLIENT: Sentinel TEST DATE(S): 2/11/2013 2/1212013 

LOCATION: 4 SAMPLER(S): .!;R"'M'--__________ _ 

SAMPLE LOCATION: Stk PROJECT MANAGER: 

TEST METHOD(S): SCAQMD 5.1 DATE DUE: 

OUTSIDE LAB REQUIRED?: No COMPLIANCE TEST? 

.,...It: 

'1i201 

1~~~1 

Water 

13 

iMc 

CA< 

Prot 

Prot 

.ine, ""t'" 

., Filter 

line, Imp. 

, Fille 

Une, -Imp. 

___ Imp. 

5.1 Filter 

Blank 

I!.ll'I 

"""Dii 

BF 

2120/2013 

Yes 

rWater-

??Ql z;e 2._r:ilrIME (0-1$ I f?8iCp?B! - I z-t3°tT1:1-ts: 

A 
,4,4c;lj /30/~O 

CHAIN OF CUSTODY 

'<t" 

CUENT: Sentinel TEST DATE(S): 2111/2013 211212013 ., 4 SAMPLER(S): RM ~ tl.. 

LOCATION: 

SAMPLE LOCATION: SII< PROJECT MANAGER: 

TEST METHOD(S): SCAQMD 25.3 DATE DUE: 

OUTSIDE LAB REQUIRED?: Yes 

~ 

? J?4- 21111201 

98'> 21111201 

'11?~ 2111/2013 "'" 

'187 2111/2013 54" 

"8'1'? 211212013 54/1 7 211212013 84/: 

!tom 

~, 

;:; 

~ 

Canister: 

Canister: 

Canister: 

Canister 

-CaillSi8r"' 

Canister 

~ 

ULL 

COMPLIANCE TEST? 

BF 

212012013 

Yes 

FU--- -- RELEASED BY - I I DATE/TIME RECElVED'BY' - -T -llATClTlME 

1t£JO /~ z-fr3It3. tCqJ _>2 5)711.11 '5 ( 0 3c) 

~ ~ ? ,#,/.2//3 . I; ~ "" , - -?"" ~J)j It::r r.no r ; 

Note: Canister ~03 and #000411 were Voided tes1$, Please dOnof analYze. 

:MFA 
Cl1ENT: 

CHAIN OF CUSTOOY ~ I 

SenHnel TEST OATE(S): t 7. 21 3 _ LOCATION: 4 SAMPLER(SG ~.iSAMPLE LOCATION: ___________________________________ PROJECT MANAGER: BF 

TEST METHOO(S): Fixed Gases ASTM 0194511946 DATE DUE: A'5:ItP 

HHV ASTM D3588 

Sulfur ASTM D5504/SCAQMD METHOD 307-91 

OUTSIDE LAB REQUIRED?: Yes COMPLIANCE TEST? Yes 

I ~ATE TIME TE T# Method SAMPLE DE CRIPTION CONTAINERS SAMPLER COMMENTS 

S4/-Fuel Surfur--1A See Above Tedlar Ba 1 M 

'l I II S4/-Fuel Sulfur 18 See Above redlar Sa 1 M 

\. • S4/-Fuel Sulfur-- 1C See Above redlar 8a 1 M , II 

I 

Total Samples 3 

Rea ent 

1 ,r, Reagent Lot #'s: 

I 

RELE Y DATEfTlME ,/7 jil£CEIVEO BY / oATEmM, 

'7'0_ Y A-o./ , 7--1 :2-2- / -7 

'-" " I' ( / y " -r / r71 7 , / - or- I -- -

Rf/IIA 
APPENDIX F INSTRUMENT STRIP CHARTS 

R041 0688 F-1 















APPENDIX G FACILITY PERMIT TO OPERATE CONDITION 029.1 

R041 0688 G-1 
SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 91765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H 

Facility ID: 

Revision II: 

Page: 35 

152707 

o 

Date: April 15, 20t 1 

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)(I)-BACT, 5-10-1996; RULE 1303(a)(I)-BACT, 12-6-2002; RULE 

1703(a)(2) - PSD-BACT, 10-7-1988; RULE 2005, 5-6-2005) 

[Devices subject to this condition: C4, CIO, C16, C22, C28, C34, C40, C46) 

D12.5 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)-Offset, 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: 049) 

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 1 hour Outlet of the SCR 

serving this equipment 

CO emissions I District method 100.1 1 hour I Outlet of the SCR 

serving this equipment 

SOX emissions I AQMD Laboratory 

Method 307-91 

Not Applicable I Fuel sample 

VOC emissions I District Method 25.3 I hour I Outlet of the SCR 

serving this equipment 
SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 91 765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H Page: 36 

Facility 10: 152707 

Revision #; 0 

Date: April 1.5,2011 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

The operator shall comply with the terms and conditions set forth below: 

PMIO 

emissions 

NID emissions 

District Method 5 

District method 207.1 

and 5.3 or EPA method 

17 

4 hours 

1 hour 

I Outlet of the SCR 

serving this equipment I Outlet of the SCR 

serving this equipment 
SOlITH COAST AIR QUALrIY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 91765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Seo;tiorl H Page:: 31 

Facility 10: 152107 

Revision II: 0 

Date: April IS, 2011 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

Tbe operator sball comply witb tbe terms and conditions set fortb below: 

The test shaH 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 shaH be notified of the date and time of the 

test at least 10 days prior to the test 

The test shaH be conducted to detennine the oxygen levels in the exhaust. In 

addition, the tests shaH measure the fuel flow rate (CFH), the flue gas flow rate, 

and the turbine generating output in MW. 

The test shaH 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 shaH 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-l2 (with pre concentration) and temperature of canisters when extracting 

samples for analysis is not below 70 deg F. 

The test shaH be conducted for compliance verification of the BACT VOC 2.0 

ppmv limit. 

The test results shaH be reported with two significant digits. 
, ._ ..... '-

SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 

21865 Copley Drive. Diamond Bar. CA 91765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H 

Facility ID: 

Revision N; 

Dale: 

Page: 38 

152707 

o 

April 15,2011 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

The operator shall comply with the terms and conditions set forth below: 

[RULE 1303(a)(I).BACT, 5-10-1996; RULE 1303(aXI)-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 subjectto this condition: DI, D7, DI3, DI9, D25, D31, 037, D43] 

D29.2 The operator shall conduct source test(s) for the pollutant(s) identified below. 

Pollutant(s) to 

be tested 

NH3 emissions 

Required Test Method(s) 

District method 207.1 

and 5.3 or EPA method 

17 

Averaging Time 

I hour 

I Test Location 

I Outlet of the 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 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)(I)-BACT, 5-10-1996; RULE J303(aXI)-BACT, 12-6·2002] 

[Devices subject to this condition: 01, 07, 013, 019, D25, D31, 037, D43J 
APPENDIX H CORRESPONDENCE AND TEST PLAN 

R041 0688 H-1 
Bob: 

Here is an answer to one of the issues for the crv Sentinel testing. 

From: Carey Willoughby [mailto:CWilioughby@aqmd.gov] 

Sent: Wednesday, January 09, 2013 10:09 AM 

To: Tom W. Andrews 

Subject: RE: CPV Sentinel VOC Tests 

Mr. Andrews, 

Simultaneous duplicate sampling (six canister samples vs. nine sample canisters) for VOC is 

acceptable to the SCAQMD. 

Sincerely, 

Carey 1ViCCoUfJfiby 

~ir Q.uaCity 'E1lIJineer II 

SC~:MD 

21865 CoyCey Drive 

Diamond 'Bar, C~ 91765 

Tel: (909) 396-3006 

:Fax: (909) 396-2099 

cwiflOuefiEy@aqnu£.[JOV 

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 VOC 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 of the 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 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 

ROBERT A. FINKEN 

DECEMBER 7,2012 

DOCUMENT NUMBER: R0210458-R1 

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. 

R021 0458·R 1 ii 
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 O2, CO2, NOx AND CO ................................................. ..................................... 8 

3.2 NH3 8Y SCAQMD METHOD 207.1 ......... .. ......................................................... 9 

3.3 SOx 8Y SCAQMD METHOD 307.91 .................................................................. 9 

3.4 ROG 8Y MODIFIED SCAQMD METHOD 25.3 .................................................. 9 

3.5 PM 8Y SCAQMD METHOD 5.1 ....................................................................... 13 

4.0 REPORTING ............................................. .. ......... ... ...................................... ..... ... . 15 

APPENDICES 

A QUALITY ASSURANCE ........... .... .. .. ..................... ...... .......................................... A-1 

B TEST METHODS ........................... ...................................................................... .. 8-1 

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

D FORMS ................................................................................................................. D-1 

E FACILITY PERMIT TO OPERATE CONDITION D29.1 .......................................... E-1 

R0210458-R1 iii JleltaIJ. '"'---
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 029.1 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 

(NOx), 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. 

R0210458-R1 1 
2.0 UNIT DESCRIPTION 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 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. 

R0210458-R1 2 JJeII8!1 "'---
FIGURE 2-1 

SIMPLIFIED PROCESS BLOCK DIAGRAM 

CPV SENTINEL 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 

R0210458-R1 3 
FIGURE 2·2 

GENERAL ARRANGEMENT OF MAJOR COMPONENTS 

-_ ............. ...... ..... -.. -- " "-- _l!==\=H=='l ._ .. .. _ .... .. _ ... ....... -

\ I 

./ 

"''1t'''1'>4 r.t<ll<·;· t .~ 

("""': 

v 

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 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 +-

Stack Exit 1080.0 in. 

Silencer Bottom 925.9 in. 

Ports 841 .6 in . 

Platform 789.6 in. 

Base 01 Stack 518.5 in . 

Grade 0.0 in. 

R021 0458-R 1 

T 

84 Distance A, Inches . 0.5 Diameters 

! Sample ports 

T 

323 Distance e, inches , 2.0 Diameters 

__ E:::;xh:::.ust Flow .' 

Elevation View 

5 

90 fl, 

66 It. 

o It. 

/Ie/II/). "'--.-
Sample 

Point 

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 in. %of in. %of in. % of 

Diameter from Wall Diameter framWall Diameter framWeli Diameter framWall 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 70.4 114.0 

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. 

R0210456-R1 6 /lelia/.). "" ..... _-

in. 

(ram 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 NOx, CO, NH3, ROG's and SOx' 

TABLE 3-1 

TEST MATRIX 

Parameter Method 50% Load 75% Load 100% Load Test Duration 

NO, SCAOMD 100.1 1 run 1 run 1 run 60 minutes 

02/C02 SCAOMD 100.1 With each run 

CO SCAOMD 100.1 1 run 1 run 1 run 60 minutes 

NH3 SCAOMD 207.1 2 runs 2 runs 2 runs 60 minutes 

S02 SCAOMD 307.91 2 samples N/A 

PM EPA 201A1SCAOMD 5.1 1 run 1 run 1 run 240 minutes 

ROG Modified SCAQMD 25.3 3 runs 3 runs 3 runs - 60 minutes" ) 

1) ROG tests will be nominally 60 minutes. Flow controllers will be setup for 60 minutes. The test will be 

performed until 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 lie/tal'!" ",--_ .. 
TABLE 3-2 

CPV SENTINEL ENERGY PROJECT 

PERMITTED EMISSION LIMITS 

Parameter Units 

ppm@15%02 

ppm@ 15% O2 

Ibs/MMscf 

co ppm@ 15% O2 

NH3 ppm@ 15% O2 

gr/dscf @ 3% O2 

Particulate gr/dscf @ 12% CO2 

Ib/hr 

Ibs/MMscl 

(Ib/hr equivalent) 

Ib/MMBtu 

Ibs/MMscf SOx 

ROG's ppm @ 15% O2 

(1) The 12.261bs1MMscf is a RECLAIM emission factor, not a limij. 

(2) This is stated in the permit as an emission factor. 

3,1 O2• CO2• NOx AND CO 

Limit 

2.5 

15 

12.26(1) 

4 

5 

0.01 

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)(I) 

O2, CO2, NOx 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. CO2 concentrations will be 

measured on a 0-10% range. O2 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 IleI/aI1 

.. _--
for system bias and analyzer drift. The drift and bias corrected result will then be used to 

calculate NOx emissions in units of ppm, ppm corrected to 15% O2, pounds per hour, 

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

3,2 NH3 BY SCAQMD METHOD 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 significant NOx 

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 H2S04 , 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 first 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 SCAQMD METHOD 307,91 

Oxides of sulfur will be measured using SCAQMD Method 307-91. Two fuel 

samples will be collected in a Tedlar bag and sent to Saybolt Laboratory for Sulfur 

analysis as total reduced sulfur as H2S. 

3.4 ROG BY MODIFIED 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 (MC) 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 is 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 maintained at between 400 and 

500 mm HG (10 - 14 in. Hg) absolute. 

R0210458-R1 9 

l1li11811 ----
Figure 3-1 presents a schematic drawing of the sample apparatus. 

FIGURE 3-1 

MODIFIED SCAQMD METHOD 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, CO2, H20, O2, N2, etc.). The oxidizer converts the NMNEOC 

to carbon dioxide. The methanizer converts the resulting CO2 to methane. The methane 

content is detected by the FlO as ppmcarbon. 

R0210458-R1 10 116/11/1 '"'=--
Modifications suggested by SCAOMD 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 Ouantitation Limit (POL) from the MOL study 

Results are reported in parts per million by volume as carbon to 2 significant 

digits, corrected to 15% O2 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 VOC testing, condition D29.1 

Mark 

The current VOC section of D29.1 is the following 

For natural gas fired turbines only, VOC compliance 

shall be demonstrated as follows: a) Stack gas s41llples 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 VOC 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 

R021 0458-R 1 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 rom Hg absolute, b) 

Pressurization of the Summa canisters are is done with 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 it 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 CARB for natural gas fired 

turbines. 

please have the VOC testing 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 

R021 0458-R 1 12 IJeIl8I'1 "'--
3.5 PM BY SCAQMD METHOD 5.1 

Particulate matter will be measured using EPA Method 201A in conjunction with 

SCAOMD 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 will prevent overstating of PM10 emissions if all of the PM emissions from these 

units are not PM1o. 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. 

R0210458-R1 13 IJeIlaI1. 

....... x--
Temperature 

Sensor Probe 

~ Pitot Tube 

Nozzle 

/ 

S-Type Pitot Tube 

FIGURE 3-3 

SCAQMD METHOD 5.1 SAMPLE SYSTEM 

Manometer 

Orifice 

Connecting 

Teflon Tubing Filter Temperature 

Gel 

Line 

The sample is recovered in two fractions: 1) nozzle, probe, connecting line and 

impinger rinse (DI water) and 2) backup filter. Filter weight gain and water solution 

weight gain are each determined gravimetrically. 

R021 0458-R 1 1Je1flt:. 14 ""---
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 

III. 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 

VIII. Appendices 

A. Test Data 

R021 0458-R 1 15 lltlliafl 

.. _--
1. Data Sheets/Stripcharts 

2. Laboratory Data 

3. Quality Assurance Data 

B. Process data 

1. Unit and control equipment operating data 

C. Calculations 

D. Quality Assurance Program Summary 

R0210458-R1 16 1Je11l!J. 

.. _--
APPENDIX A QUALITY ASSURANCE 

R021 0458-R 1 A-1 
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 "living" 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-1. 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 

R021 045B-R 1 A-2 JJelfl/1 "'---
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. 

R0210458-R1 A-3 JJeIflIJ.. .. _--
Equipment 

Pumps 

Flow Meters 

Sampling Instruments 

Integrated sampling 

tanks 

Mobile van sampling 

system 

Sampling lines 

R021 0458-R 1 

TABLE A-1 

EQUIPMENT MAINTENANCE SCHEDULE 

Acceptance Limits 

1. Absence of leaks 

2. Ability to draw 

manufacturers 

required vacuum 

and flow 

1. Free mechanical 

movement 

1. Absence of 

malfunction 

2. Proper response to 

zero, span gas 

1. Absence of leaks 

1. Absence of leaks 

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 

Depends on nature of 

use 

Depends on nature of 

use 

After each test series 

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 

1. Steam clean 

2. Leak check 

1. Change filters 

2. Change gas dryer 

3. Leak check 

4. Check for system 

contamination 

1. Blow dry, inert gas 

through line until 

dry. 

DeIIa/1 .. _--
TABLEA-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 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 Daily N02 -> NO converter > 90% 

efficiency 

S-type pitot tube Semi-annually Dimensional calibration Meet dimensional 

criteria 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 

criteria of Method 2 

Differential Pressure Semi-annually Correction factor based +/- 5% 

Gauges (except for on 5-point comparison 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 standard 

Dry gas meter Bi-monthly Calibration check at 2 +/- 2% of semi-annual 

flow rates using a NIST factor 

traceable standard 

Dry gas meter orifice Annually 4-point calibration for 

&H@ 

Temperature sensors Semi-annually 3-point calibration vs. +/- 1.5% 

NIST traceable standard 

R021 0458-R 1 A-5 hila/:). "'---
APPENDIX B TEST METHODS 

R021 0458-R 1 8-1 /lelia/'). 

... _--
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 ._- IJefl8l1 
PROCEDURES AND CALCULATIONS: 

Figure 1 presents a flow 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, 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 

is expected 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% 

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 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 Linearity = Analyzer Response - Predicted Response. 100% 

Analyzer Range 

where: 

Response to High Gas - Response to Zero Gas 

Predicted Response = • Mid Gas Value + Response to Zero Gas 

High 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 

R021 0458-R 1 8-3 ",JJe/1I1J. -_ .. -
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. 

A I D ·ft Post - Test System Bias Resonse - Pre - Test System Bias Response no yzer n = • 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 = 0 * c c C -c ma m 0 

where: 

Cc = Drift/bias corrected concentration 

C = Raw Test Average 

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

Co = Average of pre- and post-test to sample system bias zero 

Cma = 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 NOx 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 N02 to 

NO converter. This test will be performed once on the day of the test. The converter 

efficiency must be 90% or greater. 

R021 0458-R 1 8-4 
Analyzer 

Cal 

Cal No 

Error < 2% 

No 

Yes I Yes 

System Nn System IBias < 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% 

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 

1 checks are performed within 2 hours Yes 

of the previous bias check. No No 

Analyzer Cal 

Cal? Error < 2% 

Yes 

No 1 Yes 

Yes System [ Finish 

Bias < 5% ) 1-1 

FIGURE 1: SCAQMD METHOD 100.1 CALIBRATION AND TEST SEQUENCE 

R021 045B-R 1 8-5 IleIlaI1 

... _--
Temperature 

~~. 

PltotTube 

S-TypePitotTube ~ 

Manometer 

Orifice 

Connecting 

Teflon Tubing 

SCAQMD METHOD 5.1 SAMPLING TRAIN 

R021 0458-R 1 8-6 

Temperature 

Sensor 

Vacuum 

Gauge 

/Je11l!:1 

.. --.-
Filter Probe 

Flow Controller 

MODIFIED SCAQMD METHOD 25.3 SAMPLING APPARATUS 

R021 0458-R 1 8-7 0e1l811 

........ --
APPENDIX C CALCULATIONS 

R021 0456-R 1 C-1 llellatl 

... ~--
GENERAL EMISSION CALCULATIONS 

1) Stack Gas Velocity 

2) 

A. Stack gas molecular weight, Ibflb-mole 

MWdry = 0.44 * %C02 + 0.32 * %02 + 0.28 * %N2 

MWwet = MWdry * (1 -Bwo) + 18 * Bwo 

B. Absolute stack pressure, iwg 

Ps = Pbar + Psg 

13.6 

c. Stack gas velocity, ftlsec 

Vs = 2.9 * Cp * -J ilP * .JT. * 

Moisture 

A. Sample gas volume, dscf 

Vmstd = 0.03342 * Vm * (Pbar + 

B. Water vapor volume, scf 

v = 0.0472 * V. * Tret 

wsld Ie 528 oR 

29.92 * 28.95 

p. * MWwet 

ilH ) * Tret * Y

d 13.6 Tm 

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 

R021 0458-R 1 C-2 .. De/Ia/). __ ........ 
Q = Q * (1- B ) * Tref * P, 

sd wo Ts 29.92 

4) Gaseous Mass Emission Rates. Ib/hr 

M = ppm * MW, * QSd * 60 

SV * 106 

5) Emission Rates. Ib/MMBtu 

Ib _ppm*MW,*F* 20.9 

MMBtu - SV*10· 20.9-%02 

6) Emission Factor. Ib/MMSCF 

Ib Ib *HHV 

MMSCF MMBtu 

VI. Percent Isokinetic 

17.32 x T, (Vm sId) _52_8_0 _R 1= x 

(1- Bwo)O x V, x Ps x Dn2 Tn! 

VII. Particulate emissions 

a) Grain loading, gr/dscf 

C = 0.01543 (MrlVm SId) 

b) Grain loading at 12% CO2 , gr/dscf 

C12% C02 = C (12/% CO2) 

c) Grain loading at 3% O2 , gr/dscf 

C3% 02 = C· 17.9/(20.9-%02) 

d) Mass emissions, Ib/hr 

M = C x Qsd x (60 min/hr)/(7000 gr/lb) 

e) Particulate emission factor 

6 lIb 20 .. 9 

Ib 110 Btu = C x x F X 0/ 0 7000gr 20.9 - /0 2 

R021 04S8-R 1 C-3 /lelia/). "'---
Nomenclature: 

As 

Bwo 

C12%C02 

C3%02 

C 

Cp 

On 

F 

H 

HHV 

I 

Mn 

M; 

MW 

Mwi 

o 

t.P 

Pbor 

Ps 

Psg 

o 

Ow. 

OSd 

SV 

Tm 

T ref 

Ts 

Vs 

ViC 

Vm 

Vmstd 

Vwstd 

Yd 

R021 0458-R 1 

= stack area, ft2 

= flue gas moisture content, dimensionless 

= particulate grain loading, gr/dscf corrected to 12% CO2 

= particulate grain loading, gr/dscf corrected to 3% CO2 

= particulate grain loading, gr/dscf 

= pitot calibration factor, dimensionless 

= nozzle diameter, in. 

= fuel F-Factor, dscf/MMBtu @ 0% O2 

= 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, Ibllb-mole 

= molecular weight of specie i: 

802 : 64 

NOx: 46 

CO: 28 

HC: 16 

= sample time, min. 

= average velocity head, iwg = (.Jt.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 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 DeIl8!:1 "'--
APPENDIX D FORMS 

R021 0458-R 1 0-1 
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 Qua~ty 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 ofthe renewal application you submitted for approval under the South Coast 

Air Quality Management Oistric~s Laboratory Approval Program (AQMD LAP). We are pleased to 

inform you th.t your firm is approved for the period beginning January 3 1,2012, and ending January 3 I, 

2013 for the following methods: 

SCAQMD Methods 1-4 

SCAQMD Method 1O(j,1 

SCAQMD Methods 25.1 and 25.3 (Sampling) 

SCAQMD Methods 5.1, 5.2, 5.3, and 6.1 

SCAQMO Rule 1420 - (Lead) Ambient Sampling 

USEPA CTM-OJO 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:GKlgk 

cc: Mike Garibay 

Glenn Kasai 

120111 LapRenewal.doc 

R021 0458-R 1 

S;~& 

/ ~n, Senior Manager 

Laboratory Services & 

Source Test Engineering 

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State of California 

Air Resources Board 

Approved Independent Contractor 

Delta Air Quality Services, Incorporated 

This is to certify. that the company fisted iibove'nasbeen approved 

, by the Ai,' Re~6(j fE'~ 8OardlO: CQ~u.? coi);{iilance testing 

pursuant to tit1e 17 Califorriia Code;of Regulation~, section 91207 

until Ju~ :30;',2013, for those test metliods isted below: 

ARB Soare( Te.d Mdh.:Nt.s; 

" l, 2,,3, 4, 5, 6,11, 17. 20.,501 

108 '(co; co,. NO" 0" SO,) 

Alberto Ayal2\, Ph.D" M,S,E. 

Chief, Mon~oring and Laboratory Division 
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State of California 

Air Resources Board 

Approved Independent Contractor 

Delta Air quality Se'nices;.lncorporated 

This is to certify tljilt !he co!.'1pany Iiste<!'above has been approved 

by the Air Re--so~s Board to colJd~ct ·comP.liance testing 

pursuant to title'-11;';CalifomJa Code;pf Reriillations. section 91207 

until June. :30;:i013;'for thOS& test methOds'ilsted below: 

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1' • . ,1, • '/ •• " 

. 'Visible Emissions Evaluation 

U.S. EPA Test Methods 201A (l~1.ersiO~). 202,(IP91 version) 

.17 

Alberto Ayala • .Pfl.D .• M.S.E. 

Chief. Mon~oring and laboratory 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 10: .,......:--___ ---:!1~46!!>S~3~6------------------ Date(s) Tested: _____ T"'e""s"'t "=P""a"'n-,--..,....,, __ -:---:-___________ _ 

Facility Name: CPV Sentinel Energy Prolect EquipmentAdd~r-es-s-:---9~1~1~B:7lx7b~y~D7r7iv~e~~~~~-------------

City of Industrv, California 91748 

Equipment Tested: ___ -=U":n~lt~s =-1,,:' 2~,:-:3,,", =4,:,' S=,'-,:6=-:, ~7~, &'=78"'=:-:""'7.:---------

Device 10, AlN, P/N: __ ---'D ...1 .... ,..!:D .... 7 .... , ... D 1.!..:3!.L, .... D:..!.1"'9,'-'D~2""S"", .... 31 .... ,... 3",7 ,,-,&~42,,--_______ _ 

r state, as its legally authorized representative, that the source testing firm of: 

Source Test Firm: Delta Air Quality Services. Inc. 

Business Address: .:.1""84",5"-,-,N~C=as",e,",S""t",re,,,e,,,t __________________ _ 

Orange, California 92865-4234 

is 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 with District 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, or parent company or any subsidiary thereof, 

shall have no financial interest in the testing laboratory; 

(3) Any company or facility responsible for the emission of significant quantities of pollutants to 

the atmosphere, or parent company or any subsidiary thereof shall have no financial interest in 

the testing laboratory; 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 monitoring systems, for the 

company being tested 

Furthermore, r state that any contracts or agreements entered into by my source testing firm and 

the facility 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 information provided to 

the SCAQMD;._-""'") , 

Signature: (:.,_LA- (.,) ) j \. , <: 

Bob Finken 

(Name) 

President 

(Title) 

FORM ST-110 :stevforl.doc (Revised 11/18/98) 

R021 0458-R 1 0-5 

Date: ___ "'1217 ........ 1"'20"'1 ... 2'--___ _ 

714-279-6777 1217/2012 

(Phone) (Date) 

1IeI1lt:,. ""---
APPENDIX E FACILITY PERMIT TO OPERATE CONDITION 029.1 

R038842-R1 E-1 
SOUTH COAST AIR QUALITY MANAGEMENT DISTRlcr 

21865 Copley DrIve, Diamond Bar, CA 91 765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Stction H Page; 35 

Facility 10: I Sl701 

Revision #: 0 

!n1e: ApnllS,20tI 

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)(I)-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, C10, 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 1110.2,2-1-2008; RULE 1303(b)(2)-OfTset, 5-10-1996; RULE 1303(bX2) 

-Offset, 12-6-2002; RULE 1470,6-1-2007; RULE 1012, S-6-1005] 

[Devices subject to this condition: D49] 

D29.1 The operator shall conduct source testes) for the pollutant(s) identified below. 

Pollutant(s) to I Required Test Method(s) I Averaging Time I Test Location 

be tested 

NOX emissions District method 100.1 I hour Outlet of the SCR 

serving this equipment 

CO emissions I District method I 00.1 I hour I Outlet of the SCR 

serving this equipment 

SOX emissions I AQMD Laboratory I Not Applicable I Fuel sample 

Method 307-91 

VOC emissions I District Method 25.3 II hour I Outlet of the SCR 

serving this equipment 
SOUlH COAST AIR QUALITY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 91765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

SettionH 

F~ilitv 10: 

Rnisionll: 

Date: 

Page: 36 

152707 

o 

April 15.2011 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

The operator shan comply with the terms and conditions let forth below: 

PM I 0 I District Method 5 

emissions 

NH3 emissions I District method 207.1 

and 5.3 or EPA method 

17 

I 4 hours 

II hour 

I Outlet of the SCR 

serving this equipment I Outlet of the SCR 

serving this equipment 
SOlITH COAST AIR QUAlllY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 91765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H Pa,gc: 37 

Facilirv 10: 152707 

Revision M; 0 

Date: April IS, lOll 

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 

fonows: 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-l2 (with pre concentration) and temperature of canisters when extracting 

samples for analysis is not below 70 deg F. 

The test shan be conducted for compliance verification of the BACT VOC 2.0 

ppmv limit. 

The test results shall be reported with two significant digits. 
SOUlli COAST AIR QUALITY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 91765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H Page' 3' 

Facility ID: 152707 

Revmon': 0 

Date: AptillS,201I 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

The operator shall comply with the terms and conditions set forth below: 

[RULE 1303(a)(I)-BACT,5-10-1996; RULE 1303(aXl)-BACT, 12-6-2002; RULE 

1303(b)(l}-OffJet, 5-10-1996; RULE 1303(b)(2}-Offsct, 12-6-2002; RULE 1703(a)(2)-

PSD-BACT, 10-7-1988; RULE 2005, 5-6-2005] 

[Devices subjectto this condition: 01, 07, DI3, 019, D25, D31, 037, D43) 

029.2 The operator shall conduct source testes) for the pollutant(s) identified below. 

Pollutant(s) to I Required Test Method(s) 

be tested 

NH3 emissions I District method 207.1 

and 5.3 or EPA method 

17 

I Averaging Time 

II hour 

I Test Location 

I Outlet of the SCR 

serving this equipment 

The test shall be conducted and the results submined 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 NOll 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 I303(aXI}-BACT, 12-6-2002) 

[Devices subject to this condition: 01, 07, D13, 019, 025, D31, D37, 043) 
END OF DOCUMENT