April 17, 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 5 

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 5 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. Please note that one of the natural gas fuel samples taken as part of this 

test (included in Appendix B.2) had a sampling container leakage problem. Therefore, 

we are in the process of collecting additional natural gas fuel samples and will report the 

results in a separate submittal to the SCAQMD. 

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

please contact me at (916) 444-6666. 

Sincerely, 

~~---------------- Tom Andrews 

Senior Engineer 

Enclosure 

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 5 

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 

ALI ALESHAIKER I ROBERT A. FINKEN 

APRIL 15, 2013 

REPORT NUMBER: R5210729 

8el/a!1 

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. 

R521 0729 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. 

_______ G.A.<kv"'-' """""~ "'-. ==-___ Date: 

Ali Aleshaiker 

Project Engineer 

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. 

R5210729 

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 5 Stratification Test ....................................... ................. B-3 

B.1 .2 Sentinel Unit 5 Ammonia, ROG, and NOx/CO Testing ....................... . B-4 

B.1.3 Sentinel Unit 5 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 

R5210729 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 

R521 0729 v 
1.0 INTRODUCTION AND SUMMARY 

Delta Air Quality Services, Inc. has been contracted by Gemma Power Systems 

California, Inc. (GEMMA) to perform the initial Permit to Operate Compliance Testing at 

the CPV Sentinel Energy Project Units 1, 2, 3, 4, 5, 6, 7, and 8. Condition D29.1 of the 

Permit to Operate requires source tests within 180 days of initial startup. 

This document is the test report for the initial compliance for CPV Sentinel Unit 5. 

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 25-28, 2013. The Delta test crew consisted 

of Ali Aleshaiker, Ray Madrigal, Mike Chowsanitphon, and Justin Miller. 

Table 1-1 contains a summary of the test results and applicable limits. This table 

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

tested. All test results showed the unit to meet the permit limits. 

Section 2.0 of this document provides a description of the facility and sample 

locations. A description of the sampling strategy and test methods is provided in Section 

3.0. Section 4.0 contains detailed test results. Section 5 contains a discussion and test 

critique. The appendices contain all test and laboratory data, calculations, and quality 

assurance data. 

R5210729 
Parameter Units 

ppm@ 15%0, 

NO, ppm @ 15% 0, 

Ib/MMscl 

CO ppm @ 15% 0, 

NH3 ppm@ 15% 0, 

gr/dscl @ 3% 0, 

Particulate gr/dscl @ 12% CO, 

Ib/hr 

PM1O/PM'.5 Ib/MMscl 

SO,l3) Ib/MMBtu 

gr H,S/1 00 scI 

ROGs ppm @ 15% 0, 

TABLE 1-1 

CPV SENTINEL ENERGY PROJECT 

UNIT 5 

STACK TEST RESULTS SUMMARY 

100% 75% 50% 

1.68 1.54 1.97 

1.68 1.54 1.97 

706 6.29 7.96 

2.93 2.74 0.42 

3.75 1.91 0.67 

0.0007 0.0007 0.0013 

0.0008 0.0009 0.0015 

0.85 0.84 1.02 

0.97 1.19 1.90 

000002(5) 

0.006(5) 

ND<0.51 ND<0.51 ND<0.59 

(1) The 12.26 Ib/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. 

Limit 

2.5 

15 

12.26(1) 

4 

5 

0.01 

0.1 

11 

5.71(') 

0.06 

0.25(4) 

2.0 

(4) 0.25 gr H,S/100 scf sulfur content limit is based on annual average of monthly sample results. 

Rule 

1703(a)(2) 

40 CFR 60 

2012 

1703(a)(2) 

1303(a)(1) 

475 

409 

475 

40 CFR 60 

SCAQMD Permit 

Condition B61.1 

1303(a)(1) 

(5) Results from one sample. One of the duplicate samples obtained a leak and was compromised. An 

addendum to this report will be submitted with results from two new duplicate samples when the 

information becomes available. 

R521 0729 2 
2.0 UNIT DESCRIPTION AND TEST CONDITIONS 

2.1 UNIT DESCRIPTION 

CPV Sentinel Energy Project is located at 15775 Melissa Lane, North Palm 

Springs, California 92240. The facility consists of eight (8) identical generating units. 

The CPV Sentinel Energy Project consists of eight (8) LMS100PA combustion 

turbines in simple cycle operation. The units are natural gas fired with a rated heat input 

of 891.7 MMBtu per hour at 72 degrees Fahrenheit. Each LMS100PA employs water 

injection and is equipped with a CO catalyst and Selective Catalytic Reduction (SCR) 

system for NO, control. 

The LMS100PA is a General Electric (GE) combustion turbine with an intercooler 

located between the low pressure compressor (LPC) and high pressure compressor 

(HPC). Off engine combustion air to closed loop water intercooling is used for increased 

gas turbine thermal efficiency. Heat removed from the off-engine intercooler is circulated 

through a closed loop cooling system. Heat is rejected from the closed loop cooling 

system to an open loop cooling system via a shell and tube heat exchanger. The open 

loop system rejects heat via a mechanical draft counterflow cooling tower. The cooling 

tower is provided with drift elimination to comply with air emissions limits. 

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

arrangement of the major components. 

R5210729 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 

R521 0729 

Air 

Water 

Heat 

Exhaust to Atm. 

Exhaust CO Catalyst SCR -

Ammonia 

19% Aqueous 

4 
FIGURE 2-2 

GENERAL ARRANGEMENT OF MAJOR COMPONENTS 

2.2 TEST CONDITIONS 

r~AM5Tll'-"" 

T'\'~~ ~' 

!~,~~t~_ ! 

, , , , r' , , , , , 

v 

Q • '. 14 II 

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. 

R521 0729 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 5,392 7,063 8,747 

Turbine Generating Output (MW) 55.1 80.0 105.9 

Ammonia Flow, Ib/hr 103.3 130.7 193.8 

Exhaust Temperature, of 776 733 736 

Exhaust Flow Rates, kscfh 14,994 19,243 22,377 

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. 

R521 0729 6 
FIGURE 2-3 

SAMPLE LOCATION DETAILS 

Inside Diameter, in. 

- 162 -- Stack Exit 1080.0 in. 

Silencer Bottom 925.9 in. I 

Ports 841.6 in. 

Platform 789.6 in. 

84 Distance A, inches, 0.5 Diameters 

! Sam pie ports 

T 

323 Distance B, inches. 2.0 Diameters 

Base of Stack 518.5 in . 1 

__ ..::E::; xh,:::aust Flow 

Grade 0.0 in . 

Elevation View 

90 11. 

66 ft. 

o 11. 

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 0.80 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. 

R521 0729 7 
TABLE 2-2 

12-POINT STRATIFICATION CHECK RESULTS 

GEMMA POWER SYSTEMS 

CPV SENTINEL UNIT 5 

02 CO2 

Port Point % % 

West 3 13.24 4.54 

West 2 13.24 4.54 

West 1 13.25 4.54 

South 3 13.25 4.54 

South 2 13.64 4.31 

South 1 13.62 4.32 

East 3 13.55 4.40 

East 2 13.53 4.41 

East 1 13.50 4.43 

North 3 13.53 4.42 

North 2 13.53 4.43 

North 1 13.49 4.45 

Average 13.4 4.4 

Maximum 13.6 4.5 

Minimum 13.2 4.3 

Maximum Difference from Average 0.2 0.1 

Max Difference (% of average) 1.5% 3.0% 

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 

NO, CO 

ppm ppm 

2.23 2.18 

2.24 3.08 

2.24 2.40 

1.93 3.35 

1.98 3.94 

1.66 3.54 

1.92 3.80 

1.89 4.03 

1.79 4.22 

1.93 4.69 

1.90 4.17 

1.78 3.69 

2.0 3.6 

2.2 4.7 

1.7 2.2 

0.3 1.4 

15.4% 39.3% 

Table 2-3 illustrates the location of sample traverse pOints for each type of test. 

TABLE 2-3 

SAMPLE POINT LAYOUT 

PM (24 pis.) Cydonic Flow Check (16 pis.) 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 .6 19.1 19.4 31.4 29.6 46.0 

4 17.7 26.7 32.3 52.3 70.4 114.0 

5 25 40.5 67.7 109.7 85.4 136.3 

6 35.6 57.7 80.6 130.6 

7 64.4 104.3 89.5 145.0 

6 75 121 .5 

9 62.3 133.3 

10 86.4 140.0 

11 93.3 151 .1 

12 97.9 156.6 

R521 0729 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 NO" 

CO, NH3 , ROGs and SO,. 

TABLE 3-1 

TEST MATRIX 

SENTINEL UNIT 5 

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

NO, SCAQMD 100.1 2 runs· 2 runs· 2 runs· 60 minutes 

° i C02 SCAQMD 100.1 With each run 

CO SCAQMD 100.1 2 runs· 2 runs· 2 runs· 60 minutes 

NH3 SCAQMD 207.1 2 runs 2 runs 2 runs 60 minutes 

S02 SCAQMD 307.91 Fuel Sample, 2 Samples N/A 

PM SCAQMD 5.1 1 run 1 run 1 run 240 minutes 

ROG Modified SCAQMD 25.3 1 pair 1 pair 1 pair - 60 minutes!') 

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. 

R5210729 9 
TABLE 3-2 

CPV SENTINEL ENERGY PROJECT 

PERMITTED EMISSION LIMITS 

Parameter Units 

ppm@ 15%0 2 

NO, ppm @ 15% O2 

Ib/MMscf 

co ppm@ 15% O2 

NH3 ppm@15% 0 2 

gr/dscf @ 3% O2 

Particulate gr/dscf @ 12% CO2 

Ib/hr 

PM,01PM25 Ib/MMscf 

SO, Ib/MMBtu 

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 penmit as an emission factor. 

Limit 

2.5 

15 

12.26(1) 

4 

5 

0.01 

0.1 

11 

5.71(2) 

0.06 

0.25(3) 

2.0 

Rule 

1703(a)(2) 

40 CFR 60 

2012 

1703(a)(2) 

1303(a)(1 ) 

475 

409 

475 

40 CFR 60 

SCAQMD Permit 

Condition B61.1 

1303(a)(1 ) 

(3) 0.25 gr H2S/100 scf sulfur content limit is based on annual average of monthly sample results . 

3.1 O2• CO2• NOx AN D 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. 

R521 0729 10 
NOx 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. 

R5210729 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. 

R521 0729 

FIGURE 3-1 

MODIFIED SCAQMD METHOD 25.3 SAMPLING APPARATUS 

Filter Probe 

Flow Controlier 

12 

Vacuum 

Gauge 
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 ppmcart>on . 

Modifications suggested by SCAQMD to the Method 25.3 analytical procedures 

approved for MC under the lAP are: 

• Pressurization of the canisters to 900 mm Hg with Ultra High Purity (UHP) 

helium analyzed/certified to contain less than 0.05 ppmv of total hydrocarbons 

as carbon 

• Analyzing only the Summa canister fraction of the normal 25.3 sample. No 

water vial used in sampling, no water vial analysis. 

• Utilization of a larger (-2 ml) sampling loop 

• Development of a custom low level (0.1 - 5.0 ppmV propane) calibration 

curve 

• Performance of a Minimum Detection Limit (MOL) study 

• Determination of a Practical Quantitation Limit (PQl) from the MOL study 

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

digits, corrected to 15% 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 SCAQMD concerning the application of the modified 

SCAQMD Method 25.3 to permit condition 029.1 are located in the test plan in Appendix 

H. 

R5210729 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 PMlO emissions if all 

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

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

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. 

R521 0729 14 
Temperature 

Sensor Probe 

~ Pilot Tube 

Nozzle 

/ 

S-Type Pitot Tube 

R5210729 

FIGURE 3-3 

SCAQMD METHOD 5.1 SAMPLE SYSTEM 

Manometer 

Orifice 

Connecting 

TubIng 

Temperature 

Dry Gas 

Meter 

15 

Temperature 

Sensor 

Gel 

Vacuum 

Gauge 

line 
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 

NOx, CO, Ammonia (NH3) , and RaG -100% load 

PM results - 100% load 

NOx, CO, NH3, and RaG - 75% load 

PM results - 75% load 

NOx, CO, NH3 , and RaG - 50% load 

PM results - 50% load 

sax 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. 

R521 0729 16 
TABLE 4-1 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 5 

NO., CO, NH3, AND ROG 

100% LOAD 

FEBRUARY 25, 2013 

Test Number Run 1 Run 2 Average Limit 

Condition 106 MW 106 MW 

Test Date 2/25/2013 2/25/2013 

Start Time 11 :35 13:04 

Stop Time 12:43 14:17 

Fuel Flow, hscfh 8,746 8,742 

Stack Flow Rate, dscfm 416,170 393,969 

Stack 0 , (%) 13.54 13.50 13.52 

Stack NO, (ppm) @ 15% 0, 1.70 1.65 1.68 2.5 

Stack NO, (lb/MMscf) 7.36 6.77 7.06 12.261') 

Stack CO (ppm) @ 15% 0, 2.98 2.87 2.93 4 

Moisture Fraction 0.098 0.099 

PPM NH3 (flue gas) 4.59 4.78 4.69 

PPM NH3 @ 15% 0, 3.68 3.81 3.75 5 

Ib/hr NH3 5.14 5.06 5.10 

Ib/MMscf fuel NH3 5.87 5.79 5.83 

Stack ROG(1

), ppm @ 15% 0, NO<0.51 NO<0.51 2.0 

1) Collected as a simultaneous pair. 

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

R5210729 17 
TABLE 4-2 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 5 

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 25,2013 

S-5/STK-PM-100-1 

106 MW 

2/25/2013 

10:56 

15:20 

8,747 

356,867 

1347 

4.34 

0.090 

Particulate Emissions 

0.0003 

0.0007 

0.0002 

0.0008 

0.85 

0.97 

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

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

R5210729 18 

Average 

0.0003 

0.0007 

0.0002 

0.0008 

0.85 

0.97 

Limit 

0.01 

0.1 

5.71(21 

!!.f!t!!!d 
TABLE 4-3 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 5 

NO" CO, NH3, AND ROG 

75% LOAD 

FEBRUARY 25,2013 

Test Number Run 1 Run 2 Average Limit 

Condition 81 MW 80MW 

Test Date 2/25/2013 2/25/2013 

Start Time 16:42 18:07 

Stop Time 17:48 19:14 

Fuel Flow, hscfh 7,078 7,085 

Stack Flow Rate, dscfm 349,945 332,898 

Stack 0, ('!o) 13.98 14.04 14.01 

Stack NO. (ppm) @ 15% 0, 1.33 1.75 1.54 2.5 

Stack NO. (lb/MMscf) 5.63 6.94 6.29 12.261') 

Stack CO (ppm) @ 15% 0, 1.95 3.54 2.74 4 

Moisture Fraction 0.082 0.095 

PPM NH3 (flue gas) 2.60 1.86 2.23 

PPM NH3 @ 15% 0, 2.21 1.60 1.91 5 

Ib/hr NH3 2:44 1.66 2.05 

Ib/MMscf fuel NH3 3:45 2.35 2.90 

Stack ROGI1 ), ppm @ 15% 0, NO<0.51 NO<0.51 2.0 

1) Collected as a simultaneous pair. 

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

R5210729 19 
TABLE 4-4 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 5 

PM -75% LOAD 

FEBRUARY 25,2013 

Test Number S-5/STK-PM-75-1 Average Limit 

Condition 80MW 

Test Date 2/25/2013 

Start Time 16:42 

Stop Time 20:54 

Fuel Flow, hscfh 7,063 

Stack Flow Rate, dscfm 349,451 

Stack 0" % 14.01 

Stack CO" % 3.91 

Moisture Fraction 0.090 

Particulate Emissions 

Grain Loading, gr/dscf 0.0003 0.0003 

Grain Loading @ 3% 0, 0.0007 0.0007 0.01 

Grain Loading @ 15% 0, 0.0002 0.0002 

Grain Loading @ 12% CO, 0.0009 0.0009 0.1 

Mass Emissions, Ib/hr 0.84 0.84 11(11 

Emission Rate, Ib/MMscf 1,19 1,19 5.71('1 

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

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

R521 0729 20 Rff/B.A, 
TABLE 4-5 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 5 

NO" CO, NH3, AND ROG 

50% LOAD 

FEBRUARY 26, 2013 

Test Number Run 1 Run 2 Average Limit 

Condition 55MW 55MW 

Test Date 2/26/2013 2/26/2013 

Start Time 8:30 10:00 

Stop Time 9:37 11 :09 

Fuel Flow, hscfh 5,384 5,400 

Stack Flow Rate, dscfm 259,659 261 ,782 

Stack 0 , ('!o) 14.15 14.13 14.14 

Stack NO, (ppm) @ 15% 0, 1.83 2.12 1.97 2.5 

Stack NO, (lb/MMscf) 7.34 8.58 7.96 12.261') 

Stack CO (ppm) @ 15% 0, 0.41 0.43 0.42 4 

Moisture Fraction 0.091 0.092 

PPM NH3 (flue gas) 0.73 0.81 0.77 

PPM NH, @ 15% 0, 0.64 0.71 0.67 5 

Ib/hr NH3 0.51 0.57 0.54 

Ib/MMscf fuel NH3 0.94 1.06 1.00 

Stack ROG(1), ppm @ 15% 0, ND<0.59 ND<0.59 2.0 

1) Collected as a simultaneous pair. 

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

R5210729 21 
TABLE 4-6 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 5 

PM - 50% LOAD 

FEBRUARY 26, 2013 

Test Number S-5/STK-PM-50-1 Average Limit 

Condition 55MW 

Test Date 2/26/2013 

Start Time 8:30 

Stop Time 12:40 

Fuel Flow, hscfh 5,392 

Stack Flow Rate, dscfm 242,273 

Stack 0" % 14.10 

Stack CO" % 3.85 

Moisture Fraction 0.089 

Particulate Emissions 

Grain Loading, gr/dscf 0.0005 0.0005 

Grain Loading @ 3% 0, 0.0013 0.0013 0.01 

Grain Loading @ 15% 0, 0.0004 0.0004 

Grain Loading @ 12% CO, 0.0015 0.0015 0.1 

Mass Emissions, Ib/hr 1.02 1.02 11111 

Emission Rate, Ib/MMscf 1.90 1.90 5.71 1'1 

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

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

R5210729 22 
R5210729 

Test Number 

Condition 

Test Date 

SOx. Ib/MMBtu 

gr H,S/1 00 scf 

TABLE 4-7 

COMPLIANCE TEST RESULTS 

CPV SENTINEL ENERGY PROJECT 

SENTINEL UNIT 5 

SOx FROM FUEL ANALYSIS 

FEBRUARY 28,2013 

Average 

100% 

2/28/2013 

000002(') 

0.006(') 

Limit 

0.06 

0.25(1) 

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

sample results. 

(2) Results from one sample. One of the duplicate samples obtained a leak and 

was compromised. Two additional samples were collected on April? 2013. 

The samples were not analyzed due to laboratory equipment failure. 

An addendum to this report will be submitted with results from two new 

duplicate samples when the information becomes available. 

23 R,f/af.,. 
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. 

• One of the duplicate Fuel Sulfur samples obtained a leak and was compromised. 

Two additional samples were collected on April 7, 2013. The samples were not 

analyzed due to laboratory equipment failure. 

• An addendum to this report will be submitted with results from two new duplicate 

samples when the information becomes available. 

R521 0729 24 fJelfl!~ 
APPENDIX A QUALITY ASSURANCE 

R5210729 A-1 
Appendix A.1 Quality Assurance Program Summary 

R5210729 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 meetings 

• Attendance at EPA sponsored training courses 

• Maintenance of training records. 

Eguipment 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 

R5210729 A-3 
Evaluation Society. Delta personnel continually work with industry and regulatory 

agencies in monitoring and developing new methods and rules. 

Chain-of-Custody: Delta maintains chain-of-custody documentation on all data sheets 

and samples. Samples are stored in a locked area accessible only to Delta source test 

personnel. Data sheets are kept in the custody of the originator, program manager, or in 

locked storage until return to Delta's office. Upon return to the office, copies are made 

and stored in a locking file. The original data sheets are used for report preparation and 

any additions are initialed and dated. 

QA Reviews: Every Delta report is reviewed by someone separate from the report 

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

source tested. Periodic field, laboratory, and report reviews are performed by the QA 

Officer. Test plans are reviewed to ensure proper test methods are selected and reports 

are reviewed to ensure that the methods were followed and any deviations from the 

methods are justified and documented. 

R5210729 A-4 
Equipment 

Pumps 

Flow Meters 

Sampling Instruments 

Integrated sampling 

tanks 

Mobile van sampling 

system 

Sampling lines 

R521 0729 

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% 

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 

A-5 

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. 
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 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% 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 

R5210729 A-6 
Appendix A.2 SCAQMD and CARB Certifications 

R521 0729 A-7 
South Coast 

Air Quality Management District 

21865 Copley Drive, Diamond Bar, CA 91765-4178 

(909) 396-2000 • www.aqmd.gov 

Mr. Robert A. Finken 

Delta Air Quality Services, Inc. 

1845 N. Case Street 

Orange, CA 92865 

Subject: LAP Approval Notice 

Reference # 96LA 1220 

Dear Mr. Finken: 

December 19, 2012 

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

Air Quality Management District's Laboratory Approval Program (AQMD LAP). We are pleased to 

inform you that your firm is approved for the period beginning January 31 , 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 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 

121218 LapRenewal.doc 

~ Rody 

Laboratory 

Ed" 

Services 

s,~ & 

Source Test Engineering 
State of California 

Air Resources Board 

Approved Independent Contractor 

Delta Air Quality Servic~~ Incorporated . , 

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

by the Ail Resources Board 'to tonduclyompliance testing 

pursuant to title 17, California Coq~ of-Regtnat1ons, ~ection 91207 

until June 30, 2013, for 

.' 

thOse teSt methods listed below: , 

" 

" . 

.ARB S\)Ql'ce Test Methods! 

h 2, 3;_4,' 5, 6, '8, 17, 20, SOt 

100 '(CQ. cOu NO", qz, S02) 

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

Chief, Monitoring and Laboratory Division 
State of California 

Air Resources Board 

lOeaeAQent Contractor 

Delta AjfflU3JiW Set:ri es lR@{ 

This is to ("prtiM K'~t 

by the 

pursuant to ~l ~~.::tti.;~ 

until J 

f~~VoV'''.I'l~:i> \been approved 

~~~ce testing 

. . ~t~ , ection 91207 

Ti;e~~ 9! J ,d below: 

version) 

Alberto Ayala, 9fl.D. , M.S.E. 

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

R5210729 A-8 
Jf1IIPRAXAIR. Praxair Distribution, Inc. 

5700 5. Alameda 51. 

Delta Air Quality 

1845 N. Case St. 

Orange, CA 92865 

-

Los Angeles, CA 90058 

Tel: 323-585-2154 

Fax: 714-542-6689 

01/23/2013 

Work Order No. 22514330 

Customer Reference No. 

Product LotiBatch No. N109301805 

Product Part No. NI 5.5CE-AS 

C A ~/?q~/. CERTIFICATE OF ANALYSIS 

;)" '" ., NItrogen, 5.5 Continuous Emission Monitoring Zero 

Analytical Analytical Analytical 

Analyte5 Specification Results Principle Accuracy 

Nitrogen >99.9995 % >99.9995 % N 

Carbon Dioxide < 1 ppm < 0.20 ppm L ± 10 % 

Carbon Monoxide < 0.5 ppm < 0.5 ppm L ± 15 % 

Total Hydrocarbons < 0.1 ppm < 0.1 ppm Q ± 15 % 

Oxides of Nitrogen <0.1 ppm < 0.01 ppm U ± 15 % 

Oxygen < 0.5 ppm <0.5 ppm W ± 15 % 

Sulfur Dioxide < 0.1 ppm < 0.1 ppm Z ± 15 % 

Water < 2 ppm < 0.2 ppm P ± 0.4 ppm 

Analytical Instruments: Meeco-Aquavolt -Moisture-Electolytic Hygrometer 

Cylinder Style: 

Cylinder Pressure @70F: 

Cylinder Volume: 

Valve Outlet Connection: 

Cylinder No(s). 

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

Thermo Environmental-42i-Nilric Oxide Analyzer-Chemiluminescence 

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

Ionization Detector 

AMETEK-921CE-UV S02 Analyzer-Ultraviolet Absorption 

DeltaF-Nanotrace-Trace Oxygen-Electrochemical 

AS Filling Method: 

2000 pslg Date of Fill: 

158 ft3 

CGA-580 

SA21794 

Temperature/Pressure 

01/18/2013 

'""'." H,"~ .",,&06" Approved 

Signer: 

Charles MiY (/ 

E G.I CflromalO9l.phW willi f lam, Photometric: 

Deledor 

G~5 CIvomltogtlP.'Iy -..Itn ReduC\ion Gas Afl.ryze, 

M aIIUS SpearDtfleuy • loiS Of GCMS 

Q Tot~1 i'ird ~rbon An.lyzlf 

U cn.rrWluminescenet 

v PI'Ised Fluoresunet 

IMPORTANT 

B OU Chro<nllog .... phy wilh Di$dl~ on u~on 

Delee/or 

F Gn Chrom",oor.llhy with H.li<.r!llOnltllion 

Oe1ector 

Gas Cl\n:ImlllOO""phy willi ~ CondudMly 

Detector 

N a, Oilftreoee of ly~llmll\lliUes 

R W10I CIIIUlIiQI 

V Gra~lmelrt~ 

Z W Sp!cIrometry 

C G.s ChrolTUllog .. pIly wilh EJectrotyIie COIIducllvn) 

ODledor G GIS Cnromltography Willl M81f11~iler C,rtIonIler 

K 8Ir'I1I}'G!I$l\rn!Iyzlrwl\h TlIIITTUIJC~lIy 

OelG'dor 

o Parlm."n~ 

S Oeu,c;tOf T",b8 

W EIoclr~1c; Clf\lEJectrod'lernical 

o GIs Cftrom.log'lplly WIth f l..." IOr'IilPool 

DeleaD, 

H GlI$ C~rom'logtaph) with Pho!l>icniUlion De1e-ctOi 

l 1111"'1(1' FTlR 01 NctR 

P Specllic Wiler MII)'l" 

T """ X PflOiOlonlt.IIQn 

The information contained herein has been prepared at your request by pertomel within Praxalr Distribution, Inc.. While we believe the information is accurete within the limits of the analytical methods 

employed and is complete to Ihe exlent 01 the specific analyses performed, we make no warranly or rapresenLation as to Ihe suitability of the U5e of the Information for any particufar purpose The 

information is olfered with !he underslanding thaI any use of the Information is at the sole discretlon and risk cA the user. In no event shal! liabiffty of Praxair Dislriootion, Inc. arising out of the use of the 

information contained herein e~ceed the fee established fO( providing suel1 informallon. 

Pg.1 of 1 Z-I'J-IgP 
'ffff~PRAXAIR PrRXair 

5700 South Alameda Street 

Los Angeles, CA 90058 

Tel, (323) 585-2154 F,,,(714) 542-6689 

DocNumbe" 000037792 PGYPID, F22012 

-.- ,~ ~"<':'r-'<"~~r'f':':~- "" ~ L--"- '" > '. .. ) 

- €1!:I!J!!lBll24 TE OFA'H..J1.!lp"J{;S,!'8;ifJiliRR 'p:BXiJlF{f)C(f)1!; OAS 

Cus/o 

Delta Air Quality F/If IAIII:: 4/2012012 

1845 N. Case St. 

Orange, CA 92865 

Praxair Order Number: 20034099 

Customer P. O . . Vumber: 03852345 

Customer Reference Number: 

Pori Numhar: EV NICOOXE78-AS 

J,mNllmbc:,.,' 109211114 

Gyll",l,,/' Sly/~ & (Jillllf': AS eGA 590 

0" /0.00 

Cf).", t;. 00 

Certified Concentration: 140cu. ft 

Expiration Date: 

Cylinder Number: 

CC/~"'5 5.00 % 

10.00 '% 

Balance 

~"oS/OI 

511/2015 

CC181115 

CARBON DIOXIDE 

OXYGEN 

NITROGEN 

NIST Traceable 

Analytical Uncertainty: 

± 1 % 

± 1 % 

Cerli/carion Iltformalio Certification Dare: 5/112012 Term: 36 Months Expirat;on Date: 5/1/2015 

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

Do Not Use this Standard if Pressure is less than 150 PS1G 

PGVP 1.0.# F22012 

AI/Myfical Dala: (R=Reference Standard, Z::.Zero Gas, C=Gas Candida/e) 

1 . Component: CARBON DIOXIDE 

ReQuesled Concentralion 5 % 

Cer1ifiod Concentration: 5_00 % 

Instrument Used: 

Analytical Method: 

Siemens Ultremat 5E SIN A12·730 

NOIR 

Lasl Multipoint Celibrelion 411112012 

Date: 

z, 0 R, '17 C, , Cone : 

I R, 51' Z, 0 C, 5 Cone: 

Z, 0 C, 5 R, 5.17 Cone: , 

; UOM: .. Mean Test Assay: 

----

2. Component: OXYGEN 

ReQuested Concenlration: 

Certifled Concentration: 

Instrument Used: 

Ana yt~al Method: 

10% 

10.00% 

OXYMAT 5E 

PARAMAGNETIC 

las! MuMipolnt CelibraliaT 411112012 

/;;;~1~----1 

, ! 

__ : .. __ J 

(~ Anal;~~~;a-------- ~~te - - ;';7;012-- . - •• 

Z 0 R 1542 C 10 Conc 10 

R 1542 Z 0 C 10 Cone 10 

Z 0 C 10 R 1542 Conc, 10 

I UOM: % 

--------- Analyzed by: 

Reference Standard Type: 

Ref. Std. Cylinder fI : 

ReI. Std. Cooc: 

Ref. Sid. Treceapis 10 SRM 1/ ' 

SRM S<lmplo 1/ : 

SRM Cylinder * : 

GMIS 

CC263449 

5.17% 

VI. 1574P 

7·F·32 

SAL01 4&4 5 

,---.------------ -r I Second Analysis Ollta: t 

~ '~ . ~ j Oat.; 

0 Cone: 

0 Cone: 

Z: 0 C: 0 R: 0 Cone: 0 

UOM : % Mean Tesl ASSI_" _ __ 0 .~ __ 

Ref9f&nee Standard Type: 

Ref. Std. Cylinder t/. : 

Ret Std. Cone: 

GMIS 

HA 9153 

15.42 % 

Ret Std. Traceable to SRM 1/ : vs. 2559a 

SRM Sample II : 71·37·6 

SRM Cylinder II : CLM·006734 

I ."Md AMI,,,. 0 .. , 

Z: 0 R: 0 

Dale: 

C: 0 Cone: 

~M~%~· ~ C: 0 Cone: 

R: 0 Cone : 

Mean Test Assay: 

o 

o 

o 

-1 

I 

I 

Certified by: 

Sham~~ 

Information contained herein has been prepared at your reQuest by Qualifiad tI~per1s within Praxair Olslribl.llioo. Inc. While we pelieve that the informalloo Is accurate wilhinlhe limits of the analyllcal 

methods employed and Is com~eta 10 tha exlant of the specific analyses performed, we make flO warranty or representation as to the suitability of the use of the information fOf any purpose. The 

Informalion is offered with the understanding that any use of the informldion is a\ the sole discretion and risk of the user. In no avent Shall the liability of Praxair Oistribulion, Inc., arising oul 01 the 

use of Ihe Informallon con talned herein exceed Ihe fee established for providing such Information. 

/1 - 2- - /2---7 
CII.<;(O 

UffffflPRAXAIR 

DocNumber: 000038940 

Praxair 

5700 South Alameda Street 

Los Angeles, CA 90058 

Telephone: (323) 585·2154 

facsimile: (7 t 4) 542·6689 

CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS 

Delta Air Quality /';///)we : 5/22r.<012 

1845 N. Case St. 

Orange, CA 92865 

Praxair Order Number: 20362117 

Cuslomer P. 0. Number 03901124 

Customer Reference .VlImber: 

!',u'/,V"mhcr: NI CD9.503E-AS 

1."/ Number: 1092111306 

('ylill<kr Slylu cf ()III/~,: AS eGA 590 

OJ, 18.98 

Co" tf·'-z., 

CC2.~''''' E'/fos/,ot 

Certified Concentration: ( 'ylilU.kr "HM!!,. c\I Vo/""''': 2000 p$ig 

Expiration Date: 

Cylinder Number: 

9.62 % 

18,98 % 

Balance 

5/30/2015 

CC246737 

CARBON DIOXIDE 

OXYGEN 

NITROGEN 

NIST Traceab!e 

Analytical Uncertainty: 

± 1 % 

± 1 % 

Cerfijcufi()n Illformation: Certification Date: 5/30/2012 Term: 36 Months Expiration Date: 5/30/2015 

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

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

PGVP ID.# F22012 

Ana(l'licai Data: (R.,Reference Standard. Z=ZefO Gas. C"Gos Candidate) 

1 . Component: CARBON DlOXtDE 

Requested Concentration' 

Certffied Concentration: 

tnstrument Used. 

Analytical Method: 

last Multipoint Calibration: 

First Analysis Data: 

z, 0 R, 10.08 

R, 1006 Z, 0 

Z, 0 C, 9.58 

UOM: % 

2 . Component : OXYGEN 

Roquested Concentralion. 

ConJflcd Concentration 

Instrument Used' 

Analylical Method 

Last Mulllpoil1t Calibration 

First Analysis Data: 

UOM: 

o 

20 

o 

% 

R: 7.0 

Z: 0 

C: 18.98 

95% 

9.62% 

Siemens Ultramat SE SIN A12-730 

NOIR 

5/1112012 

[lata: 

C, 9.62 Cone: 

C, 9.5 Cone: 

R, 10,05 Cone: 

Mean Tost Assay: 

19% 

18.98% 

OXYMAT 5E 

PARAMAGNETIC 

5/1112012 

5/301201 .. 

9.62 

9.62 

9,61 

9.62 % 

Dale: 5/3012012 

C: 18.98 Cone: 

C: 18.98 Cone: 

R: 20 Cone: 

18.98 

18.98 

18.98 

MOiln Te~(AsSiI, 

Analyzed by \ \ 

ROll 

Reference Standard Type' 

Ref. Std, Cylinder 1# ; 

Ref. Std. Cone: 

Ref. Std. Traceable to SRM fI 

SRM Sample" 

SRM Cylinder It : 

I .- ..• -

I Second Analysis Data: 

I Z, 0 R 0 C, 

! R, 0 Z, 0 C, 

, 

i z, 0 C, 0 R, 

GMIS 

SA1471 

10.08% 

VS. 1675b 

6·F·51 

CAI.D14538 

Date: 

0 Cone: 

0 Cone: 

0 Cone: 

0 

0 

0 

I UOM: % Moan last Assay: 0% L ... _ .._ . 

Rmelence Standard Typo' 

Ref. Std. Cylinder #I : 

Ref. Std. Cone: 

Ref, Std. Traceable to SRM #I : 

SRM Sample # : 

SRM Cylinder II . 

Second Amlty$is Oatil: 

z, 0 R, 0 

R, 0 Z, 0 

2, 0 C, 0 

GMIS 

SA12632 

20.00% 

2659;j 

71·37·8 

ClM..Q0673-4 

o 

o 

o 

Dale: 

Cone: 

Cone: 

Cone: 

o 

o 

o 

UOM: % Melin Tesl Assay: 0 % 

Certified by: 

Shameela Jiffrey 

G1 

140cu fl 

Intormation ,::ootained herein has been prepared at yOU!" request by qualified experts wflnin Prllxai: DisltibutiOfl, Inc. 'oNhite we believe ttUlt ttm Information i9 aecureto witliin the IlITlits of the analyllcal 

methods employed and is complete to the cdent of the specific analyses performed, we meke no warrAnty or representation as 10 Ihe suitability of tho use of the informalion for any purpose. The 

information IS offered With the understanding that any use of the Information is at the sole discretk'n and risk of the user. In no evant Shall the liability of Pra)(sir OistribUtion,~nc., arisin 01 the 

use of the informat,on con tained herein exceed the faD established for providing such Information 

'6 ' '7 (-/1--

I 
'jff:~PRAXAIR 

DocNumber: 000042731 

Custor 

Praxair 

5700 South Alameda Street 

Los Angeles, CA 90058 

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

PGVPID: F22012 

- Delta Air Quality Praxair Order Nllmber: 21232031 PiIfDoI,: 1f1.t1i2012 

1845 N. Case St. Customer P. 0. Number; 04033576 p(lriMmllJ~,; NI N02.5ME·AS 

range CA 92865:. Customer Reference Number: ~ La/ Numbllr: 109201406 

, C)llll/du Sryle ~ 01111,,: AS eGA 660 

tJ 0 ~ 2. S 'r-E-x-p-ira-t-io-n-D-a-te-:-----9-,-11-~-:-:-:.:.:-le-d-C_o_r._.c_e_n_t_r_a_ti_o_n_: ___ N_I_S_T_:_':_·~_~_:_a~_b_I:_,, vo''' "' : 2000p~i g 1040 CU. rt. CC,,' -z. 8 C_YI ~~~~ber ppm :~::2::IDE ___ :I;~~: 1 Uncertainty: 

€'(fo' /11 fi Balance NITROGEN 

NOx = 2.56 ppm NOx for Reference Only 

CeflifcOlioll In/ormation: Certification Date: 9/1 1/2012 Term: 24 Months Expiration Date: 9/11/2014 

This cylinder was certified according 10 the 1997 EPA Traceability Protocol, Document #EPA-$OO/R·97/121, using Procedure G1 

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

Last certified concentration was 2.52 ppm, \NOxJ=2.54 ppm on 2/13/2012. 

Allaly tical Data: 

1 • Component: NITRIC OXIDE 

Requesled Concentration: 

Certified Concentration: 

Instrument Useo: 

Analytical Method. 

Last Multipoint Calibration: 

FirSI Analysis Data: 

z, 0 R, ' .95 R, 9.95 Z, 0 

i 

z, 0 c, 2,59 

UOM: ppm 

(R:Reference Standard. Z=Zero Gas. C=Gas Candida/e) 

2.5 ppm 

:2 54 ppm 

Themo EIectrO(1 42C SIN 5181 12467 

Ch milumine~ ce 

811112012 

C; 2,59 Conc: :2 59 

R: 9.95 Conc' 259 

Mean Test Assay :2 59 ppm 

C: ~5~ ~ ~:~ec: ~~ --l 

----:::::::::::.=-==- ----

Analyzed by: 

, -.--

Reference Standard Type: 

Ref. STd. Cylinder # : 

Raf. Sid. Cone: 

Ref. SIC!. Tri5Ceeble to SRM,, : 

SRM Sample" : 

SRM Cylinder 1# • 

Second AnaIY$i$ Dala: 

z, 0 

R, 0 

Z, 0 

R, 

Z, 

C, 

0 

0 

0 

c, 

C, 

R, 

GMIS 

CC335604 

995 ppm 

26298 

SO-G-1 09 

FF31631 

o 

o 

o 

0,"" -.-. - 0 - -l Conc 

Conc: 0 : 

Conc: 0 J L. _ _ -'-_ _____ M_'_an Test Assay: __ . _ _ ~ _._ UOM; ppm 

Certified by: / 

Information conlained herein has been prepared at your requesl by qualified 8lq)erts within Praxair OJstribulioo, Inc. While we believe thatille information is accurate wiU'1ln the limits of the analytical 

methods employ&d and Is complell1 to tM extent of the speCific aNllyses performed, we make no wart'enly or r8presentatiO(1 as to the ',"itability of the use of Ihe Information for any purpose. The 

Information is offerfJd with the understanding lhatany use of Ihe information is etlhe sole discretion and risk of the user. In no event shall the liabi lity of Praxair Distribution. Inc .. arising out of the 

use of the information con teined herein exceed the fee esleblished for providing such infocmalion. 
Praxair 

5700 South Alameda Street 

Los Angeles, CA 9005 8 

OocNumber: 000045093 

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

PGVPlD: F22012 

Fill DalI: 1Of5l2012 Delta Air Quality 

1845 N. Case St. 

Orange, CA 92865 

Praxalr Order Number: 21683572 

Customer P. 0. Number: 04102891 

Customer Reference Number: 

PanNllmlHr: NI N04.5ME-AS 

1.01 Numbtr: 109227908 

Cyllrnhr Stylt &- Oll/Itl: AS CGA 660 

/Joy. t./.,." Expiration Dale: 

Certified Concentration: 

11/5/2014 

Cylinder Number: CC101204 

C(:./OI.2..D 4.52 ppm NITRIC OXIDE 

NIST Traceable 

Analytical Uncertainty: 

±2 % 

Balance NITROGEN 

~yp ',/DS /''f---No- x =-4.-S2-pp-m ------N-::-Ox-:-for-Ref-eren-Ce---'OnIY 

Certi/cation Information: Cerlification Date: 11/5/2012 Term: 24 Months ExpIration Date: 11/5/2014 

2000 pslg 

This cylinder was certified according to the 1997 EPA Traceability Protocol, Document #EPA·600/R·971121 , using Procedure G1 

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

Analytical Data: (R=Reference Standard, Z"ZfJfO Gas. C=GBS Candidate) 

1 . Component: NITRIC OXIDE Reference Sten1:lerd Type: GMIS 

Ref Std. Cylinder Ii : CC335699 R,,'. ;ltd. Cone: 9.87 ppm 

Req..ested Concentrtltion: 4.5 ppm 

Certified Concentration: 4.52 ppm 

tl'\slrumttnl UStttl: Themo Electron 42C SIN 518112467 Ref. Sid. Traceable to SRM II ; 26290 

SRM Sample '# : 5O-G-,09 

SRM Cylinder Ii ' FF31631 

Analytical Method: Chemiluminescence 

Last MuUiplint Calibration: __ ~fU_'~1I~20~ 2,-_______ , 

Firsl An,lysi. Data : Dale: 1011812012 Second Analysis Dale; Dale; 1012512012 

Z, 0 R, 9.87 C, 4.52 Cone: 4.52 Z, 0 R, 9.87 C, 4.54 Cone: 4.54 

R, 9.87 Z, 0 C, 4.51 Cone: 4.51 R, 9.87 Z, 0 C, 4.53 Cone: 4.53 

z, 0 C, 4.51 R, 9.87 Cone: 4.51 Z, 0 C, 4.53 R, 9.81 Cone ; 4.53 

I UOM' ppm Me,n Tesl As5ly: 4.51 ppm UOM: ppm Mean Tnt Assay: 4.53 ppm 

Certified by: 

140eu. ft. 

Information contained herein has been prepared al your r&quelll by Qualified experts WIthln Praxair Distribulion, Inc. While we believe that the i'lformalton is accurate within the limits of the analytical 

methods employed and is complete 10 lhe extent of Ihe specific analyses perlormed, we make no warranty Of replesenialion 8S 10 Ule suitability of the use of tha information for any purpose. The 

information is offered with Ihe understanding thaI any use of the Information 15 a\ the sole discretion and risk of Ihe user. In no even! 'hall the IlsbHliy of Praxeir Distribution, Inc" arising out of u.. 

"" 0' ,he In'"m"~n ~n ",ned h"'" "oe" '''' ,,, ,,'eb","" "" "",!dIn, '"'" In'""""..,. 2 _ 'if _ I ~:('. 
/f!fl~PRAXAIR Praxair 

5700 South Alameda Street 

Los Angeles. CA 90058 

OocNumber: 000042196 

Tel; (323) 585-2154 Fax;(714) 542-6689 

PGVPID; F22012 

Delta Air Quality Praxalr Order Number: Fill Dolt: 712612012 

1845 N. Case St. 

Orange, CA 92865 -

Customer P. 0. Number: 

Customer Reference Number: 

20846451 

03972778 ParI H"mbtr; 

LoI f{"/Ilber: 

EV NINX4ME·AS 

109220806 

('yll"drr Slyl, II: O"II~/: AS CGA660 N () ~ ~ .? I Expirallon Dale 212r~:::;ed COllcen/ration: NIST

C

: :::::': " & v,/" .. 

e,. ~ 3 L 161, CY.lin_d_e_r _N3_u._mr_1b_e_" _p_p_m _ _ C_C_3_36_1_6._9 ___ ----- ____ !'~~ Iyt ca l ~ncertajnty: 

"- 7 0 NITROGEN DIOXIDE (as NOx) ± 2 % 

Balance NITROGEN 

2000 pslg 

E'ff()VZ11"L~ ____ _ 

Cerfifctltiolt Informat/on: Certification Dale: 8/27/2012 Tenn: 6 Months Expirotion Date: 2/27/2013 

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 

[NO)=O.06 ppm; for reference only. 

Analytical Data: (R=Reference Standard, Z=Zero Gas, C=GIIS Cllndlaale) 

1 . Component: NITROGEN DIOXIOE (as NOx) 

Requested Concentration: <I ppm 

Certified Conronlralion: 3.71 ppm 

Instrument Used: Thermo Electron 421 SIN 072602432C 

Analytical Method: Chemiluminescence 

Last MulUpoir.l Calibration: 811612012 

Reference Standard Type: 

Ref. Sid. Cylinder;; : 

Rei. Sid. Cone: 

ReI. Std. Traceable to SRM ti : 

SRM Sample II : 

SRM Cylinder II : 

GMIS 

CC335804 

9.95 ppm 

26298 

5O-G-l09 

FF3t631 

140 cu. ft 

r;~~An.'Y' ~Data: ~-- ~1 12012 1 

I Z: 0 R: 1032 C: 3.85 Conc: 371 

! R: 10.35 Z; 0 C; 3,63 Conc: 37 

i Z: 0 C: 3.83 R: 10.35 Cone; 37 

~o ~_ ~ ~ .. ____ ._Meso Test Asuy: _ ":1 ppm __ . 

Second An,ly:si, Dala: Date: 

M~~" 1 Z: 0 R: 10.35 C: 3.97 Cone : 

R: 1024 z : 0 C: 392 Cone : 

Z: 0 C: 3.93 R: 1022 Cone : , 

~~: __ ~pm .. ~ ____ . __ ~a .. n Test Anay: 82PP~ 

Analyzed by: ~ 

Ja~ 

Certified by: ~, 

Q'd~_ 

InforrJiarion contained herein has been prepared et your requesl by quellfied eKP8(ta wilhin PrsKair Oi&lrlbulion, Inc. While we believe thaI (he Information il aCC\I{ate within the limils of the analytical 

methods omployed and is complete to the extenl of the specific analyses performed, we make no waiTanty or representation 8S to the suilobH~y of the use of the information for ony purpose. The 

Information is offared with the understanding thai any use of the information il at the sole discretion 11M risk of the user In no evant shalt the liability 01 PrBJlsir Oistrioution, IrlC" jB'fiS illQ 0 r the 

use of the information con talned herain exceed the fee estebhehed for providing luen Informolion. ) / (-1 1 ~f:; ~ v 
Praxair 

5700 South Alameda Street 

Los Angeles, CA 90058 

DocNumber: 000041947 

Tel: (J2J) 585-2154 Fax:(114) 542-6689 

PGYPID: F22012 

CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS , ..... '." , -.. . 

Custo 

Delta Air Quality Fill Dol,: 7127/2012 

1845 N. Case SI. 

Orange, CA 92865 

Praxair Order Number: 21015531 

Customer P. 0. Number: 03998407 

Customer Reference Number: 

Pari N"mMr: 

1.f>I Number: 

NI C04.7ME·AS 

109220904 

Cy/ill,kr Slylr ,(. Q,IIlrI: AS CGA350 

Cylinder Pr.,f.wrr tf Vvl"m~ : 

co I. J. I J ~ Certified Concentration: 

T 'T 7 Expiration Date: 2120/2013 NIST Traceable 

II ~~ Cylinder Number: CC325462 Analytical Uncertainty: CC 3 ~ 5 ~· ·--4. "' -- OXtDE-- ----- -- --

2000 psig 

Balance NITROGEN 

Certijcation Information: Certification Date: 8/2012012 Term: 6 Months Expiration Date: 2/20/2013 

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

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

A nalytico/ Data: (R=Reference Standard, Z=Zero Gas, C=Gas candidate) 

1 . Component; CARBON MONOXIDE 

Requested Concentration: 4.7 ppm 

Certified Concentration: 4.49 ppm 

Insllument Used: Horiba VIA·510 SIN 576876015 

Analylical Method: NOIR 

L85t Multipoint Calibration: 

z, 0 R, 84.3 

R, 84.1 Z, 0 

811112012 

c, 36.8 

Date: 

Cone: 

817(2012 

4.45 

c: 37 Cone; 4.49 l 

Z, 0 C, 36.9 

UOM; ppm 

R: 84 Cone: 4.48 ~ 

Mean Test ASliily: 4.47 ppm 

--_. ---------

AnalYZedb~p 

<g Iwlzo 

Reference Standard Type' 

Ref. Std. Cylinder '# : 

Ref. Std. Cone: 

Ref. Std. Traceable to SRM' : 

SRM Sample' : 

SRM Cylinder 11. : ,. __ ._ .. 

i Second Analysis Data : 

I Z, o 84.3 c, 

Certified by: 

GMIS 

SA6687 

10.2 ppm 

1677e 

5-1-42 

XF 0021438 

Date; 

37.3 Cone; 

8/1512012 

4,51 

E p~ Tr-IA tltfJ,; li-ly Pf".f"U1/ .p.r Assuy Gi~ Ctl'h'/{{,,~W! 

5fA,J,I',{~_ RtVI$/o., l1y lull of- ~(oI.f~ Cu libl4-/i"", 

'0'\ /0.12 • 

140 cu, n. 

Information contained herein has been prepared at your request by qualified exper1s within Praxair Distribution, Inc. Vvhile we believe that It1e information is aCClJrate within the lim its of the analytical 

methods employed and is complete to the exlent of the specific analyses performed, we make no wurranty or representation as to the suitabiity of the use of tile information for any purpose. The 

information is offered with the understanding that any use of the information is at the sole discretion and risk of the user. In no event shaillhe ab~ity of PraxaiI Distribution, Inc., arising ou! of the 

". of 'h. ,",0""";00 ron ,.n.d h.",;n "",.d the f.e .".blohed fo' pfO,~;ng ,,,," " fom"'. n 1., _ 1 ( _ / 2-~ 

1 
I 

CIlSlOl 

i!ffiI!lPRAXAIR 

DocNumber: 000038542 

Praxair 

5700 South Alameda Street 

Los Angeles, CA 90058 

Telephone: (323) 585·2154 

Facsimile; (714) 542-6689 

CERTIFICATE OF ANALYSIS / EPA PROTOCOL GAS 

Delta Air Quality 

1845 N. Case St. 

Orange, CA 92865 

Praxair Order l\'umber: 20155225 

Customer P. 0. Number: 03870012 

(·uslorner Reference Number: 

Fill /)ole: 

J.ul N"m~"r: 

Cylill<kr Siyl~ & Ollrl~l : 

5/112012 

NI C09.5ME-AS 

109212204 

AS CGA3SO 

CO q 5 ~ CJ'Ii"derf'rnsllrc<fr'ol",,,~ Certified Concentration: 

• r-E-xp-ir-a-tio-n--D-at-e--------6-1-2-1/-20-1~5~------------------N-IS-T-T-r-a-ce-a-b-Ie-----. 

2000 psig 140 cu. fl. 

a::. '" 1'3 ott! Cylinder N~~6b=, ~~~ _ -- ~;~~~:2MONOXIDE _____ ____ A~~~;a l Uncertainty 

Balance NITROGEN 

£~,~~~~;------------~ Certifcation Information: Certification Dale: 5/21/2012 Term: 36 Months Expiration Oate: 5/21/2015 

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 I.D.# F22012 

Allalytical Data: (R"'Ref~rence Slenderd, Z"'Zero Gss, C"'GBS Ci;Jndidate) 

1 . Componenl: CARBON MONOXIDE 

Reque5ted Concentration: 

Car1i1ied Concentrahon: 

tnstrument Used 

Analytical Method' 

Last MuNipoint Calibration: 

first Analysis Data: 

z, 0 R, 168.6 

R, 168.7 Z, 0 

z, 0 C, 158.4 

UOM: ppm 

Analyzed by: 

9.5O ppm 

9.56 ppm 

Horiba VIA-510 SIN 576876015 

NOIR 

5/1112012 

Date: 

C, 158.4 Cone: 

C, 158.6 Cone: 

R, 168.8 Cone: 

Mean Test Anay: 

5/1112012 

9.58 

9.59 

9.57 

9.58 ppm 

Shameela Jiffrey 

I 

, 

I 

I 

J 

RelArence Standard TYPA: 

Ref Std. Cylinder" : 

Ref. Sid. Cone: 

Ref SId. Traceabla to SRM tI 

SRM Sample #: 

SRM Cylinder # : 

r - - -- I Second Analysis Data: , 

I Z, 0 R, 16' c, 

I "' 1685 Z, 0 c· Z, 0 C, 157.6 R, 

UOM: ppm 

Certified by: 

GMIS 

SA6687 

10.2 ppm 

1677c 

5-1-42 

XF 0021438 

Dilte: 

158.2 Cone: 

157.5 Cone: 

158.6 Cone: 

5/2112012 

9.55 

9.53 

9.54 

Information contained herein has been prepared at your requesl by qualified experts within Praxair Distribution, Inc. V..tIile we oalieve thallhe information is accurate within the limits of Ihe analytical 

methods employed and is complete to the extent of the specific analyses perform6d, we make no warranty or representation as to the suitability of the use of the informetion for any purpose. The 

information is offered with the understanding that any use of the information is at the sole discretion ami risk of the user. In no evenl shall the liability of Pra~air Distribut7 ' n, Inc. arisi out 01 the 

use of the information con lalned herein exceed the fee established for providlng:ruch information. G -(z -/1;;' 

I 
EPA Traceability Protocol for Gaseous Calibration Standards: 

What Changed? 

Background 

In June 2012, EPA published a revised version of the traceability protocol for gaseous 

calibration standards, which had not been updated since 1997. The protocol was revised in 

response to a 2009 evaluation report by the EPA Office of the Inspector General, which 

recommended that the EPA Office of Research and Development update and maintain the 

protocol gas procedures to ensure that the protocol meets the objectives of the Acid Rain, 

ambient air, and stationary source air programs. The revised protocol can be found at 

http://www.epa.gov/nrmrllappcd/mmd/db-traceability-protocol.html.ltis a significant 

improvement over earlier versions of the protocol and has received consensus support by 

EPA, NIST, specialty gas producers, and other interested parties. There are several revisions 

that may be of direct interest to Source Evaluation Society (SES) members, as is discussed 

below: 

1. New Gas Mixtures and Concentration Ranges for EPA Protocol Gases 

As a result of new or anticipated EPA regulations, the list of available EPA Protocol Gases 

has been expanded and can be seen in the table at the end of this article. The gas mix1ures 

and concentration ranges that specialty gas producers can prepare, assay, and certify as EPA 

Protocol Gases is limited to those available from the National Institute of Standards and 

Technology (NIST) as NIST-certified gaseous reference standards (e.g., Standard Reference 

Materials). NIST has or will expand the gas mix1ures and concentration ranges that it will 

certify. 

2. Extended Certification Periods for New and Existing EPA Protocol Gases 

Certification periods were ex1ended because NIST and specialty gas producers have gathered 

more information about the long-term stability of gas mix1ures than was available when the 

1997 version of the protocol was prepared. Based on this information, the certification periods 

for NIST -certified reference standards have been ex1ended. If the assumption is made that 

the cylinder passivation techniques used by specialty gas producers for EPA Protocol Gases 

are the same as they have used for preparing NIST standards, then the stability for EPA 

Protocol Gases should be similar to that for NIST standards. The certification periods for new 

EPA Protocol Gases have been changed to match those for NIST standards. Because the 

stability data are for NIST standards that were produced in the past, they should be 

representative of existing EPA Protocol Gases. Consequently, the ex1ended certification 

periods are applicable to existing EPA Protocol Gases. 

For example, an EPA Protocol Gas containing 50 ppm propane in air was originally certified 

on January 1, 2009 under the 1997 revision of the protocol. Its certification ended three years 

later on January 2, 2012. Because the new certification period for this gas mix1ure is eight 

years as a result of the 2012 revision, the new certification expiration date would be January 

2, 2017. The EPA Protocol Gas would not have to be recertified by its producer to receive the 

longer certification period, but would have to be recertified after January 2,2017. 

Producers can use their discretion regarding notifying end users about the ex1ended 

certification periods and the manner they use to make the notification. For those end users 

who are required by EPA regulations to use EPA Protocol Gases as calibration gases, some 

form of written documentation should be provided for the end users' records. For example, 

the producer could send a blanket letter or E-mail message to its end users and could offer to 

send a new certificate to those users who need written documentation and/or are required to 
report about the expiration date of their calibration gases to EPA's Emissions Collection and 

Monitoring Plan System (ECMPS). 

ECMPS was designed to flag data obtained using expired EPA Protocol Gases. This feature 

of the system has been temporarily disabled while ECMPS is being updated with the extended 

certification periods. The old expiration dates may be reported to ECMPS in the meantime. 

The extended certification periods do not protect against concentration shifts due to back 

diffusion of air from an improperly purged regulator or gas manifold into an open cylinder. End 

users still have to be cautious to prevent such concentration shifts over time by properly 

purging regulators and gas manifolds before use and by closing hand valves after use. Given 

the longer certification periods, they must be more cautious than previously. 

3. Lower Cylinder Pressure Limits 

The minimum cylinder pressure for which EPA Protocol Gases may be used has been 

lowered from 150 psig to 100 psig. Formerly, an EPA Protocol Gas could be recertified if the 

cylinder pressure was greater than 500 psig before the recertification assay. Now, it can be 

recertified if the cylinder pressure is greater than 100 psig after the recertification assay. 

4. Zero Air Materials 

The protocol includes a new procedure for the assay and certification of compressed gas zero 

air materials as conforming to 40 CFR Part 72.2 . At this time, EPA does not require the 

regulated community to use NIST-traceable zero air materials for the calibration of ambient air 

or continuous emission monitors that are required by 40 CFR Parts 50, 58, 60, and 75. 

However, end users may elect to purchase these standards from specialty gas producers who 

elect to assay and certify them. 

5. Dynamic Gas Dilution Systems 

The protocol includes a new procedure for the assay and certification of dynamic gas dilution 

systems. At this time, EPA does not require the regulated community to use NIST-traceable 

dynamic gas dilution systems certified under this protocol for the calibration of all ambient air 

quality or continuous emission monitors that are required by 40 CFR Parts 50, 58, and 60. 

End users may elect to use NIST-traceable dynamic gas dilution systems certified under this 

protocol for calibrations under these CFR parts. EPA does require NIST-traceable 

calibrations of dynamic gas dilution systems that may be used under Appendices A and C of 

Part 50 to calibrate ambient air quality monitors for S02 and CO. 40 CFR Part 75 only allows 

use of compressed gas calibration standards when calibrating CEMSs that are being used for 

purposes of Part 75 and when calibrating Test Methods 3A, 6C, and 7E when these methods 

are used for Part 75 testing. 

6. Implementation Period 

The producers of EPA Protocol Gases are allowed until June 2013 to implement the changes 

that have been made to this protocol. Afterwards, producers must follow the procedures given 

in this revision of the protocol if they wish to sell calibration gases as "EPA Protocol Gases". 

7. Protocol Gas Verification Program 

The producers of EPA Protocol Gases must also participate in the Protocol Gas Verification 

Program (PGVP). EPA air pollution monitoring regulations specify that the regulated 

community must use EPA Protocol Gases from PGVP participants. One component of the 

PGVP concerns calibration gases for ambient air quality monitoring and another component 

concerns calibration gases for continuous emission monitoring systems (CEMS). The PGVP 
is the primary accuracy assessment for EPA Protocol Gases. It provides information about 

the accuracy of the certified concentrations of EPA Protocol Gases that were purchased from 

specific specialty gas producers. As such, the PGVP results assist end users' purchasing 

decisions. See www.epa.gov/airmarkets/emissions/pgvp-detail.htmlfor details about the 

ambient air PGVP and www.epa.gov/ttnamti1/aapgvp.htmlfor details about the emission 

PGVP. 

Summary 

The protocol has been revised to allow specialty gas producers to meet the needs of 

calibration gas users for new gas mixtures and new concentrations. It presents a new method 

for generating NIST-traceable calibration gases. Calibration gas users will have greater 

confidence in EPA Protocol Gases as a result of the revision. 

Questions about the protocol can be directed to: 

Robert S. Wright 

Air Pollution Prevention and Control Division 

U.S. Environmental Protection Agency 

Phone: 919-541-4502 

E-mail: wright.bob@epa.gov 
Gas Mixtures, Concentration Ranges, and Maximum Certification Periods for 

EPA Protocol Gases under the 2012 EPA Traceability Protocol 

Components Balance gas Concentration range Period (years)· 

Ammonia Nitrogen 5 to 50 ppm 1 

Carbon dioxide Air" 360 to 420 ppm 8 

Carbon dioxide Nitrogen 5 ppm to 20% 8 

Carbon monoxide Air 40 to 500 ppb TBD 

Carbon monoxide Air 500 ppb to 10% 8 

Carbon monoxide Nitrogen 1 ppm to 15% 8 

Formaldehyde Nitrogen 0.5 to 10 ppm 1 

Hydrogen chloridec Nitrogen 10 to 5000 ppm 2 

Hydrogen sulfide Nitrogen 1 to 1000 ppm 3 

Methane Air 1 to 1000 ppm 8 

Methane Nitrogen 500 ppb to 10% 8 

Methanol or ethanol Nitrogen or Air 75 to 500 ppm 4 

Natural gas 

components' Natural gas Contact NIST 4 

Nitric oxide 02-free nitrogen" 0.5 to 50 ppm 3 

Nitric oxide 02-free nitrogen" 50 ppm to 1% 8 

Nitrous oxide Air 300 ppb to 5% 8 

Oxides of nitrogen' Air 3 ppm to 1% 3 

Oxygen Nitrogen 10 ppm to 25% 8 

Propane Air 0.1 to 500 ppm 8 

Propane Nitrogen 5 ppb to 2% 8 

Sulfur dioxide Nitrogen 1 to 50 ppm 4 

Sulfur dioxide Nitrogen 50 ppm to 1%- 8 

Volatile organics Nitrogen 1 ppb to 1 ppm 4 

Zero air materialg Air Not applicable Unlimited 

Multicomponent See protocol 

mixtures 

Mixtures with lower See protocol 

concentrations 

a Specialty gas producers may elect to certify candidate standards for less than the maximum 

certification period. Each producer has discretion in this matter. See protocol. 

b "Air" is defined as a mixture of oxygen and nitrogen where the minimum concentration of 

oxygen is 10 percent and the concentration of nitrogen is greater than 60 percent. 

C Hydrogen chloride may be contained in passivated aluminum or nickel-coated steel 

cylinders. 

, Natural gas components are methane, ethane, propane, n-butane, iso-butane, n-pentane, 

iso-pentane, helium, nitrogen, and carbon dioxide. 

" 02-free nitrogen contains ~ 100 ppb of oxygen. 

, NIST defines its total NOx standards as containing nitrogen dioxide plus contaminant nitric 

acid. 

g Concentrations of S02, NOx. and THC are not >0.1 ppm; concentration of CO is not >1 ppm; 

and concentration of CO2 is not >400 ppm as per 40 CFR Part 72.2. Zero air material may be 

contained in steel cylinders. 
Orifice Method - Triplicate RunsfFour Cahbrahon POints 

English Meter Bo~ Units, EnglISh K' Fattor 

SEMI_ANNUAL DRY GAS METER/ORIFICE CALIBRATION 

Modet # 

10#: 

Filename l\RecepbOnldeltil pubtu:\CiI!lbrallonslMetersI12·wcsI2012\(SeIl'll_Annuat MeIer CatlbfallOnl2 WC$ 10-23-12 xtsIWCS Date 

12~ 

1012312012 

File Modified From APEX 522 Senes Meter box Callbfation 

Revised 4/812005 

Volume Volume 

dH Time Initial Final 

in H2O (min (eu It) (eu It) 

011 2600 44 ,960 50,384 

011 2600 50,384 55,812 

011 26.00 55.812 61 ,279 

059 1200 61 .279 66 871 

059 1200 66,871 72.445 

0,59 12,00 72 445 78.039 

DRY GAS METER 

VOLUME VOLUME VOLUME 

CORRECTED CORRECTED CORRECTED 

Vm(std) Vrn{std) Ver{std) 

leu tt)' (liters) (eu tt) 

5.401 1530 5.236 

5.385 1525 5.236 

5.403 153,0 5.236 

5518 156 3 5,392 

5 495 1556 5392 

551 4 156 2 5392 

5 465 "" 5 "5 

"as 1554 5 "5 

5.474 155 a 5.345 

5.356 151 7 5318 

5312 150 , 5318 

5.341 1512 5318 

SIGNED Signature on File 

Bar Pressure 

Perlormed By 

2977 (m Hg) 

G Bndge 

099 

DRY GAS METER READINGS CRITICAL ORIFICE READINGS 

Volume Initial Temps Fmal Temps Onfice K' Onfice Actual 

Total Inlet Oullet Inlet Ou~el Senatit CoeffiCient Vacuum IMlal 

(cu tt (de F d. F (de F) (d F, (number) see aoove (in H (de F) 

5424 67,0 66.0 69.0 68,0 33 0 1553 235 67.0 

5426 '90 '80 71 .0 70,0 33 0.1553 235 67.0 

5.467 710 700 73.0 ; 20 33 0.1553 23,5 67.0 

5.592 730 720 7<0 73.0 " 03465 "0 '70 5574 74.0 73.0 74.0 730 " 03465 21 .0 67.0 

559' 7<0 730 7<0 730 '. 0,3465 21,0 67.0 

ORIFICE DRY GAS METER ORIFICE 

CALIBRATION FACTOR CALIBRATION FACTOR IndIvidual Individual 

VOlUME VOLUME R" Onfice 

CORRECTED NOMINAL Y dH@ 

Vcr(std) va Value Value 095 < Y Ymax - Ymin 

liters) (eu tt) (number) {in H20) < lOS? < 0,010? 

1483 5.255 0969 1.521 Pass 

148,3 5 255 0.972 1.515 Pass 

148.3 5.255 0,969 1,509 Pass 

Average 0.970 1.515 Pass 

1527 5 411 0.977 1.622 Pass 

1527 5411 0981 1620 Pass 

152.7 5411 0978 1.620 Pass 

AverOlige 0.979 1.621 POIISS 

lSI 4 5'" 0.976 1.605 Pass 

1514 5364 0974 1 803 Pass 

151 4 5'" 0976 1803 Pass 

AvetOlige 0.976 1.804 Pass 

150' 5337 0993 1.712 Pass 

1506 5337 1001 1.712 Pass 

150' 5331 0.996 1710 Pass 

Averaqe 0.997 1.111 Pass 

Average Yd : 0.980' dH@: 1.663 

Q@dH:l: 0.582 

Date: 1012312012 

Ambient Temperature 

Final Average 

(de F) (d F 

67.0 670 

67.0 '70 67.0 67.0 

67.0 '70 67.0 670 

67.0 '70 

Orifice OrifICe 

Average Average 

0.96 < YfYd dH@ - dH@av 

< 1.02? < 0, ISS? 

Pass Pass 

POIISS POIISS 

Pass Pass 

Pass Pass 

s.. ..... Annual Meter Calibral"",' 2.....,1 10·23-' 2 xis WCS 

l/1612013 

2'17 PM 
Onfice Method - Triplicale Runs/Four Calibration POints 

English Meter Box Units, English K' Factor 

SEMI-ANNUAL DRY GAS METERIORIFICE CALIBRATION 

Model #. 

10#: 

Filename \\Recepllonldella pubilc\CalibrationslMeters\I-P&M\2012~Seml Ann ual Meter Calibration l ·pm 10-26-12 xlsjWCS Dale' 

1 pam 

10/26/2012 

File Modified From: APEX 522 Senes Meter box Calibration 

ReVised 4/8/2005 

Volume Volume 

dH Time 1000Iai Final 

in H2O (mill) co, (cu ft) 

0.13 26,00 633.300 638.575 

0,13 26,00 638.575 643.880 

0.13 26 00 643.880 649.138 

067 12.00 64g,l38 654.468 

067 "00 654.468 659.800 

067 "00 659800 665140 

200 7.00 665.140 670.440 

200 7.00 670.440 675.775 

200 7.00 675.775 681 .132 

390 500 681.132 686.340 

3.90 5.00 686,340 691 .560 

3.90 5.00 691 ,560 696.807 

VOLUME VOLUME VOLUME 

CORRECTED CORRECTED CORRECTED 

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

5267 149.2 5.255 

5.22 1 147.8 5.253 

5.291 1498 5.407 

5299 150.1 5.407 

5277 1494 5.359 

5306 "OJ 5.357 

5,323 "06 5,354 

5.199 147.2 5.327 

5.211 147 6 5.327 

5.238 148.3 5.325 

SIGNED Signature on File 

Bar. Pressure' 

Performed By' 

Meter Serial # 

2985 (Ill Hg) 

gary bridge 

134641600 

DRY GAS METER READINGS CRITICAL ORIFICE READINGS 

V.""" Initial Temps Final Temps Ooliee K' Orifice Actual 

Total Inlet Outlet Inlet Outlet Senal# Coefficient Vacuum 1000Iai 

'"' {d F, " F d F, (de F numDer see above (In H ) F 5275 710 70,0 710 70.0 J3 0.1553 27.0 66.0 

5.305 710 70,0 71 .0 70.0 J3 0.1553 27.0 660 

5.258 710 700 710 70.0 J3 0.1553 27.0 66.0 

5330 71.0 700 72.0 '" " 0 3465 225 67.0 

5 332 72.0 710 720 710 " 0.3465 22.5 670 

5"0 72.0 710 720 710 " 0_ 225 670 

5.300 72.0 710 720 71.0 63 0_ 19.0 670 

5335 72.0 710 730 720 63 05888 19.0 670 

5357 73.0 720 730 72.0 63 0.5888 19.0 68.0 

5208 730 720 730 72.0 73 0.8202 16.5 68.0 

5,220 73.0 720 73.0 72.0 73 0.8202 '6 5 68.0 

5247 73.0 720 73.0 72.0 73 0.8202 16,5 68.0 

CALIBRATION FACTOR CALIBRATION FACTOR IndMdual Inchvldual 

VOLUME VOLUME Roo ""fire 

CORRECTED NOMINAL Y dH@ 

Vcr(std) Vcr Value Value 0.95 < Y Ymu-Ymin 

H20l 0< 1.05? 0< 0.010? 

779 Pass 

146,8 5.250 0.996 1779 Pass 

148,8 5.252 ' .006 1.781 Pass 

Average 1.002 1,779 Pass 

A"":' 1.843 Pass 

1531 5.411 1642 Pass 

1531 5411 1.842 Pass 

1.842 Pass 

1518 536< 1016 "" P 

151.7 5.366 , 009 '.904 Pus 

1516 5.389 , 006 , 904 Pass 

Average 1.010 1.904 Pass 

150,9 5.342 1.913 P 

1509 5.342 1913 Pass 

1SO.8 5.345 1017 1.915 Pass 

r---AVe'rage Yd: 1.014 ' dH@: 1,860 

I a@dH:l: 0,550 

Date 10126/2012 

Ambient Temperature 

Fillal Average 

{d F (de F) 

66.0 660 

66.0 660 

67,0 665 

670 670 

67.0 670 

67.0 670 

67.0 670 

68.0 675 

68.0 680 

68.0 680 

68,0 68,0 

69,0 68,5 

0,,,,, Oofice 

Avefage Average 

0.98 '" YNd dH@ - dH@ av 

'" 1.02? <0.IS5? 

Pass Pass 

Pass Pass 

Pass Pass 

Se""'Annu.1 Me! .... C.lib4"flion 1.pm 10·26--12 xis WCS 

311612013 

2~ PM 
_----e A ~j[J , 

Side View 

Acceptability 

Criteria z < 1/S" w < 1/32" 

Side View, Side View, 

Impact Impact 

Pilot 10 Date Calibrated By openings open ings 

Properly Properly 

aligned, Z < aligned, w 

11S" < 1132" 

026 y Y 

S Type Pitot Tube Dimensional Calibration Record 

1 

<\ 

i 

"3/16" < Ot < 

Ye, 3/S" 

Pa::Pb Tubing 

Diameter, dt 

Y 0.374 

~ M, -1 ~ 

~ End M, 

View 

~ 

n/. nf. n/. 

M1 M2 M3 

0.882 0.870 0.882 

n/. n/. 

M' M' 

0.876 0.437 

Reference "A Type-S Pitot Tube Calibration Study, Robert F. Vol1aro, October 15, 1975 

If tube is not visibly deformed it is assumed that Pa " Pb '" .5 x avg. of M1 M2, and that average face opening plane angles represent individual angles to tube axis 

.... 

n/. 

M6 

0.457 

----I Ms r-

;' §;C f 

-r- M: M, p, 

i ! 

-I I--

Too Viflw 

1,05 Ot< P < 1.5 

10 degrees 5 degrees Dt 

Average Face Average Face Opening Plane 

Angle, offset Opening Plane 

from Frontal Angle Ratio of PlOt Status 

perpendicular from parallel to 

to transverse Longitudinal 

axis Axis 

0.9 0.4 1.2 Pass 
Standard Pitot Tube Dimensional Calibration Record 

A 

J 

- @ 

" A 

'" , &"' 

Section AA 

• 

"' 

T 

Tip 

cce~ ,a~I IIIY 

Criteria V" V" 0" 0" 0" 0" ·0.101 M1 >6 01 M2 >8 01 

Hemispherical , 90· Bend with 

Pitot 10 Date Calibrated B Elliptical, or curved or mitered 0' 02 ., .2 Ratio 02/01 '0' 80' Status 

Conical Tip 'unction 

7 y Y 0.125 0.015 1,100 1.700 0.120 0.750 1.0 Pass 

8 y Y 0.31 0.029 2.110 2.550 0.094 1.860 2.5 Pass 

33 y Y 0,258 0.029 1.550 2.120 0.112 1.548 2.1 Pass 

79 y Y 0.25 0.029 1.500 2.200 0.116 1.500 2.0 Pass 

80 y Y 0.25 0.029 1.530 2.200 0.116 1.500 2.0 Pass 

81 y Y #DIV/O' 0.000 0.0 

84 at Doug's Y Y #DIV/Dt 0.000 0.0 

85 Y Y 0.25 0.03 1.600 2.220 0.120 1.500 2.0 Pass 

88 at DOUQ's Y Y #OIV/O! 0.000 0.0 

103 Y Y #OIV/O! 0.000 0.0 

107 #OIV/OI 0.000 0.0 

108 Y Y 0.254 0.029 1.550 2.200 0.114 1,524 2.0 Pass 

Notes: Reference · Standard Pitot Tube Calibratlons, South Coast Air Quality Management District Source Test Manual, Chapter III, March, 1989 
TEMPERATURE SYSTEM CALIBRATION 

#8 

T2 F95-195 T3 F95-195 

I D. 

I 

OIL PTC-23 360 360 360 360 360 360 360 360 0 

WATER PTC-23 214 214 214 214 212 212 212 2" 

OIL PTC-24 36' 36' 36' 36. 360 360 360 360 

WATER PTC-24 2" 2" '" '" 2" 2" 212 212 

Calibrated By: DMW, RM, RMO, DA, ME JanuOiry 2, 2013 
Reference Thermometer 1.0. 

TIC Readout 

1.0 10 

.. Reading 1 

OIL PTC-2S 362 

WATER PTC-2S 213 

ICE PTC-2S " OIL PTC-26 362 

WATE R PTC-26 211 

ICE PTC-26 32 

OIL PTC-27 362 

WATER PTC-27 213 

ICE PTC-27 30 

OIL PTC-28 36' 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-30 32 

OIL TRO-1 360 

WATER TRO-l 213 

ICE TRO-1 " OIL TRO--4 359 

WATER TRO-4 213 

ICE TRO-4 " OIL TRO-S 36' WATER TRO-S 213 

ICE TRO-S 33 

OIL TRO-6 360 

WATER TRO-6 21' IC E TRO-6 30 

OIL TRO-S 361 

WATER TRO-S 213 

ICE TRO-s 33 

OIL TRO-9 359 

WATER TRO·9 21' ICE TRO-9 32 

OIL TRO-ll 359 

WATER TRO-l1 213 

ICE TRO-l1 33 

OIL TRO·12 360 

WATER TRO-12 212 

ICE TRO-12 32 

OIL TRO-13 360 

WATER TRO-13 214 

ICE TRO-13 " OIL TRO-iS 360 

WATER TRO-IS 213 

ICE TRO-tS 30 

OIL TRO-16 36' WATER TRO-16 213 

ICE TRO-16 " OIL TRO-IS 36' WATER TRO-1S 213 

ICE TRO-1S 34 

OIL TRO-19 360 

WATER TRO·19 212 

ICE TRO-19 33 

OIL TRO-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 

ICE TRO-24 '" 32 

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

n 

TEMPERATURE SYSTEM CALIBRATION 

STANDARD 

#8 F9S·19S T2 F9S·19S T3 F9S-19S 

TIC - Readout Reference Thermometer 

of of 

Reading 2 Reading 3 Average Readil'l9 1 Reading 2 Reading 3 Average 

362 362 362 36D 36D 360 36D 

213 213 213 212 212 212 212 

" " " 32 32 32 32 

362 362 362 360 360 360 360 

21' 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 30 30 32 32 32 32 

36' 36' 36' 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 

213 213 213 212 212 212 212 

32 32 32 32 32 32 32 

360 360 360 360 360 360 360 

212 212 212 212 212 212 212 

32 32 32 32 32 32 32 

360 360 360 360 360 360 360 

213 213 213 212 212 212 212 

" " " 32 32 32 32 

359 359 359 360 360 360 360 

213 213 213 212 212 212 212 

" " " 32 32 32 32 

36 ' 361 36' 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 

21' '" 21' 212 212 212 212 

30 30 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 

359 359 359 360 360 360 360 

21' 21' 21' 212 212 212 212 

32 32 32 32 32 32 32 

35' 359 35' 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 

212 212 212 212 212 212 212 

32 32 32 32 32 32 32 

360 360 360 360 360 360 360 

214 214 214 212 212 212 212 

" " " 32 32 32 32 

360 36D 360 360 360 360 360 

213 213 213 212 212 212 212 

30 30 30 32 32 32 32 

36' 36' 36' 36D 360 36D 36D 

213 213 213 212 212 212 212 

" " " 32 32 32 32 

361 36' 36' 360 360 36D 360 

213 213 213 212 212 212 212 

34 34 34 32 32 32 32 

360 360 360 360 360 360 360 

212 212 212 212 212 212 212 

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 36D 36D 360 36D 

213 213 213 212 212 212 212 

32 32 32 32 32 32 32 

363 363 363 36D 36D 360 36D 

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 

32 32 32 32 32 32 32 

Difference 

"F 

2 

, 

, 

2 

, 

0 

2 

, 

2 

, 

, 

, 

2 

, 

0 

0 

0 

0 

0 

, 

, 

, 

, 

, 

, 

, 

, 

0 

, 

2 

, 

, 

, 

, 

, 

0 

, 

, 

, 

0 

0 

0 

0 

2 

, 

0 

, 

2 

, 

, 

, 

, 

, 

2 

0 

0 

, 

2 

, 

0 

3 

, 

0 

3 

, 

0 

2 

, 

0 

%,("R) 

0.2% 

O.t% 

0.2% 

0.2% 

0.1% 

0.0% 

0.2% 

0.1% 

04% 

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% 

0.1% 

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% 

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-9 

Oil PTC-10 

WATER PTC-10 

OIL 

WATER 

WATER 

I 

OIL 

WATER 

OIL 

WATER 

I 

PTC-22 

PTC-23 

PTC-23 

PTC-24 

PTC-24 

Calibraled By OMW, RM, RMO, DA, ME 

213 

361 

'" 

362 

'" 

213 

363 

'" 

361 

'" 

TEMPERATURE SYSTEM CALIBRATION 

213 

361 

'" 

36' 

'" 

213 

363 

'" 

361 

'" 

213 

361 

'" 

36' 

'" 

213 

363 

'" 

361 

'" 

213 

361 

'" 

213 

363 

'" 

361 

'12 

360 

'" 

'" 

360 

'" 

360 

'" 

360 

'" 

'" 

360 

'" 

360 

'" 

360 

'" 

'" 

360 

'" 

360 

'" 

'" 

360 

'" 

360 

'" 

3 

0 

January 2, 2013 
TEMPERATURE SYSTEM CALIBRATION 

#26 F95-195 

1.0 . 

Calibrated By· DMW, RM. RMO, DA, ME January 2, 2013 
A

Del/a~ ir Qualify Services, Incorporated 

NOZZLE CALIBRATION DATA 

Nozzle I.D. ').s- s ti< Date 2 ns If) 

Material C, \ By M ( 

ConfiQuration (L orffoo'R-l 

'--.....---' 

Maximum Difference Dj - Dj = 0. CC1- (must be 0.004" or less) 

Average Dn = O. 7.. ') 'i 

Note: Measure three diameters with micrometer 

DS1204098 

Della/j. .. ."."' ...................... 

Date of last revision 1/7/2013 Master Document StoragelFormslDatasheetslCalibration Forms 
Delfal1 Air Quality Services, Incorporated 

NOZZLE CALIBRATION DATA 

Nozzle 1.0. $S->fK Date 'Z/Z-GI I> 

Material \, ) Bv ,Me 

Configuration (L or(l1oolS-) 

'----' 

D, = (::.2-3 

D3 = C. 'l ].)' 

Maximum Difference D; - Dj = C -CVL. (must be 0.004" or less) 

Average Dn = 6"Z.") '1 

Note: Measure three diameters with micrometer 

DS1204098 

Della/). .. """"" ...... " ........... 

Date of last revision 1/7/2013 Master Document StoragelFormslDatasheetslCalibration Forms 
Appendix A.4 

R521 0729 

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: 

R521 0729 

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 NOx 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 
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: 

C E Analyzer Response- Cal. Gas Value * 0 

alibration rror = A I R 100 Yo 

na yzer ange 

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 Response - Predicted Response Analyzer Linearity = * 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 ±S% 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 

R5210729 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: 

c-c 

C 0 * c 

c =C-C ma 

where: 

Cc = Drift/bias corrected concentration 

C = Raw Test Average 

m 0 

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 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. 

R5210729 A-12 
Analyzer 

Cal 

Cal No 

Error < 2% 

No 

Yes IYes 

System 1 Nn System tBias < 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% 

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% I- ) 

FIGURE 1: SCAQMD METHOD 100.1 CALIBRATION AND TEST SEQUENCE 

R5210729 A·13 
APPENDIX B PROCESS DATA 

R521 0729 8-1 
Appendix B.1 Process and CEMS Data 

R521 0729 8-2 
Appendix B.1.1 Sentinel Unit 5 Stratification Test 

R5210729 B-3 
Data Summary Report 

Company : CPV Sentinel, LLC 

62575 Powerline Road 

e.1 1i~ \ ~ 

~-h~(v~17" (£-nlL 

Desert Hot Springs , CA 92240 

Source: 

Data Group : 

Report Name : 

Start of Report : 

Turbine 5 

S>l-Min Cales 

S>Summary - I-Min RATA 

02/25/2013 09,49 

G45-C4 

End of Report, 02/25/2013 11,08 

G4S-Cll G4S-C20 G45-C3 G4S-C13 

TRACE 

ElII;ironmenla l !l ~, Tll c. 

validation: All Available Data 

Group#-Channel# G4S-CIO G45-C6 G4S-C7 G4S -CS G45-C18 G4S-C 

Long Descrip. 

Short Descrip . 

Units 

G45-C2 

S;:.Stk NOx 

Stk NOx 

ppm 

0 -15 0 

5>Stk 02 5>NOx Mass S>StkFlow 5>Stk CO S>CO Mass 5>NDx Rate S>Stk NOXC s>Stk CDc 5>Gas Flow 5>NH3 Inj S>MW La 

Range 

02/25/2013 09:49 

02/25/2013 09:50 

02 /25/2013 09:51 

02/25/2013 09:52 

02/25/ 2013 09:53 

02/2 5/ 2013 09:54 

02/25/2013 09:55 

02/25/2013 09:56 

02/25/2013 09:57 

02/25/2013 09:58 

02/25/2013 09:59 

02/25/2013 10:00 

02/25/2013 10:01 

02/25/2013 10:02 

02/25/2013 10:03 

02/25/2013 10:04 

02/25/2013 10:05 

02/25/2013 10:06 

02/25/2013 10:07 

02/25/2013 10:08 

02/25/ 2013 10:09 

02/25/2013 10:10 

02/25/2013 10:11 

02/25/2013 10:12 

02/25/2013 10:13 

02/25/2013 10:14 

02/25/2013 10:15 

02/25/ 2 013 10:16 

02/25/2013 10:17 

02/25/ 2 013 10:18 

Date/Time Printed: 

1., 

1.. 

1.. 

2.0 

2.0 

1.9 

1.9 

1.9 

1.9 

1.9 

1., 

2.0 

1.9 

1.9 

1.9 

1.7 

0.3 

0.6 

0.6 

1.5 

2.1 

1.9 

1.9 

1.9 

1.9 

1.9 

1.8 

1.9 

1.9 

1.9 

stk 02 

• 

0-25 

13 .19 

13 .18 

13 .18 

13 . 19 

13 . 19 

13 .18 

13 .18 

13 . 18 

13 . 18 

13 .18 

13 .18 

13.55 

13.55 

13 . 52 

13 .47 

13 . 80 

16.53 

15 . 74 

14 . 89 

13 . 98 

13 .44 

13 .4 5 

13 .48 

13 .47 

13 .45 

13.44 

13. 4 8 

13 .47 

13 . 4 8 

13 . 48 

02/25/2013 11046 

NDx Mass 

Ib/hr 

0 - 100 

4.59 

4.59 

4.59 

5.51 

5.51 

4.59 

4.59 

4.59 

4.59 

4 .59 

4.59 

5.51 

5.51 

5.51 

5.53 

3.60 

0.22 

1.10 

1. 06 

3.80 

5.50 

5.51 

5.50 

5.51 

5.51 

5.51 

4.59 

5.50 

5.49 

5.49 

StkFlow 

kscfh 

0-300000 

21674 

21652 

21653 

21673 

21667 

21646 

21659 

21652 

21658 

21652 

21652 

22742 

22743 

22667 

22597 

18437 

9369 

12891 

16023 

19979 

2 2373 

22430 

22506 

22 4 80 

22435 

22417 

22500 

22 449 

2 2462 

22469 

Stk CO 

ppm 

0-1000 

1.4 

1.4 

2.2 

1.9 

1.7 

1.7 

3 . 1 

3.3 

3.5 

3.0 

3.0 

3.6 

3.6 

3.4 

2.4 

1.1 

0.1 

0.0 

0.2 

0.3 

1.5 

4.6 

4 . 3 

3.8 

3.1 

0.7 

1.9 

1.7 

0.6 

0.8 

CO Mass 

Ib/hr 

0-100 

1. 84 

1. 84 

3.67 

2.75 

2.75 

2.75 

4.59 

5.51 

5.51 

4.59 

4.59 

5.51 

5.51 

5.51 

3.69 

1.44 

0.00 

0.00 

0.00 

0.76 

2 . 75 

7 . 34 

7.34 

6.42 

5.51 

0.92 

2.75 

2.75 

0.92 

0.92 

NOx Rate 

Ib/mmBtu 

0-1 

0.005 

0.005 

0.005 

0.006 

0.00 6 

0 . 005 

0 . 005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.00 6 

0.006 

0.005 

0.001 

0.003 

0.002 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0-300 

1. 45 

1.45 

1.45 

1. 53 

1. 53 

1.45 

1.45 

1. 45 

1. 45 

1. 45 

1.45 

1.61 

1. 53 

1. 52 

1. 51 

1.41 

0.41 

0.69 

0.59 

1. 28 

1. 66 

1. 50 

1.51 

1. 51 

1. 50 

1. SO 

1. 43 

1. 51 

1. 51 

1. 51 

Stk COc Gas 

ppm 

0 - 1000 

1. 07 

1. 07 

1. 68 

1. 45 

1. 30 

1. 30 

2.37 

2.52 

2.67 

2.29 

2.29 

2.89 

2. 89 

2. 72 

1. 91 

0.91 

0.14 

0.00 

0 . 20 

0.26 

1.19 

3. 64 

3.42 

3.02 

2.46 

0.55 

1.51 

1.35 

0. 4 8 

0.64 

hscfh 

hscfh 

0-10000 

8742.6 

8745.0 

8745.6 

8742.0 

8739.6 

8742.6 

8748.0 

8745.0 

8747.4 

8745.0 

8745.0 

8745.0 

8745.6 

8751.6 

8784.0 

6848.4 

2142.0 

3480.0 

5038.2 

7233.0 

8731.8 

8742.6 

8736.6 

8738.4 

8744 . 4 

8749.2 

8734.2 

8726.4 

8719.8 

8722.2 

NH3Inj 

1b/hr 

0-200 

200.0 

200.0 

199.8 

200.0 

200.0 

2 00.0 

197.3 

198.8 

196.8 

198.7 

198.7 

197.7 

132.8 

198 . 7 

200.0 

186 . 5 

72.2 

114.8 

102.2 

155.0 

198.3 

196.3 

196.2 

195.8 

198.7 

200.0 

196.7 

200.0 

200.0 

199.5 

MW Lo 

0-1 

105 .. 

105 . . 

lOS. : 

105 .. 

105. 

IDS .. 

105. : 

lOS .. 

105 .. 

105 .. 

105. : 

lOS. : 

105. : 

105 .. 

106 .. 

70. : 

11. 

29 . . 

51. : 

85. 

105 . 

105 . . 

105. 

105. 

106.1 

IDS. 

105. 

106. ( 

lOS . . 

105. ! 

PagE 
Group#-Channel# 

Long Descrip . 

Short Descrip. 

Units 

Range 

02/25/2013 10:19 

02/25/2013 10:20 

02/25/2013 10:21 

02/25/2013 10:22 

02/25/2013 10:23 

02/25/2013 10:24 

02/25/2013 10:25 

02/25/2013 10:26 

02/25/2013 10:27 

02/25/2013 10:28 

02/25/2013 10:29 

02/25/2013 10:30 

02/25/2013 10:31 

02/25/2013 10:32 

02/25/2013 10:33 

02/25/ 2 013 10:34 

02/25/2013 10:35 

02/25/2013 10:36 

02/25/2013 10:37 

02/25/2013 10:38 

02/25/2013 10:39 

02/25/2013 10:40 

02/25/2013 10:41 

02/25/2013 10:42 

02/25/2013 10:43 

02/25/2013 10:44 

02/25/2013 10:45 

02/25/2013 10:46 

02/25/2013 10:47 

02/25/2013 10:48 

02/25/2013 10:49 

02/25/2013 10:50 

02/25/2013 10:51 

02/25/2013 10:52 

02/25/2013 10:53 

02/25/2013 10:54 

02/25/2013 10:55 

02/25/2013 10:56 

02/25/2013 10:57 

02/25/2013 10:58 

Date/Time Printed : 

G45-C2 G45-C4 G45-C11 G45-C20 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 5>StkFlow 

2.6 

2.2 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.8 

1.9 

1.8 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.8 

1.8 

1.8 

1.8 

1.9 

1.8 

1.8 

1.8 

Stk 02 

% 

0-25 

13.47 

13.47 

13 . 47 

13 .47 

13 .48 

13 .48 

13 . 49 

13 . 4 8 

13.48 

13 .48 

13 .48 

13 .47 

13.48 

13 .47 

13. 4 7 

13 .47 

13 .48 

13 .48 

13 .48 

13.48 

13.48 

13 . 48 

13 . 48 

13 .4 8 

13 .47 

13 .48 

13 .47 

13 .48 

13.48 

13. 4 7 

13 . 48 

13 .48 

13.48 

13 .48 

13 .48 

13 .49 

13 .48 

13 .4 8 

13. 4 7 

13.47 

02/25/2013 11046 

NOx Mass 

lb/hr 

0-100 

7.33 

5.50 

5.51 

5.51 

5.51 

5.51 

5.50 

5.50 

5.50 

4.59 

5 .51 

4.59 

5.50 

5.51 

5.50 

5.51 

5.50 

5.50 

5.50 

5.50 

5.50 

5.50 

5.50 

5.50 

5.50 

5.50 

5.50 

5.50 

5.50 

5.50 

5.51 

5.51 

4.59 

4.59 

4.59 

4.59 

5.51 

4.60 

4.60 

4.59 

StkFlow 

kscfh 

0-300000 

22462 

22455 

22500 

22492 

22515 

22515 

22522 

22493 

22504 

22518 

22513 

22478 

22483 

22489 

22474 

2 2485 

22479 

22486 

22487 

22496 

22501 

22484 

22486 

22506 

22460 

22489 

22451 

22475 

22481 

22471 

22 517 

22526 

22526 

22527 

22532 

22547 

22521 

22552 

22520 

22509 

G4S-C3 G45-C13 G45 - C10 G4S-C6 G45 - C7 G4S-C8 G45-C18 G45-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXc 5>Stk COc 5>Gas Flow 5>NH3 Inj 5>MW La 

Stk CO 

ppm 

0-1000 

1.2 

loS 

3.4 

3.9 

4.0 

3.1 

3.1 

2.7 

2.3 

2.8 

3.0 

2.8 

2.3 

2.6 

2.S 

2.3 

2.4 

2.3 

2.6 

2.9 

2.3 

2.S 

2.6 

2.9 

2.7 

2.S 

2.S 

2.3 

2.S 

2.8 

3.1 

3.3 

3.1 

3.4 

3.0 

3.3 

2.9 

3 . S 

3.9 

3.8 

CO Mass 

lb/hr 

0 -1 00 

1. 83 

2.75 

5.51 

6.43 

6.42 

5.51 

5.50 

4 . 58 

3.67 

4.59 

4.59 

4.59 

3.67 

4.59 

3.67 

3.67 

3.67 

3.67 

4.58 

4.59 

3.67 

3.67 

4.58 

4.59 

4.58 

3.67 

3.67 

3.66 

3.67 

4.59 

5.51 

5.51 

5.51 

5.51 

4.59 

5.51 

4.59 

5.52 

6.43 

6.43 

NOx Rate 

lb/mmBtu 

0-1 

0.008 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

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 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.005 

0.005 

0.005 

0.006 

0 . 005 

0.005 

0.005 

Stk NOXc 

ppm 

0 - 300 

2.06 

1. 75 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1.43 

1. 51 

1.43 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1.51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1.51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 43 

1. 43 

1.43 

1.43 

1. 51 

1.43 

1. 43 

1. 43 

Stk COc Gas hscfh 

ppm 

0-1000 

0.95 

1.19 

2.70 

3.10 

3.18 

2.46 

2.47 

2.15 

1. 83 

2.23 

2.39 

2.22 

1. 83 

2.06 

1. 99 

1. 83 

1. 91 

1. 83 

2.07 

2.31 

1. 83 

1. 99 

2.07 

2.31 

2.14 

1. 99 

1. 99 

1. 83 

1. 99 

2 . 22 

2.46 

2.62 

2.46 

2.70 

2.39 

2.63 

2.31 

2.78 

3.10 

3.02 

hscfh 

0-10000 

8731. 2 

8728.8 

8746.2 

8743.2 

8740.2 

8740.2 

8731.2 

8731.8 

8736.0 

8741.4 

8739.6 

8737 8 

8727.6 

8742.0 

8736.0 

8740.2 

8726.4 

8728.8 

8729.4 

8733.0 

8734.8 

8728.2 

8728.8 

8736.6 

8730.6 

8730.0 

8727.0 

8724.6 

8727.0 

8734.8 

8740 . 8 

8744.4 

8744.4 

8745.0 

8746.8 

8740.8 

8742.6 

8754.6 

8754. a 

8749.8 

NH3Inj 

1b/hr 

0-200 

171.7 

198.5 

196.2 

197.0 

197.3 

197.2 

197.3 

197.0 

199.0 

198.0 

197.0 

198.0 

197.5 

197.5 

198.3 

197.3 

196.7 

196.8 

196.3 

196.7 

197.7 

196.5 

196.0 

196.5 

195.8 

196.2 

196.5 

196.7 

194 . 8 

196.7 

196.0 

196.7 

196.5 

196.2 

196.7 

195.3 

196.8 

196.5 

1 95.8 

194.8 

S>Summary - l-Min RATA - Continued 

MW Lo 

0-1 

105. : 

105. : 

105 .. 

105 .. 

105. : 

105. : 

105. : 

106.1 

105. : 

105. 

106 .• 

105 .. 

105. ~ 

106.1 

105 . ~ 

105. : 

105.: 

105 .. 

105. : 

105. 

105 . . 

105. 

105 . 

105 .. 

105 .. 

105. : 

105. 

105 . . 

106. 1 

105. 

106.1 

105 . . 

106 . 1 

105. : 

105. : 

106.1 

105. 

105 .. 

105. 

105. : 

Pagf 
Group#-Channel# 

Long Descrip . 

Short Descrip. 

Units 

Range 

02/25/2013 10;59 

02/25/2013 11:00 

02/25/2013 11:01 

02/25/2013 11:02 

02/25/2013 11:03 

02/25/2013 11:04 

02/25/2013 11:05 

02/25/2013 11:06 

02/25/2013 11:07 

02/25/2013 11:08 

Period Average 

Period Max Value 

Period Min Value 

Period Totals = 

Period % Recovery 

Date/Time Printed: 

G45-C2 G4S-C4 G45 -C11 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

Stk 02 

• 

0-25 

1.8 13.47 

1.9 13.48 

1.8 13.47 

1.8 13.47 

1.8 13.48 

1.9 13.48 

1.8 13.48 

1.8 13.47 

1.8 13.47 

1.8 13.47 

1.8 13.53 

2.6 16.53 

0.3 13.18 

1.4690E+2 1.0825E+3 

100.0 100 . 0 

02/25/2013 11,46 

NOx Mass 

Ib/hr 

0-100 

4.59 

5 . 51 

4.60 

4.60 

4.59 

5.52 

4.60 

4.59 

4.60 

4.59 

5.00 

7.33 

0.22 

3.9983E+2 

100.0 

G4S-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

22509 

22544 

22525 

22528 

22540 

22555 

22 552 

22509 

22519 

22 514 

21943 

22743 

9369 

1.7554E+6 

100.0 

G45 - C3 G45 - C13 G45-C10 G4S -C6 

5>Stk CO 

Stk CO 

S>CO Mass S>NOx Rate 5>Stk NOXc 

ppm 

0-1000 

CO Mass 

Ib/hr 

0-100 

3.8 6.43 

3.5 5.51 

4.2 6.44 

3.9 6.44 

4.2 6.43 

3.7 6.44 

3.7 6.43 

3.9 6.43 

3.4 5.51 

3.8 6.43 

2.7 4.33 

4.6 7.34 

0.0 0.00 

2.1460E+2 3.4646E+2 

100.0 100.0 

NOx Rate 

Ib/mmBtu 

0-1 

0.005 

0.006 

0.005 

0.005 

0.005 

0.006 

0.005 

0.005 

0.005 

0.005 

0.006 

0.008 

0.001 

4.4100E-1 

100 . 0 

Stk NOXc 

ppm 

0-300 

1.43 

1. 51 

1. 43 

1. 43 

1. 43 

1. 51 

1. 43 

1. 43 

1. 43 

1.43 

1.46 

2.06 

0.41 

1.1673E+2 

100.0 

G45-C7 G4S-C8 

S>Stk COc S>Gas Flow 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0 -1 0000 

3.02 

2.78 

3.34 

3.10 

3.34 

2.94 

2.94 

3.10 

2.70 

3.02 

2.13 

3.64 

0.00 

1.7000E+2 

100 . 0 

8749.8 

8751. 6 

8755.8 

8757.0 

8749.8 

8755.8 

8754.6 

8749.8 

8753.4 

8751.6 

8503.8 

8784.0 

2142.0 

6.8030E+5 

100.0 

G45-C18 

S>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

194.8 

196.3 

196.3 

197.2 

194.7 

194.8 

196.0 

194.7 

195.2 

195.0 

191.7 

200.0 

72.2 

1.5332E+4 

100.0 

S>Summary - I-Min RATA - Continued 

G45-C 

5>MW La 

MW La 

0-1 

105. 

105 

105.' 

105.: 

I DS .! 

105.' 

105.: 

106 .1 

105.: 

106.1 

102.2 

106. 

11. 

8.1775E+ 

100. 

PagE 
Appendix B.1.2 Sentinel Unit 5 Ammonia, ROG and NOxlCO Testing 

R521 0729 8·4 
Data Summary Report 

Company: CPV Sentinel, LLC 

62575 Powerline Road 

Desert Hot Springs, CA 92240 

Source: Turbine 5 

Data Group: 

Report Name: 

5l t'\ fill(, I ~ 

7:170 

COVl\p';~"'<. 

TRACE 

Elw ironmenlai Syslems, lllc. 

, I 

Start of Report: 

5::>1-Min Cales 

s>Summary - 1 - Min RATA 

02/26/2013 08,30 End of Report, 02/26/2013 09,37 validation: All Available Data 

Group#-Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/26/2013 08:30 

02/26/2013 08:31 

02/26/2013 08:32 

02/26/2013 08:33 

02/26/2013 08:34 

02/26/2013 08:35 

02/26/2013 08:36 

02/26/2013 08:37 

02/26/2013 08:38 

02/26/2013 08:39 

02/26/2013 08:40 

02/26/2013 08:41 

02/26/2013 08:42 

02/26/2013 08:43 

02/26/2013 08:44 

02/26/2013 08:45 

02/26/2013 08:46 

02/26/2013 08:47 

02/26/2013 08:48 

02/26/2013 08:49 

02/26/2013 08:50 

02/26/2013 08:51 

02/26/2013 08:52 

02/26/2013 08:53 

02/26/2013 08:54 

02/26/2013 08:55 

02/26/2013 08:56 

02/26/2013 08:57 

02/26/2013 08:58 

02/26/2013 08:59 

Date/Time Printed: 

G45-C2 G45 - C4 G45-C11 

5>Stk NOx 

Stk NOx 

ppm 

0 - 150 

5 >Stk 02 5 >NOx Mass 

1.4 

1.4 

1.4 

1.4 

1.5 

1.5 

1.5 

1.4 

1.4 

1.5 

1.4 

1.5 

1.5 

1.6 

1.6 

1.6 

1.7 

1.7 

1.6 

1.7 

1.7 

1.8 

1.7 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.5 

Stk 02 

% 

0 - 25 

14.07 

14.06 

14.06 

14.07 

14.08 

14.07 

14.06 

14.07 

14.06 

14.06 

14.07 

14.07 

14.06 

14.06 

14.06 

14. OS 

14.05 

14.05 

14.05 

14.06 

14.05 

14.05 

14.05 

14.05 

14.03 

14.02 

14.03 

14.04 

1 4.02 

14.03 

02/26/2013 10,13 

NOx Mass 

Ib/hr 

0 - 100 

2.24 

2.25 

2.25 

2.24 

2.80 

2.81 

2.81 

2.24 

2.25 

2.81 

2.24 

2.80 

2.81 

2.81 

2.80 

2.81 

2.81 

2.82 

2.82 

2.81 

2.82 

3.39 

2.82 

2.83 

3.41 

3.41 

3.40 

3.41 

3.42 

2.85 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

14953 

14969 

14953 

14953 

14953 

14966 

14976 

14943 

14976 

14976 

14939 

14931 

14964 

14936 

14916 

14922 

14936 

14963 

15003 

14954 

14963 

15009 

15001 

15043 

15063 

15024 

15031 

15081 

15077 

15093 

G45 - C3 

5>Stk CO 

Stk CO 

ppm 

0 - 1000 

0.2 

0.2 

0.1 

0.1 

0.2 

0.2 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0 . 1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.0 

0.0 

0.0 

0.0 

0 . 1 

G4S - C13 G45 - C10 G45-C6 

5>CO Mass 5>NOx Rate 5 >Stk NOXc 

CO Mass 

lb/hr 

0-100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

NDx Rate 

Ib/mmBtu 

0-1 

0.004 

0.004 

0.004 

0.004 

0.005 

0.005 

0.005 

0.004 

0.004 

0.005 

0.004 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

Stk NDXc 

ppm 

0-300 

1. 21 

l. 21 

1. 21 

l. 21 

l. 30 

l. 30 

l. 29 

l. 21 

1.21 

1.29 

1.21 

1.30 

1. 29 

1. 38 

1. 38 

l. 38 

l. 46 

l. 46 

l. 38 

l. 47 

1.46 

1.55 

1.46 

1.46 

1. 55 

1. 54 

l. 55 

1. 55 

l. 54 

1. 29 

G45 - C7 G45 - C8 

5>Stk COc 5 >Gas Flow 

Stk CDc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.17 

0.17 

0.09 

0.09 

0.17 

0.17 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.00 

0.00 

0.00 

0.00 

0.09 

5343.0 

5356.8 

5350.8 

5343.0 

5335.2 

5347.8 

5359.2 

5339.4 

5359.2 

5359.2 

5338.2 

5335.2 

5355.0 

5344.8 

5337.6 

5347.8 

5352.6 

5362.2 

5376.6 

5351.4 

5362.2 

5379.0 

5376.0 

5391. 0 

5413.8 

5407.8 

5402.4 

5412.6 

5427.0 

5424.6 

G4S-C18 

5>NH3 Inj 

NlBlnj 

lb/hr 

0 - 200 

104.7 

104 . 5 

103.7 

104.5 

104 . 3 

103.7 

103.8 

105.0 

103.8 

104.7 

104.3 

103.8 

103.8 

102.8 

102.8 

103.0 

102.8 

104.2 

104.3 

104.3 

104.5 

103.8 

105.7 

106.3 

107.7 

107.5 

108.7 

108.8 

109.2 

108.3 

G45-C 

5>MW Lo 

MW Lo 

0 - 1 

54. ( 

54. ( 

54. ! 

54. ! 

53 .. 

54. 1 

54. ( 

54. ! 

54. ( 

54. ! 

54. ( 

53. : 

54.J 

54. ! 

53 .. 

54. ! 

54. : 

54 .. 

54. ' 

54. ( 

54. ! 

54. ! 

54 .. 

54. 

55. ( 

55. ( 

54. : 

55. ( 

55 .J 

55. ( 

pagE 
Group#-Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/26/2013 09:00 

02/26/2013 09:01 

02/26/2013 09:02 

02/26/2013 09:03 

02/26/2013 09:04 

02/26/2013 09:05 

02/26/2013 09:06 

02/26/2013 09:07 

02/26/2013 09:08 

02/26/2013 09:09 

02/26/2013 09:10 

02/26/2013 09:11 

02/26/2013 09:12 

02/26/2013 09:13 

02/26/2013 09:14 

02/26/2013 09:15 

02/26/2013 09:16 

02/26/2013 09:17 

02/26/2013 09:18 

02/26/2013 09:19 

02/26/2013 09:20 

02/26/2013 09:21 

02/26/2013 09:22 

02/26/2013 09:23 

02/26/2013 09:24 

02/26/2013 09:25 

02/26/2013 09:26 

02/26/2013 09:27 

02/26/2013 09:28 

0 2 /26/2013 09:29 

02/26/2013 09:30 

02/26/2013 09:31 

02/26/2013 09 :3 2 

02/26/2013 09:33 

02/26/2013 09:3 4 

02/ 26 /2013 09:35 

02/26/2013 09:36 

02/26/2013 09:37 

Date/Time Printed: 

G45-C2 G45-C4 G45-C11 

5>Stk NOx 

Stk NOx 

5>Stk 02 5>NOx Mass 

ppm 

0-150 

1.6 

1.6 

1.7 

1.6 

1.6 

1.6 

1.6 

1.6 

1.7 

1.7 

1.7 

1.7 

1.7 

1.6 

1.6 

1.7 

1.6 

1.6 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

Stk 02 

• 

0-25 

14.01 

14.02 

14.02 

14.03 

14.04 

14.03 

14.02 

14.03 

14.03 

14.02 

14.02 

14 . 02 

14 . 02 

14.02 

14.02 

14.02 

14.03 

14.04 

14.03 

14.02 

1 4. 02 

14.03 

14.04 

14.04 

14 . 04 

14. OS 

14.05 

14.04 

14.03 

14.03 

14.03 

14.02 

14.02 

14.02 

14.02 

14.03 

14.03 

14.03 

02/26/2013 10,13 

NOx Mass 

Ib/hr 

0-100 

2.85 

2.85 

2.85 

2.84 

2.83 

2.84 

2.85 

2.84 

2.85 

2.85 

2.85 

2.84 

2.85 

2.84 

2.84 

2.84 

2.84 

2.83 

2.83 

2.83 

2.84 

2.83 

2.82 

2.82 

2.82 

2.82 

3.37 

3.39 

3.38 

3.39 

3.39 

2.83 

2 .83 

2.83 

2.83 

2.83 

2.83 

2.83 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

15077 

15071 

15094 

15034 

15033 

15046 

15062 

15063 

15096 

15057 

15067 

15047 

15059 

15029 

15051 

15042 

15033 

15041 

15021 

14996 

15007 

15006 

14964 

14973 

1 4 944 

14971 

14931 

14976 

14946 

14971 

14961 

14962 

14962 

14962 

14962 

15002 

15002 

15002 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

0.1 

0.2 

0.2 

0 . 2 

0.2 

0.2 

0.2 

0 . 2 

0.2 

0 . 2 

0 .2 

0.2 

0.2 

0.2 

0.2 

0.2 

o 2 

0.2 

0.2 

0.2 

0 . 2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0 .1 

0.2 

0.2 

0 .2 

0.2 

0 .2 

0.2 

0.2 

0.2 

0.2 

G45-C13 G45-C10 G45-C6 

5>CO Mass 5>NOx Rate 5>Stk NOXc 

CO Mass 

lb/hr 

0-100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

0.00 

0.00 

0 . 00 

0.00 

0 . 00 

0.00 

0.00 

0.00 

0.00 

NOx Rate 

lb/mmBtu 

0-1 

0.005 

0.005 

0 . 005 

0.005 

0.005 

0.005 

0 . 005 

0.005 

0.005 

0.005 

0.005 

0 . 005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0 . 005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.005 

0 . 005 

0.005 

0 . 005 

0.005 

0.005 

Stk NOXc 

ppm 

0-300 

1. 37 

1. 37 

1. 46 

1.37 

1.38 

1.37 

1.37 

1.37 

1. 46 

1. 46 

1.46 

1.46 

1.46 

1.37 

1.37 

1.46 

1. 37 

1. 38 

1.46 

1.46 

1.46 

1. 46 

1. 46 

1. 46 

1. 46 

1.46 

1.55 

1. 55 

1. 55 

1. 55 

1. 55 

1.46 

1.46 

1.46 

1. 4 6 

1. 46 

1.46 

1.46 

G45-C7 G45-C8 

5>Stk COc 5>Gas Flow 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.09 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0 . 17 

0.17 

0.17 

0.17 

0.17 

0.09 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

5434.8 

5424.6 

5433.0 

5403.6 

5395 . 2 

5407.8 

5421.6 

5413 .8 

5425 .8 

5419 . 8 

5423.4 

5416.2 

54 2 0.4 

5409 . 6 

5417 . 4 

5414.4 

5403.0 

5398.2 

5398.8 

5397.6 

5401.8 

5393.4 

5370 . 6 

5373.6 

5363.4 

5365 .2 

5350.8 

5374.8 

5371. 8 

5380.8 

5377.2 

5385 . 6 

5385.6 

5385.6 

5385.6 

5392.2 

5392.2 

5392.2 

G45-C18 

5>NH3 Inj 

NH3lnj 

lb/hr 

0-200 

105.5 

103.3 

102 . 8 

103.2 

102.5 

103.2 

103.7 

102.5 

102.3 

102.5 

102.3 

102.0 

102 . 7 

103.0 

102.5 

102.3 

102.8 

102.5 

102.5 

101. 3 

101.3 

101.2 

101.2 

101. 3 

101.8 

101.3 

101.2 

101.2 

100.8 

101.2 

101. 5 

102.5 

102.5 

102.5 

102.5 

101.8 

101. 8 

101.8 

S>Summary - I - Min RATA - Continued 

G45-C 

5>MW Lo 

MW Lo 

0-1 

55.: 

55. : 

55. -

55. ( 

55. ( 

55. ( 

55.1 

55. ( 

55.1 

55. ( 

55. : 

55.1 

55. : 

55.1 

55.1 

55 .1 

55.1 

55.1 

55.1 

55 . 1 

55. ! 

55. ( 

54 .. 

54. ' 

54. 

54 .. 

54 

54 .. 

54.: 

54. : 

54. : 

54. : 

54. : 

54. : 

54. : 

54. : 

54. : 

54. : 

PagE 
Period Average = 1.6 14.04 2 .86 15000 0. 2 0.00 0 . 005 1.41 0.13 5384 .0 103 . 4 54.6 

Period Max Value 1. 8 14.08 3.42 15096 0.2 0.00 0 . 006 1. 55 0 . 17 5434 . 8 109.2 55. 

Period Min Value 1. 4 1 4. 01 2. 24 14916 0.0 0.00 0 . 00 4 1. 21 0.00 5335.2 100 . 8 53. 

Period Totals = 1.1170E+2 9.54 6 7E+2 1 . 94 51E+2 1 . 019 9E+6 1.0400E+l O. OOOOE+O 3.4400E-l 9 . 6060E+l 8 . 9600E+0 3.6611E+5 7.0341E+3 3.7129E+ 

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 

5~+;1\(,\ ~ 

t]1)'J" 

CJ>Mp. 2. 

Source : 

Data Group: 

Report Name: 

Start of Report: 

Turbine 5 

5>1-Min Cales 

S>Summary - I-Min RATA 

02/26/2013 10,00 

G45-C4 

End of Report, 02/26/2013 11,09 

G45-Cl1 G45-C13 

TRACE 

E,wirollmenlal Systems, [IIC. 

Validation : All Available Data 

Group#-Channel# G4S-CIO G45-C6 G45-C7 G45-C8 

Long Descrip . 

Short Descrip. 

Units 

G45-C2 

5>Stk NOx 

stk NOx 

ppm 

0-150 

5>Stk 02 S>NOx Mass 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

G45-C3 

s>Stk CO 

Stk CO 

ppm 

0-1000 

S>CO Mass 5>NOx Rate s>Stk NOXc 5>Stk COe S>Gas Flow 

G45-C18 

5>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

G45-C 

5>MW Lo 

MW Lo 

Range 

02/26/2013 10;00 

02/26/ 2 013 10 ; 01 

02/26/2013 10;02 

02/26/2013 10 ; 03 

02/26/2013 10;04 

02/26/2013 10;05 

02/26/2013 10;06 

02/26/2013 10:07 

02/26/2013 10;08 

02/26/ 2 013 10:09 

02/26/2013 10:10 

02/26/2013 10:11 

02/26/2013 10:12 

02/26/2013 10;13 

02/26/2013 10;14 

02/26/2013 10;15 

02/26/2013 10:16 

02/26/2013 10,17 

02/26/2013 10:18 

02/26/2013 10:19 

02/26/2013 10 : 20 

02/26/2013 10:21 

02/26/2013 10;22 

02/26/ 2 013 10:23 

02/26/2013 10:24 

02/26/2013 10,25 

02/26/2013 10:26 

02/26/2013 10;27 

02/26/2013 10:28 

02/26/2013 10:29 

Date/Time Printed : 

1.7 

loB 

1.8 

loB 

1.8 

1.7 

1.7 

loB 

1.8 

1.8 

1.8 

1.8 

loB 

1.8 

1.8 

1.9 

1.9 

1.8 

1.8 

1.8 

1.8 

1.9 

1.9 

loB 

1.8 

loB 

1.8 

1.8 

1.8 

1.8 

Stk 02 

• 

0-25 

14.00 

14.01 

14.01 

14.01 

14.01 

1 4. 00 

14.00 

14.00 

14.00 

14 . 00 

14.00 

14.01 

14.01 

14.01 

14.01 

14.01 

14.01 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

1 4. 02 

14.02 

14.02 

14.02 

14.02 

14 . 02 

02/26/2013 11,31 

NOx Mass 

1b/hr 

0-100 

2.88 

3.43 

3.43 

3.43 

3.43 

2 . 88 

2.88 

3.44 

3.44 

3.44 

3.44 

3.42 

3.42 

3 . 42 

3.42 

3.43 

3.43 

3.41 

3.41 

3.41 

3.41 

3.40 

3.40 

3 . 43 

3.43 

3.43 

3.43 

3. 4 1 

3.41 

3.41 

15190 

15122 

15122 

15122 

15122 

15220 

15220 

15112 

15112 

15112 

15112 

15055 

15055 

15055 

15055 

15089 

15089 

15044 

15044 

15044 

15044 

15004 

15004 

15124 

15124 

15124 

15124 

15021 

150 2 1 

15021 

0.2 

0.2 

0.2 

0. 2 

0.2 

0 . 2 

0 .2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0 .2 

0.2 

0.2 

0 .2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0 . 2 

0.2 

CO Mass 

Ib/hr 

0-100 

0.00 

0.00 

0.00 

0.00 

0.00 

0 .00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

0 . 00 

0.00 

0 . 00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

0.00 

0 . 00 

0.00 

0 . 00 

0.00 

0.00 

0.00 

NOx Rate 

Ib/mmBtu 

0-1 

0.005 

0 . 006 

0.006 

0 . 006 

0.006 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0 . 006 

0.006 

0 . 006 

0.006 

0.006 

0 . 006 

0 . 006 

0.006 

0.006 

0.006 

0 . 006 

0.006 

0 . 006 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0-300 

1. 45 

1. 54 

1. 54 

1. 54 

1. 54 

1. 45 

1. 45 

1.54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 63 

1. 63 

1. 54 

1.54 

1. 54 

1. 54 

1. 63 

1. 63 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

Stk COe Gas 

ppm 

0-1000 

0 .17 

0 . 17 

0.17 

0 . 17 

0 . 17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

0 . 17 

0.17 

0.17 

0 . 17 

0.17 

0.17 

0 . 17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

hscfh 

hscfh 

0-10000 

54 83 .4 

5451. 0 

5451.0 

5451 . 0 

5451. 0 

5494.2 

5494.2 

5 4 55 . 2 

5455.2 

5455.2 

5455.2 

5427.0 

5427.0 

5427 . 0 

5427.0 

5439.0 

5439.0 

5415.0 

5415.0 

5 4 15.0 

5415.0 

5400.6 

5400.6 

5443.8 

5443 .8 

5443.8 

5443.8 

5406.6 

5406.6 

5406.6 

101.5 

100.8 

100.8 

100 . 8 

100.8 

103.2 

103.2 

101.5 

101. 5 

101 . 5 

101.5 

101. 2 

101. 2 

101.2 

101. 2 

101.7 

101.7 

102.0 

102.0 

102.0 

102 . 0 

101.2 

101.2 

102.5 

102 . 5 

102.5 

102.5 

103 . 2 

103.2 

103 . 2 

0-1 

56 . 1 

55. 

55. : 

55. : 

55. 

56 .. 

56 .. 

56. ! 

56.1 

56. ( 

56.1 

5S. : 

55 . 

55 . 

55. : 

55 .. 

55 .. 

55 .. 

55 .. 

55 .. 

55 .. 

55 .. 

55. : 

56.1 

56 . ( 

56.1 

56. ( 

55. ! 

55. ! 

55. ! 

PagE 
Group#-Channe l # 

Long Descrip . 

Shor t Descrip. 

Units 

Range 

02/26/2013 10:30 

02/26/2013 10:31 

02/26/2013 10:32 

02/26/2013 10:33 

02/26/2013 10:34 

02/26/2013 10:35 

02/26/2013 10:36 

02/26/2013 10:37 

02/26/2013 10:38 

02/26/2013 10:39 

02/26/2013 10:40 

02/26/2013 10:41 

02/26/2013 10:42 

02/26/2013 10:43 

02/26/2013 10:44 

02/26/2013 10:45 

02/26/2013 10:46 

02/26/2013 10:47 

02/26/2013 10;48 

02/26/2013 10:49 

02/26/2013 10:50 

02/26/2013 10:51 

02/26/2013 10:52 

02/26/2013 10:53 

02/26/2013 10:54 

02/26/2013 10:55 

02/26/2013 10:56 

02/26/2013 10:57 

02/26/2013 10:58 

02/26/2013 10:59 

02/26/2013 11:00 

02/26/2013 11:01 

02/26/2013 11:02 

02/26/2013 11:03 

02/26/2013 11:04 

02/26/2013 11:05 

02/26/2013 11:06 

02/26/2013 11:07 

02/26/2013 11:08 

02/26/2013 11:09 

Date/Time Printed: 

G45-C2 G45-C4 G45-C11 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

1.8 

2.0 

2.0 

1.9 

1.9 

1.. 

1.. 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.. 

1.. 

1.8 

stk 02 

• 

0-25 

14.02 

14 .02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.04 

14.04 

14.03 

14.03 

14.04 

14.04 

14.05 

14.05 

14.05 

14.05 

14.05 

14.05 

14.04 

14 .04 

14.04 

14.04 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.03 

14.03 

14.03 

14.03 

14.03 

14.03 

14.03 

14 . 03 

14.02 

14.02 

14.02 

02/26/2013 11,31 

NOx Mass 

1b/hr 

0 - 100 

3.41 

3.41 

3.41 

3.40 

3.40 

3.40 

3.40 

3.38 

3.38 

3.39 

3.39 

3.37 

3.37 

3.36 

3.36 

3.36 

3.36 

3.37 

3.37 

3.36 

3.36 

3.36 

3.36 

3.39 

3.39 

3 . 39 

3.39 

3.39 

3.39 

3.39 

3.39 

3.38 

3.38 

3.38 

3.38 

3.39 

3.39 

3.39 

3.39 

3.39 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

15021 

15019 

15019 

14987 

14987 

14987 

14987 

14957 

14957 

14971 

14971 

14921 

14921 

14901 

14901 

14901 

14901 

14917 

14917 

14867 

14867 

14867 

14867 

14961 

14961 

14961 

14961 

14939 

14939 

14962 

14962 

14939 

14939 

14936 

14936 

14964 

14964 

14969 

14969 

14962 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.2 

0.2 

0.2 

0.2 

0.1 

0.1 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

G45-C13 G45-C10 G45 - C6 

5>CO Mass 5>NOx Rate s>Stk NOXc 

CO Mass 

Ib/hr 

0-100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

NOx Rate 

lb/mmBtu 

0-1 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

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 

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. 54 

1. 72 

1. 72 

1. 63 

1. 63 

1. 63 

1. 63 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1.55 

1.55 

1. 55 

1. 55 

1. 55 

1.55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 63 

1. 63 

1. 54 

G45-C7 G45-C8 

5>Stk COc 5>Gas Flow 

Stk COc Gas hscfh 

ppm 

0-1000 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.17 

0.17 

0.17 

0.17 

0.09 

0.09 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

hscfh 

0 - 10000 

5406.6 

5406.0 

5406.0 

5394.6 

5394.6 

5394.6 

5394.6 

5368.2 

5368.2 

5380.8 

5380.8 

5355.0 

5355.0 

5340.0 

5340.0 

5340.0 

5340.0 

5346.0 

5346.0 

5335.8 

5335.8 

5335.8 

5335.8 

5385.0 

5385.0 

5385.0 

5385.0 

5377.2 

5377.2 

5377.8 

5377.8 

5369.4 

5369.4 

5368.2 

5368.2 

5378.4 

5378.4 

5388.0 

5388.0 

5385.6 

G45-C18 

5>NH3 Inj 

NH3Inj 

1b/hr 

0-200 

103.2 

102.3 

102.3 

101. 7 

101.7 

101.7 

101. 7 

101. 3 

101. 3 

102.8 

102.8 

102.5 

102.5 

102.5 

102.5 

102 . 5 

102.5 

102.5 

102.5 

103.2 

103.2 

103.2 

103.2 

103.7 

103.7 

103.7 

103.7 

104.2 

104.2 

103.2 

103.2 

104.2 

104.2 

104.5 

104.5 

103.7 

103.7 

102.8 

102.8 

103.7 

S>Summary - I-Min RATA - Continued 

G45 - C 

5>MW Lo 

MW La 

0-1 

S5 . ~ 

55.: 

55.' 

55.1 

55.1 

55.1 

55.1 

55.1 

55.1 

55.1 

55.1 

54 .. 

54 . . 

S4.: 

54 .. 

54. : 

S4. : 

54. 

54 .. 

54 . . 

54 . . 

S4 . . 

54 . . 

55 .. 

55 .. 

55.: 

55 .. 

5S .1 

55.1 

S5.: 

55 

55.1 

55.1 

5S .1 

5S .1 

55.1 

5S .1 

S5.1 

55.1 

55. 

pag~ 
Period Average = 1.8 14.02 3.38 15008 0.2 0.00 0.006 1. 56 0.16 5399.8 102.5 55.2 

Period Max Value 2.0 14 . 05 3.44 15220 0.2 0.00 0.006 1. 72 0.17 5494.2 104.5 56. 

Period Min Value 1.7 14.00 2.88 14867 0.1 0.00 0.005 1.45 0.09 5335.8 100.8 54. 

Period Totals = 1 . 2710E+2 9.8160E+2 2.3637E+2 1.0505E+6 1.2800E+1 O.OOOOE+O 4.1700E-1 1.0903E+2 1.0940E+1 3.7798E+5 7.1746E+3 3.8682E+ 

Period % Recovery 100.0 100 . 0 100.0 1 00.0 100.0 100.0 100 . 0 100.0 100.0 100 . 0 100.0 100 . 
Data Summary 

Company: 

Source: 

Data Group: 

Report Name: 

Start of Report : 

Report 

CPV Sentinel, LLC 

62575 Powerline Road 

Desert Hot Springs, CA 

Turbine 5 

S>l-Min Cales 

S>Summary - I-Min RATA 

02/25/2013 16,42 

G45-C4 

92240 

5el\+i1K. \ 5 ~ (' \i(..ru \ 

~~~ 

-:wiD 

End of Report , 02/25/2013 17 ,4 8 

G45-Cll G4S -C13 

TRACE 

ElIlJ;rolllllelllal Systems, Illc. 

Validation: All Available Data 

Group#-Channel# G45-CIO G45 - C6 G45-C7 G4S-C8 

Long Descrip. 

Short Descrip . 

Units 

G4 5-C2 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

s>Stk 02 5>NOx Mass 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

5>CO Mass 5>NOx Rate S,Stk NOXc S>Stk CDc S>Gas Flow 

Stk CDc Gas hscfh 

G45-C18 

5>NH3 Inj 

NH3Inj 

1b/hr 

0-200 

G45-C 

5>MW Lo 

MW Lo 

Range 

02/25/2013 16:42 

02/25/2013 16 :43 

02/25/ 2013 16 :44 

02/25/2013 16:45 

02/25/2013 16:46 

02/25/2013 16:47 

02/25/2013 16:48 

02/2 5/2013 16:49 

02/25/2013 16:50 

02/25/2013 1 6:51 

02/25/2013 16:52 

02/25/2013 16:53 

02/25/2013 16:54 

02/ 2 5/2013 16:55 

02/25/2013 16:56 

02/25/2013 16:57 

02/25/2013 16 :58 

02 / 25/2013 16:59 

02/25/2013 17:00 

02/25/2013 17:01 

02/25/2013 17:02 

02/25/2013 17:0) 

02/25/2013 17:04 

02/25/2013 17:05 

02/25/ 2013 17:06 

02/25/2013 17:07 

02/25/2013 17:08 

02/25/2013 17:09 

02/25/2013 17:10 

02/25/2013 17:11 

Date/Time Printed: 

1.2 

1.3 

1.3 

1.3 

1.3 

1.3 

1.3 

1.3 

1., 

1., 

1., 

1.4 

1.. 

1., 

1., 

1., 

1., 

1., 

1.' 

1., 

1.5 

1.5 

1.5 

1.5 

1.5 

1.6 

1.5 

1.5 

1.6 

1.5 

Stk 02 

, 

0-25 

13.91 

13.91 

13.90 

13.90 

13. 90 

13.89 

13. 88 

13.88 

13.88 

13.89 

13.89 

13.88 

13 .89 

13.89 

13.89 

13.89 

13.90 

13.89 

13.88 

13.88 

13.86 

13 .89 

13.88 

13 .86 

13.86 

13.89 

13.88 

13 .86 

13.87 

13.86 

02/25/2013 18,46 

NOx Mass 

1b/hr 

0 - 100 

2.94 

2.93 

2.94 

2.93 

2.94 

2.96 

2 .96 

2.97 

2.97 

2.96 

2.96 

2.97 

2.96 

2.96 

2.94 

2.95 

2.94 

2.95 

2.95 

2.95 

3.71 

3.67 

3.70 

3.72 

3.73 

3.70 

3.70 

3.71 

3.70 

3.71 

19140 

19108 

19136 

19080 

19139 

19195 

19207 

19224 

19258 

19213 

19238 

19232 

19189 

19200 

19117 

19145 

19084 

19141 

19140 

19144 

19188 

19069 

19196 

19239 

19281 

19190 

19214 

19187 

19178 

19193 

0. ' 

0.' 

0.' 

D.' 

0.' 

0.3 

0.3 

0.3 

0.3 

A.' 

0.4 

0.' 

0.' 

0.' 

A.' 

0.' 

0.' 

0.' 

0.8 

1.8 

3.3 

2.5 

1.8 

3.0 

6.0 

2.8 

2.3 

'.9 

1.9 

3.0 

CO Mass 

1b/hr 

0-100 

0.74 

0 .7 3 

0.74 

0.73 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.73 

0.74 

1. 48 

2.21 

4.4 5 

3.67 

2.22 

4.46 

8.20 

3.70 

2.96 

6.68 

2.96 

4.45 

NOx Rate 

Ib/mmBtu 

0-1 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

Stk NOXc 

ppm 

0 - 300 

1. 01 

1.10 

1.10 

1.10 

1.10 

1.09 

1. 09 

1. 09 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1. 26 

1. 26 

1.26 

1.26 

1. 26 

1. 35 

1. 26 

1. 26 

1. 34 

1. 26 

ppm hscfh 

0-1000 0 - 10000 

0.34 

0.34 

0.34 

0.34 

0.34 

0.25 

0.25 

0 . 25 

0.25 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.34 

0.67 

1. 51 

2.77 

2.10 

1.51 

2.51 

5.03 

2.36 

1. 93 

4.11 

1. 59 

2.51 

6999.6 

6987.6 

7008.0 

6987.6 

7009.2 

7039.8 

7054.2 

7 060.2 

7072.8 

7046.4 

7055.4 

7063.2 

7037.4 

7041.6 

7011.0 

7021.2 

6988.8 

7020.0 

7029.6 

7030.8 

7067.4 

6993.6 

7050.0 

7086.0 

7101.6 

7038.0 

7056.6 

7066.8 

7053.6 

7069.2 

148.2 

149.0 

149.5 

148 . 3 

149.5 

149.2 

148 . 7 

149.3 

148.2 

147.7 

147.5 

147. 7 

146.2 

147 . 3 

144. 7 

145.3 

145. 7 

145.7 

140.5 

135.0 

132.8 

131.8 

134.8 

133.0 

128.8 

134.7 

133.8 

129.2 

133.8 

131.3 

0-1 

80.! 

80. ! 

80. ! 

80.: 

80.1 

80. ! 

80 .. 

81.1 

81.1 

81.1 

81.1 

81.1 

80. : 

80 .. 

80. 

80. : 

80.1 

80.: 

80.1 

80 .. 

80. ! 

79. i 

80.1 

80. : 

80. : 

80. : 

80. : 

80. i 

80. ! 

80. i 

PagE 
Group#-Channel # 

Long Descrip . 

Short Desc r i p . 

Units 

Range 

02/25/2013 17:12 

02/25/2013 17:13 

02/25/2013 17:14 

02/25/2013 17:15 

02/25/2013 17:16 

02/25/2013 17:17 

02/25/2013 17:18 

02/25/2013 17:19 

02/25/2013 17:20 

02/25/2013 17:21 

02/25/2013 17:22 

02/25/2013 17:23 

02/25/2013 17:24 

02/25/2013 17:25 

02/25/2013 17:26 

02/25/2013 17:27 

02/25/2013 17:28 

02/25/2013 17:29 

02/25/2013 17:30 

02/25/2013 17:31 

02/25/2013 17:32 

02/25/2013 17:33 

02/25/2013 17:34 

02/25/2013 17:35 

02/25/2013 17:36 

02/25/2013 17:37 

02/25/2013 17:38 

02/25/2013 17:39 

02/25/2013 17:40 

02/25/2013 17:41 

02/25/2013 17:42 

02/25/2013 17:43 

02/25/2013 17:44 

02/25/2013 17:45 

02/25/2013 17:46 

02/25/2013 17:47 

02/25/2013 17:48 

Date/Time Printed: 

G45-C2 G45-C4 G45-C11 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

1.6 

1.6 

1.6 

1.6 

1.5 

1.6 

1.6 

1.6 

1.6 

1.7 

1.6 

1.7 

1.7 

1.7 

1.7 

1.8 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.8 

1.8 

1.7 

Stk 02 

• 

0-25 

13.86 

13.87 

13.87 

13.87 

13.86 

13.86 

13.86 

13.86 

13.85 

13.85 

13.85 

13.84 

13.84 

13.82 

13.82 

13.82 

13.84 

13.86 

13.85 

13.84 

13.84 

13.84 

13.85 

13.84 

13.84 

13.84 

13.85 

13.84 

13.84 

13.84 

13 . 84 

13.84 

13.84 

13.83 

13.83 

13.83 

13.83 

02/25/2013 18,46 

NOx Mass 

lb/hr 

0-100 

3.72 

3.72 

3.71 

3.71 

3.71 

3.72 

3.72 

3.73 

3.72 

3.73 

3.73 

3.74 

3.74 

3.75 

3.75 

4.50 

3.73 

3.72 

3.72 

3.73 

3.73 

3.73 

3.72 

3.74 

3.73 

3.74 

3.73 

3.74 

3.74 

3.73 

3.74 

3.75 

3.75 

3.75 

4.51 

4.51 

3.76 

G45-C20 

5 >StkFlow 

StkFlow 

ksefh 

0 - 300000 

19226 

19276 

19226 

19217 

19203 

19218 

19216 

19275 

19189 

19239 

19261 

19264 

19266 

19265 

19262 

19273 

19223 

19219 

19225 

19238 

19223 

19220 

19233 

19277 

19251 

19301 

19249 

19301 

19298 

19256 

19275 

19314 

19329 

19316 

19346 

19339 

19357 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

.3.6 

2.9 

2.3 

2.1 

2.7 

2.8 

2.1 

2.1 

2.3 

2.0 

2.7 

2.3 

2.1 

2.9 

2.7 

2.3 

2.3 

2.4 

2.3 

2.3 

2.0 

2.2 

2.3 

2.2 

2.0 

2.3 

2.1 

2.1 

2.3 

2.9 

3.1 

2.6 

2.6 

2.6 

2.8 

3.1 

2.9 

G45-C13 G45 - C10 G45-C6 

5>CO Mass 5>NOx Rate 5>Stk NOXe 

CO Mass 

lb/hr 

0-100 

5.20 

3.72 

2.97 

2.97 

3.71 

3.72 

2.97 

2.98 

2.97 

2.98 

3.73 

2.99 

2.99 

3.75 

3.75 

3.00 

2.98 

3.72 

2.98 

2.98 

2.98 

2.98 

2.98 

2.99 

2.99 

2.99 

2.98 

2.99 

2.99 

3.73 

4.49 

3.75 

3.75 

3.75 

3.76 

4.51 

3.76 

NOx Rate 

lb/mmBtu 

0 - 1 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

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 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.005 

Stk NOXe 

ppm 

0-300 

1. 34 

1. 34 

1. 34 

1. 34 

1. 26 

1. 34 

1. 34 

1. 34 

1. 34 

1. 42 

1. 34 

1. 42 

1. 42 

1. 42 

1.42 

1. 50 

1.42 

1.42 

1.42 

1.42 

1.42 

1. 42 

1.42 

1.42 

1. 42 

1. 42 

1. 42 

1. 42 

1. 42 

1. 42 

1.42 

1.42 

1.42 

1.42 

1. 50 

1. 50 

1.42 

G45-C7 G45-C8 

5>Stk COe 5>Gas Flow 

Stk COe Gas hsefh 

ppm hscfh 

0-1000 0-10000 

3.02 

2.43 

1. 93 

1. 76 

2.26 

2.35 

1. 76 

1. 76 

1.92 

1. 67 

2.26 

1. 92 

1. 7S 

2.42 

2.25 

1. 92 

1. 92 

2.01 

1. 92 

1. 92 

1. 67 

1. 84 

1. 92 

1. 84 

1. 67 

1. 92 

1. 76 

1. 75 

1. 92 

2.42 

2.59 

2.17 

2.17 

2.17 

2.34 

2.59 

2 . 42 

7081. 2 

7089.6 

7071.0 

7068.0 

7072.8 

7078.2 

7077.6 

7099.2 

7077.6 

7096.2 

7104.0 

7115.4 

7116.0 

7135.8 

7134.6 

7138.8 

7100.4 

7078.8 

7090.8 

7105.8 

7100.4 

7099.2 

7093.8 

7120.2 

7110.6 

7129.2 

7099.8 

7129.2 

7128.0 

7112.4 

7119.6 

7134.0 

7139.4 

7144.8 

7155.6 

7153.2 

7159.8 

G45-C18 

5>NH3 Inj 

NH3Inj 

lb/hr 

0 - 200 

132.2 

132.3 

133.5 

132.8 

132.3 

132.3 

134.2 

133.8 

133.2 

134.0 

133.3 

133.7 

135.2 

131. 0 

132.5 

133.5 

132. S 

133.0 

132.0 

133.3 

133.0 

133.2 

131.7 

133.7 

132.2 

134.5 

133.7 

133.0 

134.0 

132.2 

132.5 

132.8 

132.7 

131.8 

132.3 

132.2 

133.0 

S>Summary - I-Min RATA - Continued 

G45-C 

5>MW Lo 

MW La 

0-1 

80 . ~ 

81.1 

81.1 

80 .. 

80.! 

80. : 

80. 

81.1 

80. ! 

81.1 

80. : 

81.1 

81.1 

81.: 

81.1 

81.1 

80.! 

80.: 

80.! 

80 .. 

81.1 

80 .. 

80 . . 

81.1 

81.1 

81. . 

80. ! 

81.1 

81.1 

80. : 

81.1 

80. : 

81.: 

81.1 

81. . 

81.: 

81.: 

PagE 
Period Average = 1.6 13 . 8 6 3. S3 19223 2.0 2.78 0.005 1. 31 1. 65 7077.7 137.0 80.6 

Period Max Value 1.8 13.91 4.51 19357 6.0 8.20 0.00 6 1. 50 5.03 7159.8 149.5 81. 

Period Min Value 1.2 13 .82 2.93 19069 0.3 0.73 0 . 004 1. 0 1 0.25 6987.6 128.8 79. 

Period Totals = 1. 0440E+2 9.2878E+2 2.3648E+2 1.287 9E+6 1.3220E+2 1.8616E+2 3.1800E-1 8.7510E+1 1.1067E+2 4.7420E+5 9 . 1763E+3 5.4056E+ 

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 

Source : TUrbine 5 

Data Group : 

Report Name: 

Start of Report : 

5>1-Min Cales 

S>Summary - I-Min RATA 

02/25/2013 18,07 

5eA,'N-\ ~ 

1-'7'1# C-p \~1A14.{. z.. 

~ rA- (2y.Y\ {o 

End of Report, 02/25/2013 19,14 

G45-C4 G45-Cll G45-C20 G45-C3 G45 - C13 

TRACE 

Environmenta l S y stellls, Inc. 

validation: All Available Data 

Group#-Channel# G45 - CIO G45-C6 G45-C7 G45 - C8 G45-CIB G4S-C 

Long Descrip. 

Short Descrip. 

Units 

G45-C2 

S>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 5>StkFlow 5>Stk CO 5>CO Mass S:>NOx Rate 5>Stk NOXc S>Stk CDc 5>Gas Flow 5>NH3 Inj 5>MW La 

Range 

02/25/2013 18;07 

02/25/2013 18:08 

02/25/2013 18:09 

02/25/2013 18:10 

02/25/2013 18;11 

02/25/2013 18:12 

02/25/2013 18:13 

02/25/2013 18:14 

02/25/2013 18:15 

02/25/2013 18:16 

02/25/2013 18:17 

02/25/2013 18:18 

02/25/2013 18:19 

02 /25/2013 18:20 

02/25/2013 18:21 

02/25/ 2013 18:22 

02/25/2013 18:23 

02/25/2013 18:24 

02/25/2013 18:25 

02/25/2013 18:26 

02/25/2013 18:27 

02/25/2013 18:28 

02/25/201 3 18:29 

02/25/2013 18:30 

02/25/2013 18:31 

02/25/2013 18:32 

02/25/2013 18:33 

02/25/2013 1 8:34 

02/2 5/2 013 18:35 

02/25/2013 18:36 

Date/Time Printed: 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.6 

1.6 

1.7 

1.7 

1.7 

1.7 

1.6 

1.7 

1.7 

1.7 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.8 

1.7 

1.8 

1.7 

1.8 

1.8 

1.8 

1.8 

Stk 02 

• 

0-25 

13.86 

13 . 87 

13 . 87 

13.87 

13 .87 

13.88 

13.87 

13.87 

13.87 

13 . 87 

13 . 86 

13 . 87 

13 . 88 

13. 8 8 

13.87 

13.88 

13.88 

13.88 

13 . 89 

13.88 

13.89 

13 . 88 

13.88 

13.88 

13 . 88 

13 . 88 

13 . 88 

13 . 89 

13. 8 8 

13. 8 9 

02/25/2013 20,45 

NOx Mass 

Ib/hr 

0-100 

3.72 

3.72 

3.71 

3.71 

3.71 

3.70 

3.71 

3.72 

3.70 

3.71 

3.72 

3.72 

3.72 

3.72 

3.73 

3.71 

4.47 

4.45 

3.70 

3.71 

3.71 

3.71 

4.46 

3.72 

4.47 

3.73 

4.47 

4.46 

4. 4 6 

4.47 

StkFlow 

kscfh 

0 -3 00000 

19237 

19258 

19226 

19203 

19226 

19196 

19196 

19242 

19170 

19221 

19228 

19289 

19281 

19312 

19302 

19251 

19302 

19250 

19231 

19240 

19256 

19220 

19268 

19300 

19300 

19328 

19309 

19316 

19268 

19334 

Stk CO 

ppm 

0-1000 

3.4 

2.8 

2.8 

2.3 

3.8 

3.3 

3.0 

4.2 

3.6 

3.9 

3. 4 

3.4 

4 . 1 

4.1 

5.3 

4.1 

3.7 

2.8 

3.4 

3.8 

3.2 

3.5 

3 . 0 

3.9 

3.6 

4.0 

3.7 

2.4 

3 . 6 

3.1 

CO Mass 

1b/hr 

0-100 

4.46 

3.72 

3.71 

2.97 

5.20 

4.44 

4.45 

5.94 

5.18 

5.20 

4.46 

4.47 

5 . 95 

5.96 

7.45 

5.94 

5.21 

3.71 

4.44 

5.19 

4.45 

5.19 

4.46 

5.21 

5.21 

5 . 96 

5.21 

3.72 

5.20 

4 . 4 7 

NOx Rate 

Ib/mmBtu 

0 -1 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.005 

0.005 

0.005 

0.005 

0.006 

0.005 

0.006 

0.005 

0.006 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0 - 300 

1.42 

1.43 

1. 43 

1.43 

1.43 

1. 43 

1. 34 

1. 34 

1. 43 

1.43 

1.42 

1.43 

1. 34 

1. 43 

1.43 

1.43 

1. 51 

1. 51 

1.43 

1.43 

1.43 

1.43 

1. 51 

1. 43 

1. 51 

1. 43 

1.51 

1. 51 

1. 51 

1. Sl 

Stk CDc Gas hscfh 

ppm hscfh 

0 - 1000 0-10000 

2.85 7085.4 

2.35 7083.0 

2.35 7071.0 

1.93 7062.6 

3.19 7071.0 

2.77 7050.0 

2.52 7060.2 

3 . 52 7077.0 

3 . 02 7050.6 

3 . 27 7069.2 

2 . 85 7081.8 

2.85 

3. 45 

3 . 45 

4.45 

3.45 

3 . 11 

2.35 

2 . 86 

3.19 

2.69 

2.94 

2.52 

3 . 28 

3.03 

3 . 36 

3.11 

2.02 

3 . 03 

2.61 

7094.4 

7081.2 

7092.6 

7099.2 

7070.4 

7089.0 

7069.8 

7053.0 

7066 . 2 

7062.0 

7059.0 

7076. 4 

7088.4 

7088.4 

7098.6 

7091.4 

708 4 .2 

7076.4 

7090.8 

NH3Inj 

lb/hr 

0 - 200 

130.7 

130.8 

129.7 

130.5 

129.8 

128.8 

129.2 

128.0 

127.2 

128.0 

128.8 

129.3 

128.5 

127.7 

127.3 

127.7 

126.8 

129.0 

128.2 

127.7 

127.5 

128.0 

128.0 

128.0 

129.0 

128.2 

128.8 

129.2 

127.2 

129.0 

MW La 

0-1 

80.1 

80.1 

80.1 

80.1 

80. 1 

79. 

79. ' 

80. I 

80. 1 

80.1 

80 .. 

80. 

80. : 

80 . . 

80.1 

80.1 

80,1 

80. I 

79 . . 

80 .. 

79. : 

80, 1 

80.1 

80 .. 

80.1 

80, ' 

80 .. 

80. : 

80. : 

80 .. 

pagE 
Group#-Channel# 

Long Descrip . 

Sho rt Des crip. 

Uni ts 

Range 

02/25/2013 18:37 

02/25/2013 18:38 

02/25/2013 18:39 

02/25/2013 18:40 

02/25/2013 18:41 

02/25/2013 18:42 

02/25/2013 18:43 

02/25/2013 18:44 

02/25/2013 18;45 

02/25/2013 18;46 

02/25/2013 18;47 

02/25/2013 18:48 

02/25/2013 18;49 

02/25/2013 18;50 

02/25/2013 18:51 

02/25/2013 18;52 

02/25/2013 18:53 

02/25/2013 18:54 

02/25/2013 18:55 

02/25/2013 18:56 

02/25/2013 18;57 

02/25/2013 18:58 

02/25/2013 18:59 

02/25/2013 19:00 

02/25/2013 19:01 

02/25/2013 19:02 

02/25/2013 19:03 

02/25/2013 19;04 

02/25/2013 19;05 

02/25/2013 19:06 

02/25/2013 19:07 

02/25/2013 19:08 

02/25/2013 19:09 

02/25/2013 19:10 

02/25/2013 19:11 

02/25/2013 19:12 

02/25/2013 19;13 

02/25/2013 19:14 

Date/Time Printed: 

G45-C2 G45-C4 G45 -C11 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

1.8 

1.8 

1.8 

1.8 

1.. 

1.8 

1.. 

1., 

1.. 

2.0 

1.. 

1.. 

1.' 

1.8 

1.8 

1.7 

1.8 

1.8 

1.8 

1.8 

1.. 

1.8 

1.8 

1.7 

1.8 

1.7 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

Stk 02 

• 

0-25 

13 . 89 

13.87 

13.88 

13.87 

13.86 

13.87 

13.86 

13.86 

13.87 

13.88 

13.87 

13.87 

13.88 

13.88 

13.89 

13.90 

13.89 

13.89 

13 .89 

13.89 

13.90 

13.89 

13.90 

13.89 

13.89 

13.88 

13.88 

13.89 

13.89 

13.89 

13.89 

13.90 

13.90 

13.89 

13.89 

13.88 

13.89 

13 . 88 

02/25/2013 20,45 

NOx Mass 

1b/hr 

0-100 

4.46 

4.48 

4.48 

4.49 

4.50 

4.49 

4.50 

4.50 

4.50 

4.50 

4.50 

4.49 

4.49 

4.47 

4.45 

3.70 

4.45 

4.44 

4.45 

4.45 

4.44 

4.45 

4.45 

3.70 

4.46 

3.72 

3.72 

4.46 

4.46 

4.46 

4.45 

4.45 

4.45 

4.46 

4.46 

4.48 

4.47 

4.47 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

19313 

19332 

19346 

19385 

19386 

19387 

19407 

19389 

19418 

19434 

19439 

19392 

19392 

19326 

19277 

19224 

19248 

19222 

19240 

19269 

19260 

19267 

19274 

19240 

19302 

19302 

19310 

19318 

19323 

19307 

19272 

19296 

19296 

19310 

19318 

1 9344 

19325 

19333 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

3.5 

4.4 

3.6 

4.2 

3.4 

3.7 

4.2 

2.6 

3.2 

3.0 

3.2 

2.8 

3.4 

4.2 

4.0 

4.1 

3.0 

3.7 

3.5 

3.8 

3.0 

2.6 

3.2 

3.0 

3.3 

4.1 

4.3 

4.7 

3.6 

4.0 

4.0 

2.6 

3.2 

3.4 

3.4 

3.1 

3.6 

3.4 

G45 -C13 G45-C10 G45-C6 

5>CO Mass 5>NOx Rate 5>Stk NOXc 

CO Mass 

1b/hr 

0-100 

5.21 

5.97 

5.22 

5.99 

4.50 

5.24 

6.00 

3.75 

4.50 

4.50 

4.50 

3.74 

4.49 

5.96 

5.94 

5.91 

4.45 

5.18 

5.19 

5.19 

4.44 

3.71 

4.45 

4.45 

4.46 

5.95 

5.96 

6.70 

5.21 

5.95 

5.94 

3.71 

4.45 

4.46 

4.46 

4.48 

5.21 

4.47 

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 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

stk NOXc 

ppm 

0-300 

1. 51 

1. 51 

1. 51 

1. 51 

1.59 

1. 51 

1. 59 

1. 59 

1. 59 

1. 68 

1. 59 

1. 59 

1. 60 

1. 51 

1. 51 

1.43 

1. 51 

1. 51 

1. 51 

1. 51 

1. 60 

1. 51 

1. 52 

1.43 

1. 51 

1.43 

1.43 

1. 51 

1. 51 

1. 51 

1. 51 

1. 52 

1. 52 

1.51 

1. 51 

1. 51 

1. 51 

1. 51 

G45-C7 G45-C8 

5>Stk COc 5>Gas Flow 

Stk CDc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

2.95 

3.69 

3.03 

3.52 

2.85 

3.11 

3.52 

2.18 

2.69 

2.52 

2.69 

2.35 

2.86 

3.53 

3.37 

3.46 

2.52 

3.11 

2.95 

3.20 

2.53 

2.19 

2 . 70 

2.52 

2.78 

3.45 

3.61 

3.96 

3.03 

3.37 

3 . 37 

2.19 

2.70 

2.86 

2.86 

2.61 

3 . 03 

2.86 

7083.0 

7110.0 

7105.2 

7129.8 

7140.0 

7130.4 

7147.8 

7141.2 

7141.8 

7137.6 

7149.6 

7132.2 

7122.0 

7098.0 

7069.8 

7040.4 

7059.0 

7049.4 

7056.0 

7066.8 

7053.6 

7066.2 

7058.4 

7056.0 

7078.8 

7089.0 

7092.0 

7084.8 

7086.6 

7080.6 

7068.0 

7066.8 

7066.8 

7081. 8 

7084.8 

7104.6 

7087.2 

7100.4 

G45 -C18 

5>NH3 Inj 

NH3Inj 

1b/hr 

0-200 

128.0 

127.7 

128.8 

128.0 

130.0 

129.8 

129.5 

130.0 

129.8 

129.3 

129.5 

131. 0 

128.8 

128.5 

128.0 

127.5 

129.3 

128.0 

127.7 

129. 0 

129.3 

131.0 

130.0 

130.2 

128.2 

129.7 

128.5 

127.7 

128.8 

129.3 

128.0 

129.7 

129.3 

127.8 

128.8 

129.0 

130.0 

128.8 

S>Summary - I-Min RATA - Continued 

G45-C 

5>MW Lo 

MW Lo 

0-1 

80.: 

80 .. 

80. 

81. I 

81.1 

81. I 

81.1 

81.( 

81.( 

81.· 

81. ~ 

81.1 

81. 

80 . . 

80. : 

79. ! 

80.1 

79 .. 

79.l 

80.1 

80. ( 

80. ( 

80.1 

80.1 

80. : 

80. ! 

80.: 

80. : 

80.: 

80.: 

7'. 

80 .. 

80 .. 

80. 

80. 

80 .. 

80 .. 

80 . ~ 

PagE 
Period Average = 1.8 13.88 4.18 19294 3.5 4.96 0.006 1.49 2.96 7085.4 128.8 80.2 

Period Max Value 2.0 13.90 4.50 19439 5.3 7.45 0.006 1. 68 4.45 7149.6 131. 0 81. 

Period Min Value 1.6 1 3.86 3.70 19170 2.3 2.97 0.005 1.34 1. 93 7040.4 126.8 79. 

Period Totals = 1.2050E+2 9.4388E+2 2.8422E+2 1.3119E+6 2.3920E+2 3.3702E+2 3.8200E-l 1.0117E+2 2.0109E+2 4.8180E+5 8.7589E+3 5.4594E+ 

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 

5Q.v.41 A( \ ? 

Desert Hot Springs, CA 92240 (2Jr11\- ~p. \ 

So urce : Turbine 5 100'7, (~p\'llMUt Data Group : 5>1 - Min Cales 

Report Name: 

Start of Report : 

S>Summary - l - Min RATA 

02/25/2013 11,35 

G45-C4 

End of Report , 02/25/2013 12,43 

G45-Cll G45 - C13 

TRACE 

\ Ellvironmental Systems, [IIC. 

validation: All Available Data 

Group#-Channel# G45-CIO G45 -C6 G45-C7 G45-CB G45-C18 

Long Descrip . 

Short Descrip . 

Units 

G45-C2 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

G45-C20 

S>StkFlow 

StkFlow 

kscfh 

G4S - C3 

s>Stk CO 

Stk CO 

5>CO Mass S>NOx Rate s>Stk NOXc S>Stk CDc S>Gas Flow 5>NH3 Inj 

G45-C 

5>MW Lo 

MW Lo 

Range 

02/25/2013 11:35 

02/25/2013 11:36 

02/25/2013 11:37 

02/25/2013 11:38 

02/25/2013 11:39 

02/25/2013 11:40 

02/25/2013 11:41 

02/25/2013 11:42 

02/25/2013 11:43 

02/25/2013 11:44 

02/25/ 2013 11:45 

02/25/2013 11:46 

02/25/2013 11: 4 7 

02/25/2013 11:48 

02/25/2013 11:49 

02/25/2013 11:50 

02/25/2013 11:51 

02/25/2013 11:52 

02/25/2013 11:53 

02/25/2013 11:54 

02/25/2013 11;55 

02/25/2013 11:56 

02/25/2013 11:57 

02/25/2013 11:58 

02/25/2013 11:59 

02/25/2013 12:00 

02/25/2013 12:01 

02/25/2013 12:02 

02/25/ 2 013 12:03 

02/25/2013 12:04 

Date/Time Printed: 

l.9 

l.9 

l.9 

l.9 

l.9 

l.9 

l.9 

1.9 

1.9 

1.9 

l.9 

l.9 

1.9 

1.9 

1.9 

1.9 

1.9 

l.9 

1.9 

1.9 

l.9 

1.9 

1.9 

1.9 

1.9 

1.9 

2.7 

2.0 

1.9 

l.9 

Stk 02 

% 

0-25 

13 .47 

13 . 4 7 

13 .47 

13 .46 

13 .46 

13 .46 

13 . 47 

13 .46 

13. 4 6 

13 .46 

13 .46 

13 .46 

13 .45 

13 .45 

13 .46 

13 .46 

13 .46 

13 . 46 

13.46 

13 . 47 

13 . 4 6 

13.46 

13 . 4 5 

13 .45 

13.45 

13 .46 

13 .46 

13.45 

13 . 4 6 

13 .46 

02/25/2013 12,55 

NOx Mass 

Ib/hr 

0-100 

5.51 

5.51 

5.51 

5.51 

5.52 

5.51 

5.51 

5.52 

5.51 

5.52 

5.51 

5.51 

5.52 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.50 

7.34 

5.51 

5.51 

5.50 

0-300000 

22511 

22508 

22503 

22487 

22490 

22471 

22509 

22490 

22487 

22498 

22487 

22478 

22460 

224 4 1 

22454 

22462 

22471 

22471 

22476 

22494 

22467 

22450 

22446 

224 44 

22444 

22447 

22454 

22424 

22450 

22441 

ppm 

0-1000 

2.' 

3.0 

2.' 

3.0 

3.7 

3.7 

3.5 

3 . ' 

3.6 

3.5 

3.5 

3.3 

3.9 

3.0 

2.9 

2.5 

2.5 

2.8 

2.9 

3.1 

2.7 

2.7 

2.5 

3.2 

3.2 

2.8 

2.9 

3.1 

2.9 

3.0 

CO Mass 

1b(hr 

0-100 

4.59 

4.59 

4.59 

4.60 

6.43 

6.43 

5.51 

6.43 

5.51 

5.52 

5.51 

5.51 

6.43 

4.59 

4.59 

3.67 

3.67 

4.59 

4 .59 

5.51 

4.59 

4.59 

3.67 

5.51 

5.51 

4.59 

4.59 

5.51 

4.59 

4.59 

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 

0.006 

0.006 

0.006 

0.006 

0 .006 

0.006 

0.006 

0.006 

0.006 

0.008 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0-300 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1.51 

1. 51 

1. 51 

1. 51 

1. 50 

1. 50 

1. 51 

1.51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1.50 

1. 50 

1. 50 

1. 51 

2.14 

1. 58 

1. 51 

1. 51 

Stk CDc Gas hscfh NH3Inj 

ppm 

0-1000 

2.22 

2.38 

2.22 

2.38 

2.93 

2.93 

2.78 

3.01 

2.85 

2.78 

2.78 

2.62 

3 . 09 

2 . 38 

2.30 

1. 98 

1. 98 

2.22 

2.30 

2.46 

2.14 

2.14 

1. 98 

2.53 

2.53 

2.22 

2.30 

2.46 

2.30 

2.38 

hscfh 

0-10000 

8750.4 

8749 . 2 

8747.4 

8752.8 

8754.0 

8746.8 

8749.8 

8754.0 

8752.8 

8757.0 

8752.8 

8749.2 

8754.0 

8746.8 

8740.2 

8743.2 

8746.8 

8746.8 

8748 . 6 

8743.8 

8745.0 

8738.4 

8748.6 

8748.0 

8748.0 

8737.2 

8740.2 

8740.2 

8738 . 4 

8734.8 

lb/hr 

0-200 

196.2 

196.2 

195.8 

195.8 

195.0 

195.7 

195.7 

163.8 

196.0 

196 .5 

195.3 

196.3 

194.3 

196 . 0 

196.5 

196.2 

196.3 

197.0 

198.0 

196.0 

196.0 

197.3 

195 . 7 

196.5 

196.5 

179.2 

189.2 

196.2 

196.3 

196.5 

0-1 

105.: 

105. : 

105. : 

106.! 

106.! 

1 05.: 

106.4 

105. : 

106.1 

106.1 

105. : 

105. : 

106.1 

106.4 

106.! 

106.1 

106.1 

105. : 

106.1 

105. : 

106.1 

1 05. : 

106.1 

105. : 

105.: 

106.4 

105. : 

105 .. 

106.1 

106.1 

pag£ 
Group#-Channel# 

Long Descrip . 

Sho rt De scrip. 

Units 

Range 

02/25/2013 12:05 

02/25/2013 12:06 

02/25/2013 12:07 

02/25/2013 12:08 

02/25/2013 12:09 

02/25/2013 12:10 

02/25/2013 12:11 

02/25/2013 12:12 

02/25/2013 12:13 

02/25/2013 12:14 

02/25/2013 12:15 

02/25/2013 12:16 

02/25/2013 12:17 

02/25/2013 12:18 

02/25/2013 12:19 

02 /25/ 2 013 12:20 

02/25/2013 12:21 

02/25/2013 12:22 

02/25/2013 12:23 

02/25/2013 12:24 

02/25/2013 12:25 

02/25/2013 12:26 

02/25/2013 12:27 

02/25/2013 12:28 

02/25/2013 12:29 

02/25/2013 12:30 

02/25/2013 12:31 

02/25/2013 12:32 

02/25/2013 12:33 

02/25/2013 12:34 

02/25/2 013 12:35 

02/25/ 2 013 12:36 

02/25/2013 12:37 

02/25/2013 12:38 

02/25/2013 12:39 

02/25/2013 12:40 

02/25/2013 12:41 

02/25/2013 12:42 

02/25/ 2 013 12:43 

Date/Time Printed: 

G45-C2 G45 - C4 G45-C11 G45-C20 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 5>StkFlow 

1.9 

1.9 

1.9 

1.9 

1 .9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

Stk 02 

t 

0-25 

13 .4 5 

13 . 4 6 

13 . 46 

13 .45 

13 .45 

13 .45 

13 .45 

13 .4 5 

13 . 4 5 

13 .45 

13 .45 

13.44 

13.44 

13. 44 

13 .44 

13. 44 

13 . 44 

13 .45 

13 .45 

13 .45 

13.45 

13.44 

13. 44 

13. 44 

13. 4 3 

13.44 

13 .44 

13 .44 

13 . 4 4 

13 . 44 

13 .44 

13 . 4 4 

13. 44 

13 .44 

13 .43 

13 .43 

13 . 44 

13 .44 

13 .44 

02/25/2013 12,55 

NOx Mass 

1b/hr 

0-100 

5.50 

5.51 

5.50 

5.50 

5.51 

5.51 

5.51 

5.51 

5.50 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.52 

5.51 

5.51 

5.51 

5.51 

5.52 

5.51 

5.51 

5.51 

5.51 

5.S1 

5.51 

5.51 

5.51 

5.51 

5.52 

5.51 

5.51 

5.51 

5.51 

StkFlow 

kscfh 

0-300000 

22 4 15 

22453 

22436 

22415 

22430 

22427 

22432 

224 40 

22 415 

22424 

22424 

22408 

22405 

22420 

2 2410 

22 420 

22 4 02 

22443 

2243 4 

22463 

22430 

22411 

22422 

22 420 

22407 

22396 

22420 

22402 

22408 

22422 

224 25 

22419 

22423 

22405 

22404 

22395 

22423 

2 2399 

2 2417 

G45-C3 G45 -C13 G45-C10 G45 -C6 G45-C7 G45-C8 G45-C18 G45-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXc 5>Stk COe 5>Gas Flow 5>NH3 Inj 5>MW Lo 

Stk CO 

ppm 

0-1000 

3.6 

3.0 

3.1 

2 .• 

3.2 

3.' 

3.1 

3.1 

2.9 

3.2 

3.6 

3.1 

3.2 

3.' 

3.' 

3.7 

3.7 

3.3 

3.1 

3.2 

3.6 

3.5 

3 .• 

3.3 

3.6 

3.2 

3.5 

3.6 

3.0 

3.2 

3.6 

3.1 

3.6 

3.6 

3.2 

3.1 

2 .• 

3.0 

2.5 

CO Mass 

1b/hr 

0 - 100 

5.50 

4.59 

5.50 

4.59 

5.51 

5.51 

5.51 

5.5 1 

4.59 

5.51 

5.S1 

4.59 

5.51 

5.51 

5.51 

6. 43 

6. 43 

5.51 

5.51 

5.52 

5.51 

5.51 

6.43 

5.51 

5.52 

5.51 

5.51 

5.51 

4.59 

5.51 

5.51 

4.59 

5.51 

5.51 

5.52 

4.60 

4.59 

4 .59 

3.67 

NOx Rate 

Ib/mmBtu 

0-1 

0 . 00 6 

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 

0.00 6 

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 

0.00 6 

0.00 6 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0 . 006 

0.00 6 

Stk NOXe 

ppm 

0-300 

1. SO 

1. 51 

1. 51 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1.50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

Stk COe Gas 

ppm 

hsefh 

hsefh 

0-1000 

2 . 85 

2 .38 

2.46 

2.22 

2.53 

2.69 

2 .4 6 

2 .46 

2.30 

2.53 

2.85 

2.45 

2.53 

2.69 

2. 6 9 

2.93 

2.93 

2.61 

2.46 

2.53 

2.85 

2.77 

3.01 

2.61 

2.84 

2.53 

2.77 

2.85 

2.37 

2.53 

2. 85 

2 . 45 

2.85 

2.85 

2.53 

2.45 

2.21 

2. 37 

1. 98 

0-10000 

8736.6 

8739.6 

8733.0 

8736.6 

8742.6 

8741. 4 

8743.2 

8746.2 

8736.6 

8740.2 

8740.2 

8745.6 

8744.4 

8750.4 

8746.2 

8750.4 

8743.2 

8747.4 

8743 . 8 

8755.2 

8742.6 

8746.8 

8751 . 0 

8750.4 

8757.0 

8740.8 

8750.4 

8743.2 

8745.6 

8751.0 

8752 . 2 

8749.8 

8751.6 

8744.4 

8755.8 

8752.2 

8751 . 6 

8742 . 0 

8749.2 

NH3Inj 

1b/hr 

0-200 

195 . 3 

197.3 

197.0 

197.3 

197. 0 

195.7 

197.2 

197.3 

196.7 

196.3 

195.7 

195.7 

195.8 

195.7 

195.2 

1 96 .5 

196.8 

196.2 

195.7 

197 .5 

196.5 

196.3 

195.3 

195.8 

194.5 

195.5 

195.3 

194.2 

196.3 

195.7 

196.0 

196.2 

195.7 

195.2 

195.7 

194.7 

196.0 

1 96.5 

196.0 

S>Summary - I-Min RATA - Continued 

MW Lo 

0-1 

105. : 

106.1 

105 .. 

106.1 

105. : 

105. : 

106 . 1 

106.1 

106 . 1 

106.1 

105. 

106.4 

106.1 

106.1 

106.1 

105. : 

105. : 

105. : 

106.1 

106.1 

106.1 

106.1 

106 . 1 

106.1 

106. t 

106.1 

105. : 

106.4 

105. : 

106.1 

10 6 .1 

106.1 

105. : 

106.1 

105. 

106.1 

106.1 

106.1 

105. 

Pagf 
Period Average ~ 1.9 13 .45 5.54 22442 3.2 5.19 0.006 1. 51 2.53 8746.3 195.3 105.9 

Period Max Value 2.7 13.47 7.34 22511 3.9 6.43 0.008 2.14 3.09 8757.0 198.0 106. 

Period Min value 1.9 13 .43 5.50 22395 2.S 3.67 0.006 1. SO l. 98 8733.0 163.8 105. 

Period Totals = l.3200E+2 9.2809E+2 3.8203E+2 1.5484E+6 2.2070E+2 3.5815E+2 4.1600E-1 1.0447E+2 1.7479E+2 6.0349E+5 1. 34 73E+4 7.3084E+ 

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

Company : CPV Sentinel, LLC 

62575 Powerline Road 

De-sert Hot Springs, CA 92240 

~A+;1o\L1 $ 

fZAn\ ~I'\ Z 

IWL C ''"It riltt1c.t t. 

Source: 

Data Group : 

Report Name : 

Start of Report : 

Turbine 5 

S>l-Min Cales 

s>Summary - I-Min RATA 

02/25/2013 13,04 

G45-C4 

End of Report, 02/25/2013 14,17 

G4S-Cll G45-C13 

TRACE 

Environmental Systems, Inc. 

validation: All Available Data 

Group#-Channel# G45-CIO G45-C6 G45-C7 G45-Ca 

Long Descrip . 

Short Descrip . 

units 

G45-C2 

S>Stk NOx 

Stk NOx 

ppm 

0-150 

S>Stk 02 5>NOx Mass 

G45-C20 

S>StkFlow 

StkFlow 

kscfh 

0-300000 

G4S-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

5>CO Mass 5>NOx Rate 5>Stk NOXc 5>Stk CDc S>Gas Flow 

Stk CDc Gas hscfh 

G45-C18 

5>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

G45-C 

5>MW Lo 

MW Lo 

Range 

02/25/2013 13:04 

02/25/2013 13:05 

02/25/2013 13:06 

02/25/2013 13:07 

02/25/2013 13:08 

02/25/2013 13:09 

02/25/2013 13:10 

02/25/2013 13:11 

02/25/2013 13:12 

02/25/2013 13:13 

02/25/2013 13:14 

02/25/2013 13:15 

02/25/ 2013 13:16 

02/25/2013 13:17 

02/25/ 2013 13:18 

02/25/2013 13:19 

02/25/2013 13:20 

02/25/2013 13:21 

02/25/2013 13:22 

02/25/2013 13:23 

02/25/2013 13:24 

02/25/2013 13:25 

02/25/2013 13:26 

02/25/2013 13:27 

02/25/2013 13:28 

02/25/2013 13:29 

02/25/2013 13:30 

02/25/2013 13:31 

02/25/2 013 13:32 

02/ 25/2013 13:33 

Date/Time Printed: 

1., 

1.. 

1.. 

1.. 

1.9 

1.. 

1.9 

1.9 

1.. 

1.9 

1.. 

1.9 

1.9 

1.9 

1.9 

1.. 

1.9 

1.. 

1.. 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

2.6 

2.3 

Stk 02 

% 

0-25 

13.43 

13 .43 

13 .43 

13 . 4 3 

13 .4 3 

13 . 4 2 

13 . 43 

13 .4 3 

13 .43 

13.43 

13. 42 

13 . 4 2 

13 . 41 

13 .42 

13 .42 

13 .4 3 

13 .42 

13.42 

13.42 

13 . 4 1 

13 . 4 2 

13 .4 2 

13 .4 2 

13 .41 

13 .4 1 

13 .41 

13 .41 

13. 41 

13 . 4 1 

13. 4 0 

02/25/2013 14,59 

NOx Mass 

Ib/hr 

0-100 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.50 

5.50 

5.50 

5.50 

5.51 

5.51 

5.50 

5.50 

5.50 

5.50 

5.51 

5.50 

5.50 

5.50 

5.50 

5.50 

5.51 

5.50 

5.50 

5.50 

5.50 

7.33 

6.42 

22367 

22384 

22373 

22370 

2 2364 

22354 

22358 

22355 

22343 

22347 

22325 

22334 

22 305 

22 305 

22314 

22349 

22316 

22330 

22324 

22 2 89 

2 2308 

2 2304 

22324 

22312 

22291 

22285 

22274 

22271 

22283 

22255 

2.' 

2.' 

2.' 

2.6 

2.8 

3.1 

2.5 

2.4 

2.5 

2.3 

2.7 

2.5 

2.4 

2.5 

2.' 

2.3 

2.' 

2.5 

2.8 

2.8 

2.2 

2.5 

2.1 

2.7 

3.1 

2.6 

2 . ' 

2.5 

2 . ' 

2.8 

CO Mass 

1b/hr 

0-100 

4.59 

4.59 

4.59 

4.59 

4.59 

4.59 

3 . 67 

3.67 

3.67 

3.67 

4.59 

3.67 

3.67 

3.67 

3.67 

3.67 

3.67 

3.67 

4.59 

4.59 

3.67 

3.67 

3.67 

4.59 

4.59 

4.58 

4.58 

3.67 

4.58 

4.58 

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 

0.00 6 

0.006 

0.006 

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 

0.006 

0.00 8 

0.007 

Stk NOXc 

ppm 

0 - 300 

1. 50 

1. 50 

1.50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. SO 

1. 50 

1. 50 

1. 50 

1. 50 

1. SO 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

2.05 

1. 81 

ppm hscfh 

0-1000 0-10000 

2.29 

2.29 

2.29 

2.05 

2 . 21 

2 .45 

1. 97 

1. 90 

1. 97 

1.82 

2 .13 

1. 97 

1. 8 9 

1. 97 

1. 89 

1. 82 

1. 89 

1. 97 

2.21 

2.21 

1. 74 

1. 97 

1 66 

2 . 13 

2.44 

2.05 

2.28 

1. 97 

2. 28 

2.20 

8741.4 

8748.0 

8743.8 

8742.6 

8740.2 

8748.0 

8737.8 

8736.6 

8731.8 

8733.6 

8736.6 

8740.2 

8740.2 

8728.8 

8732.4 

8734.2 

8733.0 

8738.4 

8736.0 

8734.2 

8730.0 

8728.2 

8736.0 

8743.2 

8734.8 

8732.4 

8728.2 

8727.0 

8731. 8 

8732.4 

197.3 

196.3 

196.7 

196.8 

197.3 

196.8 

197.3 

196.3 

196.8 

198.7 

196.5 

196.5 

196.2 

197.7 

197.8 

198.3 

197.8 

196.8 

197.2 

197 . 2 

197.7 

198.3 

198.2 

197.0 

196.3 

197.7 

198.3 

1 97. 8 

1 6 5.3 

198 . 5 

0-1 

105. : 

105. : 

106.1 

106. t 

105. : 

106 . 1 

106.1 

106.1 

106.1 

105. : 

105.: 

106. t 

106.1 

106.1 

105. : 

105. : 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106. r 

106.1 

106.1 

106. ( 

pagf 
Group#-Channe l# 

Long Descri p. 

Short Descrip . 

units 

Range 

02/25/2013 13:34 

02/25/2013 13:35 

02/25/2013 13:36 

02/25/2013 13:37 

02/25/2013 13:38 

02/25/2013 13:39 

02/25/2013 13:40 

02/25/ 2 013 13:41 

02/25/2013 13:42 

02/25/2013 13:43 

02/25/2013 13:44 

02/25/2013 13:45 

02/25/2013 13:46 

02/25/2013 13:47 

02/25/2013 13:48 

02/25/2013 13:49 

02/25/2013 13:50 

02/25/2013 13:51 

02/25/2013 13:52 

02/25/2013 13:53 

02/25/2013 13:54 

02/25/2013 13:55 

02/25/2013 13:56 

02/25/2013 13:57 

02/25/2013 13:58 

02/25/2013 13:59 

02/25/2013 14:00 

02/25/2013 14:01 

02/25/2013 14:02 

02/25/2013 14:03 

02/25/2013 14:04 

02/25/2013 14:05 

02/25/2013 14:06 

02/25/2013 14:07 

02/25/2013 14:08 

02/25/2013 14:09 

02/25/2013 14:10 

02/25/2013 14:11 

02/25/2013 14:12 

02/25/2013 14:13 

Date/Time Printed: 

G45 -C2 G45-C4 G45-C11 G45-C20 

5>Stk NOx 

Stk NOx 

ppm 

0 -15 0 

5>Stk 02 5>NOx Mass 5>StkFlow 

1.9 

2.0 

1.9 

1.9 

2.2 

1.9 

1.9 

2.1 

2.0 

2.0 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

2.5 

2.2 

2.6 

2.2 

1.9 

1.9 

1.9 

1.9 

1.8 

1.9 

1.8 

1.8 

1.9 

1.9 

1.8 

1.9 

1.9 

1.9 

1.9 

1.9 

Stk 02 

• 

0-25 

13. 4 1 

13.41 

13.41 

13 . 41 

13 .41 

13 .41 

13 .40 

13 .40 

13 .41 

13 .41 

13 .41 

13 .40 

13 .40 

13.39 

13.39 

13 .4 1 

13 .41 

13.41 

13.40 

13 .41 

13 .41 

13 .41 

13 .4 0 

13 .41 

13.41 

13 .41 

13 .41 

13 .4 0 

13 .40 

13 .41 

13 .40 

13.40 

13 .40 

13 .40 

13.40 

13 .39 

13 .39 

13.40 

13 . 4 1 

13 .40 

02/25/2013 14,59 

NOx Mass 

lb/hr 

0-100 

5.50 

5.50 

5.50 

5.51 

5.50 

5.50 

5.51 

5.51 

5.51 

5.50 

5.50 

5.51 

5.51 

4.59 

4.59 

5.50 

5 . 51 

5.51 

5.50 

5 . 51 

6.43 

5.52 

7.35 

5.51 

5.51 

5.51 

5.51 

5.52 

4.60 

5.51 

4.60 

4.60 

5.51 

5.52 

4.60 

4.60 

4.59 

5.51 

5.52 

5.52 

StkFlow 

kscfh 

0-300000 

22282 

222 77 

22291 

22323 

22295 

22289 

22272 

222 87 

22315 

22297 

22280 

22292 

22276 

22259 

22267 

22279 

22306 

22301 

22258 

22329 

22334 

22340 

22296 

22331 

22334 

22321 

22324 

22312 

22308 

22324 

22310 

22305 

22305 

22310 

22305 

22291 

22274 

22293 

22340 

223 18 

G45-C3 G45-C13 G45-C10 G45-C6 G45-C7 G45 - C8 G45-C18 G45-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXc 5>Stk COc 5>Gas Flow 5>NH3 Inj 5>MW Lo 

Stk CO 

ppm 

0-1000 

2.4 

2.5 

2.3 

3.1 

2.8 

2.8 

2.6 

2.6 

3.3 

2.8 

2.8 

2.7 

2.9 

3.2 

3.1 

3.1 

2.8 

3.3 

2.9 

3.3 

3.8 

3.5 

3.6 

3.9 

3.9 

3.8 

3.6 

3.7 

3.6 

4.2 

4.1 

4.2 

4.0 

3.8 

4.1 

4.2 

4.4 

4.3 

4.0 

4.4 

CO Mass 

lb/hr 

0-100 

3.67 

3.67 

3.67 

4.59 

4.59 

4.59 

4.59 

4. 59 

5.51 

4.59 

4.58 

4.59 

4.59 

5.51 

4.59 

4.58 

4.59 

5.51 

4.59 

5.51 

6.43 

5.52 

5.51 

6.43 

6.43 

6.43 

5.51 

6 . 43 

5.51 

6.43 

6.43 

6.43 

6.43 

6.43 

6.43 

6.44 

7.35 

7.35 

6.43 

7.36 

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 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

0.006 

0.008 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.005 

0.005 

0.006 

0.006 

0.005 

0.005 

0.005 

0.006 

0.006 

0.00 6 

Stk NOXc 

ppm 

0 - 300 

1. 50 

1. 58 

1. 50 

1. SO 

1. 73 

1. 50 

1. 49 

1. 65 

1. 58 

1. 58 

1. SO 

1.49 

1.49 

1.49 

1.49 

1. SO 

1. 50 

1. SO 

1.49 

1. 50 

1. 97 

1. 73 

2.05 

1.73 

1. SO 

1. 50 

1. 50 

1.49 

1. 42 

1. 50 

1. 42 

1. 42 

1. 49 

1. 49 

1.42 

1.49 

1.49 

1.49 

1. 50 

1. 49 

Stk COc Gas 

ppm 

hscfh 

hscfh 

0-1000 

1. 89 

1. 97 

1. 81 

2.44 

2.21 

2.21 

2.05 

2.05 

2.60 

2.21 

2.21 

2.12 

2.28 

2.51 

2.44 

2.44 

2 . 21 

2.60 

2.28 

2.60 

2.99 

2.7G 

2.83 

3.07 

3.07 

2.99 

2.84 

2.91 

2.83 

3 .3 1 

3.23 

3.30 

3.15 

2.99 

3.23 

3.30 

3.46 

3 . 38 

3.15 

3.46 

0-10000 

8731.2 

8729.4 

8734.8 

8747.4 

8736.6 

8734.2 

8739.0 

8745.0 

8744.4 

8737.2 

8730.6 

8746.8 

8740.8 

8745 . 6 

8748.6 

8730.0 

8740.8 

8739.0 

8733.6 

8749.8 

8751.6 

8754.0 

8748.6 

8750.4 

8751. 6 

8746.8 

8748.0 

8754.6 

8753.4 

8748.0 

8754.0 

8752.2 

8752.2 

8754.0 

8752.2 

8758.2 

8751.6 

8747.4 

8754.0 

8757.0 

NH3Inj 

lb/hr 

0-200 

198.3 

197.8 

198.2 

199.0 

182.2 

200.0 

199.3 

190 . 3 

198.2 

199.3 

198.7 

198.0 

198.5 

198.0 

198.3 

163.8 

199.8 

165.7 

199.3 

165.5 

170.5 

199.8 

170.2 

200.0 

165.8 

199.0 

199.0 

200.0 

200.0 

198.8 

198.3 

198.7 

198.2 

198.7 

198.3 

197.2 

198.0 

164 . 3 

199.2 

197.7 

S>Summary - l-Min RATA - Continued 

MW Lo 

0-1 

106. ( 

105. : 

105.: 

105. : 

106. ( 

106. ( 

106.( 

106. ( 

106. ( 

106. ( 

105. 

106.( 

106.: 

106. ( 

106. ( 

106.( 

106 . ( 

106. ( 

106. ( 

106.( 

106. ( 

106. ( 

105. 

106. ( 

106. ( 

106. ( 

106.( 

lOG. ( 

106. ( 

105. : 

105 . : 

106. ( 

106. ( 

106. ( 

106. ( 

105. : 

105.: 

lOG .( 

106. ( 

105. : 

pagE 
Group#-Channel# G45-C2 G45-C4 G45-Cll G45-C20 G45-C3 G45-C13 G45-C10 G45-C6 G45-C7 G45-C8 G45-C18 G4S-C 

Long Descrip. 5>Stk NOx 5>Stk 02 5>NOx Mass S>StkFlow S>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXc S>Stk COc 5>Gas Flow 5>NH3 Inj 5>MW La 

Short Descrip. Stk NOx Stk 02 NOx Mass StkFlow Stk CO CO Mass NOx Rate Stk NOXc Stk CDc Gas hscfh NH3Inj MW Lo 

units ppm • 1b/hr kscfh ppm 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 0-200 0-1 

02/25/2013 14:14 1.9 13.41 5.51 22338 4.0 6.43 0.006 1. 50 3.15 8753.4 198.3 106. t 

02/25/2013 14;15 1.9 13.41 5.51 22331 3.7 6.43 0.006 1. 50 2.91 8750.4 198.5 105. : 

02/25/2013 14:16 1.9 13.40 5.52 22312 4.1 6.43 0.006 1.49 3.23 8754.6 197.5 106.1 

02/25/2013 14:17 1.9 13 .40 5.S1 22299 3.9 6.43 0.006 1.49 3.07 8749.8 199.7 106.1 

Period Average 1.9 13 .41 5.48 22311 3.1 5.00 0.006 1. 53 2.45 8742.1 194.3 105.9 

Period Max Value 2.6 13 .43 7.35 22384 4.4 7.36 0.008 2.05 3.46 8758.2 200.0 106. 

Period Min Value 1.8 13.39 4.59 22255 2.1 3.67 0.005 1. 42 1. 66 8727.0 163.8 105. 

Period Totals = 1.4400E+2 9.9239E+2 4.0572E+2 1.6510E+6 2.3060E+2 3.6999E+2 4.4200E-1 1. 1349E+2 1.8165E+2 6.4691E+5 1. 4381E+4 7.8406E+ 

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: 02/25/2013 14,59 S;:.Summary - 1-Min RATA - Continued Pagf 
Appendix 8.1.3 Sentinel Unit 5 PM Testing 

R521 0729 8·5 
Data Summary Report 

Company : CPV Sentinel, LLC 

62575 Powerline Road 

5 ty. nV\(.\ ~ 

Desert Hot Springs , CA 92240 Ljrflo PM Source: 

Data Group : 

Report Name : 

Start of Report : 

Turbine 5 

S>l-Min Cales 

S>Summary - I-Min RATA 

02/26/2013 08,30 

G45-C4 

End of Report , 02/26/2013 12,40 

G4S-Cll G45-C13 

TRACE 

EIII';rtmmental Systems, In c. 

Validation: All Available Data 

Group#-Channe l# G45-CIO G45-C6 G45-C7 G45-C8 

Long Descrip. 

Short Descrip. 

Units 

G45-C2 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

G45-C20 

5>StkF!ow 

StkFlow 

kscfh 

0-300000 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

5>CO Mass 5>NDx Rate s>Stk NOXc S>Stk CDc 5>Gas Flow 

Stk CDc Gas hscfh 

G45 -C18 

5>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

G45-C 

S,.MW Lo 

MW Lo 

Range 

02/26/2013 08:30 

02/26/2013 08:31 

02/26/2013 08:32 

02/26/2013 08:33 

02/26/2013 08:34 

02/26/2013 08,35 

02/2 6 /2013 08:36 

02/26/2013 08:37 

02/26/2013 08:38 

02/26/2013 08:39 

02/26/2013 08:40 

02/26/2013 08;41 

02/26/ 2013 08:42 

02/26/2013 08:43 

02/26/2013 08:44 

02/26/2013 08:45 

02/26/2013 08:46 

02/26/2013 08;47 

02/26/2013 08:48 

02/26/2013 08:49 

02/26/ 2 013 08:50 

02/26/ 2 013 08:51 

02/26/2013 08;52 

02/26/2013 08:53 

02/26/2013 08;54 

02/26/2013 08;55 

02/26/2013 08;56 

02/26/2013 08:57 

02/ 2 6/ 2 013 08:58 

02/26/2013 08:59 

Date/Time Printed: 

1.4 

1.4 

1.4 

1.4 

1.5 

1.5 

1.5 

1.4 

1.4 

1.5 

1.4 

1.5 

1.5 

1.6 

1.6 

1.6 

1.7 

1.7 

1.6 

1.7 

1.7 

1.8 

1.7 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.5 

Stk 02 

• 

0-25 

14 . 07 

14.06 

14.06 

14.07 

14. 08 

14.07 

14.06 

14.07 

14.06 

14.06 

14.07 

14.07 

14.06 

14 .06 

14.06 

14. OS 

14 . 05 

14.05 

14.05 

14.06 

1 4. 05 

14. OS 

14.05 

14.05 

14.03 

14.02 

14.03 

14.04 

14. 02 

14 . 03 

02/26/2013 12 , 55 

NOx Mass 

Ib/hr 

0-100 

2.24 

2.25 

2.25 

2.24 

2.80 

2.81 

2.81 

2.24 

2.25 

2.81 

2.24 

2.80 

2.81 

2.81 

2.80 

2.81 

2.81 

2.82 

2.82 

2.81 

2.82 

3.39 

2.82 

2.83 

3.41 

3.41 

3.40 

3.41 

3.42 

2.85 

14953 

14969 

14953 

14953 

1 4 953 

1 4 96 6 

1 4 976 

1 4 943 

14976 

14976 

14939 

14931 

14 964 

14936 

14916 

14922 

14936 

14963 

15003 

14954 

14 963 

15009 

15001 

15043 

15063 

15024 

15031 

15081 

15077 

15093 

0.2 

0.2 

0.1 

0.1 

0.2 

0.2 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0 . 1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.0 

0.0 

0.0 

0.0 

0.1 

CO Mass 

Ib/hr 

0 -100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

NOx Rate 

Ib/mmBtu 

0-1 

0.004 

0.004 

0.004 

0.004 

0.005 

0 . 005 

0.005 

0.004 

0.004 

0.005 

0.004 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0 . 00 6 

0.005 

Stk NOXc 

ppm 

0 -3 00 

1. 21 

1. 21 

1. 21 

1. 21 

1. 30 

1. 30 

1. 29 

1. 21 

1. 21 

1. 29 

1. 21 

1. 30 

1. 29 

1.38 

1.38 

1.38 

1.46 

1.46 

1. 38 

1. 47 

1. 46 

1. 55 

1. 46 

1.46 

1. 55 

1. 54 

1. 55 

1. 55 

1. 54 

1. 29 

pp m hscfh 

0-1000 0-10000 

0 . 17 

0.17 

0.09 

0.09 

0.17 

0 . 17 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0 . 09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0 . 09 

0.09 

0.09 

0.09 

0.00 

0.00 

0.00 

0 . 00 

0.09 

5343.0 

5356.8 

5350.8 

5343.0 

5335.2 

5347.8 

5359.2 

5339.4 

5359.2 

5359.2 

5338.2 

5335.2 

5355.0 

5344.8 

5337.6 

5347.8 

5352.6 

5362.2 

5376.6 

5351. 4 

5362.2 

5379.0 

5376.0 

5391.0 

5413.8 

5407.8 

5402.4 

5412.6 

5427.0 

5424.6 

104.7 

104.5 

103.7 

104.5 

104.3 

103.7 

103.8 

105.0 

103.8 

104.7 

104.3 

103.8 

103.8 

102.8 

102.8 

103.0 

102.8 

104.2 

104.3 

104.3 

104 .5 

103 . 8 

105.7 

106.3 

107.7 

107.5 

108.7 

1 08.8 

109.2 

108.3 

0-1 

54.1 

54. 1 

54.1 

54. ( 

53 .. 

54.1 

54.1 

54.1 

54.1 

54.1 

54.1 

53. : 

54. t 

54. t 

53 .. 

54.1 

54.: 

54 . . 

54 .. 

54.1 

54.1 

54 . ~ 

54.' 

54.' 

55.1 

55,( 

54.: 

55.1 

55. 1 

55.1 

PagE 
Group#-Channel# 

Long Descrip. 

Short Descri p . 

Uni.ts 

Range 

02/26/2013 09:00 

02/26/2013 09:01 

02/26/2013 09:02 

02/26/2013 09,03 

02/26/2013 09:04 

02/26/2013 09:05 

02/26/2013 09:06 

02/26/2013 09:07 

02/26/2013 09:08 

02/26/2013 09:09 

02/26/2013 09:10 

02/26/2013 09:11 

02/26/2013 09:12 

02/26/2013 09:13 

02/26/2013 09:14 

02/26/2013 09:15 

02/26/2013 09:16 

02/26/2013 09:17 

02/26/2013 09:18 

02/26/2013 09:19 

02/26/2013 09:20 

02/26/2013 09:21 

02/26/2013 09:22 

02/26/2013 09:23 

02/26/2013 09:24 

02/26/2013 09:25 

02/26/2013 09:26 

02/26/2013 09:27 

02/26/2013 09:28 

02/26/2013 09:29 

02/26/2013 09:30 

02/26/2013 09:31 

02/26/2013 09:32 

02/26/2013 09:33 

02/26/2013 09:34 

02/26/2013 09:35 

02/26/2013 09:36 

02/26/2013 09:37 

02/26/2013 09:38 

02/26/2013 09,39 

Date/Time Printed: 

G45-C2 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

1.6 

1.6 

1.7 

1.6 

1.6 

1.6 

1.6 

1.6 

1.7 

1.7 

1.7 

1.7 

1.7 

1.6 

1.6 

1.7 

1.6 

1.6 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.8 

G45-C4 G45-C11 

5>Stk 02 5>NOx Mass 

Stk 02 

• 

0-25 

14.01 

14.02 

14. 02 

14. 03 

14. 04 

14.03 

14.02 

14.03 

14.03 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.03 

14.04 

14 .03 

14.02 

14.02 

14.03 

14.04 

14.04 

14.04 

14.05 

14.05 

14.04 

14.03 

14.03 

14.03 

14.02 

14.02 

14.02 

14.02 

14.03 

14.03 

14.03 

14.03 

14.01 

NOx Mass 

1b/hr 

0-100 

2.85 

2.85 

2.85 

2.84 

2.83 

2.84 

2.85 

2.84 

2.85 

2.85 

2.85 

2.84 

2.85 

2.84 

2.84 

2.84 

2.84 

2.83 

2.83 

2.83 

2.84 

2.83 

2.82 

2.82 

2.82 

2.82 

3.37 

3.39 

3.38 

3.39 

3.39 

2.83 

2.83 

2.83 

2.83 

2.83 

2.83 

2.83 

2.83 

3.43 

02/26/2013 12,55 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

15077 

15071 

15094 

15034 

15033 

15046 

15062 

15063 

15096 

15057 

15067 

15047 

15059 

15029 

15051 

15042 

15033 

15041 

15021 

14996 

15007 

15006 

14964 

14973 

14944 

14971 

14931 

14976 

14946 

14971 

14961 

14962 

14962 

14962 

14962 

15002 

15002 

15002 

15002 

15089 

G45-C3 

s>Stk CO 

Stk. CO 

ppm 

0-1000 

0.1 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0 . 2 

0.2 

0.2 

0.2 

0.2 

0.2 

0 . 1 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

G4S-C13 G4s-C10 G4S - C6 

5>CO Mass S>NOx Rate s>Stk NOXc 

CO Mass 

1b/hr 

0-100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

NOx Rate 

Ib/mmBtu 

0 - 1 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

Stk NOXc 

ppm 

0 - 300 

1. 37 

1. 37 

1. 46 

1. 37 

1. 38 

1. 37 

1. 37 

1. 37 

1.46 

1. 46 

1. 46 

1.46 

1. 46 

1. 37 

1. 37 

1. 46 

1.37 

1.38 

1. 46 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1. 55 

1. 55 

1. S5 

1.55 

1. 55 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1. 54 

G45-C7 G45 - C8 

5>Stk COc 5>Gas Flow 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.09 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

0 . 17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

0.17 

0.17 

0.17 

0.09 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

0.17 

0.17 

5434.8 

5424.6 

5433.0 

5403.6 

5395.2 

5407.8 

5421.6 

5413.8 

5425.8 

5419.8 

5423.4 

5416.2 

5420.4 

5409.6 

5417.4 

5414.4 

5403.0 

5398.2 

5398.8 

5397.6 

5401.8 

5393.4 

5370.6 

5373.6 

5363.4 

5365.2 

5350.8 

5374.8 

. 5371.8 

5380.8 

5377.2 

5385.6 

5385.6 

5385.6 

5385.6 

5392.2 

5392.2 

5392.2 

5392.2 

5439.0 

G45-C18 

5>NH3 Inj 

NH3Inj 

lb/m 

0-200 

105.5 

103.3 

102.8 

103.2 

102.5 

103.2 

103.7 

102.5 

102.3 

102.5 

102.3 

102.0 

102.7 

103.0 

102.5 

102.3 

102.8 

102.5 

102.5 

101. 3 

101. 3 

101. 2 

101. 2 

101. 3 

101.8 

101. 3 

101.2 

101.2 

100.8 

101. 2 

101.5 

102.5 

102.5 

102.5 

102.5 

101. 8 

101.8 

101. 8 

101.8 

101.3 

S>Summary - I -Min RATA - Continued 

G45-C 

5>MW Lo 

MW Lo 

0-1 

55. : 

55 .. 

55.: 

55.1 

55. ! 

55. ( 

55. ! 

55. ( 

55. ( 

55. t 

55.: 

55. ! 

55. -

55. ! 

S5 . ( 

55. ( 

55. ( 

55. ( 

55. ( 

55. ! 

55. ( 

55.1 

54 .. 

54 .. 

54 . ~ 

54.' 

54.: 

54.' 

54.: 

54.1 

54. 1 

54.1 

54. : 

54. 1 

54.: 

54. : 

54.1 

54.1 

54.: 

5S.~ 

pag( 
Group#-Channel# 

Long De scrip . 

Sho rt Descrip . 

Units 

Range 

02/26/2013 09:40 

02/26/2013 09:41 

02/26/2013 09:42 

02/26/2013 09:43 

02/26/2013 09;44 

02/26/2013 09:45 

02/26/2013 09:46 

02/26/2013 09:47 

02/26/2013 09:48 

02/26/2013 09:49 

02/26/2013 09:50 

02/26/2013 09:51 

02/26/2013 09:52 

02/26/2013 09:53 

02/26/2013 09:54 

02/26/2013 09:55 

02/26/2013 09:56 

02/26/2013 09:57 

02/26/2013 09:58 

02/26/2013 09:59 

02/26/2013 10:00 

02/26/2013 10:01 

02/26/2013 10:02 

02/26/2013 10:03 

02/26/2013 10:04 

02/26/2013 10:05 

02/26/2013 10;06 

02/26/2013 10;07 

02/26/2013 10:08 

02/26/2013 10:09 

02/26/ 2013 10:10 

02/26/2013 10:11 

02/26/2013 10:12 

02/26/2013 10:13 

02/26/2013 10:14 

02/26/2013 10:15 

02/26/2013 10;16 

02/2 6 /2013 10:17 

02/26/2013 10:18 

02/26/2013 10:19 

Date/Time Printed: 

G45-C2 G45-C4 G45 -Cll 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5 >Stk 02 5 >NOx Mass 

1.8 

1.8 

1.8 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.8 

1.8 

1.8 

1.8 

1.7 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 I.. 

I.' 

1.8 

1.8 

1.8 

Stk 02 

• 

0-25 

14 .01 

14.01 

14.01 

14.02 

14.02 

14.03 

14 . 03 

14.03 

1 4 .03 

14.03 

14.03 

14.02 

14.02 

14.01 

1 4. 01 

1 4. 03 

14.03 

14.03 

14.03 

14.00 

14.00 

14.01 

14.01 

14.01 

14 . 01 

14.00 

14.00 

14.00 

14.00 

14.00 

14. 00 

14 . 01 

14. 01 

14 . 01 

14 .01 

14.01 

14 . 01 

14.02 

14 . 02 

14.02 

02/26/2013 12,55 

NOx Mass 

1b/hr 

0-100 

3.43 

3.43 

3.43 

3.41 

3.41 

2 . 84 

2.84 

2.84 

2.84 

2.85 

2.85 

2.84 

2.84 

2.85 

2.85 

2.84 

2.84 

2.84 

2.84 

2.88 

2.88 

3.43 

3.43 

3.43 

3.43 

2.88 

2.88 

3.44 

3.44 

3.44 

3.44 

3.42 

3.42 

3 A2 

3.42 

3.43 

3 A3 

3.41 

3.41 

3.41 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

15089 

15089 

15089 

15024 

15024 

15056 

15056 

15056 

15056 

15083 

15083 

15042 

15042 

15060 

15060 

15033 

15033 

15033 

15033 

15190 

15190 

15122 

15122 

15122 

15122 

15220 

15220 

15112 

15112 

15112 

15112 

15055 

15055 

15055 

15055 

15089 

15089 

1504 4 

15044 

15044 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0 . 2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

G45 -C13 G45 - ClO G45-C6 

5>CO Mass 5>NOx Rate 5>Stk NOXc 

CO Mass 

1b/hr 

0-100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

NOx Rate 

lb/mmBtu 

0-1 

0.006 

0.006 

0 . 006 

o 006 

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 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.005 

0.005 

0.006 

0.006 

0.006 

0.00 6 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0-300 

1.54 

1.54 

1.54 

1.54 

1.54 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1.46 

1A6 

1.46 

1.46 

1.46 

1A5 

1.45 

1.54 

1.54 

1.54 

1.54 

1.45 

1.45 

1.54 

1. 54 

1. 54 

1.54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 63 

1.63 

1. 54 

1. 54 

1. 54 

G45-C7 G45-C8 G45 -C18 

5>Stk COc 5>Gas Flow 5>NH3 Inj 

Stk COc Gas hscfh NH3Inj 

ppm hscfh lb/hr 

0-1000 0-10000 0-200 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0 . 17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0 . 17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0 . 17 

0.17 

0.17 

5439.0 

5439.0 

5439.0 

5407.8 

5407.8 

5411.4 

5411.4 

5411.4 

5411 . 4 

5421.0 

5421. 0 

5414.4 

5414.4 

5428.8 

5428.8 

5403.0 

5403.0 

5403.0 

5403.0 

5483.4 

5483.4 

5451.0 

5451.0 

5451.0 

5451.0 

5494.2 

5494.2 

5455.2 

5455.2 

5455.2 

5455.2 

5427.0 

5427.0 

5427.0 

5427.0 

5439.0 

5439.0 

5415.0 

5415.0 

5415.0 

101.3 

101.3 

101.3 

101.0 

101.0 

101.3 

101.3 

101.3 

101.3 

102.2 

102.2 

100.8 

100.8 

102.7 

102.7 

102.2 

102.2 

102.2 

102.2 

101. 5 

101. 5 

100.8 

100 . 8 

100 . 8 

100.8 

103.2 

103.2 

101. 5 

101. 5 

101.5 

101.5 

101.2 

101. 2 

101.2 

101.2 

101.7 

101.7 

102.0 

102.0 

102.0 

S>Summary - I-Min RATA - Continued 

G45-C 

5>MW Lo 

MW Lo 

0-1 

55. ! 

55. 

55. 

55.1 

55.1 

55.1 

55. j 

55. ( 

55. j 

55. c 

55.1 

S5.1 

55. j 

55. : 

55. : 

55. : 

55. : 

55. : 

55. : 

56.1 

56.1 

55. : 

55. : 

55 . : 

55. : 

56.: 

56.: 

56.1 

56.1 

56. j 

56. j 

55. : 

S5. : 

S5. : 

55. : 

55 .. 

55 .. 

55 .. 

55 . . 

55 .. 

pagE 
Group#-Channel# 

Long Descrip . 

Short Descrip. 

Units 

Range 

02/26/2013 10:20 

02/26/2013 1 0:21 

02/26/2013 10:22 

02/26/2013 10:23 

02/26/2013 10:24 

02/26/2013 10:25 

02/26/2013 10:26 

02/26/2013 10:27 

02/26/2013 10:28 

02/26/2013 10:29 

02/26/2013 10:30 

02/26/2013 10:31 

02/26/2013 10:32 

02/26/2013 10:33 

02/26/2013 10:34 

02/26/2013 1 0:35 

02/26/2013 10:36 

02/26/ 2013 10:37 

02/26/2013 10:38 

02/26/2013 10:39 

02/26/2013 10:40 

02/26/2013 10:41 

02/26/2013 10:42 

02/26/2013 10:43 

02/26/2013 10:44 

02/26/2013 10:45 

02/26/2013 10:46 

02/26/2013 10:47 

02/26/2013 10;48 

02/26/2013 10:49 

02/26/2013 10:50 

02/26/2013 10:51 

02/26/2013 10:52 

02/26/2013 10:53 

02/26/2013 10:54 

02/26/2013 10:55 

02/26/2013 10:56 

02/26/2013 10:57 

02/26/2013 10:58 

02/26/2013 10:59 

Date/Time Printed: 

G45-C2 G45-C4 G45-Cll G45 - C20 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 5>StkFlow 

1.8 

1.. 

1.. 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

2.0 

2.0 

1.. 

1.. 

1.. 

1.. 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1. 8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

Stk 02 

• 

0-25 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14 . 02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.04 

14. 04 

14. 03 

14.03 

14.04 

14.04 

14.05 

14.05 

14 . 05 

14 . 05 

14.05 

14. 05 

14.04 

14.04 

14.04 

14.04 

14.02 

14.02 

14.02 

14.02 

14. 02 

1 4. 02 

14.03 

02/26/2013 12,55 

NOx Mass 

1b/hr 

0-100 

3.41 

3.40 

3.40 

3.43 

3.43 

3.43 

3.43 

3.41 

3.41 

3.41 

3.41 

3.41 

3.41 

3.40 

3.40 

3.40 

3.40 

3.38 

3.38 

3.39 

3.39 

3.37 

3.37 

3.36 

3.36 

3.36 

3.36 

3.37 

3.37 

3.36 

3.36 

3.36 

3.36 

3.39 

3.39 

3.39 

3.39 

3.39 

3.39 

3.39 

StkFlow 

ksefh 

0-300000 

15044 

15004 

15004 

15124 

15124 

15124 

15124 

15021 

15021 

15021 

15021 

15019 

15019 

14987 

14987 

14987 

14987 

14957 

14957 

14971 

14971 

14921 

14921 

14901 

14901 

14901 

14901 

14917 

14917 

14867 

14867 

14867 

14867 

14961 

14961 

14961 

14 961 

14939 

14939 

14962 

G45-C3 G45-C13 G45-CI0 G45-C6 G45-C7 G45-C8 G45 - C18 G45-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXe 5>Stk COe 5>Gas Flow 5>NH3 Inj 5>MW Lo 

Stk CO 

ppm 

0-1000 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0 . 2 

0 .2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.2 

0.2 

0.2 

CO Mass 

1b/hr 

0-100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

NOx Rate 

lb/mmBtu 

0-1 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

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 

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. 54 

1. 63 

1.63 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 72 

1. 72 

1. 63 

1. 63 

1. 63 

1. 63 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 55 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 54 

1. 55 

Stk COe Gas hsefh 

hsefh 

0-10000 

ppm 

0-1000 

0.17 

0 .17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.09 

0.09 

0.09 

O. 09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.17 

0.17 

0.17 

5415.0 

5400.6 

5400.6 

5443.8 

5443.8 

5443.8 

5443.8 

5406.6 

5406.6 

5406.6 

5406.6 

5406.0 

5406.0 

5394.6 

5394.6 

5394.6 

5394.6 

5368.2 

5368.2 

5380.8 

5380.8 

5355.0 

5355.0 

5340.0 

5340.0 

5340.0 

5340.0 

5346.0 

5346.0 

5335.8 

5335.8 

5335.8 

5335.8 

5385.0 

5385.0 

5385.0 

5385.0 

5377.2 

5377.2 

5377.8 

NH3Inj 

1b/hr 

0-200 

102.0 

101.2 

101.2 

102.5 

102.5 

102.5 

102.5 

103.2 

103.2 

103.2 

103.2 

102.3 

102.3 

101.7 

101.7 

101.7 

101.7 

101.3 

101. 3 

102.8 

102.8 

102.5 

102.5 

102.5 

102.5 

102.5 

102.5 

102.5 

102.5 

103.2 

103.2 

103.2 

103.2 

103.7 

103.7 

103.7 

103.7 

104.2 

104.2 

103.2 

5>Summary - I-Min RATA - Continued 

MW La 

0-1 

55 .. 

S5 .. 

55. ; 

56.1 

56.1 

56.1 

56.1 

55. ! 

55. 1 

55. 

55. 

55.: 

55 

55.1 

55. 1 

55. 1 

55.1 

55. 1 

55.1 

55.1 

55.1 

54 .. 

54 . . 

54 .. 

54 

54 

54 .. 

54 . . 

54 . . 

54. 

54 . . 

54. 

54 . . 

55 . . 

55. : 

55. : 

5S. : 

55.1 

55.1 

55. ; 

PagE 
Group#-Channel# 

Long Descrip. 

Short Descrip . 

units 

Range 

02/26/2013 11:00 

02/26/2013 11:01 

02/26/2013 11:02 

02/26/2013 11 :03 

02/26/2013 11:04 

02/26/2013 11:05 

02/26/2013 11:06 

02/2 6 /2013 11:07 

02/26/2013 11:08 

02/26/2013 11:09 

02/26/2013 11:10 

02/26/2013 11:11 

02/26/2013 11:12 

02/26/2013 11:13 

02/26/2013 11:14 

02/ 26 / 2 013 11:15 

02/26/2013 11:16 

02/26/2013 11:17 

02/26/2013 11:18 

02/26/2013 11:19 

02/26/2013 11:20 

02/26/2013 11:21 

02/26/ 2013 11 : 22 

02/26/2013 11:23 

02/26/2013 11:24 

02/26/2013 11:25 

02/26/2013 11:26 

02/26/2013 11:27 

02/26/2013 11:28 

02/26/2013 11:29 

02/ 26/ 2013 11:30 

02/26/2013 11:31 

02/26/2013 11:32 

02/26/2013 11:33 

02/26/2013 11:34 

02/26/2013 11:35 

02/26/2013 11:36 

02/26/ 2013 11:37 

02/26/2013 11:38 

02/26/ 2013 11:39 

Date/Time Printed: 

G45-C2 G45-C4 G45-C11 

5>Stk NOx 

stk NOx 

ppm 

0-150 

S>Stk 02 5>NOx Mass 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

I.. 

I.' 

1.8 

1.8 

1.8 

1.8 

1.7 

1.7 

I.. 

I.. 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1. 7 

1.7 

1.7 

1.7 

1.8 

I.' 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

Stk 02 

• 

0-25 

14. 03 

14.03 

14.03 

14.03 

14.03 

14.03 

14 . 03 

14 .0 2 

1 4. 02 

14.02 

14.02 

14.03 

14.03 

14 . 05 

1 4. 05 

14 . 04 

1 4 .0 4 

14.04 

14.04 

14 . 02 

14.02 

14.02 

14 .0 2 

14 . 03 

14.03 

14 . 03 

14.03 

14.03 

14.03 

14. 05 

14 . 05 

14 .03 

14.04 

14.03 

14.04 

14 . 04 

14.02 

1 4. 04 

14 . 04 

14.03 

02/26/2013 12,55 

NOx Mass 

Ib/hr 

0-100 

3.39 

3.38 

3.38 

3.38 

3 .38 

3.39 

3.39 

3.39 

3.39 

3.39 

3.39 

3.38 

3.38 

2.81 

2.81 

3.39 

3.39 

3.38 

3.38 

3.40 

3.40 

3.40 

3.40 

2.82 

2.82 

2.82 

2.82 

2.82 

2.82 

2.81 

2.80 

3.37 

3.38 

3.38 

3.37 

3.38 

3.3' 

3.37 

3.38 

3.39 

G45 - C20 

5>StkFlow 

StkFlow 

ksefh 

0-300000 

14962 

14939 

14939 

14936 

14936 

14964 

14964 

14 969 

14 969 

14962 

14962 

14907 

14907 

1 4 934 

1 4 934 

14984 

14984 

14964 

14964 

14989 

14989 

15009 

15009 

1 4 941 

14941 

14919 

14919 

14939 

14924 

14911 

1 4 879 

14896 

14936 

14917 

14911 

14926 

14 944 

14 916 

14937 

14954 

G4S-C3 

5>Stk CO 

Stk CO 

ppm 

0 - 1000 

0.2 

0.1 

0.1 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.2 

0.1 

0.1 

0.1 

0.1 

0.2 

0.2 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.2 

0.1 

0.2 

0.2 

0.2 

0.2 

0.1 

0.2 

0.1 

0.2 

G45 -C13 G4S-C10 G45-C6 

5>CO Mass S>NOx Rate S>Stk NOXe 

CO Mass 

Ib/hr 

0 -100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

NOx Rate 

Ib/mmBtu 

0-1 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0 . 00 6 

0.006 

0.006 

0.006 

0.006 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.00 5 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.00 6 

0 . 006 

0 . 00 6 

0.00 6 

stk NOXe 

ppm 

0 - 300 

1. 55 

1. 55 

1. 55 

1.55 

1. 55 

1. 55 

1. 55 

1. 63 

1. 63 

1. 54 

1.54 

1. 55 

1. 55 

1.46 

1.46 

1. 63 

1. 63 

1. 55 

1. 55 

1. 54 

1. 54 

1. 54 

1. 54 

1. 46 

1. 46 

1. 46 

1.46 

1.46 

1.46 

1.46 

1.46 

1. 55 

1. 63 

1. 55 

1.55 

1. 55 

1. 54 

1. 55 

1. 55 

1. 55 

G4S-C7 G45-C8 

5>Stk COe 5>Gas Flow 

Stk COe Gas hsefh 

ppm hsefh 

0-1000 0 -100 00 

0.17 

0.09 

0.09 

0.17 

0.17 

0.17 

0 . 17 

0.17 

0 . 17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.17 

0.09 

0.09 

0.09 

0.09 

0.17 

0.17 

0 . 09 

0.09 

0.0 9 

0.09 

0.09 

0.09 

0.09 

0.09 

0 . 09 

0.17 

0 . 09 

0.17 

0.17 

0.17 

0.17 

0.09 

0 . 17 

0 . 09 

0.17 

5377.8 

5369.4 

5369.4 

5368.2 

5368.2 

5378.4 

5378.4 

5388.0 

5388.0 

5385.6 

5385.6 

5358.0 

5358.0 

5352.0 

5352.0 

5377.8 

5377.8 

5370.6 

5370.6 

5395.2 

5395.2 

5402 . 4 

5402.4 

5370.0 

5370.0 

5362.2 

5362.2 

5369.4 

5364.0 

5343.6 

5332.2 

5353.8 

5360.4 

5361.6 

5351. 4 

5356.8 

5379.0 

5353.2 

5361.0 

5374.8 

G45 - C18 

5>NH3 Inj 

NH3Inj 

Ib/hr 

0 - 200 

103.2 

104.2 

104.2 

104.5 

104.5 

103.7 

103.7 

102.8 

102.8 

103.7 

103.7 

102.5 

102.5 

104.0 

10 4 .0 

103.8 

103.8 

104.3 

104.3 

104.5 

104.5 

104.7 

104 . 7 

104.3 

104.3 

104.8 

104.8 

105.0 

104.0 

104.7 

103.2 

103.7 

103.3 

104.0 

103.8 

103.5 

104.0 

102.7 

103.3 

104.2 

S>Summary - l-Min RATA - Continued 

G4S-C 

5>MW Lo 

MW Lo 

0 - 1 

55. : 

55.1 

55.1 

55.1 

55.1 

55.1 

55.1 

55 . 1 

SS .1 

55 

55.: 

55 

55 

55.1 

55.1 

55. 1 

55.1 

55 . . 

55 . . 

55. 

55. ; 

55 . . 

55 .. 

55. 1 

5S .1 

55. 1 

55.1 

55. 

55.1 

55 . 1 

54 . : 

55.1 

54 .. 

55.1 

54. ; 

55. 1 

55.1 

55.1 

55.1 

55. : 

PagE 
Group#-Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/26/2013 11:40 

02/26/2013 11:41 

02/26/2013 11:42 

02/26/2013 11:43 

02/26/2013 11:44 

02/26/2013 11:45 

02/26/2013 11:46 

02/26/2013 11:47 

02/26/2013 11:48 

02/26/2013 11:49 

02/26/2013 11:50 

02/26/2013 11:51 

02/26/2013 11:52 

02/26/2013 11:53 

02/26/ 20 13 11:54 

02/26/2013 11:55 

02/26/2013 11:56 

02/26/2013 11:57 

02/26/2013 11:58 

02/26/2013 11:59 

02/26/2013 12:00 

02/26/2013 12:01 

02/ 26/2013 12:02 

02/26/2013 12:03 

02/26/2013 12:04 

02/26/2013 12:05 

02/26/2013 12:06 

02/26/2013 12:07 

02/26/2013 12:08 

02/26/2013 12:09 

02/26/2013 12:10 

02/26/2013 12:11 

02/26/2013 12:12 

02/26/2013 12:13 

02/26/2013 12:14 

02/26/2013 12:15 

02/26/2013 12:16 

02/26/2013 12:17 

02/26/2013 12:18 

02/26/2013 12:19 

Date/Time Printed: 

G45 - C2 G45-C4 G45 - C11 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

1.8 

1.7 

1.8 

1.8 

1.8 

1.7 

1.7 

1.8 

1.7 

1.8 

1.7 

1.8 

1.7 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.8 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.6 

1.7 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.6 

1.7 

1.7 

1.7 

Stk 02 

% 

0-25 

14 . 03 

14.03 

14.03 

14.03 

14.03 

14.04 

14.04 

14.05 

14.04 

14.03 

14.04 

14 .03 

14.03 

14.02 

14 .02 

14.02 

14.02 

14.02 

14.02 

14.02 

14.01 

14.02 

14.02 

14.02 

14.02 

14.01 

14.01 

14.00 

14.01 

14.01 

14.00 

1 4.00 

14.01 

14.00 

13.99 

14.00 

14.01 

1 4.00 

14.00 

14.00 

02/26/2013 12 , 55 

NOx Mass 

1b/hr 

0-100 

3.39 

2.82 

3.38 

3.38 

3.37 

2.80 

2.80 

3.36 

2.80 

3.37 

2.81 

3.38 

2.81 

3.38 

3.38 

2.82 

2.82 

2.82 

2.81 

3 . 38 

3.39 

3.40 

2.84 

2.85 

2.84 

2.85 

2.84 

2.84 

2.84 

2.85 

2.85 

3.42 

3.41 

3.41 

3.42 

3.44 

2.84 

2.85 

2.86 

2 . 84 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

14974 

14969 

14934 

14914 

14884 

14854 

14867 

14879 

14862 

14896 

14892 

14922 

14889 

14914 

14899 

14921 

14932 

14912 

14889 

14912 

14926 

15004 

15041 

15061 

15002 

15074 

15026 

15004 

15026 

15055 

15037 

15055 

14999 

15014 

15038 

15103 

15002 

15040 

15097 

14985 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

0.1 

0.1 

0.1 

0.1 

0.2 

0.2 

0.1 

0.2 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.1 

0.2 

0.1 

0.1 

0 . 2 

0.1 

0.1 

0.1 

0.1 

0.1 

0.2 

0.1 

0.2 

0.2 

0.2 

0.2 

0.2 

0.1 

0.1 

0.2 

G45-C13 G45-C10 G45-C6 

5>CO Mass 5>NOx Rate 5>Stk NOXc 

CO Mass 

Ib/hr 

0-100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

NOx Rate 

Ib/mmBtu 

0-1 

0.006 

0.005 

0.006 

0.006 

0.006 

0.005 

0.005 

0.006 

0.005 

0.006 

0.005 

0.006 

0.005 

0.006 

0.006 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.005 

0 . 005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.005 

0.005 

0.005 

Stk NOXc 

ppm 

0 - 300 

1.55 

1. 46 

1. 55 

1. 55 

1. 55 

1.46 

1.46 

1. 55 

1.46 

1. 55 

1.46 

1. 55 

1. 46 

1. 54 

1. 54 

1. 46 

1. 46 

1.46 

1.46 

1. 54 

1. 54 

1. 54 

1.46 

1. 46 

1. 46 

1. 46 

1.46 

1.45 

1.37 

1.46 

1.45 

1. 54 

1. 54 

1. 54 

1. 54 

1.54 

1.37 

1.45 

1.45 

1.45 

G45-C7 G45 - C8 

5>Stk COc 5>Gas Flow 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0 - 10000 

0.09 

0 . 09 

0.09 

0.09 

0.17 

0.17 

0 . 09 

0.17 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0.09 

0 . 09 

0 .17 

0.09 

0.09 

0.17 

0.09 

0.09 

0.09 

0.09 

0.09 

0.17 

0.09 

0.17 

0.17 

0.17 

0.17 

0.17 

0.09 

0.09 

0.17 

5382.0 

5380.2 

5367.6 

5360.4 

5349.6 

5331.0 

5335.8 

5332.2 

5334.0 

5353.8 

5344.8 

5363.4 

5351.4 

5368.2 

5362 . 8 

5370.6 

5374.8 

5367.6 

5359.2 

5367.6 

5380.2 

5400.6 

5413.8 

5421.0 

5400.0 

5433.6 

5416.2 

5416.2 

5416.2 

5427.0 

5428 . 2 

5434.8 

5406.6 

5419.8 

5436.6 

5452.2 

5407.8 

5429.4 

5449.8 

5409.6 

G45-C18 

5>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

103.3 

105.0 

103.8 

103.3 

103.8 

104.0 

104 . 2 

103.8 

102.8 

103.8 

103.7 

104.2 

104.3 

104.5 

104.7 

104.7 

105.2 

104.8 

104.3 

104.8 

104.5 

104.7 

105.8 

105.3 

105.5 

106.3 

106.0 

104.7 

106.8 

105.3 

105.2 

105.0 

104.3 

104.8 

104.5 

104.7 

105.2 

105.7 

105 . 2 

104.3 

5>Summary - 1-Min RATA - Continued 

G45-C 

5>MW La 

MW Lo 

0-1 

55.1 

55.1 

55 . 1 

55. 1 

55.1 

54 . . 

54. 

54 .. 

54 .. 

55.1 

55.1 

55 .. 

55.1 

55.1 

55.1 

55 .. 

55.1 

55.1 

55.1 

55.: 

55. : 

56.1 

56.1 

56. : 

56 . 1 

56.1 

56. 1 

56. 1 

56.1 

56.1 

56 .1 

56.1 

55 .. 

56.1 ' 

56.1 

56.1 

56.1 

56.1 

56. ! 

56.1 

PagE 
Group# - Channel# 

Long Descrip . 

Short Descrip . 

Units 

Range 

02/26/2013 12:20 

02/26/2013 12:21 

02/26/2013 12:22 

02/26/2013 12:23 

02/26/2013 12:24 

02/26/2013 12:25 

02/26/2013 12:26 

02/26/ 2 013 12:27 

02/26/2013 12:28 

02/26/2013 12:29 

02/26/2013 12:30 

02/26/2013 12:31 

02/26/2013 12:32 

02/26/2013 12:33 

02/26/2013 12;34 

02/26/2013 12:35 

02/26/2013 12:36 

02/26/2013 12:37 

02/26/2013 12:38 

02/26/2013 12:39 

02/ 26 /2013 12:40 

Period Average 

Period Max Value 

Period Min Value 

Period Totals = 

Period % Recovery 

Date/Time Printed: 

G45-C2 G45 - C4 G45-C11 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5.>Stk 02 5>NOx Mass 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.7 

1.7 

1.7 

1.8 

1.8 

1.9 

1.7 

1.7 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.8 

1.7 

2 .0 

1.4 

4.3650E+2 

100.0 

Stk 02 

• 

0-25 

14.01 

14 .00 

14.00 

14.00 

13.99 

14.00 

14.01 

14.02 

14 .02 

14.02 

14.02 

14.02 

14. 03 

14.03 

14.02 

14.02 

1 4.02 

14.02 

1 4 .02 

14.01 

14.01 

14.03 

14.08 

13 . 99 

3.5207E+3 

100.0 

02/26/2013 12,55 

NOx Mass 

lb/hr 

0-100 

2.85 

3.43 

3.44 

3.43 

3.44 

3.43 

2.85 

2.83 

2.82 

3. 4 0 

3.39 

3.39 

2.82 

2.82 

3.39 

3.38 

2.81 

2.82 

2.81 

2.83 

3.38 

3.11 

3.44 

2 . 24 

7.8130E+2 

100.0 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

15050 0.2 

15062 0.1 

15118 0.1 

15090 0.2 

15092 0.2 

15069 0.2 

15044 0.2 

14987 0.1 

14937 0.2 

14991 0.1 

14962 0.2 

14967 0.2 

14957 0.1 

14927 0.2 

14934 0.1 

1 4919 0.1 

14889 0.1 

14916 0.1 

14886 0.1 

14946 0 .1 

14876 0.1 

14994 0.2 

15220 0.2 

14854 0.0 

3.7634E+6 4.0200E+1 

100.0 100.0 

G45-C13 G45-C10 G45-C6 

S>CO Mass 5>NOx Rate 5>Stk NOXc 

CO Mass 

Ib/hr 

0-100 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

0.00 

0 . 00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0.00 

0 . 00 

O.OOOOE+O 

100.0 

NOx Rate 

Ib/mmBtu 

0-1 

Stk NOXc 

ppm 

0-300 

0.005 1.46 

0.006 1.54 

0.006 1.54 

0.006 1.54 

0.006 1.54 

0.006 1 .5 4 

0.005 1. 4 6 

0.005 1.46 

0.005 1.46 

0.006 1.54 

0.006 1.54 

0.006 1 .63 

0.005 1.46 

0.005 1.46 

0.006 1 . S4 

0.006 1.54 

0.005 1.46 

0.005 1.46 

0.005 1.46 

0.005 1.46 

0.006 1.54 

0.005 1.49 

0.006 1.72 

0.004 1.21 

1.3800E+0 3.7469E+2 

100.0 100.0 

G45-C7 G45-C8 

5.>Stk COc 5>Gas Flow 

stk CDc Gas hscfh 

ppm hscfh 

0-1000 0-10000 

0.17 

0.09 

0.09 

0.17 

0.17 

0.17 

0.17 

0 . 09 

0.17 

0 . 09 

0.17 

0.17 

0 . 09 

0.17 

0.09 

0.09 

0.09 

0.09 

0.09 

0 . 09 

0.09 

0.14 

0.17 

0.00 

3.4630E+1 

100.0 

5425.2 

5437.2 

5457.6 

5447.4 

5455 . 8 

5439.6 

5422.8 

5394.6 

5376.6 

5395.8 

5385.6 

5387.4 

5376.0 

5365.2 

5375.4 

5370.0 

5359.2 

5368.8 

5358.0 

5387.4 

5362.2 

5391.5 

5494.2 

5331.0 

1.3532E+6 

100.0 

G45-C18 

5>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

104.2 

105.3 

104.5 

103.7 

104 . 0 

105.0 

105.0 

105.2 

103.7 

103.8 

103.7 

103.5 

104.3 

103.0 

103.0 

103.3 

104.0 

102.8 

104.7 

104.7 

103.8 

103.3 

109.2 

100.8 

2.5935E+4 

100.0 

S>Summary - 1-Min RATA - Continued 

G45-C 

5>MW Lo 

MW Lo 

0-1 

56.1 

56 .. 

56.1 

56. : 

56. : 

56. : 

55. 

55. 

55 . . 

55 .. 

55. : 

55 . . 

55. 1 

55. : 

55. c 

S5.1 

55.1 

SS .1 

55.1 

55 .. 

55.1 

55.1 

56. 

53 . 

1.3833E+ 

100. 

pagE 
Data Summary Report 

Company : CPV Sentinel, LLC 

62575 Powerline Road 

5 

Desert Hot Springs, CA 92240 

5eAt.v-\ 

17'714 

PM Source: Turbine 5 

Data Group: 5>1-Min Cales 

Report Name : 

Start of Report : 

S>Summary - I-Min RATA 

02/25/2013 16,42 

G4S-C4 

End of Report , 02/25/2013 20,54 

G45-Cll G45-C13 

TRACE 

Environmenta l S y stems, Inc. 

validation : All Available Data 

Group#-Channe l# G45-CIO G45-C6 G4S-C7 G4S - C8 

Long Descrip. 

Short Descrip . 

Units 

G4S-C2 

S>Stk NOx 

Stk NOx 

ppm 

0 - 150 

5>Stk 02 5>NOx Mass 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

5>CO Mass S>NDx Rate 5>Stk NOXC S>Stk COc 5>Gas Flow 

Stk CDc Gas hscfh 

G45-C18 

5>NH3 Inj 

NlBlnj 

Ib/hr 

0-200 

G45-C 

5>MW Lo 

MW Lo 

Range 

02/25/2013 16:42 

02/25/2013 16;43 

02/25/2013 16:44 

02/25/2013 16:45 

02/25/2 013 16;46 

02/25/2013 16:47 

02/25/2013 16:48 

02/25/2013 16:49 

02/25/2013 16:50 

02/25/2013 16:51 

02/25/2013 16:52 

02/25/2013 16:53 

02/25/2013 16;54 

02/ 2 5/2013 16:55 

02/25/2013 16;56 

02/25/2013 16:57 

02/25/2013 16:58 

02/25/2013 16:59 

02/25/2013 17:00 

02/25/2013 17;01 

02/ 25/ 2 013 17:02 

02/25/2013 17:03 

02/25/2013 17:04 

02/25/2013 17:05 

02/25/2013 17;06 

02/25/2013 17:07 

02/25/2013 17:08 

02/25/ 2013 17:09 

02/25/ 2013 17:10 

02/25/2013 17:11 

Date/Time Printed: 

1.2 

1.3 

1.3 

1.3 

1.3 

1.3 

1.3 

1.3 

I., 

I., 

I., 

I.' 

I., 

I., 

I., 

I., 

I., 

I.' 

I., 

I., 

1.5 

1.5 

1.5 

1.5 

1.5 

1.6 

1.5 

1.5 

1.6 

1.5 

Stk 02 

• 

0- 2 5 

13.91 

13.91 

13.90 

13.90 

13.90 

13 . 8 9 

13 . 8 8 

13.88 

13.88 

13 .89 

13 .89 

13.88 

13.89 

13 . 89 

13.89 

13.89 

13.90 

13.89 

13.88 

13 . 88 

13.86 

13.89 

13.88 

13.86 

13.86 

13.89 

13.88 

13 . 86 

13.87 

13.86 

02/25/2013 21 , 33 

NOX Mass 

Ib/hr 

0 - 100 

2.94 

2.93 

2.94 

2.93 

2.94 

2.96 

2.96 

2.97 

2.97 

2.96 

2.96 

2.97 

2.96 

2.96 

2.94 

2.95 

2.94 

2.95 

2.95 

2.95 

3.71 

3.67 

3.70 

3.72 

3.73 

3.70 

3.70 

3.71 

3.70 

3.71 

19140 

191 08 

19136 

19080 

19139 

19195 

19207 

19224 

19258 

19213 

19238 

19232 

19189 

19200 

19117 

19145 

19084 

19141 

19140 

19144 

1 9188 

19069 

19196 

19239 

19281 

19190 

19214 

19187 

19178 

19193 

D.' 

0.' 

D.' 

a.' 

a.' 

0.3 

0.3 

0.3 

0.3 

a.' 

0.4 

a.' 

a.' 

0.4 

a.' 

0.' 

D.' 

0.4 

0.8 

1.8 

3.3 

2.5 

1.8 

3.0 

6.0 

2.8 

2.3 

'.9 

1.9 

3.0 

CO Mass 

Ib/hr 

0-100 

0.74 

0.73 

0.74 

0.73 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.74 

0.73 

0.74 

1. 48 

2.21 

4 .45 

3.67 

2.22 

4.46 

8.20 

3.70 

2.96 

6.68 

2.96 

4.45 

NOx Rate 

Ib/mmBtu 

0-1 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.004 

0.00 4 

0.00 4 

0.00 4 

0.004 

0.004 

0.004 

0.004 

0.004 

0 . 005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

Stk NOXc 

ppm 

0 - 300 

1. 01 

1.10 

1.10 

1.10 

1.10 

1. 09 

1. 09 

1. 09 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.18 

1.26 

1.26 

1. 26 

1.26 

1. 26 

1. 35 

1. 26 

1. 26 

1. 34 

1. 26 

ppm hscfh 

0-1000 0 - 10000 

0.34 

0.34 

0.34 

0.34 

0.34 

0.25 

0 . 25 

0.25 

0.25 

o 3' 

0.34 

0 . 34 

0.34 

0 . 34 

0 . 34 

0.34 

0.34 

0.34 

0.67 

1.51 

2 .77 

2 .10 

1. 51 

2.51 

5.03 

2.36 

1. 93 

4.11 

1. 59 

2.51 

6999.6 

6987.6 

7008.0 

6987.6 

7009.2 

7039 . 8 

7054.2 

7060.2 

7072.8 

7046.4 

7055.4 

7063.2 

7037.4 

7041.6 

7011.0 

7021. 2 

6988.8 

7020.0 

7029.6 

7030.8 

7067.4 

6993.6 

7050.0 

7086.0 

7101.6 

7038.0 

7056.6 

7066.8 

7053.6 

7069.2 

148.2 

149. a 

149.5 

148.3 

149.5 

149.2 

148.7 

149.3 

148.2 

147.7 

147.5 

147.7 

146.2 

147.3 

144.7 

145.3 

145.7 

145.7 

140.5 

135.0 

132.8 

131.8 

134.8 

133.0 

128.8 

134.7 

133.8 

129.2 

133.8 

131. 3 

0-1 

80.1 

80.1 

80.1 

80 .: 

80.1 

80.! 

80 . . 

81.1 

81.1 

81.1 

81. t 

81.1 

80. : 

80 . . 

80. : 

80 . . 

80.1 

80. : 

80.1 

80.: 

80.! 

79. : 

80. 

80. 

80. 

80 . . 

80. : 

80 . : 

80 . ~ 

80. : 

Pagt 
Group#-Channel# 

Long Descrip . 

Sh o rt Descrip . 

Units 

Range 

02/25/2013 17:12 

02/25/2013 17:13 

02/25/2013 17:14 

02/25/2013 17:15 

02/25/2013 17:16 

02/25/2013 17:17 

02/25/2013 17:18 

02/25/ 2 013 17:19 

02/25/2013 17:20 

02/25/2013 17:21 

02/25/2013 17:22 

02/25/2013 17:23 

02/25/2013 17:24 

02/25/2013 17:25 

02/25/2013 17:26 

02/25/2013 17:27 

02/25/2013 17:28 

02/25/2013 17:29 

02/25/2013 17:30 

02/25/2013 17:31 

02/25/2013 17:32 

02/25/2013 17:33 

02/25/2013 17:34 

02/ 2 5/2013 17:35 

02/25/2013 17:36 

02/25/2013 17:37 

02/25/2013 17:38 

02/25/2013 17:39 

02/25/2013 17:40 

02/25/2013 17:41 

02/25/2013 17:42 

02/25/2013 17:43 

02/25/2013 17:44 

02/25/2013 17:45 

02/25/2013 17:46 

02/25/2013 17:47 

02/25/2013 17:48 

02/25/2013 17:49 

02/25/2013 17:50 

02/25/2013 17:51 

Date/Time Printed: 

G45-C2 G45-C4 G45-C11 

5>Stk NOx 

Stk NOx 

5>Stk 02 5>NOx Mass 

ppm 

0-150 

1.6 

1.6 

1.6 

1.6 

1.5 

1.6 

1.6 

1.6 

1.6 

1.7 

1.6 

1.7 

1.7 

1.7 

1.7 

1.8 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.8 

1.8 

1.7 

1.7 

1.8 

1.7 

Stk 02 

• 

0-25 

13.86 

13.87 

13.87 

13.87 

13.86 

13.86 

13 . 86 

13.86 

13.85 

13.85 

13 . 85 

13.84 

13.84 

13.82 

13.82 

13.82 

13.84 

13.86 

13.85 

13.84 

13.84 

13.84 

13 . 85 

13.84 

13.84 

13.84 

13.85 

13.84 

13.84 

13.84 

13.84 

13.84 

13 . 84 

13.83 

13.83 

13.83 

13.83 

13 .84 

13 . 83 

13.84 

02/25/2013 21,33 

NOx Mass 

Ib/hr 

0-100 

3.72 

3.72 

3.71 

3.71 

3.71 

3.72 

3.72 

3.73 

3.72 

3.73 

3.73 

3.74 

3.74 

3.75 

3.75 

4.50 

3.73 

3.72 

3.72 

3.73 

3.73 

3.73 

3.72 

3.74 

3.73 

3.74 

3.73 

3.74 

3.74 

3.73 

3.74 

3.75 

3.75 

3.75 

4.51 

4.51 

3.76 

3.74 

4.51 

3.75 

G45-C20 

5>StkFlow 

StkFlaw 

kscfh 

0-300000 

19226 

19276 

19226 

19217 

19203 

19218 

19216 

19275 

19189 

19239 

19261 

19264 

19266 

19265 

19262 

19273 

19223 

19219 

19225 

19238 

19223 

19220 

19233 

19277 

19251 

19301 

19249 

19301 

19298 

19256 

19275 

19314 

19329 

19316 

19346 

19339 

19357 

19306 

19349 

19313 

G45-C3 

5>Stk CO 

Stk co 

ppm 

0-1000 

3.6 

2.9 

2.3 

2.1 

2.7 

2.8 

2 . 1 

2.1 

2.3 

2.0 

2.7 

2.3 

2.1 

2.9 

2.7 

2.3 

2.3 

2.' 

2.3 

2.3 

2.0 

2.2 

2.3 

2.2 

2.0 

2.3 

2.1 

2.1 

2.3 

2.9 

3.1 

2.6 

2.6 

2.6 

2.8 

3 . 1 

2.9 

2.8 

2.9 

3.0 

G45-C13 G45-C10 G45-C6 

5>CO Mass 5>NOx Rate 5>Stk NOXe 

CO Mass 

lb/hr 

0-100 

5.20 

3.72 

2.97 

2.97 

3.71 

3.72 

2.97 

2.98 

2.97 

2.98 

3.73 

2 . 99 

2.99 

3.75 

3.75 

3.00 

2.98 

3.72 

2.98 

2.98 

2.98 

2.98 

2 . 98 

2.99 

2.99 

2.99 

2.98 

2.99 

2 . 99 

3.73 

4.49 

3.75 

3.75 

3.75 

3.76 

4.51 

3.76 

3.74 

3.76 

4.49 

NOx Rate 

lb/mmBtu 

0-1 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

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 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.005 

0.005 

0.006 

0.005 

Stk NOXc 

ppm 

0-300 

1. 34 

1. 34 

1. 34 

1. 34 

1. 26 

1. 34 

1. 34 

1. 34 

1. 34 

1. 42 

1. 34 

1. 42 

1. 42 

1. 42 

1.42 

1. 50 

1.42 

1.42 

1.42 

1.42 

1.42 

1. 42 

1. 42 

1. 42 

1. 42 

1.42 

1.42 

1.42 

1.42 

1.42 

1. 42 

1.42 

1.42 

1.42 

1. 50 

1. SO 

1.42 

1.42 

1. 50 

1. 42 

G45-C7 G45-C8 

5>Stk COe 5>Gas Flow 

Stk COe Gas hscfh 

ppm hscfh 

0-1000 0-10000 

3.02 

2.43 

1. 93 

1. 76 

2.26 

2.35 

1. 76 

1. 76 

1. 92 

1. 67 

2 . 26 

1. 92 

1. 75 

2.42 

2.25 

1. 92 

1. 92 

2.01 

1. 92 

1.92 

1. 67 

1. 84 

1.92 

1. 84 

1. 67 

1. 92 

1. 76 

1. 75 

1. 92 

2.42 

2.59 

2.17 

2.17 

2.17 

2.34 

2.59 

2. 4 2 

2 . 34 

2.42 

2 . 51 

7081. 2 

7089.6 

7071. 0 

7068.0 

7072.8 

7078.2 

7077.6 

7099.2 

7077.6 

7096.2 

7104.0 

7115.4 

7116.0 

7135.8 

7134.6 

7138.8 

7100.4 

7078.8 

7090.8 

7105.8 

7100.4 

7099.2 

7093 . 8 

7120.2 

7110.6 

7129.2 

7099.8 

7129.2 

7128.0 

7112.4 

7119.6 

7134.0 

7139.4 

7144.8 

7155.6 

7153.2 

7159.8 

7131.0 

7156.8 

7133.4 

G45-C18 

5>NH3 Inj 

NH3Inj 

Ib/hr 

0-200 

132.2 

132.3 

133.5 

132.8 

132.3 

132.3 

134.2 

133.8 

133.2 

134.0 

133.3 

133.7 

135.2 

131.0 

132.5 

133.5 

132.5 

133.0 

132.0 

133.3 

133.0 

133.2 

131.7 

133.7 

132.2 

134.5 

133.7 

133.0 

134.0 

132.2 

132.5 

132.8 

132.7 

131. 8 

132.3 

132.2 

133.0 

132.7 

132.7 

132.5 

S>Summary - l-Min RATA - Continued 

G45-C 

5>MW La 

MW La 

0-1 

80. 

81.1 

81. ! 

80 .. 

80. ! 

80. 

80. 

81.( 

80 . 

81.( 

80. : 

81.1 

81.1 

81." 

81.1 

81.1 

80. ' 

80.: 

80. 

80 .. 

81.( 

80 . . 

80. : 

81.1 

81.1 

81.: 

80. ! 

81.1 

81.1 

80. t 

81. ! 

80. : 

81.: 

81.( 

81." 

B1.: 

B1.: 

81.1 

81. . 

81.1 

pagE 
Group#-Channel # 

Long Descrip. 

Short Des crip . 

Units 

Range 

02/25/2013 17:52 

02/25/2013 17:53 

02/25/2013 17:54 

02/25/2013 17:55 

02/25/2013 17:56 

02/25/2013 17:57 

02/25/2013 17;58 

02/25/ 2 013 17:59 

02/25/2013 18:00 

02/25/2013 18:01 

02/25/2013 18:02 

02/25/2013 18:03 

02/25/2013 18;04 

02/25/2013 18:05 

02/25/2013 18:06 

02/25/2013 18:07 

02/25/2013 18:08 

02/25/2013 18:09 

02/25/2013 18:10 

02/25/2013 18:11 

02/25/2013 18:12 

02/25/2013 18:13 

02/25/2013 18:14 

02/25/2013 18:15 

02/25/2013 18:16 

02/25/2013 18:17 

02/25/2013 18:18 

02/25/2013 18:19 

02/25/2013 18:20 

02/25/2013 18;21 

02/25/2013 18:22 

02/25/2013 18;23 

02/25/2013 18:24 

02/25/2013 18;25 

02/25/2013 18:26 

02/25/2013 18:27 

02/25/2013 18:28 

02/25/2013 18:29 

02/25/2013 18;30 

02/25/2013 18:31 

Date/Time Printed: 

G45-C2 G4 5-C4 G45-Cll G45-C20 

5>Stk NOx 

Stk NOx 

ppm 

0 - 150 

5>stk 02 5>NOx Mass 5>StkFlow 

1.7 

1.6 

1.7 

1 7 

1.7 

1.7 

1.7 

1.7 

1.6 

1.7 

1.7 

1.B 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.7 

1.6 

1.6 

1.7 

1.7 

1.7 

1.7 

1.6 

1.7 

1.7 

1.7 

1.B 

1.B 

1.7 

1.7 

1.7 

1.7 

1.B 

1.7 

1 .B 

Stk 02 

• 

0-25 

13.85 

13.85 

13.85 

13.85 

13.86 

13.86 

13.84 

13 .86 

13.86 

13.86 

13.84 

13.85 

13.85 

13 . 84 

13.85 

13 .86 

13.87 

13.87 

13 .87 

13.87 

13.88 

13.87 

13 .8 7 

13.87 

13 . 87 

13.86 

13.87 

13.88 

13.88 

13.87 

13.88 

13 .8 8 

13.88 

13.89 

13.88 

13.89 

13.88 

13.88 

13.88 

13.88 

02/25/2013 21,33 

NOx Mass 

1b/hr 

0-100 

3.73 

3.73 

3.73 

3.72 

3.71 

3.70 

3.72 

3.70 

3.70 

3.72 

3.73 

4.47 

3.73 

3.73 

3.73 

3.72 

3.72 

3.71 

3.71 

3.71 

3.70 

3.71 

3.72 

3.70 

3.71 

3.72 

3 .72 

3.72 

3.72 

3.73 

3.71 

4.47 

4.45 

3.70 

3.71 

3.71 

3.71 

4.46 

3.72 

4.47 

StkFlow 

ksefh 

0 - 300000 

19262 

19267 

19274 

19192 

19162 

19146 

19204 

19136 

19149 

19236 

19243 

19256 

19262 

19251 

19272 

19237 

19258 

19226 

19203 

19226 

19196 

19196 

19242 

19170 

19221 

19228 

19289 

19281 

19312 

19302 

19251 

19302 

19250 

19231 

19240 

19256 

19220 

19268 

19300 

19300 

G45-C3 G45 -C13 G45-CI0 G45 -C6 G45 - C7 G45-C8 G45-C18 G45-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXe 5>Stk COe 5>Gas Flow 5>NH3 Inj 5 >MW Lo 

Stk co 

ppm 

0-1000 

2.9 

3.3 

3.7 

3.6 

3.7 

4.0 

4.1 

4.2 

4.8 

4.5 

4.1 

2.5 

3. 1 

3.1 

3.1 

3.4 

2.B 

2.B 

2.3 

3.B 

3.3 

3.0 

4.2 

3.6 

3.9 

3.4 

3.4 

4.1 

4.1 

5.3 

4.1 

3.7 

2.B 

3.4 

3.B 

3.2 

3.5 

3.0 

3.9 

3.6 

CO Mass 

l b /hr 

0 - 100 

3.73 

4.48 

5.22 

5.20 

5.19 

5.92 

5.96 

5.92 

6.67 

5.95 

5.97 

3.73 

4.48 

4.48 

4.48 

4.46 

3.72 

3.71 

2.97 

5.20 

4.44 

4 .45 

5.94 

5.18 

5.20 

4.46 

4.47 

5.95 

5.96 

7.45 

5.94 

5.21 

3.71 

4.44 

5.19 

4.45 

5.19 

4.46 

5.21 

5.21 

NOx Rate 

lb/mmBtu 

0-1 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.00 6 

0.005 

0.005 

0.005 

0.005 

0.006 

0.005 

0.006 

Stk NOXc 

ppm 

0-300 

1.42 

1. 34 

1.42 

1. 42 

1. 42 

1. 42 

1. 42 

1. 42 

1. 34 

1. 42 

1. 42 

1. 51 

1.42 

1.42 

1.42 

1.42 

1.43 

1.43 

1 43 

1. 43 

1. 43 

1. 34 

1.34 

1.43 

1.43 

1.42 

1.43 

1. 34 

1. 43 

1.43 

1.43 

1. 51 

1. 51 

1.43 

1. 43 

1. 43 

1. 43 

1. 51 

1.43 

1. 51 

Stk COe Gas 

ppm 

0-1000 

hscfh 

hscfh 

0-10000 

2 . 43 

2.76 

3.10 

3.01 

3.10 

3.35 

3.43 

3 . 52 

4.02 

3.77 

3.43 

2.09 

2.59 

2.59 

2.59 

2.85 

2.35 

2.35 

1. 93 

3.19 

2.77 

2.52 

3 . 52 

3.02 

3.27 

2.85 

2.85 

3.45 

3.45 

4.45 

3 .4 5 

3.11 

2 . 35 

2.86 

3.19 

2.69 

2 . 94 

2.52 

3.28 

3 . 03 

7104.6 

7106. 4 

7108.8 

7078.8 

7057.8 

7051. 8 

7093.2 

7048.2 

7053.0 

7084.8 

7107.6 

7102.2 

7104.6 

7110.6 

7108.2 

7085.4 

7083.0 

7071. 0 

7062.6 

7071. 0 

7050.0 

7060.2 

7077.0 

7050.6 

7069.2 

7081.8 

7094.4 

7081. 2 

7092.6 

7099.2 

7070.4 

7089.0 

7069.8 

7053.0 

7066.2 

7062.0 

7059.0 

7076.4 

7088.4 

7088.4 

NH3Inj 

lb/hr 

0 - 200 

131.3 

132 . 2 

130.7 

130.5 

129.3 

128.0 

129.2 

128.8 

128.0 

129.0 

130.2 

131.8 

131. 0 

131. 2 

129.3 

130 . 7 

130.8 

129.7 

130.5 

129.8 

128.8 

129.2 

128.0 

127.2 

128.0 

128.8 

129.3 

128.5 

127.7 

127.3 

127.7 

126.8 

129.0 

128.2 

127.7 

127.5 

128.0 

128.0 

128.0 

129.0 

S>Summary - I-Min RATA - Continued 

MW Lo 

0-1 

80. ! 

80 .. 

BO. 

BO 

80.1 

80. ! 

80 . . 

79. 

79 .. 

80.1 

BO. 

80. : 

80. 

80. I 

80.! 

80.1 

80.1 

80.1 

80.1 

80 . 1 

79. 

79 .. 

80.1 

80.1 

80.1 

80 

80. 

80. : 

80. : 

80.1 

80.1 

80. 1 

80.1 

79 . . 

80. : 

79. 

SO. ! 

80. ! 

80 .. 

80. ( 

Pagt 
Group#-Channel# 

Long Descrip . 

Short Desc r i p. 

Units 

Range 

02/25/2013 18:32 

02/25/2013 18:33 

02/25/2013 18:34 

02/25/2013 18:35 

02/25/2013 18:36 

02/25/2013 18;37 

02/25/2013 18:38 

02/25/2013 18:39 

02/25/2013 18:40 

02/25/2013 18:41 

02/25/2013 18:42 

02/25/2013 18:43 

02/25/2013 18:44 

02/25/2013 18:45 

02/25/2013 18:46 

02/25/2013 18:47 

02/25/2013 18:48 

02/25/2013 18:49 

02/25/2013 18:50 

02/25/2013 18:51 

02/25/2013 18:52 

02/25/2013 18:53 

02/25/2013 18:54 

02/25/2013 18:55 

02/25/2013 18:56 

02/25/2013 18:57 

02/25/2013 18:58 

02/25/2013 18:59 

02/25/2013 19:00 

02/25/2013 19:01 

02/25/2013 19:02 

02/25/2013 19:03 

02/25/2013 19:04 

02/25/2013 19:05 

02 / 25/2013 19:06 

02/25/2013 19:07 

02/25/2013 19:08 

02/25/2013 19:09 

02/25/2013 19:10 

02/25/2013 19:11 

Date/Time Printed: 

G45-C2 G45-C4 G45-Cl1 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.9 

1.8 

1.9 

1.9 

1.9 

2.0 

1.9 

1.9 

1.9 

1.8 

1.8 

1.7 

1.8 

1.8 

1.8 

1.8 

1.9 

1.8 

1.8 

1.7 

1.8 

1.7 

1.7 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

Stk 02 

• 

0-25 

13. SS 

13. S8 

13 . 89 

13.88 

13.89 

13.89 

13.87 

13.88 

13 . 87 

13.86 

13.87 

13.86 

13.86 

13.87 

13.88 

13.87 

13.87 

13.88 

13.88 

13.89 

13.90 

13.89 

13.89 

13 . 89 

13.89 

13.90 

13.89 

13.90 

13.89 

13.89 

13.88 

13.88 

13.89 

13.89 

13.89 

13.89 

13.90 

13.90 

13 . 89 

13.89 

02/25/2013 21,33 

NOx Mass 

1b/hr 

0-100 

3.73 

4.47 

4.46 

4.46 

4.47 

4.46 

4.48 

4.48 

4.49 

4.50 

4.49 

4.50 

4.50 

4.50 

4.50 

4. SO 

4.49 

4.49 

4.47 

4.45 

3.70 

4.45 

4.44 

4.45 

4.45 

4.44 

4.45 

4.45 

3.70 

4.46 

3.72 

3.72 

4.46 

4.46 

4.46 

4.45 

4.45 

4.45 

4.46 

4.46 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

19328 

19309 

19316 

19268 

19334 

19313 

19332 

19346 

19385 

19386 

19387 

19407 

19389 

19418 

19434 

19439 

19392 

19392 

19326 

19277 

19224 

19248 

19222 

19240 

19269 

19260 

19267 

19274 

19240 

19302 

19302 

19310 

19318 

19323 

19307 

19272 

19296 

19296 

19310 

19318 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

4.0 

3.7 

2.4 

3.6 

3.1 

3.5 

4.4 

3.6 

4.2 

3.4 

3.7 

4.2 

2.6 

3.2 

3.0 

3 . 2 

2.8 

3.4 

4.2 

4.0 

4.1 

3.0 

3.7 

3.5 

3.8 

3.0 

2.6 

3.2 

3.0 

3.3 

4.1 

4.3 

4.7 

3.6 

4.0 

4.0 

2.6 

3.2 

3.4 

3.4 

G45 - C13 G45-C10 G45-C6 

5>CO Mass 5>NOx Rate 5>Stk NOXc 

CO Mass 

Ib/hr 

0-100 

5.96 

5.21 

3.72 

5.20 

4.47 

5.21 

5.97 

5.22 

5.99 

4.50 

5.24 

6.00 

3.75 

4.50 

4.50 

4.50 

3.74 

4.49 

5.96 

5.94 

5.91 

4.45 

5.18 

5.19 

5.19 

4.44 

3.71 

4.45 

4.45 

4.46 

5.95 

5.96 

6.70 

5 . 21 

5.95 

5.94 

3.71 

4.45 

4.46 

4.46 

NOx Rate 

Ib/mmBtu 

0-1 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.00 6 

0.006 

0.006 

0.006 

o 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 

0.005 

0.006 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0 - 300 

1. 43 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 59 

1. 51 

1. 59 

1. 59 

1. 59 

1. 68 

1 . 59 

1. 59 

1. 60 

1. 51 

1. 51 

1. 43 

1. 51 

1. 51 

1. 51 

1. 51 

1. 60 

1. 51 

1. 52 

1. 43 

1. 51 

1. 43 

1. 43 

1. 51 

1. 51 

1. 51 

1. 51 

1. 52 

1. 52 

1. 51 

1. 51 

G45-C7 G45-C8 G45 - C18 

5>Stk CDc S>Gas Flow S>NH3 Inj 

Stk CDc Gas hscfh NH3Inj 

ppm hscfh Ib/hr 

0-1000 0 - 10000 0-200 

3 . 36 

3.11 

2.02 

3.03 

2.61 

2.95 

3.69 

3.03 

3.52 

2.85 

3.11 

3.52 

2.18 

2.69 

2.52 

2.69 

2.35 

2.86 

3.53 

3.37 

3.46 

2.52 

3.11 

2.95 

3.20 

2.53 

2.19 

2.70 

2.52 

2.78 

3.45 

3 . 61 

3.96 

3.03 

3.37 

3.37 

2.19 

2.70 

2.86 

2.86 

7098.6 

7091.4 

7084.2 

7076.4 

7090.8 

7083.0 

7110.0 

7105.2 

7129.8 

7140.0 

7130.4 

714 7.8 

7141.2 

7141.8 

7137.6 

7149.6 

7132.2 

7122.0 

7098.0 

7069.8 

7040.4 

7059.0 

7049.4 

7056.0 

7066.8 

7053.6 

7066.2 

7058.4 

7056.0 

7078.8 

7089.0 

7092.0 

7084.8 

7086.6 

7080.6 

7068.0 

7066.8 

7066.8 

7081.8 

7084.8 

128.2 

128.8 

129.2 

127.2 

129.0 

128.0 

127.7 

128 . 8 

128.0 

130.0 

129.8 

129.5 

130.0 

129.8 

129.3 

129.5 

131.0 

128.B 

128.5 

128.0 

127.5 

129.3 

12B.0 

127.7 

129.0 

129.3 

131. 0 

130.0 

130.2 

128.2 

129.7 

12B.5 

127.7 

12B.8 

129.3 

128.0 

129.7 

129.3 

127.8 

128.8 

S>Summary - I-Min RATA - Continued 

G45-C 

5>MW Lo 

MW Lo 

0-1 

BO. ! 

BO .. 

80. : 

80 .. 

80. -

80 .. 

80 .. 

80. 

81.1 

81.1 

81.1 

81.1 

81.1 

81.1 

81.: 

81. 

81.1 

81.' 

80 . . 

80.: 

79. 

80.1 

79 . . 

79. : 

80.1 

80.1 

80.1 

80.1 

80.1 

80.: 

80.! 

80. : 

80.: 

80. : 

80. : 

79. : 

80. 

80. 

80.! 

80 .. 

PagE 
Group#-Channel# 

Long Descrip . 

Short Descrip. 

units 

Range 

02/25/2013 19:12 

02/25/2013 19:13 

02/25/2013 19:14 

02/25/2013 19;15 

02/25/2013 19;16 

02/25/2013 19:17 

02/25/2013 19:18 

02/25/2013 19:19 

02/25/ 2 013 19:20 

02/25/2013 19:21 

02/25/2013 19:22 

02/25/2013 19:23 

02/25/2013 19:24 

02/25/2013 19:25 

02/25/2013 19:26 

02/25/2013 19:27 

02/25/2013 19:28 

02/25/2013 19:29 

02/25/2013 19:30 

02/25/2013 19:31 

02/25/2013 19:32 

02/25/2013 19:33 

02/ 2 5/2013 19:34 

02/25/2013 19:35 

02/25/2013 19:36 

02/25/2013 19:37 

02/25/2013 19:38 

02/25/2013 19:39 

02/25/2013 19:40 

02/25/2013 19:41 

02/25/2013 19:42 

02/25/2013 19 :43 

02/25/2013 19:44 

02/25/2013 19:45 

02/25/2013 19:46 

02/25/2013 19:47 

02/25/2013 19:48 

02/ 25 /2013 19:49 

02/25/2013 19:50 

02/25/2013 19:51 

Date/Time Printed: 

G45 - C2 G45-C4 G45-C11 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

1.8 

1.8 

1.8 

1.8 

1.. 

1.8 

1.8 

1.. 

1.B 

1.7 

1.7 

1.7 

1.B 

1.7 

1.7 

1.B 

1.7 

1.7 

1.7 

1.B 

1.8 

1.B 

1.8 

1.B 

1.B 

1.B 

1.7 

1.7 

1.7 

1.7 

1.7 

1.B 

1.8 

1.8 

1.7 

1.B 

1.7 

1.7 

1.7 

1.8 

Stk 02 

• 

0-25 

13.88 

13.89 

13.88 

13.90 

13.89 

13.89 

13.89 

13.90 

13.91 

13.91 

13.92 

13.91 

13.90 

13.89 

13.89 

13.88 

13.89 

13.88 

13.89 

13.88 

13.87 

13 .88 

13.87 

13.88 

13.88 

13.88 

13.88 

13.89 

13.90 

13.89 

13.89 

13.89 

13.90 

13.91 

13.90 

13.91 

13.92 

13.92 

13.91 

13.91 

02/25/2013 21,33 

NOx Mass 

Ib/hr 

0-100 

4.48 

4.47 

4.47 

4.47 

4.47 

4.46 

4.47 

4.47 

4 . 4 5 

3.71 

3.70 

3.70 

4.45 

3.72 

3.71 

4.47 

3.71 

3.71 

3.71 

4.46 

4.47 

4.46 

4.47 

4.46 

4.47 

4.46 

3.71 

3.71 

3.70 

3.72 

3.71 

4.46 

4.45 

4.44 

3.70 

4.43 

3.68 

3.68 

3.68 

4.43 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

19344 

19325 

19333 

19374 

19359 

19308 

19331 

19370 

19329 

19329 

19314 

19273 

19290 

19307 

19287 

19300 

19258 

19251 

19272 

19273 

19279 

19286 

19289 

19259 

19309 

19292 

19243 

19276 

19260 

19298 

19290 

19300 

19287 

19252 

19229 

19245 

19197 

19199 

19176 

19221 

G45-C3 

5>Stk CO 

Stk CO 

ppm 

0-1000 

3.1 

3.6 

3.4 

3.' 

3.' 

3.6 

3.B 

3.6 

3.2 

3.0 

2.6 

3.3 

3.0 

3.1 

3.0 

3.2 

3.2 

2.9 

2.8 

3.1 

2.7 

2.5 

2.7 

3.2 

2.9 

3.2 

3.3 

4.3 

3.0 

3.0 

3.3 

3.4 

3.4 

3.8 

3.6 

3.B 

3.2 

3.4 

3.2 

4.3 

G45-C13 G45-C10 G45-C6 

5>CO Mass 5>NOx Rate 5>Stk NOXc 

CO Mass 

Ib/hr 

0-100 

4.48 

5.21 

4.47 

5.22 

5.22 

5 . 20 

5 . 21 

5.21 

4.45 

4.45 

3.70 

4.44 

4.45 

4.46 

4.46 

4.47 

4.45 

3.71 

3.71 

4.46 

3.72 

3.72 

3.72 

4.46 

3.72 

4.46 

4.45 

5.94 

4.44 

4.46 

4.46 

4.46 

4.45 

5.17 

5.18 

5.17 

4.42 

4.42 

4.42 

5.90 

NOx Rate 

Ib/mmBtu 

0-1 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.005 

0.005 

0.006 

0.005 

0.005 

0.006 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.005 

0.006 

0.005 

0.005 

0.005 

0.006 

Stk NOXc 

ppm 

0-300 

1. 51 

1. 51 

1. 51 

1. 52 

1. 60 

1. 51 

1. 51 

1. 60 

1. 52 

1.43 

1.44 

1.43 

1. 52 

1. 43 

1.43 

1. 51 

1.43 

1.43 

1.43 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1.51 

1. 43 

1.43 

1.43 

1.43 

1.43 

1. 51 

1. 52 

1. 52 

1. 43 

1. 52 

1. 44 

1. 44 

1. 43 

1. 52 

G45-C7 G45 -C8 G4S-C18 

5>Stk COc 5>Gas Flow S;:.NH3 Inj 

Stk COc Gas hscfh NH3Inj 

ppm hscfh Ib/hr 

0-1000 0 -10000 0-200 

2.61 

3.03 

2.86 

3.29 

3.28 

3 .03 

3.20 

3.03 

2 . 70 

2.53 

2.20 

2.79 

2.53 

2.61 

2.52 

2.69 

2.69 

2.44 

2.36 

2 . 61 

2.27 

2.10 

2.27 

2.69 

2.44 

2.69 

2.77 

3.62 

2.53 

2.52 

2.78 

2.86 

2.87 

3.21 

3.03 

3.21 

2.70 

2.87 

2.70 

3.63 

7104.6 

7087.2 

7100.4 

7095.0 

7099.8 

7081.2 

7089.6 

7093.8 

7068.6 

7068.6 

7053.0 

7048.2 

7064.4 

7080.6 

7073.4 

7088.4 

7062.6 

7070.4 

7068.0 

7078.2 

7090.8 

7083.0 

7094.4 

7073.4 

7091. 4 

7085.4 

7067.4 

7069.2 

7053.6 

7077.6 

7074.6 

7078.2 

7063.2 

7040.4 

7042.2 

7038.0 

7010.4 

7011.0 

7012.8 

7029.0 

129.0 

130 . 0 

128.8 

130.0 

129.3 

129.0 

129.8 

129.7 

129.5 

129 .0 

129. B 

129.2 

127.8 

129.5 

129.7 

130.3 

129.3 

129.5 

128.8 

128.5 

130.2 

129.7 

130.8 

129.7 

129.8 

129.2 

129.5 

128.0 

128.2 

130.7 

129.0 

128.0 

128.0 

128.3 

128.2 

127.7 

128.5 

126.7 

127.2 

127.7 

S>Summary - I-Min RATA - continued 

G45-C 

5>MW Lo 

MW Lo 

0-1 

80.' 

80.' 

BO. 

80.' 

BO.: 

80.' 

80 . ~ 

80 . ~ 

80. I 

80.1 

80 .. 

79. : 

80. : 

80 . . 

80,1 

aD .: 

80,1 

aD .: 

80.1 

80.: 

80 , . 

80, : 

80 . ~ 

80. : 

80, : 

ao. : 

80,1 

80,1 

80. 

80. : 

80,1 

80.: 

79. 

79, . 

79. : 

79. ! 

79 , 1 

79. : 

79,1 

79. 

PagE 
Group#-Channel # 

Long Descrip. 

Sho rt Desc rip. 

Un its 

Range 

02/25/2013 19:52 

02/25/2013 19:53 

02/25/2013 19:54 

02/25/2013 19:55 

02/25/2013 19:56 

02/25/2013 19:57 

02/25/2013 19:58 

02/25/2013 19:59 

02/2S/2013 20:00 

02/25/2013 20:01 

02/25/2013 20:02 

02/25/2013 20:03 

02/25/2013 20:04 

02/25/2013 20:05 

02/25/2013 20:06 

02/25/2013 20:07 

02/25/2013 20:08 

02/25/2013 20:09 

02/25/2013 20:10 

02/25/2013 20:11 

02/25/2013 20:12 

02/25/2013 20:13 

02/25/2013 20:14 

02/25/2013 20:15 

02/25/2013 20:16 

02/25/2013 20:17 

02/25/2013 20:1S 

02/25/2013 20:19 

02/25/2013 20:20 

02/25/2013 20:21 

02/25/2013 20:22 

02/25/2013 20:23 

02/25/2013 20:24 

02/25/2013 20:25 

02/25/2013 20:26 

02/25/2013 20:27 

02/25/2013 20:28 

02/ 2 5/ 2013 20:29 

02/25/2013 20:30 

02/25/2013 20:31 

Date/Time Printed: 

G45-C2 G4S-C4 G45-C11 G4S - C20 

5>Stk NOx 

Stk NOx 

S>Stk 02 5>NOx Mass S>StkFlow 

ppm 

0-150 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.7 

1.8 

1.7 

1.8 

1.9 

1.8 

1.9 

1.9 

1.8 

1.8 

1.8 

1.9 

1.7 

1.8 

1.9 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.8 

1.7 

1.7 

1.8 

1.8 

1.7 

1.7 

1.8 

1.7 

1.8 

1.6 

1.6 

1.7 

Stk 02 

• 

0-25 

13.92 

13.93 

13.91 

13.92 

13.92 

13 . 93 

13.91 

13.90 

13.90 

13.91 

13.91 

13.90 

13.90 

13.89 

13.89 

13.91 

13.90 

13.91 

13.90 

13.92 

13.92 

13.92 

13 . 94 

13.92 

13.90 

13.90 

13.91 

13.94 

13.94 

13.91 

13.90 

13.91 

13.92 

13.91 

13.91 

13.92 

13.93 

13.93 

13.93 

13 . 93 

02/25/2013 21,33 

NOx Mass 

1b/hr 

0-100 

4.42 

4.42 

4.43 

4.42 

4.43 

4.41 

3.68 

4.42 

3.70 

4.44 

4.45 

4.47 

4.45 

4.47 

4.48 

4.47 

4.47 

4.46 

3.72 

4.44 

4.44 

4.44 

4.42 

4.43 

4.43 

4.44 

4.45 

4.41 

3.68 

3.68 

4.42 

4.41 

3.67 

3.68 

4.42 

3.67 

4.40 

3.66 

3.66 

3.66 

StkFlow 

kscfh 

0-300000 

19217 

19228 

19226 

19215 

19242 

19215 

19183 

19172 

19224 

19254 

19331 

19357 

19290 

19359 

19369 

19383 

19374 

19357 

19346 

19309 

19312 

19289 

19284 

19253 

19210 

19249 

19321 

19238 

19238 

19185 

19152 

19142 

19132 

19155 

19188 

19161 

19152 

19139 

19095 

19097 

G4S-C3 G45-C13 G4S-CI0 G4S-C6 G45-C7 G45-C8 G4S - C18 G4S-C 

s>stk CO S>CO Mass S>NOx Rate 5>Stk NOXc S>Stk COc S>Gas Flow S>NH3 Inj 5>MW La 

Stk CO 

ppm 

0-1000 

4.7 

3.7 

3.0 

2.7 

3.7 

2.7 

4.0 

3.4 

3.4 

4.2 

3.3 

3.3 

2.9 

3.2 

3.6 

3.5 

5.0 

2.4 

4.2 

3.7 

3.4 

3.5 

3.1 

3.4 

3.0 

3.0 

4.1 

3.1 

3.4 

3.8 

3.0 

2.8 

3.3 

4.1 

3.1 

3.8 

3 . 1 

4.1 

4.6 

3.1 

CO Mass 

Ib/hr 

0-100 

6.63 

5.15 

4.43 

3.68 

5.16 

3.68 

5.89 

4 . 42 

4 . 44 

5.91 

4.45 

4.47 

3.71 

4.47 

5.22 

5.21 

6.71 

3.72 

5.95 

5.18 

4.44 

5.18 

4.42 

4.43 

4.43 

4.44 

5.94 

4.41 

4.41 

5.16 

4.42 

3.68 

4.40 

5.88 

4.42 

5.14 

4.40 

5.86 

6 . 58 

4.39 

NOx Rate 

Ib/mmBtu 

0 - 1 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.005 

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 

0.005 

0.005 

0.006 

0.006 

0.005 

0.005 

0.006 

0.005 

0.006 

0.005 

0.005 

0.005 

Stk NOXc 

ppm 

0-300 

1. 52 

1. 52 

1. 52 

1. 52 

1. 52 

1. 52 

1.43 

1. 52 

1.43 

1. 52 

1. 60 

1. 52 

1. 60 

1. 60 

1. 51 

1.52 

1. 52 

1.60 

1.43 

1. 52 

1. 61 

1. 52 

1. 53 

1. 52 

1. 52 

1. 52 

1. 52 

1. 53 

1. 44 

1. 43 

1. 52 

1. 52 

1.44 

1. 43 

1. 52 

1. 44 

1. 52 

1. 35 

1. 35 

1. 44 

Stk COc Gas 

ppm 

hscfh 

hscfh 

0-1000 

3.97 

3.13 

2.53 

2.28 

3.13 

2.29 

3.38 

2. 87 

2.87 

3.55 

2.79 

2.78 

2.44 

2.69 

3.03 

2.95 

4.21 

2.03 

3.54 

3.13 

2 . 87 

2.96 

2.63 

2.87 

2.53 

2.53 

3.46 

2.63 

2. S8 

3.21 

2.53 

2.36 

2.79 

3.46 

2.62 

3.21 

2.62 

3.47 

3.89 

2.62 

0-10000 

7017.6 

7011.6 

7030.8 

7017.0 

7026.6 

7006.8 

7015.2 

7021.2 

7040.4 

7041.0 

7069.2 

7089.0 

7064.4 

7099.8 

7103.4 

7088.4 

7095.0 

7078.8 

7084.S 

7051.2 

7052.4 

7044.0 

7021.8 

7030.8 

7035.0 

7049.4 

7065.6 

7005.0 

7005.0 

7015.8 

7014.0 

7000.2 

6986.4 

7005.0 

7017.0 

6997.2 

6984 . 0 

6979.2 

6963.0 

6963.6 

NH3Inj 

1b/hr 

0 - 200 

125.8 

126.0 

128.3 

128.7 

126.8 

128.2 

126.0 

127.0 

126.8 

125.7 

128.8 

130.3 

129.2 

129.0 

128.3 

129.2 

126.8 

131. 0 

128.0 

128.2 

12S.2 

12S.5 

127.7 

127.5 

128.0 

12S.0 

12S.2 

127.3 

127 . 3 

126.2 

128.7 

126 . 7 

127.3 

126.5 

127.7 

127.8 

127.2 

127.0 

126.5 

126.8 

S>Summary - 1-Min RATA - Continued 

MW Lo 

0-1 

79 .. 

79 .. 

79 .. 

79. : 

79 .. 

79" 

79. ( 

79 . . 

79 .. 

79 . 

80. ( 

80. f 

80 .. 

80.: 

80 .. 

80. 

80 

80.: 

80.f 

79. 

80 .. 

SO .1 

79. : 

79 .. 

79 .. 

80. f 

80. ( 

79. : 

79. ( 

79 .. 

79. : 

79.( 

79. t 

79.: 

79. ( 

79. ( 

79. ( 

78 .. 

78 .. 

78. ( 

Pag( 
Group#-Channel# 

Lo ng Des cri p. 

Short De scrip . 

Units 

Range 

02/25/2013 20:32 

02/25/2013 20:33 

02/25/2013 20:34 

02/25/2013 20:35 

02/25/2013 20:36 

02/25/2013 20:37 

02/25/2013 20:38 

02/25/ 2 013 20:39 

02/25/2013 20:40 

02/25/2013 20:41 

02/25/2013 20:42 

02/25/2013 20:43 

02/25/2013 20:44 

02/25/2013 20:45 

02/25/2013 20:46 

02/25/2013 20:47 

02/25/2013 20:48 

02/25/2013 20:49 

02/25/2013 20:50 

02/25/2013 20:51 

02/25/2013 20:52 

02/25/2013 20:53 

02/25/2013 20:54 

Period Average 

Period Max Value 

Period Min Value 

Period Totals = 

Period % Recovery 

Date/Time Printed: 

G45-C2 G45 - C4 G45-C11 G45-C20 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 5>StkFlow 

1.7 

1.7 

1.7 

1.8 

1.6 

1.6 

1.8 

1.7 

1.8 

1.8 

1.8 

1.8 

1.7 

1.7 

1.7 

1.7 

1.6 

1.7 

1.6 

1.7 

1.7 

1.8 

1.7 

1.7 

2.0 

1.2 

Stk 02 

• 

0-25 

13 . 93 

13.92 

13.91 

13 .92 

13.91 

13.91 

13.93 

13 . 90 

13.90 

13.89 

13.90 

13.92 

13.92 

13.92 

13.92 

13.92 

13.93 

13.93 

13.93 

13.92 

13.91 

13.92 

13.92 

13.88 

13.94 

13.82 

4.3120E+2 3.5126E+3 

100.0 100.0 

02/25/2013 21,33 

NOx Mass 

1b/hr 

0-100 

3.66 

3.67 

3.67 

4.39 

3.67 

3.67 

4.38 

3.67 

4.41 

4.41 

4.40 

4.40 

3.66 

3.65 

3.65 

3.66 

3.65 

3.66 

3.65 

3.66 

3.67 

4.39 

3.66 

3.95 

4.51 

2.93 

StkFlow 

ksefh 

0-300000 

19115 

19122 

19132 

19100 

19131 

19116 

19085 

19100 

19098 

19078 

19084 

19140 

19112 

19049 

19045 

19074 

19059 

19098 

19080 

19076 

19116 

19063 

19100 

19243 

19439 

19045 

9.9986E+2 4.8684E+6 

100.0 100.0 

G45-C3 G45-C13 G45-C10 G45-C6 G45-C7 G45-C8 G45-C18 G45-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXe 5>Stk COe 5>Gas Flow 5>NH3 Inj 5>MW Lo 

Stk CO 

ppm 

0-1000 

3.2 

3.3 

5.3 

3.6 

5.5 

6.4 

2.8 

4.6 

3.9 

3.1 

2.9 

2.8 

3.0 

1.9 

1.7 

1.7 

2.7 

1.8 

3.1 

3.4 

4.8 

2.9 

3.4 

3.1 

6.4 

0.3 

7.7340E+2 

100.0 

CO Mass 

1b/hr 

0-100 

4.39 

4.40 

7.35 

5.13 

7.35 

8.81 

3.65 

6.61 

5.14 

4.41 

3.67 

3.67 

4.40 

2.92 

2.19 

2.19 

3.65 

2.19 

4.38 

4.39 

6.61 

3.65 

4.39 

4.27 

8.81 

0.73 

1.0814E+3 

100.0 

NOx Rate 

lb/mmBtu 

0-1 

0.005 

0.005 

0.005 

0.006 

0.005 

0.005 

0.006 

0.005 

0.006 

0.006 

0.006 

0.006 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.005 

0.006 

0.005 

0.005 

0.006 

0.004 

Stk NOXe 

ppm 

0-300 

1. 44 

1. 44 

1. 43 

1. 52 

1.35 

1. 35 

1. 52 

1. 43 

1. 52 

1. 51 

1. 52 

1. 52 

1.44 

1. 44 

1. 44 

1. 44 

1. 35 

1. 44 

1. 35 

1.44 

1.43 

1. 52 

1.44 

1. 43 

1. 68 

1. 01 

1.3480E+0 3.6243E+2 

100.0 100.0 

Stk COe Gas 

ppm 

0-1000 

hsefh 

hsefh 

0 - 10000 

2.71 

2.79 

4.47 

3.04 

4.64 

5.40 

2.37 

3.88 

3.29 

2.61 

2.44 

2.37 

2.54 

1. 61 

1.44 

1.44 

2.29 

1. 52 

2.62 

2.87 

4.05 

2.45 

2.87 

2.57 

5.40 

0.25 

6970.2 

6982.8 

6996.6 

6975.0 

6996.0 

6990.6 

6959.4 

6994.8 

6994.2 

6996.6 

6988.8 

6989.4 

6979.2 

6956.4 

6954.6 

6965.4 

6949.8 

6964.2 

6957.6 

6966.0 

6990.6 

6961.2 

6975.0 

7063.1 

7159.8 

6949.8 

NH3Inj 

1b/hr 

0-200 

126.2 

126.5 

125.0 

127.3 

124.8 

124.2 

127.3 

125.2 

126.2 

127.2 

126.8 

127.8 

125.7 

127.5 

128.2 

128.3 

126.0 

127.5 

124.7 

126.0 

124.2 

126.5 

126.0 

130.7 

149.5 

124.2 

MW Lo 

0-,1 

78 .. 

78. 

79.1 

78.: 

78. : 

78. ! 

78 .. 

78. 

79.1 

79.1 

79.1 

79.1 

78 .. 

78. : 

78 .. 

78. : 

78.1 

78. : 

78.1 

78. 

78. : 

78. : 

78 .. 

80.0 

81. 

78. 

6.5051E+2 

100.0 

1.7869E+6 3.3069E+4 2.0259E+ 

100.0 100.0 100. 

5>Summary - I-Min RATA - Continued PagE 
Data Summary Report 

Company: CPV Sentinel. LLC 

62575 Powerline Road 

Desert Hot Springs, CA 92240 

»~A.l\ 

l Orl'}D 

6 

PM 

Source: 

Data Group : 

Report Name : 

Start of Report: 

Turbine 5 

5>1~Min Cales 

S>Summary - 1 - Min RATA 

02/25/2013 10,56 

G45-C4 

End of Report, 0 2 / 25/2013 15,20 

G4S-Cll G4S-C20 G4S-C3 G4S - C13 

TRACE 

Environmental Systems, fllC. 

Validation: All Available Data 

Group#-Channel# G45-CIO G45 - C6 G4S-C7 G4S - C8 G45 - C18 G45 - C 

Long Descrip. 

Short Descrip. 

Units 

G45 - C2 

S>Stk NOx 

Stk NOx 

ppm 

0 - IS0 

5>Stk 02 5>NOx Mass 5>StkFlow s>Stk CO S>CO Mass S>NOx Rate 5>Stk NOXc 5>Stk CDc 5>Gas Flow 5>NH3 Inj 5>MW La 

Range 

02/25/2013 10:56 

02/25/2013 10:57 

02 / 25/2013 10:58 

02/25/2013 10:59 

02/25/2013 11:00 

02/25/2013 11:01 

02/25/2013 11:02 

02/25/2013 11:03 

02/25/2013 11:04 

02 / 25/2013 11:05 

02 / 25/2013 11:06 

02/25/2013 11:07 

02/25/2013 11:08 

02/25/2013 11:09 

02/25/2013 11:10 

02 / 25/2013 11:11 

02 / 25/2013 11:12 

02/25/2013 11: 13 

02/25/2013 11:14 

02/25/2013 11:15 

02/25/2013 11:16 

02/25/2013 11:17 

02/25/2013 11:18 

02 / 25/2013 11:19 

02/25/2013 11:20 

02 / 25/2013 11:21 

02/25/2013 11:22 

02/25/2013 11:23 

02/25/2013 11:24 

02/25/2013 11:25 

Date/Time Pri nted: 

1.8 

1.8 

1.8 

1.8 

1.9 

1.8 

1.8 

1.8 

1.9 

1.8 

1.8 

1.8 

1.8 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.8 

1.9 

1.9 

1.8 

1.9 

1.9 

Stk 02 

• 

0-25 

13 .48 

13 .47 

13 .47 

13 .47 

13 .48 

13 .47 

13 .47 

13 .48 

13.48 

13 .48 

13 .47 

13 .47 

13 .47 

13 .47 

13 .47 

13 .47 

13.47 

13 .47 

13 .47 

13 .48 

13 .48 

13 .48 

13 .47 

13.47 

13 .48 

13 .47 

13 .46 

13 .46 

13 . 46 

13.46 

02/25/2013 21,)2 

NOx Mass 

1b/hr 

0-100 

4.60 

4.60 

4.59 

4.59 

5.51 

4.60 

4.60 

4 . 59 

5 . 52 

4.60 

4.59 

4.60 

4.59 

5.52 

5.51 

5.52 

5 . 51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

4 . 59 

5.51 

5.52 

4.59 

5.51 

5.51 

stkFlow 

kscfh 

0-300000 

22552 

22520 

22509 

22509 

22544 

22525 

22528 

22540 

22555 

22552 

22509 

22519 

22514 

22520 

22512 

22522 

22492 

22483 

22494 

22530 

22527 

22524 

22488 

22506 

22538 

22500 

22495 

22481 

22488 

22462 

Stk CO 

ppm 

0 - 1000 

3.5 

3.9 

3.8 

3.8 

3.5 

4.2 

3.9 

4.2 

3.7 

3.7 

3.9 

3.4 

3.8 

3.6 

3.8 

2.8 

2.9 

2 . 7 

2.6 

2.7 

2.8 

2.7 

2.6 

2.8 

2.6 

3. 0 

2.8 

3.7 

2.9 

3 . 1 

CO Mass 

1b/hr 

0 - 100 

5.52 

6.43 

6.43 

6.43 

5 . 51 

6.44 

6.44 

6.43 

6.44 

6.43 

6.43 

5.51 

6.43 

5.52 

6.43 

4.60 

4 . 59 

4.59 

4.59 

4.59 

4.59 

4.59 

4.59 

4.59 

4.59 

4.59 

4.60 

6.43 

4.60 

5.51 

NOx Rate 

Ib/mmBtu 

0-1 

0.005 

0.005 

0.005 

0.005 

0.006 

0.005 

0.005 

0.005 

0.006 

0.005 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.006 

0.005 

0.006 

0.006 

Stk NOXc 

ppm 

0 - 300 

1.43 

1. 43 

1. 43 

1. 43 

1. 51 

1. 43 

1.43 

1. 43 

1. 51 

1.43 

1.43 

1. 43 

1. 43 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 5 1 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1.43 

1. 51 

1. 51 

1. 43 

1. 51 

1. 51 

Stk CDc Gas 

ppm 

0-1000 

hscfh 

hscfh 

0 - 10000 

2.78 

3.10 

3.02 

3.02 

2.78 

3.34 

3.10 

3.34 

2.94 

2.94 

3.10 

2.70 

3.02 

2.86 

3.02 

2.22 

2.30 

2.14 

2.06 

2.15 

2.23 

2.15 

2.06 

2.22 

2.07 

2.38 

2.22 

2.93 

2.30 

2.46 

8754.6 

8754.0 

8749.8 

8749.8 

8751.6 

8755.8 

8757.0 

8749.8 

8755.8 

8754.6 

8749.8 

8753.4 

8751.6 

8754.0 

8751.0 

8754.6 

8743 . 2 

8739.6 

8743.8 

8746.2 

8745.0 

8743.8 

8741.4 

8748.6 

8749.2 

8746.2 

8755.8 

8750.4 

8753.4 

8743.2 

NH3Inj 

Ib/hr 

0 - 200 

196.5 

195.8 

194.8 

194.8 

196.3 

196.3 

197.2 

194.7 

194.8 

196.0 

194.7 

195 . 2 

195.0 

194.5 

195.5 

196.2 

195.7 

196.5 

196.0 

195.7 

194.7 

195.0 

197.3 

195.8 

197.2 

195.8 

196.7 

195.0 

197.0 

195.8 

MW Lo 

0-1 

105 .. 

105. : 

105. : 

105. 1 

105 . . 

105 .. 

105. 

105. 

105 . . 

IDS. : 

106.1 

105. 

106. ( 

105. ! 

105. 1 

105 . . 

1 05. 

105 

105. 

106. : 

106.1 

105. : 

106.1 

106.1 

105 . . 

106.1 

105. : 

106. ( 

lOS. : 

106.1 

PagE 
Group#-Channel# 

Long Descrip . 

Sh ort Des c rip . 

Units 

Range 

02/25/2013 11:26 

02/25/2013 11:27 

02/25/2013 11:28 

02/25/2013 11:29 

02/25/2013 11 ;30 

02/25/2013 11:31 

02/25/2013 11:32 

02/25/2013 11:33 

02/25/2013 11:34 

02/25/2013 11:35 

02/25/2013 11:36 

02/25/2013 11:37 

02/25/2013 11: 38 

02/25/2013 11:39 

02/25/ 2 013 11:40 

02/25/2013 11:41 

02/25/2013 11:42 

02/25/2013 11:43 

02/25/2013 11:44 

02/2 5/2013 11:45 

02/25/2013 11:46 

02/25/2013 11:47 

02/25/2013 11:48 

02/25/2013 11:49 

02/25/2013 11:50 

02 / 25/2013 11:51 

02/25/2013 11:52 

02/25/2013 11:53 

02/25/2013 11:54 

02/25/2013 11:55 

02/25/2013 11:56 

02/25/2013 11: 5 7 

02/25/2013 11:58 

02/25/2013 11: 59 

02/2 5/2013 12:00 

02/25/2013 12:01 

02/25/2013 12:02 

02/25/2013 12:03 

02/25/2013 12:04 

02/25/2013 12:05 

Date/Time Printed: 

G45-C2 G45-C4 G45-C11 G45-C2 0 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 5>StkFlow 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

2.7 

2.0 

1.9 

1.9 

1.9 

Stk 02 

• 

0-25 

13 . 46 

13 .46 

13 .47 

13 .46 

13.47 

13 .47 

13 .46 

13.46 

13.46 

13 . 47 

13.47 

13 .47 

13.46 

13. 4 6 

13 . 46 

13.47 

13.46 

13 .46 

13 .46 

13 .46 

13 .46 

13 . 45 

13. 4 5 

13.46 

13. 4 6 

13.46 

13 .46 

13 .46 

13 .47 

13 .46 

13 .46 

13 . 45 

13 .45 

13.45 

13 .46 

13 .46 

13 .45 

13 .46 

13 .46 

13 .45 

02/25/2013 21,32 

NOx Mass 

1b/hr 

0-100 

5.51 

5.5 1 

5.51 

5.51 

5.51 

5.51 

5 .51 

5.52 

5.52 

5.51 

5.51 

5.51 

5.51 

5.52 

5.51 

5.51 

5.52 

5.51 

5.52 

5.51 

5.51 

5.52 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.50 

7.34 

5.51 

5.51 

5.50 

5.50 

StkFlow 

kscfh 

0-300000 

22488 

22471 

22509 

22462 

22492 

22497 

22467 

22490 

22490 

22511 

2250B 

22503 

22487 

22490 

2 2471 

22509 

22490 

22487 

22498 

22487 

22478 

22460 

22441 

22454 

22462 

22471 

22471 

22476 

22494 

22467 

22 4 50 

22446 

22444 

22444 

22447 

22454 

22424 

22450 

22441 

22415 

G45-C3 G45-C13 G45-C10 G45-C6 G45-C7 G45-CB G45-C18 G45-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXc 5>Stk COc 5>Gas Flow 5>NH3 Inj 5>MW Lo 

Stk CO 

ppm 

0-1000 

2.9 

2.9 

3.0 

2.9 

3.1 

3.0 

2.7 

3.0 

3.1 

2." 

3.0 

2." 

3.0 

3.7 

3.7 

3.5 

3." 

3.6 

3.5 

3.5 

3.3 

3.9 

3.0 

2.9 

2.5 

2.5 

2." 

2.9 

3.1 

2.7 

2.7 

2.5 

3.2 

3.2 

2." 

2.9 

3.1 

2.9 

3.0 

3.6 

CO Mass 

1b/hr 

0-100 

4.60 

4. 59 

4.59 

4.59 

5.51 

4.59 

4.59 

4.60 

5.52 

4.59 

4.59 

4.59 

4.60 

6.43 

6 . 43 

5.51 

6.43 

5.51 

5.52 

5.51 

5.51 

6.43 

4.59 

4.59 

3.67 

3.67 

4.59 

4.59 

5.51 

4.59 

4.59 

3.67 

5.51 

5.51 

4.59 

4.59 

5.51 

4.59 

4.59 

5.50 

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 

0.006 

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 

0 . 006 

0.006 

0.006 

0.006 

0.006 

0.008 

0.006 

0.006 

0.006 

0.006 

Stk NOXc 

ppm 

0 -3 00 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

l. 51 

1. 51 

l. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 50 

1. SO 

1. 51 

l. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1. 51 

1.50 

1.50 

1. 50 

1. 51 

2.14 

1. 58 

1. 51 

1. 51 

1. SO 

Stk COc Gas hscfh 

ppm hscfh 

0-1000 0 - 10000 

2.30 

2.30 

2 . 38 

2.30 

2.46 

2.38 

2.14 

2.38 

2.46 

2 . 22 

2.38 

2.22 

2.38 

2.93 

2.93 

2.78 

3.01 

2. B5 

2.78 

2.78 

2.62 

3.09 

2 . 38 

2.30 

1. 98 

1. 98 

2.22 

2.30 

2.46 

2.14 

2.14 

1. 98 

2.53 

2.53 

2.22 

2.30 

2.46 

2.30 

2.38 

2.85 

8753.4 

8746.8 

8749.8 

874.3 .2 

8743.2 

8745.0 

8745.0 

8754.0 

8754.0 

8750.4 

8749.2 

8747.4 

8752 . 8 

8754.0 

8746.8 

8749.8 

8754.0 

8752.8 

8757.0 

8752.8 

8749.2 

8754.0 

8746.8 

8740.2 

8743.2 

8746.8 

8746.8 

8748.6 

8743.8 

8745.0 

8738.4 

8748.6 

8748.0 

8748.0 

8737.2 

8740.2 

8740.2 

8738.4 

8734.8 

8736.6 

NH3Inj 

1b/hr 

0 -200 

196.3 

196.7 

195.7 

196 .7 

196.5 

197.5 

197.0 

195 . 0 

196.2 

196.2 

196 .2 

195.8 

195.8 

195.0 

195.7 

195.7 

163.8 

196.0 

196.5 

195.3 

196.3 

194.3 

196.0 

196.5 

196 .2 

196 .3 

197.0 

198.0 

196.0 

196.0 

197.3 

195.7 

196.5 

196.5 

179.2 

189.2 

196.2 

196.3 

196.5 

195.3 

S>Summary - I-Min RATA - Continued 

MW Lo 

0-1 

106.1 

105. ' 

106. 1 

105. ' 

106.1 

106.1 

106,1 

105. : 

106.1 

105. : 

105. : 

105. : 

106. r 

106.1 

lOS, 

106.1 

105. 

106.1 

106. r 

105, : 

105. : 

106,1 

106.1 

106.1 

106,1 

106.1 

105. 

106.1 

105. : 

106.1 

105. : 

106.1 

105. : 

105. : 

106, 1 

105. 

105. 

106.1 

106,1 

105. : 

PagE 
Group#-Channel# 

Long Descrip. 

Short Descrip. 

units 

Range 

02/25/2013 12:06 

02/25/2013 12 :07 

02/25/2013 12:08 

02/25/2013 12:09 

02/25/2013 12:10 

02/25/2013 12:11 

02/25/2013 12:12 

02/25/2013 12:13 

02/25/2013 12;14 

02/25/2013 12;15 

02/25/2013 12;16 

02/25/2013 12;17 

02/25/2013 12;18 

02/25/2013 12;19 

02/25/2013 12;20 

02/25/2013 12:21 

02/25/2013 12:22 

02/25/2013 12:23 

02/25/2013 12:24 

02/25/2013 12:25 

02/25/2013 12;26 

02/25/2013 12:27 

02/25/2013 12;28 

02/25/2013 12:29 

02/25/2013 12:30 

02/25/2013 12:31 

02/25/2013 12:32 

02/25/2013 12:33 

02/25/2013 12:34 

02/25/2013 12:35 

02/25/2013 12;36 

02/25/2013 12:37 

02/25/2013 12:38 

02/25/2013 12:39 

02/25/2013 12:40 

02/25/2013 12;41 

02/25/2013 12:42 

02/25/2013 12:43 

02/25/2013 12:44 

02/25/2013 12:45 

Date/Time Printed: 

G4S-C2 G45-C4 G4S-C11 G4S-C20 

S>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 5>StkFlow 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.8 

1.9 

Stk 02 

• 

0-25 

13.46 

13.46 

13.45 

13.45 

13. 4 5 

13.45 

13.45 

13. 4 5 

13.45 

13 .4 5 

13.44 

13.44 

13.44 

13 .44 

13 .44 

13 .44 

13 .45 

13 .45 

13 .45 

13 .45 

13 .44 

13 .44 

13 .44 

13 .43 

13.44 

13 .44 

13.44 

13.44 

13 .44 

13 .44 

13 .44 

13 .44 

13.44 

13.43 

13.43 

13 .44 

13.44 

13 .44 

13 .43 

13 .44 

02/25/2013 21,32 

NOx Mass 

1b/hr 

0-100 

5.51 

5.50 

5.50 

5.51 

5.51 

5.51 

5.51 

5.50 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.52 

5.51 

5.51 

5.51 

5.51 

5.52 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.52 

5.51 

5.51 

5.51 

5.51 

4.60 

5.51 

StkFlow 

kscfh 

0-300000 

22453 

22436 

22415 

22430 

22427 

22432 

22440 

22415 

22424 

22424 

22408 

22405 

22420 

22410 

22420 

22402 

22443 

22434 

22463 

22430 

22411 

22422 

22420 

22407 

22396 

22420 

22402 

2240 8 

22422 

22425 

22419 

22423 

22405 

22404 

22395 

22423 

22399 

22417 

22396 

22408 

G4S-C3 G45-C13 G45-C10 G45-C6 G45 - C7 G45-C8 G4 5 - C18 G4S-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXc 5>Stk COc S>Gas Flow S>NH3 Inj 5>MW Lo 

Stk co 

ppm 

0-1000 

3.0 

3.1 

2.8 

3.2 

3.4 

3.1 

3.1 

2.9 

3.2 

3.6 

3.1 

3.2 

3.4 

3.4 

3.7 

3.7 

3.3 

3.1 

3.2 

3.6 

3.5 

3.8 

3.3 

3 . 6 

3.2 

3.5 

3.6 

3.0 

3.2 

3.6 

3.1 

3.6 

3.6 

3.2 

3.1 

2.8 

3.0 

2.5 

2.8 

2.7 

CO Mass 

1b/hr 

0-100 

4.59 

5.50 

4.59 

5.51 

5.51 

5.51 

5.51 

4.59 

5.51 

5.51 

4.59 

5.51 

5.51 

5.51 

6.43 

6.43 

5.51 

5.51 

5.52 

5.51 

5.51 

6.43 

5.51 

5.52 

5.51 

5.51 

5.51 

4.59 

5.51 

5.51 

4.59 

5.51 

5.51 

5.52 

4.60 

4.59 

4.59 

3.67 

4.60 

4.59 

NDx 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 

0.006 

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 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

Stk NOXc 

ppm 

0-300 

1. 51 

1. 51 

1. 50 

1. 50 

1.50 

1. SO 

1. 50 

1. SO 

1. 50 

1. SO 

1. SO 

1. 50 

1. SO 

1.50 

1.50 

1. SO 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. SO 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. SO 

1. 50 

1. 50 

1. SO 

1. 50 

1. 50 

1. SO 

1. 50 

1. 42 

1. SO 

Stk CDc Gas 

ppm 

0-1000 

2.38 

2.46 

2.22 

2.53 

2.69 

2.46 

2 .4 6 

2.30 

2.53 

2.85 

2.45 

2.53 

2.69 

2.69 

2.93 

2.93 

2.61 

2.46 

2.53 

2.85 

2.77 

3 . 01 

2.61 

2.84 

2.53 

2.77 

2.85 

2.37 

2.53 

2.85 

2.45 

2.85 

2.85 

2.S3 

2.45 

2.21 

2.37 

1. 98 

2.21 

2.14 

hscfh 

hscfh 

0-10000 

8739.6 

8733.0 

8736.6 

8742.6 

8741. 4 

8743.2 

8746.2 

8736.6 

8740.2 

8740.2 

8745.6 

8744.4 

8750.4 

8746.2 

8750.4 

8743.2 

8747.4 

8743.8 

8755.2 

8742.6 

8746.8 

8751.0 

8750.4 

8757.0 

8740.8 

8750.4 

8743.2 

8745.6 

8751.0 

8752.2 

8749.8 

8751.6 

8744.4 

8755.8 

8752.2 

8751.6 

8742.0 

8749.2 

8752.8 

8745.6 

NH3Inj 

1b/hr 

0-200 

197.3 

197.0 

197.3 

197.0 

195.7 

197.2 

197.3 

196.7 

196.3 

195.7 

195.7 

195.8 

195.7 

195.2 

196.5 

196.8 

196.2 

195.7 

197.5 

196.5 

196.3 

195.3 

195.8 

194.5 

195.5 

195.3 

194.2 

196.3 

195.7 

196.0 

196.2 

195.7 

195.2 

195.7 

194.7 

196.0 

196.5 

196.0 

197.2 

195.8 

S>Summary - 1-Min RATA - Continued 

MW Lo 

0-1 

106.1 

105 .. 

106.1 

105. 

105. 

106. ( 

106. ( 

106 . 1 

106. ( 

105. : 

106.1 

106. ( 

106. t 

106.1 

105. 

105. : 

105. 

106.1 

106. ( 

106.1 

106. ( 

106.1 

106.1 

106.1 

106.1 

105. : 

106.1 

105. : 

106.1 

106.1 

106.1 

105. 

106. ( 

105. : 

106.1 

106.t 

106.1 

105. : 

106.1 

106.1 

Pag( 
Group#-Channe l# 

Long Descr i p . 

Short De sc r i p . 

Units 

Range 

02/25/2013 12:46 

02/25/2013 12:47 

02/25/2013 12:48 

02/25/2013 12:49 

02/25/2013 12:50 

02/25/2013 12:51 

02/25/2013 12:52 

02/25/2013 12:53 

02/25/2013 12:54 

02/25/2013 12:55 

02/25/2013 12:56 

02/25/2013 12:57 

02/25/2013 12:58 

02/25/2013 12:59 

02/25/2013 13:00 

02/25/2013 13:01 

02/25/2013 13:02 

02/25/2013 13:03 

02/25/2013 13:04 

02/25/2013 13:05 

02/25/2013 13:06 

02/25/2013 13:07 

02/25/2013 13:08 

02/25/2013 13:09 

02/25/2013 13:10 

02/25/2013 13:11 

02/25/2013 13:12 

02/25/2013 13:13 

02/25/2013 13:14 

02/25/2013 13:15 

02/25/2013 13:16 

02/25/2013 13:17 

02/25/2013 13:18 

02/25/2013 13:19 

02/25/2013 13:20 

02/25/2013 13:21 

02/25/2013 13:22 

02/25/2013 13:23 

02/25/2013 13:24 

02/25/2013 13:25 

Date/Time Printed: 

G45 - C2 G45-C4 G4S-Cl1 

5::>Stk NOx 

Stk NOx 

ppm 

0 - 150 

5::>Stk 02 5::>NOx Mass 

1.. 

1.' 

2.8 

2.0 

2.0 

1.' 1.. 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 1., 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

Stk 02 

% 

0-25 

13. 4 3 

13.43 

13.43 

13.44 

13.44 

13 .43 

13 . 43 

13.43 

13.43 

13 .43 

13 .42 

13 .43 

13 .43 

13 .43 

13 . 42 

13.42 

13.43 

13 .43 

13.43 

13 .43 

13 .43 

13 .43 

13 .43 

13 .42 

13 .43 

13.43 

13.43 

13 .43 

13 .42 

13 .42 

13 .41 

13 .42 

13 .42 

13 .43 

13.42 

13.42 

13.42 

13 . 41 

13 . 42 

13.42 

02/25/2013 21,32 

NOx Mass 

1b/hr 

0 -100 

5.51 

5.51 

7.34 

5.51 

5.50 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.51 

5.50 

5.50 

5.50 

5.50 

5.51 

5.51 

5.50 

5.50 

5.50 

5.50 

5.51 

5.50 

5.50 

5.50 

5.50 

G45-C20 

5::>StkFlow 

StkFlow 

ksefh 

0-300000 

22393 

22367 

22347 

22397 

22385 

22367 

22375 

22364 

22373 

22369 

22356 

22366 

22361 

22361 

22348 

22342 

22380 

22373 

22367 

22384 

22373 

22370 

22364 

22354 

22358 

22355 

22343 

22347 

22325 

22334 

22305 

22305 

22314 

22349 

22316 

22330 

22324 

22289 

22308 

22304 

G45-C3 

5::>Stk CO 

Stk CO 

ppm 

0-1000 

3.2 

3.2 

3.4 

2.9 

3.0 

2.5 

3.0 

2.8 

2.8 

2.8 

3.2 

3.3 

2.8 

2.8 

2.7 

2.8 

3.3 

2.7 

2.9 

2.9 

2.9 

2.6 

2.8 

3.1 

2.5 

2.4 

2.5 

2.3 

2.7 

2.5 

2.4 

2.5 

2.4 

2 . 3 

2.4 

2.5 

2.8 

2.8 

2.2 

2.5 

G45 -C13 G45-ClO G45-C6 

5::>CO Mass 5::>NOx Rate 5::>Stk NOXe 

CO Mass 

1b/hr 

0-100 

5.51 

5.51 

5.50 

4.59 

4.59 

3.67 

4.59 

4.59 

4.59 

4.59 

5.51 

5.51 

4.59 

4.59 

4.59 

4.59 

5.51 

4.59 

4.59 

4.59 

4.59 

4.59 

4.59 

4.59 

3.67 

3.67 

3.67 

3.67 

4.59 

3.67 

3.67 

3.67 

3.67 

3.67 

3.67 

3.67 

4.59 

4.59 

3.67 

3.67 

NOx Rate 

lb/mmBtu 

0-1 

0.006 

0.006 

0.008 

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 

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. 50 

1. SO 

2.21 

1. 58 

1. 58 

1. 50 

1. SO 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. SO 

1. 50 

1. SO 

1. 50 

1. SO 

1. 50 

1. 50 

1. SO 

1. SO 

1. SO 

1. SO 

1. SO 

1. 50 

1. SO 

1. SO 

1. 50 

1. SO 

1. SO 

1. 50 

1. 50 

1. SO 

1. SO 

1. 50 

1. SO 

1. 50 

1. SO 

1. SO 

1. SO 

G4S-C7 G45-C8 

5::>Stk COe 5::>Gas Flow 

Stk COe Gas hsefh 

ppm hsefh 

0-1000 0-10000 

2.53 

2.53 

2.69 

2.29 

2.37 

1. 97 

2.37 

2.21 

2.21 

2.21 

2.52 

2.61 

2.21 

2.21 

2.13 

2.21 

2.61 

2.13 

2.29 

2.29 

2.29 

2.05 

2.21 

2.45 

1. 97 

1. 90 

1. 97 

1.82 

2.13 

1. 97 

1. 89 

1. 97 

1. 89 

1. 82 

1. 89 

1. 97 

2.21 

2 . 21 

1. 74 

1. 97 

8751.6 

8741 4 

8733.6 

8741. 4 

8736.6 

8741.4 

8744.4 

8740.2 

8743.8 

8742.0 

8748.6 

8740.8 

8739.0 

8739.0 

8745.6 

8743.2 

8746.2 

8743.8 

8741.4 

8748.0 

8743.8 

8742.6 

8740.2 

8748.0 

8737.8 

8736.6 

8731.8 

8733.6 

8736.6 

8740.2 

8740 . 2 

8728.8 

8732.4 

8734.2 

8733.0 

8738.4 

8736.0 

8734.2 

8730.0 

8728.2 

G45-C18 

5::>NH3 Inj 

NH3Inj 

1b/hr 

0-200 

195.3 

120 . 8 

173.0 

195.5 

196.7 

197.5 

196.8 

197.2 

197.0 

196.7 

197.2 

197.5 

197.8 

197.8 

197.2 

195.8 

196.3 

163.8 

197.3 

196.3 

196.7 

196.8 

197.3 

196.8 

197.3 

196.3 

196.8 

198.7 

196.5 

196.S 

196.2 

197.7 

197.8 

198.3 

197.8 

196.8 

197.2 

197.2 

197.7 

198.3 

S>Summary - l-Min RATA - Continued 

G45-C 

5>MW Lo 

MW Lo 

0-1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

105. : 

106.1 

105. : 

106.1 

106. 1 

105. 

105. : 

106 . ( 

106. : 

106.1 

106.1 

IDS. : 

lOS .: 

106.1 

106.1 

105. 

106.1 

106.1 

106.1 

106.1 

IDS. 

lOS. 

106.1 

106.1 

106.1 

105. : 

105. : 

106.1 

106.1 

106.1 

106.1 

106.1 

106. 1 

Pagt 
Group#- Channel# 

Long Descri p . 

Short Descri p. 

Units 

Range 

02/25/2013 13:26 

02/25/2013 13:27 

02/25/2013 13:28 

02/25/2013 13:29 

02/25/2013 13:30 

02/25/2013 13:31 

02/25/2013 13:32 

02/25/2013 13:33 

02/25/2013 13:34 

02/25/2013 13:35 

02/25/2013 13:36 

02/25/2013 13:37 

02/25/2013 13:38 

02/25/2013 13:39 

02/25/2013 13:40 

02/25/2013 13:41 

02/25/2013 13:42 

02/25/2013 13:43 

02/25/2013 13:44 

02/25/2013 13:45 

02/25/2013 13:46 

02/25/2013 13:47 

02/25/2013 13:48 

02/25/2013 13:49 

02/25/2013 13:50 

02/25/2013 13:51 

02/25/2013 13:52 

02/25/2013 13:53 

02/25/2013 13:54 

02/25/2013 13:55 

02/25/2013 13:56 

02/25/2013 13:57 

02/25/2013 13:58 

02/25/2013 13:59 

02/25/2013 14:00 

02/25/2013 14:01 

02/25/2013 14:02 

02/25/2013 14:03 

02/25/2013 14:04 

02/25/2013 14:05 

Date/Time Printed: 

G45-C2 G45-C4 G45-C11 G45-C20 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 5>StkFlow 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

2.6 

2.3 

1.9 

2.0 

1.9 

1.9 

2.2 

1.9 

1.9 

2.1 

2.0 

2.0 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

2.5 

2.2 

2.6 

2.2 

1.9 

1.9 

1.9 

1.9 

1.8 

1.9 

1.8 

1.8 

Stk 02 

• 

0-25 

13 .42 

13.41 

13 .41 

13.41 

13.41 

13.41 

13 . 41 

13.40 

13.41 

13 .41 

13.41 

13 .41 

13 .41 

13 .41 

13 .40 

13 .40 

13 .41 

13 .41 

13.41 

13.40 

13 .40 

13 .39 

13.39 

13 .41 

13 .41 

13 .41 

13.40 

13.41 

13.41 

13 .41 

13 .40 

13 .41 

13 .41 

13.41 

13.41 

13.40 

13 .40 

13 .41 

13 .40 

13 .40 

02/25/2013 21,32 

NOx Mass 

lb/hr 

0-100 

5.50 

5.51 

5.50 

5.50 

5.50 

5.50 

7.33 

6.42 

5.50 

5.50 

5.50 

5.51 

5.50 

5.50 

5.51 

5.51 

5.51 

5.50 

5.50 

5.51 

5.51 

4.59 

4.59 

5.50 

5.51 

5.51 

5.50 

5.51 

6.43 

5.52 

7.35 

5.51 

5.51 

5.51 

5.51 

5.52 

4.60 

5.51 

4.60 

4.60 

StkFlow 

kscfh 

0-300000 

22324 

22312 

22291 

22285 

22274 

22271 

22283 

22255 

22282 

22277 

22291 

22323 

22295 

22289 

22272 

22287 

22315 

22297 

22280 

22292 

22276 

22259 

22267 

22279 

22306 

22301 

22258 

22329 

22334 

22340 

22296 

22331 

22334 

22321 

22324 

22312 

22308 

22324 

22310 

22305 

G45-C3 G45-C13 G45-C10 G45-C6 G45-C7 G45-C8 G45-C18 G45-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXc 5>Stk CDc 5>Gas Flow 5>NH3 Inj 5>MW Lo 

Stk CO 

ppm 

0-1000 

2.1 

2.7 

3.1 

2.6 

2.9 

2.5 

2.9 

2.8 

2.4 

2.5 

2.3 

3.1 

2.8 

2.8 

2.6 

2.6 

3.3 

2.8 

2.8 

2.7 

2.9 

3.2 

3.1 

3.1 

2.8 

3.3 

2.9 

3.3 

3.8 

3.5 

3.6 

3.9 

3.9 

3.8 

3.6 

3.7 

3.6 

4.2 

4.1 

4.2 

CO Mass 

1b/hr 

0-100 

3.67 

4.59 

4.59 

4.58 

4.58 

3.67 

4.58 

4.58 

3.67 

3.67 

3.67 

4.59 

4.59 

4.59 

4.59 

4.59 

5.51 

4.59 

4.58 

4.59 

4.59 

5.51 

4.59 

4.58 

4.59 

5.51 

4.59 

5.51 

6.43 

5.52 

5.51 

6.43 

6.43 

6.43 

5.51 

6.43 

5.51 

6.43 

6.43 

6.43 

NOx Rate 

lb/mmBtu 

0-1 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.008 

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 

0.005 

0.005 

0.006 

0.006 

0.006 

0.006 

0.006 

0.007 

0.006 

0.008 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.005 

0.005 

Stk NOXc 

ppm 

0-300 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

1. 50 

2.05 

1. 81 

1. 50 

1. 58 

1. 50 

1.50 

1. 73 

1. 50 

1.49 

1. 65 

1. 58 

1. 58 

1. 50 

1. 49 

1. 49 

1. 49 

1.49 

1. 50 

1. 50 

1. 50 

1.49 

1. 50 

1. 97 

1. 73 

2.05 

1. 73 

1.50 

1. 50 

1. 50 

1.49 

1.42 

1. 50 

1.42 

1. 42 

Stk COc Gas hscfh 

hscfh 

0-10000 

ppm 

0-1000 

1. 66 

2.13 

2.44 

2.05 

2.28 

1. 97 

2.28 

2.20 

1. 89 

1. 97 

1. 81 

2.44 

2.21 

2.21 

2.05 

2.05 

2.60 

2.21 

2.21 

2.12 

2.28 

2.51 

2.44 

2.44 

2.21 

2.60 

2.28 

2.60 

2.99 

2.76 

2.83 

3.07 

3.07 

2.99 

2.84 

2.91 

2.83 

3.31 

3.23 

3.30 

8736.0 

8743.2 

8734.8 

8732.4 

8728.2 

8727.0 

8731.8 

8732.4 

8731.2 

8729.4 

8734.8 

8747.4 

8736.6 

8734.2 

8739.0 

8745.0 

8744.4 

8737.2 

8730.6 

8746.8 

8740.8 

8745.6 

8748.6 

8730.0 

8740.8 

8739.0 

8733.6 

8749.8 

8751.6 

8754.0 

8748.6 

8750 4 

8751.6 

8746.8 

8748.0 

8754.6 

8753.4 

8748.0 

8754.0 

8752.2 

NH3Inj 

lb/hr 

0-200 

198.2 

197. 0 

196.3 

197.7 

198.3 

197.8 

165.3 

198.5 

198.3 

197.8 

198.2 

199.0 

182.2 

200.0 

199.3 

190.3 

198.2 

199.3 

198.7 

198.0 

198.5 

198.0 

198.3 

163.8 

199.8 

165.7 

199.3 

165.5 

170.5 

199.8 

170.2 

200.0 

165.8 

199.0 

199.0 

200.0 

200.0 

198.8 

198.3 

198.7 

S>Summary - I-Min RATA - Continued 

MW Lo 

0-1 

106.1 

106.1 

106.1 

106.1 

106.1 

106. ! 

106.1 

106.1 

106.1 

105. 

105. : 

105. : 

106.1 

106.1 

106. 1 

106.1 

106.1 

106.1 

105. : 

106. c 

106 .. 

106. ! 

106. c 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

105. : 

106.c 

106.1 

106.! 

106. c 

106.1 

106. c 

105. 

105. 

106. c 

PagE 
Group# - Channel# 

Long Descrip. 

Short Descrip. 

Units 

Range 

02/25/2013 14;06 

02/25/2013 14:07 

02/25/2013 14:08 

02/25/2013 14:09 

02/25/ 20 13 14;10 

02/25/2013 14;11 

02/25/2013 14:12 

02/25/2013 1 4:13 

02/25/2013 14:14 

02/25/2013 14;15 

02/25/2013 14:16 

02/ 25 /2013 14:17 

02/25/2013 14:18 

02/25/2013 14:19 

02/25/2013 14:20 

02/25/2013 14:21 

02/25/2013 14:22 

02/25/2013 14:23 

02/25/2013 14:24 

02/25/2013 14:25 

02/25/2013 14:26 

02/25/2013 14:27 

02/25/2013 14:28 

02/25/2013 14 : 2 9 

02/25/ 2013 14:30 

02/25/2013 14:31 

02/25/2013 14:32 

02/25/2013 14:33 

02/25/2013 14:34 

02/2 5 /2013 14:35 

02/2 5 /2013 14:36 

02/25/2013 14:37 

02/25/2013 14:38 

02/ 25 / 20 13 1 4 :39 

02/ 25 /2013 14:40 

0 2 / 25/2013 14:41 

02/25/2013 14:42 

Q. .Q .~ 1; ~ 

02/25/2013 14,44 

02/25/2013 14:45 

Date/Time Printed: 

G45-C2 G45-C4 G45-C11 G45 - C20 

S>Stk NOx 

Stk NOx 

ppm 

0 - 150 

5>Stk 02 5>NOx Mass 5>StkFlow 

1.9 

1.9 

1.8 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

1.9 

2.4 

2.5 

2.2 

2.1 

2.8 

2.0 

1.8 

1.9 

1.9 

1.9 

1.9 

1.8 

1.9 

1.9 

1.8 

1.9 

.. , 

1.9 

1.9 

Stk 02 

• 

0-25 

13 .4 0 

13 .40 

13 .40 

13 .39 

13.39 

13.40 

13.41 

13 .40 

13 .4 1 

13 .41 

13. 4 0 

13.40 

13.40 

13 .4 0 

13. 4 1 

13 .40 

13 .39 

13 .4 0 

13 .40 

13 .40 

13 .40 

13 .4 1 

13 .41 

13 .41 

13 .4 1 

13.40 

13 .41 

13.41 

13 . 40 

13 .40 

13 .40 

13 .40 

13 .40 

13 .40 

13.40 

13. 40 

13.40 

lJ , 10 

13 .40 

13 .4 0 

02/25/2013 21,32 

NOx Mass 

Ib/hr 

0 - 100 

5.51 

5.52 

4.60 

4.60 

4.59 

5.51 

5.52 

5.52 

5.51 

5.51 

5.52 

5.51 

5.52 

5.52 

5.51 

5.52 

4.60 

5.52 

5.51 

5.52 

5.51 

6.43 

6 . 4 3 

5.52 

5.51 

7.35 

5.51 

4.59 

5.51 

5.51 

5.52 

5.51 

4.59 

5.51 

5.51 

4.60 

5.51 

:J ,:n 

5.51 

5.51 

StkFlow 

kscfh 

0-300000 

22305 

22310 

22305 

22291 

22274 

22293 

22340 

22318 

22338 

22331 

22312 

22299 

22316 

22312 

22309 

22313 

22282 

22312 

22308 

22316 

22298 

22332 

22309 

22344 

22314 

22313 

22326 

22317 

22307 

22299 

22310 

22305 

22296 

22299 

22293 

22305 

22279 

ZZZ'G 

22284 

22308 

G45-C3 G45-C13 G45 - C10 G45-C6 G45-C7 G45 - C8 G45 - C18 G45-C 

5>Stk CO 5>CO Mass 5>NOx Rate 5>Stk NOXe 5>Stk COe 5>Gas Flow 5 >NH3 Inj 5>MW La 

Stk CO 

ppm 

0-1000 

4.0 

3.8 

4.1 

4.2 

4.4 

4.3 

4.0 

4.4 

4.0 

3.7 

4.1 

3.9 

3.9 

3.7 

3.6 

3.4 

3.9 

4.0 

3.8 

4.2 

3.8 

3.5 

3.2 

3.' 

3.6 

3.7 

4.0 

3.4 

3.5 

3.5 

3.5 

3.9 

4.0 

3 .1 

3.6 

3 .6 

3.' 

J .G 

3.5 

3. 4 

CO Mass 

Ib/hr 

0-100 

6.43 

6.43 

6.43 

6.44 

7.35 

7.35 

6.43 

7 . 36 

6.43 

6.43 

6.43 

6.43 

6 . 44 

6.43 

5.51 

5.52 

6.43 

6.43 

6.43 

6.44 

6.43 

5.51 

5.51 

5.52 

5 . 51 

6.44 

6.43 

5.51 

5.51 

5.51 

5.52 

6.43 

6.43 

4.59 

5.51 

5 . 51 

5.51 

5.51 

5.51 

5.51 

NOx Rate 

Ib/mmBtu 

0 - 1 

0.006 

0.006 

0.005 

0.005 

0.005 

0.006 

0.006 

0.006 

0 . 006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.006 

0.006 

0.006 

0.007 

0.007 

0.006 

0.006 

0.008 

0.006 

0.005 

0.006 

0.006 

0.006 

0.006 

0.005 

0.006 

0.006 

0.005 

0.006 

0 . 006 

0.006 

0.006 

Stk NOXc 

ppm 

0-300 

1.49 

1.49 

1.42 

1.49 

1.49 

1.49 

1. SO 

1.49 

1. 50 

1. 50 

1. 49 

1.49 

1.49 

1.49 

1. 50 

1. 49 

1. 49 

1. 49 

1. 49 

1.49 

1. 49 

1. 89 

1. 97 

1. 73 

1. 65 

2.20 

1. 58 

1.42 

1.49 

1.49 

1. 49 

1. 49 

1. 4 2 

1.49 

1. 49 

1.42 

1.49 

1.4' 

1.49 

1.49 

Stk COe Gas 

ppm 

hsefh 

hsefh 

0-1000 

3.15 

2.99 

3.23 

3.30 

3.46 

3.38 

3.15 

3.46 

3.15 

2.91 

3.23 

3.07 

3.07 

2.91 

2.84 

2.67 

3.06 

3.15 

2.99 

3.30 

2.99 

2.76 

2.52 

2.68 

2.84 

2.91 

3.15 

2.68 

2.75 

2.75 

2.75 

3.07 

3.15 

2.44 

2 .83 

2.83 

2.67 

2.6J 

2.75 

2.67 

0 - 10000 

8752.2 

8754.0 

8752.2 

8758.2 

8751.6 

8747.4 

8754.0 

8757.0 

8753. 4 

8750.4 

8754.6 

8749.8 

8756.4 

8754.6 

8742.0 

8755.2 

8754.6 

8754.6 

8753.4 

8756.4 

8749.2 

8751.0 

8742.0 

8755.8 

8743.8 

8755.2 

8748.G 

8745.0 

8752.8 

8749.8 

8754.0 

8752.2 

8748.6 

8749.8 

8747.4 

8752.2 

8742.0 

6746.6 

874 3. 8 

8753.4 

NH3Inj 

Ib/ hr 

0-200 

198.2 

198.7 

198.3 

197.2 

198.0 

1G4.3 

199.2 

197.7 

198.3 

198.5 

197.5 

199.7 

196.8 

198.8 

198.3 

198.3 

199.5 

198.7 

199.2 

197.5 

197.5 

163.7 

200.0 

187.5 

162.3 

200.0 

199 . 8 

200.0 

159 . 5 

200.0 

200.0 

198.2 

198.5 

200.0 

199.7 

200.0 

199.5 

D~.O 

200.0 

199.3 

S>Summary - I-Min RATA - Continued 

MW La 

0-1 

106.1 

lOG. ~ 

106.1 

IDS. 

105. 

106. ~ 

106.1 

105. 

106.1 

105. : 

106. ! 

lOG .1 

106 .1 

106.1 

106. 1 

106.1 

106.1 

lOG .1 

lOG .1 

106. ! 

106, ! 

106. ! 

106. ! 

106 . ! 

lOG. ! 

106.1 

105 

106.1 

106 . . 

106.1 

106,1 

106.1 

106 .1 

106.1 

10 6 .1 

106,1 

106 . 1 

106. 

IDS. 

106.1 

Pag( 
Group#-Channel# 

Long Descrip . 

Short Descrip . 

Units 

Range 

02/25/2013 14:46 

02/25/2013 14:47 

02/25/2013 14:48 

02/25/2013 14:49 

02/25/2013 14;50 

02/25/2013 14:51 

02/25/2013 14:52 

02/25/ 2 013 14:53 

02/25/2013 14:54 

02/25/2013 14:55 

02/25/2013 14:56 

02/25/2013 14:57 

02/25/2013 14:58 

02/25/2013 14:59 

02/25/2013 15:00 

02/25/2013 15:01 

02/25/2013 15:02 

02/25/2013 15:03 

02/25/2013 15:04 

02/25/2013 15:05 

02/25/2013 15:06 

02/25/2013 15:07 

02/25/2013 15:08 

02/25/2013 15:09 

02/25/2013 15:10 

02/25/2013 15:11 

02/25/2013 15:12 

02/25/2013 15:13 

02/25/2013 15:14 

02/25/2013 15:15 

02/25/2013 15;16 

02/25/201) 15:17 

02/25/2013 15;18 

02/25/2013 15:19 

02/25/2013 15:20 

Date/Time Printed: 

G45-C2 G45-C4 G45-Cll 

5>Stk NOx 

Stk NOx 

ppm 

0-150 

5>Stk 02 5>NOx Mass 

1.8 

1.8 

2.6 

1.9 

1.8 

1.8 

1.9 

2.1 

2.9 

2.1 

1.9 

1.8 

1.9 

1.9 

1.8 

1.8 

1.8 

2.7 

2.0 

1.9 

6.1 

2.0 

1.8 

1.8 

1.8 

2.1 

2.7 

1.9 

1.9 

2.6 

1.9 

1.9 

2.7 

1.9 

1.8 

Stk 02 

• 

0-25 

13 .40 

13 .40 

13 .40 

13 .40 

13 .40 

13 . 40 

13 .40 

13 .4 0 

13 .39 

13 .40 

13 .39 

13 .39 

13.38 

13.38 

13.39 

13.39 

13 .39 

13.40 

13.39 

13 .40 

13 .40 

13.39 

13 .39 

13 . 39 

13.39 

13.39 

13.39 

13.39 

13.40 

13 .39 

13 .39 

13 .40 

13 .39 

13.39 

13.39 

02/25/2013 21 ,32 

NOx Mass 

lb/hr 

0-100 

4.60 

4.60 

7.35 

5.51 

4.59 

4.60 

5.52 

5.52 

7.36 

5.51 

4.60 

4.60 

4.60 

4.60 

4.59 

4.60 

4.60 

7.36 

5.52 

5.52 

16.55 

5.52 

4.60 

4.60 

4.60 

5.52 

7.36 

4.60 

5.52 

7.36 

4 .60 

5.52 

7.36 

4.60 

4.60 

G45-C20 

5>StkFlow 

StkFlow 

kscfh 

0-300000 

22307 

22310 

22293 

22307 

22296 

22308 

22331 

22315 

22285 

22299 

22299 

22311 

22278 

22278 

22238 

22286 

22291 

22334 

22303 

22321 

22319 

22282 

22292 

22305 

22292 

22308 

22294 

22314 

22330 

22292 

22302 

22328 

22305 

22305 

22305 

G45-C3 

5>Stk CO 

Stk co 

ppm 

0-1000 

3.7 

3.1 

3.6 

3.4 

3 .6 

3.7 

3.9 

3.8 

4.2 

3.7 

4.0 

4.5 

4.7 

4.7 

4.6 

4.1 

4.2 

4.4 

4.1 

4.4 

4.0 

3.9 

4.3 

4.3 

4.5 

4.0 

4.4 

4.3 

4.2 

4.4 

4.1 

4.3 

4.3 

4.7 

4.5 

G45-C13 G45 - C10 G45-C6 

5>CO Mass S>NOx Rate 5>Stk NOXe 

CO Mass 

lb/hr 

0-100 

6.43 

4.60 

5.51 

5.51 

5.51 

6 .4 3 

6.44 

6.44 

6 .44 

6.43 

6.44 

7.36 

7.36 

7.36 

7.34 

6.44 

6.44 

7.36 

6.44 

7.36 

6.44 

6.43 

7.36 

7.36 

7.36 

6.44 

7.36 

7.36 

6.44 

7.36 

6.44 

7.36 

7.36 

7.36 

7.36 

NOx Rate 

lb/mmBtu 

0-1 

0.005 

0.005 

0.008 

0.006 

0.005 

0.005 

0.006 

0.006 

0.008 

0.006 

0.005 

0.005 

0.005 

0 . 005 

0.005 

0.005 

0.005 

0.008 

0.006 

0.006 

0.018 

0.006 

0.005 

0.005 

0.005 

0.006 

0.008 

0.005 

0.006 

0.008 

0.005 

0.006 

0.008 

0.005 

0.005 

Stk NOXe 

ppm 

0-300 

1.42 

1.42 

2.05 

1.49 

1.42 

1.42 

1.49 

1. 65 

2.28 

1. 65 

1.49 

1.41 

1.49 

1.49 

1.41 

1. 41 

1. 41 

2.12 

1. 57 

1. 49 

4.80 

1. 57 

1.41 

1.41 

1.41 

1. 65 

2.12 

1.49 

1.49 

2.04 

1.49 

1.49 

2.12 

1.49 

1.41 

G45 - C7 G45-C8 

5>Stk CDc 5>Gas Flow 

Stk COe Gas hsefh 

ppm hsefh 

0-1000 0-10000 

2.91 

2.44 

2.83 

2.67 

2 . 83 

2.91 

3.07 

2.99 

3.30 

2.91 

3.14 

3.54 

3.69 

3.69 

3.61 

3.22 

3.30 

3.46 

3.22 

3 . 46 

3 . 15 

3.06 

3.38 

3 . 38 

3.54 

3.14 

3.46 

3.38 

3.30 

3.46 

3.22 

3.38 

3.38 

3.69 

3.54 

8752.8 

8754.0 

8747.4 

8752.8 

8748.6 

8753.4 

8762.4 

8755.8 

8755.8 

8749.8 

8761.2 

8766.0 

8764.8 

8764.8 

8737.2 

8756.4 

8758.2 

8763.6 

8763.0 

8758.2 

8757.6 

8754.6 

8758.8 

8763.6 

8758.8 

8764.8 

8759.4 

8767.2 

8761. 8 

8758.8 

8762.4 

8761.2 

8763.6 

8763.6 

8763.6 

G45-C18 

5>NH3 Inj 

NH3Inj 

lb/hr 

0-200 

134.2 

200.0 

176.2 

200.0 

200.0 

199.0 

200.0 

180.7 

164.8 

200.0 

200.0 

165.5 

199.0 

199.0 

200.0 

200.0 

191. 3 

178.5 

166.2 

188.0 

164.3 

200.0 

200.0 

200.0 

181. 5 

200.0 

176.5 

200.0 

173.0 

200.0 

200.0 

168.7 

200.0 

200.0 

200.0 

S>Summary - l-Min RATA - Continued 

G45-C 

5>MW Lo 

MW La 

0-1 

106.1 

106. 1 

106. ( 

106.1 

106.1 

105. 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106. ( 

106.: 

106.1 

106. : 

106. ( 

105. 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106.1 

106. ( 

106. ( 

106. 1 

106. ( 

106.1 

106. 1 

106 .1 

Pag( 
Period Average = 2.0 13 . 43 5 . 49 22377 3.3 5.40 0.006 1. S4 2.63 874 7.4 193.8 105.9 

Period Max Value 6.1 13 . 4 8 16.SS 22SSS 4.7 7.36 0.018 4 .80 3.69 8767.2 200.0 106. 

Period Min Value l.8 13 . 38 4.S9 22238 2.1 3.67 0.005 1.41 1. 66 8727.0 120.8 105. 

Period Totals =: 5.1840E+2 3.5584E+3 1.4549E+3 5.9299E+6 8.8230E+2 1.4311E+3 1 . 5840E+0 4.0917E+2 6.9651E+2 2.3180E+6 5.1355E+4 2.8074E+ 

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. 
Appendix B.2 Fuel Analysis Data 

R521 0729 8-6 
SAYBOLTLP 

21730 S. Wilmington Avenue 

Suite 201 

Fast To The Point .4\ 

5aybol1: 

Carson, CA 90810 

310-518-4400 Telephone 

310-518-4455 Facsimile 

Saybolt LP 

" [ORI LABORAtORIES CnMPAHY 

SUBMITTED LAB ANALYSIS CONFIRMA nON FORM 

CUSTOMER INFORMATION SA YBOL T INFORMATION 

Customer Name: DELTA AIR QUALITY SERVICES Completed By: Gary Dela Cruz 

Job Nominated By: BOB FINKEN Date: 31112013 

Report Results To: BOB FINKEN Job Number: 1300191 

Phone Number: (714)279-6777 

Fax Number: (714)279-6781 

Email: 

SAMPLE INFORMATION 

Product: Quanti!): Received: V essellT ankIDescriution: TYQe of Saml21e: Samu1e Marked As: POIRef# 

Gas I-tedlar bag Sample #S5lFuel Sulfur - Submitted Sample #S5lFuel Sulfur - I A 

Gas I-tedlar bag Sample #S5lFuel Sulfur - Submitted Sample #S5lFuel Sulfur - 1 B 

Gas I-tedlar bag Sample #S6lFuel Sulfur - Submitted Sample #S6lFuel Sulfur - IA 

Gas I-tedlar bag Sample #S6lFuel Sulfur - Submitted Sample #S6lFuel Sulfur - I B 

Referring to your sample submission dated 3/112013 1:32:34 PM, we would like to thank you for appointing Saybolt 

and herewith confirm acceptance of your order for the analyses listed below: 

TEST 1 METHOD (IF KNOWN) 

Carbon Dioxide I ASTM D19451D1946 

Hydrogen Sulfide I AQMD 307/ASTM 05504 

COST DISTRIBUTION: 

Client 

DELTA AIR QUALITY SERVICES 

Percent 

100 

TEST 1 METHOD (IF KNOWN) 

Hydrogen I ASTM Dl9451D1946 

Molar Mass Ratio I ASTM 0-3588 

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ariginal informalion~ 

elF 05-06-004 rev 0 Page 1 of 1 
A 

5aybolt: II CORE LABORAT ORIES COM PANY 

SAYBOLT LP 

21730 S. Wilmington Avenue 

Suite 201 

Carson, CA 90810 

310-518-4400 Telephone 

310-518-4455 Facsimile 

Fast To The Point 

Saybolt LP 

Certificate of Analysis 

DELTA AIR QUALITY SERVICES 

BOB FINKEN 

1845 N. CASE 

ORANGE, CA 92865 

Date Sampled: 2/28/2013 

Report Date: 3/612013 Product: Gas 

Job No: 13091-00008644 Location: Santa Ana, CA 

Sample Number: 1300191-01 Sample ID: Sample #S5/Fuel Sulfur - 1 A 

Client Ref: Sentinel Vessel: 

Test Method Result Units 

Refinery Gas Analysis 

Hydrogen ASTM D1945/D1946 <0001 mole% 

Carbon Dioxide ASTM D1945/D1946 0.321 mole% 

Carbon Monoxide ASTM D1945/D1946 <0001 mole% 

Nitrogen ASTM D1945/D1946 3.261 mole% 

Oxygen ASTM D 1945/D 1946 0.007 mole% 

Methane ASTM D 1945/D 1946 90.772 mole% 

Ethylene ASTM D1945/D1946 <0001 mole% 

Ethane ASTM D 1945/D 1946 4.803 mole% 

Propane ASTM D 1945/D 1946 0.670 mole% 

Propylene ASTM D 1945/D 1946 <0001 mole% 

Isobutane ASTM D1945/D1946 0.042 mole% 

n-Butane ASTM D 1945/D 1946 0.083 mole% 

1-Butene ASTM D 1945/D 1946 <0001 mole% 

Isobutylene ASTM D 1945/D 1946 <0.001 mole% 

t-2-Butene ASTM D1945/D1946 <0.001 mole% 

c-2-Butene ASTM D1945/D1946 <0.001 mole% 

1,3-Butadiene ASTM D1945/D1946 <0001 mole% 

Isopentane ASTM D1945/D1946 0.009 mole% 

n-Pentane ASTM D1945/D1946 0.009 mole% 

Hexanes Plus ASTM D1945/D1946 0.023 mole% 

Total ASTM D1945/D1946 100.000 mole% 

Molar Mass Ratio ASTM D-3588 0.60306 

Relative Density ASTM D-3588 0.60521 

Compressability Factor ASTM D-3588 0.996 

Gross Heating Value (Dry-Ideal) ASTM D-3588 1025 BTU/cf 

Gross Heating Value (Dry-Real) ASTM D-3588 1029 BTU/cf 

Gross Heating Value (Wet-Ideal) ASTM D-3588 1007 BTU/cf 

Net Heating Value (Dry-Ideal) ASTM D-3588 923 BTU/cf 

Issue r warrants that it has exercised due diligence and care with respect to thc information and professional judgments embodied in this repon. This report reAeets only the fi ndings al the lime and place of inspection 

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

upon this repon should be aware that issuer's activities are carried out un<Jer their general terms and conditions 

"Precision parameters apply in the evaluation of the test re sults specified above, Please also refer!O ASTM D3244 (eXCept for analysis ofRFG) and IP 367 with respect to the utilization of the test data to determine 

conformance with specifications," 

Page 1 of 12 
SAYBOLTLP 

21730 S. Wilmington Avenue 

Suite 201 

Fast To The Point 

5ayb[)It 

Carson, CA 90810 

310-518-4400 Telephone 

310-518-4455 Facsimile A CORt LABnRATORIES COtlPAHf 

OELTA AIR QUALITY SERVICES 

BOB FINKEN 

1845 N. CASE 

ORANGE, CA 92865 

Report Oate: 3/6/2013 

Job No: 13091-00008644 

Sample Number: 1300191-01 

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 Oioxide 

Methyl Mercaptan 

Certificate of Analysis 

Oate Sampled: 

Product: 

Location: 

Sample 10: 

Vessel: 

Method Result 

ASTM 0-3588 14.696 

ASTM 0-3588 <0.001 

ASTM 0-3588 1.282 

ASTM 0-3588 0.184 

ASTM 0-3588 <0001 

ASTM 0-3588 0.014 

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 0.003 

ASTM 0-3588 0.003 

ASTM 0-3588 0.009 

ASTM 0-3588 1.521 

ASTM 0-3588 71.148 

ASTM 0-3588 23.019 

ASTM 0-3588 5.232 

ASTM 0 -3588 0.601 

ASTM 0-3588 21866 

ASTM 0-3588 8831 

ASTM 0 -3588 1747 

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 

2/28/2013 

Gas 

Santa Ana, CA 

Sample #S5/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/lb 

SCF/m m BTU 

ppm v/v 

ppm v/v 

ppm v/v 

ppm v/v 

Issuer warrants thai il has ex~rcised due diligence and care wilh res~t 10 the information.nd professional judgments embodied in this report This repon reflects only tile findings at the lirne and place of in spec lion 

and testing. Issuer expressly disclaims any further indemnity of any kind. This repon is not a guarantee or policy of insurance with respect 10 the goods or the contractual performance of any party AIly person relying 

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

"Precision parameters apply in the evaluation of the test results spedfied above. Please al50 refer to ASTM 03244 (except for analysis ofRFG) and JP 367 with respect to the utiliution of the test data to determine 

conformall(:e with specifications."' 

Page 2 of 12 
SAYBOLTLP 

21730 S. Wilmington Avenue 

Suite 201 

Fast To The Point 

SByb[]lt: 

Carson, CA 90810 

310-518-4400 Telephone 

310-518-4455 Facsimile 

Say bolt LP 

A CDIU LABDRATORIES COI1PA KY 

DELTA AIR QUALITY SERVICES 

BOB FINKEN 

1845 N. CASE 

ORANGE, CA 92865 

Report Date: 3/612013 

Job No 13091-00008644 

Sample Number: 1300191-01 

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 

Certificate of Analysis 

Date Sampled: 2/28/2013 

Product: Gas 

Location: Santa Ana, CA 

Sample ID: Sample #S5/Fuel Sulfur - 1A 

Vessel: 

Method Result Units 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AOMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AOMD 307/ASTM D5504 <0.1 ppm v/v 

AOMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0. 1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 0.1 ppm v/v 

Approved BY:,3 CV){Y'I,& YlCD c\?h-....O~ Francine Hanby~-::..J 

Laboratory Manager 

Issuer warrants that it has exerci~ d due diligence and care with respect to the information and professional judgments embodied in this report. This report reOects only the findings at the time an d place of inspection 

and testing. issuer expressly disclaims any further indemnity of any kind . This repon is not a guarant ee or policy of insurance with respect to the goods or the contractua l perfonnance 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 results specified above Please also refer to ASTM D3244 (except for analysis of RFG) and IP 367 with respect to the milization of the test data to determine 

conformance with specifications" 

Page 3 of 12 
Saybol't II COilE LABORATORIES COI'!PA NY 

SAYBOLTLP 

21730 S. Wilmington A venue 

Suite 20 1 

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: 

3/6/2013 

13091-00008644 

Sample Number: 1300191-02 

Client Ref: Sentinel 

Test 

Refinery Gas Analysis 

Hydrogen 

Carbon Dioxide 

Carbon Monoxide 

Nitrogen 

Oxygen 

Methane 

Ethylene 

Ethane 

Propane 

Propylene 

Isobutane 

n-Butane 

1-Butene 

Isobutylene 

t-2-Butene 

c-2-Butene 

1,3-Butadiene 

Isopentane 

n-Pentane 

Hexanes Plus 

Total 

Molar Mass Ratio 

Relative Density 

Compressability Factor 

Gross Heating Value (Dry-Ideal) 

Gross Heating Value (Dry-Real) 

Gross Heating Value (Wet-Ideal) 

Net Heating Value (Dry-Ideal) 

Method 

ASTM 01945101946 

ASTM 01945101946 

ASTM 01945/01946 

ASTM 01945/01 946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/0 1946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/0 1946 

ASTM 0 1945/0 1946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 01945/01946 

ASTM 0 -3588 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0-3588 

ASTM 0-3588 

Date Sampled 2/28/201 3 

Product: 

Location: 

Sample 10: 

Vessel: 

Result 

<0001 

0.302 

<0.001 

14.666 

0.739 

79.050 

<0001 

4.453 

0.637 

<0001 

0.037 

0.082 

<0001 

<0001 

<0001 

<0001 

<0.001 

0.012 

0.005 

0.017 

100.000 

0.65177 

0.65345 

0.997 

899 

901 

883 

806 

Gas 

Santa Ana, CA 

Sample #S5/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 has uercised due diligeoce and care witll respect to the information and professional judgmenu embodied in this n:pon This rcport reneels only the findings at lhe lime and place of inspection 

and testing. Issuer expressly disclaims lny further indemnity of any kind This report is 1101 a guarantee or policy ofinsuraocc with respect 10 the goods or the conlraclUal pcrfomlance of any pany Any peTSOn relying 

upon this report should be aware \hall!Wer's ac;livilies are carried out under their general tenns and conditions 

"Precision parameters apply in the eyalUaTion of The TeS! resulTs specified above Please also refer TO ASTM D3~44 (except for analysis of RFG) and lP 367 with respect 10 lhe UTilization of the les\ data to determine 

conformance with specifica tions." 

Page 4 of 12 
SAYBOLTLP 

2 1730 S. Wilmington Avenue 

Suite 201 

Fast To The Point 

5aybolt 

Carson, CA 90810 

3 10-518-4400 Telephone 

310-518-4455 Facsimile A toRr LABOIlATOR[[S COItPANY 

Certificate of Analysis 

OEL TA AIR QUALITY SERVICES 

BOB FINKEN 

1845 N. CASE 

ORANGE, CA 92865 

Oate Sampled: 

Report Oate: 3/6/2013 Product: 

Job No: 13091-00008644 Location: 

Sample Number: 1300191-02 Sample 10: 

Client Ref: Sentinel Vessel: 

Test Method Result 

Refinery Gas Analysis 

Pressure Base ASTM 0-3588 14.696 

Ethylene ASTM 0-3588 <0001 

Ethane ASTM 0-3588 1.188 

Propane ASTM 0-3588 0.175 

Propylene ASTM 0-3588 <0.001 

Isobutane ASTM 0-3588 0.012 

n-Butane ASTM 0-3588 0.026 

1-Butene ASTM 0 -3588 <0.001 

Isobutylene ASTM 0-3588 <0.001 

t-2-Butene ASTM 0-3588 <0.001 

c-2-Butene ASTM 0-3588 <0.001 

1,3-Butadiene ASTM 0-3588 <0.001 

Isopentane ASTM 0-3588 0.004 

n-Pentane ASTM 0-3588 0.002 

Hexanes Plus ASTM 0-3588 0.007 

Total ASTM 0-3588 1.414 

Carbon ASTM 0-3588 57.806 

Hydrogen ASTM 0 -3588 18.660 

Nitrogen ASTM 0 -3588 21.769 

Oxygen ASTM 0 -3588 1.765 

Gross Heating Value ASTM 0-3588 17726 

Fuel Factor (FD) ASTM 0 -3588 8948 

Average Molecular Weight ASTM 0-3588 18.88 

Sulfur Speciation 

Hydrogen Sulfide AQMO 307/ASTM 05504 <0.1 

Carbonyl Sulfide AQMO 307/ASTM 05504 <0.1 

Sulfur Oioxide AQMO 307/ASTM 05504 <0.1 

Methyl Mercaptan AQMO 307/ASTM 05504 <0.1 

Saybolt LP 

2/28/2013 

Gas 

Santa Ana, CA 

Sample #S5/Fuel Sulfur - 1 B 

Units 

psi 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

GPM 

wt% 

wt% 

wt% 

wt% 

BTUllb 

SCF/mm BTU 

ppm v/v 

ppm v/v 

ppm v/v 

ppm v/v 

Issuer warrann thaI it has exercised due diligence and care with respect to the information and professional judgments embodied in this report This report rcileclS only the findings 81 ttle time and place of inspection 

and testing. (ssucr expressly disclaims any further indemnity of any kind. This report is 1'101 a guarantee or policy of insurance with respect !O the goods or the contractual performance efany party_ Any person relying 

upon this report shol.lld be aware that issuer's activities are carried out under their generallerms and conditions. 

"Precision parameters apply in the evaluation of the test results specified above Please also refer to ASTM D3244 (e~cept for analysis of RFG) and lP 367 with respect to lhe utilization of the lest data to determine 

conformance with specifications." 

Page 5 of 12 
SAYBOLT LP 

21730 S. Wilmington Avenue 

Suite 20 I 

Fast To The Point 

Saybolt: ,., (ORE LABORATDRIES CUMP"HY 

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 : 2/28/2013 

Report Date: 

Job No: 

3/612013 

13091-00008644 

Sample Number: 1300191-02 

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: Gas 

Location: Santa Ana, CA 

Sample ID: Sample #S5/Fuel Sulfur - 1 B 

Vessel: 

Method Result Units 

AQMD 307/ASTM D5504 <0. 1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0. 1 ppm v/v 

AQMD 307/ASTM D5504 <0. 1 ppm v/v 

AQMD 307/ASTM D5504 <0. 1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0. 1 ppm v/v 

AQMD 307/ASTM D5504 <0. 1 ppm v/v 

AQMD 307/ASTM D5504 0. 1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 <0.1 ppm v/v 

AQMD 307/ASTM D5504 0. 1 ppm v/v 

AQMD 307/ASTM D5504 0.2 ppm v/v 

Approved By: .3-- Francine Hanby 

Laboratory Manager 

Issuer warrants that it has exercised due diligence and care with respe<:t to the information and professional judgments embodied in this report, This report reflects only the r,n di ng, at the time and place of inspection 

and testing. Issuer expressly disclaims any further indemnity of any kind. This report is not 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 tcrms and conditions 

"Precision parameters apply in the evaluation of the test results specified above. Please also ref ... ,. to ASTM 0 3244 (e~c pt for analysis of RFG) and IP 367 with respect to the utilization of the test data to determine 

conformance with specifications." 

Page 6 of 12 
APPENDIXC TEST DATA 

R521 0729 C-1 
Appendix C.1 Stratification and Preliminary Flow Rate Tests 

R5210729 C·2 
12-POINT STRATIFICATION CHECK 

Gemma 

5 

2/25/2013 

02 CO2 NOx CO 

Port Point % % ppm ppm 

W 3 13.24 4.54 2.23 2.18 

W 2 13.24 4.54 2.24 3.08 

W 1 13.25 4.54 2.24 2.40 

S 3 13.25 4.54 1.93 3.35 

S 2 13.64 4.31 1.98 3.94 

S 13.62 4.32 1.66 3.54 

E 3 13.55 4.40 1.92 3.80 

E 2 13.53 4.41 1.89 4.03 

E 13.50 4.43 1.79 4.22 

N 3 13.53 4.42 1.93 4.69 

N 2 13.53 4.43 1.90 4.17 

N 13.49 4.45 1.78 3.69 

Average 13.4 4.4 2.0 3.6 

Maximum 13.6 4.5 2.2 4.7 

Minimum 13.2 4.3 1.7 2.2 

Maximum Difference from Average 0.2 0.1 0.3 1.4 

Max Difference (% of average) 1.5% 3.0% 15.4% 39.3% 

Criteria: 

If < 10%, use single point. 
TEST CONSTANTS 

RELATIVE ACCURACY TEST 

DATA AND WORKSHEET 

CPV Sentinel·5·CEMS·1 02-STRAT 

TEST VARIABLES 

Station: CPV Sentinel Start Dale: 2/25/2013 

Unit: 5 

Performed By: AA, MC, RM, JM 

Cp: 0.84 

Tref: 68 of 

Stack Area : 143.14 ft' 

MeterYd: 1.014 

METHOD 2,1 DATA 

dP Temp Vel. 

Point (in. H2O) sqrt(dP) of (fps) 

4 1.80 1.3416 723 113.63 

3 2.10 1.4491 722 122.68 

2 2.20 1.4832 722 125.57 

1 2.50 1.5811 722 133.86 

4 1.90 1.3784 728 116.99 

3 2.10 1.4491 728 122.99 

2 2.70 1.6432 726 139.35 

1 2.10 1.4491 725 122.84 

4 2.40 1.5492 730 131 .60 

3 2.50 1.5811 731 134 .37 

2 2.90 1.7029 732 144.78 

1 3.60 1.8974 730 161.17 

4 1.70 1.3038 726 110.57 

3 1.90 1.3784 727 116.94 

2 2.10 1.4491 726 122.89 

1 2.00 1.4142 726 119.93 

Average 2.2596 1.5032 726.5 127.51 

Slack Flow Rate: 1,095.1 kwacfm 

Stack Flow Rate: 451 .5 kdscfm 

Dry Gas Meter 

Time Vol. T m(in) T m(out) #/MaU. 

Start 138.944 88 88 H, O 

87 87 H,O 

78 78 Empty 

End 156.968 79 79 SG 

Line Rinse 

Total 18.024 83.0 Tolal 

NOx ppm 

NOx , ppm @ 15% O2 

NOx Ib/MMBlu 

NO" Ib/hr 

CO ppm 

CO, ppm @ 15% 0 , 

CO Iblhr 

O2 % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

CT Load MW 

SCR NH3 Injection Ib/hr 

NO, Ib/MMSCF 

CO Ib/MMBtu 

CO Ib/MMSCF 

Start/End Time: 9:49 

Load (MW)/Replicate# 102 

Barom. Pressure: 29.60 

Pstack: 2.80 

Pstack: 29.81 

MW: 28.44 

METHOD 100.1 DATA 

0, CO, 

Analyzer Range 20 10 

Cal Gas Value 18.98 9.62 

Pre-Test Direct Zero 0.14 0.03 

Pre-Test Direct Span 19.02 9.62 

Pre-Test System Zero 0.15 0.09 

Pre-Test System Span 19.00 9.66 

Post-Test System Zero 0.16 0.24 

Post-Test System Span 18.93 9.82 

Post-Test Direct Zero 0.11 0.20 

Post-Test Direct Span 18.95 9.85 

Average 13.45 4.44 

Corr. results 13.41 4.30 

Pre-test zero bias 0.0% 0.6% 

Pre-lest span bias -0.1% 0.4% 

Post-test zero bias 0.2% 0.3% 

Post-test span bias -0.1% -0.3% 

Zero drift 0.1% 1.4% 

Span drift -0.4% 1.6% 

METHOD 4.1 DATA 

Impingers 

End Start Diff. 

807.1 684 .8 122.3 Meter Pressure: 

657 .7 656.9 0.8 

578.6 578.5 0.1 Sample Volume: 

997.8 992.9 4.9 H20 Volume : 

100.0 -100.0 Moisture Content: 

28.1 

RESULTS 

Ref. Meth CEMS Diff. Diff. % 

1.98 1.80 0.18 9.1% 

1.56 1.46 0.10 6.4% 

0.006 0.006 0.000 0.0%. 

6.41 5.00 1.41 21 .9% 

3.44 2.70 0.74 21 .5% 

2.71 2.13 0.58 21.4% 

6.77 4.33 2.44 36.0% 

13.41 13.53 -0.12 -0.9% 

27,091,703 21,943,000 5,148,703 19.0% 

- 8,503.8 -

- - - 102 - - - 191 .7 - - 7.53 

0.006 - 6.38 

11 :08 

STRAT 

iwg 

"H9 

Ib/lb-mole 

NO, CO 

5 10 

4.62 9.56 

-0.02 0.01 

4.60 9.57 

-0.01 0.25 

4.58 9.85 

-0.01 0.02 

4.57 9.63 

-0.01 -0.03 

4.60 9.55 

1.96 3.59 

1.98 3.44 

0.3% 2.4% 

-0.5% 2.8% 

0.1% 0.5% 

-0.5% 0.8% 

0.0% -2.3% 

-0. 1% -2.2% 

1.5 iwg 

17.646 dscf 

1.326 scf 

7.0 % 

Sentinel Unit 5 RATA.xls 

3/14/2013 

12:22 PM 
Port Point Date 

W 3 2/25/2013 

W 2 2/25/2013 

W 1 2/25/2013 

5 3 2/25/2013 

S 2 2125/2013 

S 1 2/25/2013 

E 3 2/25/2013 

E 2 2/25/2013 

E 1 2/25/2013 

N 3 2/25/2013 

N 2 2/25/2013 

N 2125/2013 

Average 

DBhaAlrQual/fY SBtYlceS 

1845 N. Case Street 

Orange, California 92865 

714·279·6777 

Time 

9:50 

9:52 

9:54 

9:59 

10:01 

10:03 

10:55 

10:57 

10:59 

11 :04 

11:06 

11 :08 

REFERENCE METHOD 1·MINUTE AVERAGE DATA 

0, CO, NO, CO 

13.239 4.54 2.231 2.179 

13.242 4.54 2.236 3.083 

13.247 4.536 2.236 2.401 

13.247 4.535 1.934 3.354 

13.643 4.311 1.975 3.938 

13.624 4.323 1.656 3.541 

13.551 4.4 1.924 3.798 

13.533 4.41 1.894 4.026 

13.495 4.434 1.79 4.219 

13.533 4.42 1.925 4.692 

13.525 4.426 1.898 4.171 

13.486 4.45 1.779 3.694 

13.45 4.44 1.96 3.59 

Sentinel Unit 5 RATA-xis 

3/4/2013 

10:02 AM 
Port Point Angle 

N 4 2 

N 3 0 

N 2 2 

N 1 1 

E 4 1 

E 3 0 

E 2 1 

E 1 0 

S 4 0 

S 3 0 

S 2 1 

S 1 0 

W 4 0 

W 3 3 

W 2 2 

W 0 

Average 0.8 

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: C-ev""'- vVI."I , PERFORMED BY: IS' k\ ~ ,) ::V'\ 

LOCATION: SoQ!"~' "\Y \ BAR. PRESSURE:_~2",,"\....l.-'- ' "",l ,"'-,, ______ _ 

UNIT: '-2 STATIC PRESSURE:--'.j+--,2-",,'--,--, ... h..l--____ _ 

TEST DATE: '2../ Z- ~ - \» TC READOUT ID:_-:-1L.:2.~...:.""-'.=...:..\ ...... S'---____ _ TEST NUMBER: TC ID::-=:-I,=,:L::-:-,:::-:-,v-",--",:L -"'j...,.,,-_______ _ 

LEAK CHECK PRE- V POST- , V PITOT TUBE ID:-=',:l:b ~_'\:1::'o~"::__---;---,;--;,----

c.P INDICATOR TYPE: (2 - \ 0 \~cA:> PITOT TUBE COEFFICIENT: ?', b L( 

c.P INDICATOR 10: \ 0 - c/ C "> ZERO: ~ ,,/ LEVEL:_-6b""'L"--__ _ 

Yaw Angle, c.P, Temperature, 

Time Port Point Degrees(1) inches H2O OF 

I:U) <::, IV Lj lj 'Z- 1, g 7 2 7 

'7., ~ () '2, \ 72.2-

'2 '7 2 2, 2- 72.2-

I l 2 , ::;- 72-"2-

t2-1 U r;: L/ ;, , \ ' i1 72-'(-

:s 7 Q 2 , I '726 

2 2- \ n , 7 '72 (., 

I () 2 , , '72 )-

12-ls "S I- U 0 '2 , L/ 1Ju 

'OS ~ 0 2, :; '7 J i 

2. ,') J 2 , t1 73 2 

I I 0 '). (.", 7?,D 

12'2.() I t.( ) U Li 0 I , 'I 72[, 

;;; i "7 [ , '1 12-7 

2 ,., 

t.- 2 '2. / '/2-(' 

I \ ;) '2 , 0 72- f: 

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

1IIIIta~ "'---

Date of last revision 11/13/08 

DS834033 

Master Document StoragelFormslDatasheetslField Datasheets 
Appendix C.2 CEM Data 

R5210729 C-3 
Appendix C.2.1 CEM Quality Assurance Measurements 

R521 0729 C-4 
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 5 

2/25-26/2013 

Delta Air Quality Services, Inc. 

714-279-6777 

contact@deltaags.com 

Aleshaiker 

Ali 

M 

November 21 , 2008 

Source Evaluation Society 

gstiprogram@gmail.com 
Della Ail QualifY SelVices 

CEMS PERFORMANCE DATA SHEET 

Client: Gemma Date: 2/25-26/2013 

Location: CPV Sentinel Unit 5 Performed By: M, MC, RM, JM 

CEMS 10#: -=5-c-C::..;E=.cM"'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 Length : 200' 

Upscale Response Time: 30 Downscale Response Time: 

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

Sample Flow Rate: 8 SCFH 

S02 

--

Gas Temp: 735 of 

Gas Temp: 300 of 

Gas Temp: 31 of 

30 seconds 

NA 

Sentinel Unit 5 CEMS QA.xls 

3/16/2013 

2:40 PM 
Della Ai, Quality SefVices 

SPAN GAS RECORD AND SCAQMD CALIBRATION ERROR/LINEARITY 

CLIENT/LOCATION: Gemma CPV Sentinel Unit 5 DATE: 2/25/13 

TRUCK/CEM I.D.: .,::::5-....::C:..:E::,:M,:.::SC-. _________ _ BY: AA, MC, RM, JM 

Exp. Vendor %of 

Gas Cylinder # Value Date ID Range 

ZERO Low SA21794 0.0 1/8/18 F22013 

0, Mid CC181115 10.00 5/1/15 F22012 50.0% 

0, High CC246737 18.98 5/30/15 F22012 94.9% 

CO, Mid CC181115 5.00 5/1/15 F22012 50.0% 

CO, High CC246737 9.62 5/30/15 F22012 96.2% 

NO, Mid CC363284 2.56 9/11/14 F22012 51.2% 

NO, High CC101204 4.62 11/5/14 F22012 92.4% 

NO, NO, CC336169 3.71 2/27113 F22012 74.2% 

CO Mid CC325462 4.49 8/20/20 F22012 44.9% 

CO High CC313042 9.56 5/21/15 F22012 95.6% 

PRE-TEST INSTRUMENT CALIBRATION ERROR 

ANALYZER 

0, CO, NO, CO 

Analyzer Range 20 10 5 10 

Zero Gas Value 0.0 0.0 0.0 0.0 

AnalYzer Reads 0.14 0.03 -0.02 0.01 

Error (% of scale) 0.7% 0.3% -0.5% 0.1% 

Hiah Gas Value 18.98 9.62 4.62 9.56 

Analyzer Reads 19.02 9.62 4.60 9.57 

Error (% of scale) 0.2% 0.0% -0.3% 0.1% 

Mid Gas Value 10.00 5.00 2.56 4.49 

Analyzer Reads 10.10 5.05 2.53 4.49 

Error (% of scale) 0.5% 0.5% -0.6% 0.0% 

Linearity at Mid Point 0.1% 0.4% -0.2% -0.1% 

POST-TEST INSTRUMENT CALIBRATION ERROR 

ANALYZER 

0, CO, NOx CO 

Analyzer Range 20 10 5 10 

Zero Gas Value 0.0 0.0 0.0 0.0 

Analyzer Reads 0.12 0.10 -001 0.03 

Error (% of scale) 0.6% 1.0% -0.2% 0.3% 

HTcih Gas Value 18.98 9.62 4.62 9.56 

AnalYzer Reads 18.88 9.70 4.56 9.58 

Error (% of scale) -0.5% 0.8% -1.1% 0.1% 

Mid Gas Value 10.00 5.00 2.56 4.49 

AnalYzer Reads 10.01 5.12 2.53 4.49 

Error (% of scale) 0.0% 1.2% -0.7% 0.0% 

Linearity at Mid Point 0.0% 0.3% 0.0% -0.2% 

STATUS 

--

-- PASS 

--

-- PASS 

--

-- PASS 

PASS 

STATUS 

--

-- PASS 

--

-- PASS 

--

-- PASS 

PASS 

Sentinel Unit 5 CEMS QA.xls 

3/12/2013 

3:30 PM 
Della Air Quality Services 

SPAN GAS RECORD AND SCAQMD CALIBRATION ERROR/LINEARITY 

CLIENT/LOCATION: Gemma CPV Sentinel Unit 5 DATE: 2/26/13 

TRUCK/CEM 1.0.: ..:5_-Co..;E::;.M;.;.S"-__________ _ BY: AA, MC, RM , JM 

Exp, Vendor 'loaf 

Gas Cylinder # Value Date to Range 

ZERO Low SA21794 0.0 1/8/18 F22013 

0, Mid CC181115 10.00 5/1/15 F22012 50.0% 

0, High CC246737 18.98 5/30/15 F22012 94.9% 

CO, Mid CC181115 5.00 5/1/15 F22012 50.0% 

CO, High CC246737 9.62 5/30/15 F22012 96.2% 

NO, Mid CC363284 2,56 9/11/14 F22012 51.2% 

NO, High CC101204 4,62 11 /5/14 F22012 92.4% 

NO, NO, CC336169 3,71 2/27113 F22012 74.2% 

CO Mid CC325462 4.49 8/20/20 F22012 44.9% 

CO High CC313042 9.56 5/21 /15 F22012 95,6% 

PRE-TEST INSTRUMENT CALIBRATION ERROR 

ANALYZER 

0, CO, NO, CO 

Analyzer Range 20 10 5 10 

Zero Gas Value 0,0 0,0 0,0 0.0 

Analyzer Reads 0.11 0.07 -003 -0.04 

Error (% of scale) 0,6% 0,7% -0.5% -0.4% 

High Gas Value 18,98 9.62 4,62 9.56 

Analyzer Reads 18,95 9,68 4,60 9.55 

Error (% of scale) -0.1% 0.6% -0.4% -0,1 % 

Mid Gas Value 10,00 5,00 2,56 4.49 

Analyzer Reads 10,06 5.11 2.53 4,51 

Error (% of scale) 0.3% 1,1% -0.6% 0.2% 

Linearity at Mid Point 0,1% 0.4% -0.1% 0.4% 

POST-TEST INSTRUMENT CALIBRATION ERROR 

ANALYZER 

0, CO, NO, CO 

Analyzer Range 20 10 5 10 

Zero Gas Value 0,0 0,0 0.0 0,0 

Analyzer Reads 0.11 0,12 -0,01 0,04 

Error (% of scale) 0,6% 1.2% -0.3% 0.4% 

High Gas Value 18.98 9,62 4.62 9.56 

Analyzer Reads 18,90 9,76 4,59 9.60 

Error (% of scale) -0.4% 1.4% -0,5% 0.4% 

Mid Gas Value 10.00 5.00 2.56 4.49 

Analyzer Reads 10,02 5.18 2,55 4,51 

Error (% of scale) 0,1% 1,8% -0,2% 0,2% 

Linearity at Mid Point 0,1% 0,5% 0,2% -0.1% 

STATUS 

--

-- PASS 

--

--

PASS 

--

-- PASS 

PASS 

STATUS 

--

-- PASS 

--

-- PASS 

--

--

PASS 

PASS 

Sentinel Unit 5 CEMS QA.xls 

311612013 

2:15 PM 
Analyzer Manufacturer: 

Analyzer Model: 

Analyzer Serial Number: 

Date: 

ANALYZER 

GAS MODE 

Zero NO, 

Zero NO 

NO NO, 

NO NO 

NO, NO 

NO, NO, 

Abs. Value Co-C,: 

Abs. Value C,-C,: 

C, /C, 

CE = D,/D, * 100%: 

Della Air Quality Sefllices 

NO, to NO Converter Efficiency Test 

Gemma CPV Sentinel Unit 5 

600CLD 

V10043 

2/25/13 

ANALYZER 

RESPONSE 

-0.02 

-0.03 

4.60 

4.57 

0.00 

3.45 

Label 

3.7 D, 

3.4 D, 

1% D3 

93% 

NO Cal Gas Value: 4.62 

NO, Cal Gas Value: 3.71 

Performed By: AA 

CEMS ID#: 5-CEMS 

CAL 

CORRECTED LABEL 

0.0 C, 

3.5 C, 

Requirement 

<5% 

> 90% 

Sentinel Unit 5 CEMS QA.xls 

3/16/2013 

2:16 PM 
Analyzer Manufacturer: 

Analyzer Model: 

Analyzer Serial Number: 

Date: 

ANALYZER 

GAS MODE 

Zero NO, 

Zero NO 

NO NO, 

NO NO 

NO, NO 

NO, NO, 

Abs. Value Co-C,: 

Abs. Value C,-C,: 

C,/C, 

CE = D,/D, * 100%: 

Della Air QualitY Services 

NO, to NO Converter Efficiency Test 

Gemma CPV Sentinel Unit 5 

600CLD 

V10043 

2/26/13 

ANALYZER 

RESPONSE 

-0.03 

-0.04 

4.61 

4.60 

0.00 

3.47 

Label 

3.7 D, 

3.4 D, 

1% D3 

94% 

NO Cal Gas Value: 4.62 

NO, Cal Gas Value: 3.71 

Performed By: AA 

CEMS ID#: 5-CEMS 

CAL 

CORRECTED LABEL 

0.0 C, 

3.5 C, 

Requirement 

<5% 

> 90% 

Sentinel Unit 5 CEMS QA.xls 

3/16/2013 

2:16 PM 
Appendix C.2.2 NOx and CO Compliance 

R521 0729 C-5 
COMPLIANCE TEST 

OATA AND WORKSHEET 

CPV Sentinel-5-CEMS-100-1 

TEST CONSTANTS 

Stalion: CPV Sentinel 

Unit; 5 

Performed By: AA, MC, RM, JM 

Cp: 0.99 

Tret: 60 of 

Stack Area: 143.14 ft' 

Meter Yd: 1.014 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H,O) sqrt(dP) of (Ips) 

4 1.70 1.3038 732 131.39 

3 1.60 1.2649 733 127.52 

2 1.50 1.2247 734 123.52 

1 1.40 1.1832 733 119.28 

4 1.50 1.2247 734 123.52 

3 1.40 1.1832 735 119.38 

2 1.70 1.3038 736 131 .61 

1 1.90 1.3784 734 139.02 

4 0.98 0.9899 735 99.88 

3 1.70 1.3038 736 131 .61 

2 1.90 1.3784 735 139.07 

1 1.70 1.3038 734 131.50 

4 1.10 1.0488 735 105.82 

3 1.30 1.1402 736 11 5.09 

2 1.50 1.2247 730 123.31 

1 1.40 1.1832 735 119.38 

Average 1.5067 1.2275 734 .2 123.81 

Stack Flow Ra te: 1,063.3 kwacfm 

Stack Flow Rate: 416.2 kdscfm 

Dry Gas Meter 

Time Vol. Tm(in) T m(out) #IMati. 

Start 158.456 79 78 H,O 

77 78 H,O 

End 202.298 76 75 Emply 

73 74 SG 

Total 43.842 76.3 Total 

NO, ppm 

NOx , ppm @ 15% O2 

NO~ Ib/MMBtu 

NO~ lb/hr 

CO ppm 

CO, ppm@ 15% O2 

CO Iblhr 

O2 % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

CT Load MW 

SCR NH3 Injection Ib/hr 

NO, IblMMSCF 

CO IblMMBlu 

CO IblMMSCF 

TEST VARIABLES 

Start Dale: 2125113 

Start/End Time: 11 :35 12:43 

Load (MW)/Replicate# 100 1 

Barom. Pressure: 29.60 

Pstack: 2.80 iwg 

Pstack: 29.81 "Hg 

MW: 28. 12 Ib/lb-mole 

METHOD 100,1 DATA 

0, CO, NO, CO 

Analyzer Range 20 10 5 10 

Cal Gas Value 18.98 9.62 4.62 9.56 

Pre· Test Direct Zero 0. 11 0.20 -0.01 -0.03 

Pre-Test Direct Span 18.95 9.85 4.60 9.55 

Pre-Test System Zero 0.16 0.24 -0.01 0.02 

Pre-Test Syslem Span 18.93 9.82 4.57 9.63 

Post-Tesl System Zero 0.16 0.25 -0.01 -0.01 

Post-Test System Soan 18.83 9.85 4.56 9.59 

Post-Test Direct Zero 0.11 0.20 -0.02 -0.03 

Post-Test Direct Span 18.89 9.86 4.60 9.55 

Average 13.51 4.44 2.10 3.75 

Carr. results 13.54 4.21 2.13 3.72 

Pre-test zero bias 0.2% 0.3% 0.1% 0.5% 

Pre-test span bias -0.1% -0.3% -0.5% 0.8% 

Post-lest zero bias 0.2% 0.5% 0.1% 0.1% 

Post-test span bias -0.3% -0.1% -0.7% 0.4% 

Zero drift 0.0% 0.2% 0.0% -0.3% 

Span drift -0.5% 0.3% -0.2% -0.4% 

METHOD 4,1 DATA 

Impingers 

End Start Diff. 

910.2 728.7 181 .5 Meter Pressure: 1.5 iwg 

743.5 742.2 1.3 Sample Volume: 42.803 dscl 

630.0 628.2 1.8 H20 Volume : 4.635 scI 

946.9 931.8 15.1 Moisture Content: 9.8 % 

Ir 100 99.7 

RESULTS 

Ref. Meth CEMS 

2.13 1.90 

1.70 1.51 

0.006 0.01 

6.44 5.54 

3.72 3.20 

2.98 2.53 

6.76 5.19 

13.54 13.45 

24,970,209 22.442,000 

- 8,746 

-

- 106 

- 195 

7.36 

0.007 

7.03 -

Sentinel Unit 5 100% NOx-NH3-ROG Compliance.xls 

3116/2013 

2:46 PM 
COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentinel-5-CEMS-100-2 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit: 5 

Performed By: AA, MC, RM, JM 

Cp: 0.99 

Tref: 60 of 

Stack Area: 143.14 ft' 

Meier Y(j: 1.014 

METHOD 2,1 DATA 

dP Temp Vel. 

Point (in. H,O) sqrt(dP) of (fps) 

4 1,20 1.0954 736 110.58 

3 1.30 1.1402 737 115.15 

2 1.40 1.1832 738 119.54 

1 1,60 1,2649 736 127.69 

4 1.30 1.1402 737 115.15 

3 1.80 1.3416 739 135.61 

2 1,90 1.3784 740 139.38 

1 1.60 1.2649 739 127.85 

4 1.10 1.0488 740 106.05 

3 1.20 1,0954 741 110.82 

2 1.40 1.1832 739 119.59 

1 1,60 1.2649 738 127.80 

4 1.00 1.0000 740 101 .12 

3 1.20 1.0954 739 110.72 

2 1.20 1,0954 739 110.72 

1 1,10 1,0488 737 105.92 

Average 1.3574 1,1651 738.4 117.73 

Stack Flow Rate: 1,011 .1 kwacfm 

Stack Flow Rate: 394 .0 kdsefm 

Dry Gas Meter 

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

Slart 204,664 78 76 H,O 

74 74 H,O 

End 240,825 76 76 Emply 

74 74 SG 

Total 36.161 75,3 Total 

NOx ppm 

NOx , ppm @ 15% O2 

NO, Ib/MMBlu 

NOx Ib/hr 

CO ppm 

CO, ppm@ 15% O2 

CO Ib/hr 

O2 % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

CT Load MW 

SCR NH3 Injection Ib/hr 

NO, Ib/MMSCF 

CO Ib/MMBlu 

CO Ib/MMSCF 

TEST VARIABLES 

Start Date: 2/25/13 

Start/End Time : 13:04 14:17 

Load (MW)/Replicale# 100 2 

Baram. Pressure: 29,60 

Pstack: 2.80 iwg 

Pstack: 29.81 "Hg 

MW: 28,11 Ib/lb-mole 

METHOD 100,1 DATA 

0, CO, NO, CO 

Analyzer Range 20 10 5 10 

Cal Gas Value 18,98 9.62 4.62 9.56 

Pre-Test Direct Zero 0.11 0.20 -0.02 -0.03 

Pre-Test Direct Span 18.89 9.86 4,60 9.55 

Pre-Test System Zero 0.16 0.25 -0.01 -0.01 

Pre-Test System Span 18.83 9.85 4.56 9.59 

Post-Test System Zero 0.14 0.21 -0.01 0.02 

Post-Test System Span 18.79 9,80 4,55 9.51 

Post-Test Direct Zero 0.11 0,19 -0,01 -0,03 

Post-Test Direct Span 18.89 9,84 4.57 9.57 

Average 13.42 4.46 2.03 3.60 

Carr. results 13.50 4,24 2,06 3.60 

Pre-lest zero bias 0.2% 0.5% 0.1% 0.1% 

Pre-lest span bias -0.3% -0. 1% -0.7% 0.4% 

PosHest zero bias 0.1% 0.2% 0.0% 0.5% 

Post-test span bias -0.5% -0.4% -0.5% -0.5% 

Zero drift -0.1% -0.4% 0.0% 0.3'% 

Span drift -0.2% -0.5% -0.3% -0.8% 

METHOD 4,1 DATA 

Impingers 

End Start Diff, 

856.7 683.6 173,1 Meter Pressure: 1.5 iwg 

664.0 662,2 1.8 Sample Volume: 35.370 dsel 

579.9 579,6 0.3 H20 Volume : 3.868 sef 

948.7 940.7 8.0 Moisture Content: 9.9 % 

Ir 100 83,2 

RESULTS 

Ref, Melh CEMS 

2.06 1.90 

1.65 1,53 

0,006 0.01 

5.92 5.48 

3.60 3,10 

2,87 2.45 

6,19 5,00 

13,50 13.41 

23,638,158 22,311 ,000 

- 8,742 

-

- 106 

- 194 

6.77 -

0.006 - 6.77 -

Sentinel Unit 5 100% NOx-NH3-ROG Compliance.xls 

3/16/2013 

2:46 PM 
REFERENCE METHOD 1-MINUTE AVERAGE DATA 

Port Point Date Time 0, CO, NO, CO 02-ln NOx-ln CO-In THC-In 

W 3 2/25/2013 11 :36 13.521 4.45 2.215 3.458 

W 3 2/25/2013 11 :37 13.526 4.447 2.211 3.719 

W 3 2/25/2013 11 :38 13.528 4.446 2 .206 3.499 

W 3 2/25/2013 11 :39 13.517 4.453 2.188 3.752 

W 3 2/25/201 3 11 :40 13.513 4.456 2.198 4.326 

W 2 2/25/2013 11 :41 13.525 4:449 2.268 4.375 

W 2 2/25/2013 11 :42 13.535 4:443 2.288 4.314 

W 2 2/25/2013 11 :43 13.534 4:441 2.343 4.551 

W 2 2/25/2013 11 :44 13.534 4.438 2.363 4:426 

2/25/2013 11 :47 13.557 4:42 2.409 4.156 

2/25/2013 11 :48 13.558 4.42 2:423 4.708 

2/25/2013 11 :49 13.555 4.419 2:436 3.834 

1 2/25/2013 11 :50 13.577 4:409 2:47 3.786 

5 3 2/25/2013 11 :54 13:498 4.45 1.829 3.193 

S 3 2/25/2013 11 :55 13.51 4.448 1.824 3.398 

S 3 2/25/2013 11 :56 13.5 4:454 1.822 2.962 

S 3 2/25/2013 11 :57 13.504 4:451 1.845 2.952 

S 3 2/25/2013 11 :58 13:499 4.454 1.813 2.825 

S 2 2/25/2013 11 :59 13.497 4:459 1.835 3.538 

S 2 2/25/2013 12 :00 13.515 4:45 1.722 3.224 

S 2 2/25/2013 12 :01 13.519 4.449 1.711 3.005 

S 2 2/25/2013 12:02 13.521 4:449 2.345 3.023 

S 2 2/25/2013 12:03 13.519 4:45 1.821 3.234 

S 1 2/25/2013 12:04 13.536 4:438 1.69 3.086 

S 1 2/25/2013 12:05 13.55 4.431 1.584 3.289 

S 2/25/2013 12:06 13.548 4:429 1.588 3.487 

S 2/25/2013 12:07 13.555 4:421 1.571 3.139 

E 3 2/25/2013 12:13 13.5 4:433 2.049 3.397 

E 3 2/25/2013 12:14 13.501 4.431 2.022 3:432 

E 3 2/25/2013 12:15 13.5 4:432 2.055 3.647 

E 3 2/25/2013 12:16 13:499 4:433 2.046 3.845 

E 2 2/25/2013 12:17 13:493 4:435 2.06 3.618 

E 2 2/25/2013 12:18 13:493 4:436 2.108 3.648 

E 2 2/25/2013 12:19 13.493 4:437 2.034 3.831 

E 2 2/25/2013 12:20 13:488 4:436 2.07 3.834 

E 2/25/2013 12:23 13:495 4:436 2.041 3.757 

E 2/25/2013 12:24 13:496 4:436 2.044 3.62 

E 1 2/25/2013 12:25 13:487 4:439 1.978 3.653 

E 1 2/25/2013 12:26 13:484 4:443 1.969 3.852 

N 3 2/25/2013 12:29 13.496 4:436 2.184 3.933 

N 3 2/25/2013 12:30 13:486 4:44 2.172 4.255 

N 3 2/25/2013 12:31 13:495 4:435 2.219 3.802 

N 3 2/25/2013 12:32 13:487 4:44 2.159 4.132 

N 3 2/25/2013 12:33 13.492 4:436 2.158 4.142 

N 2 2/25/2013 12:34 13:49 4:436 2.188 3.684 

N 2 2/25/2013 12:35 13:48 4:441 2.161 3.907 

N 2 2/25/2013 12:36 13:483 4:436 2.186 4.091 

N 2 2/25/2013 12:37 13:473 4:44 2.154 3.927 

N 2/25/2013 12:40 13.494 4:431 2.373 

N 2/25/2013 12:41 13:496 4:43 2.413 

N 2/25/2013 12:42 13.5 4:43 2:439 

N 2/25/2013 12:43 13.505 4:428 2.407 

Average 13.51 4.44 2.10 3.75 13.26 31.79 92.03 

Della Ai' QualitY Services 

1845 N. Case Street Sentinel Unit 5 100% NOx-NH3-ROG Compliance.xls 

Orange, California 92865 3/16/2013 

714-279-6777 2:47 PM 
REFERENCE METHOD 1-MINUTE AVERAGE DATA 

Port Point Date Time 0, CO, NO, CO 

W 3 2/25/2013 13:05 13.424 4.465 1.784 3.191 

W 3 2/25/2013 13:06 13.422 4.466 1.764 3.218 

W 3 2/25/2013 13:07 13.425 4.462 1.802 3.208 

W 3 2/25/2013 13:08 13.422 4.466 1.762 2.924 

W 3 2/25/2013 13:09 13.422 4.465 1.767 3.104 

W 2 2/25/2013 13:10 13.426 4.462 1.689 3.255 

W 2 2/25/2013 13: 11 13.432 4.456 1.698 2.758 

W 2 2/25/2013 13:12 13.434 4.455 1.716 2.712 

w 2 2/25/2013 13:13 13.435 4.456 1.706 2.727 

W 2 2/25/2013 13:14 13.437 4.453 1.689 2.598 

W 1 2/25/2013 13:15 13.451 4.448 1.6 2.915 

W 2/25/2013 13:16 13.462 4.445 1.622 2.774 

W 2/25/2013 13:17 13.455 4.448 1.625 2.744 

W 2/25/2013 13:18 13.466 4.446 1.609 2.698 

W 1 2/25/2013 13:19 13.458 4.45 1.616 2.725 

S 3 2/25/2013 13:28 13.394 4.49 1.952 3.265 

S 3 2/25/2013 13:29 13.393 4.493 1.98 3.398 

S 3 2/25/2013 13:30 13.395 4.489 1.975 3.114 

S 3 2/25/2013 13:31 13.396 4.487 1.979 3.181 

S 2 2/25/2013 13:34 13.382 4.497 2.417 3.145 

S 2 2/25/2013 13:35 13.38 4.498 1.992 2.975 

S 2 2/25/2013 13:36 13.385 4.494 1.991 2.865 

S 2 2/25/2013 13:37 13.375 4.499 1.902 2.803 

S 2/25/2013 13:38 13.358 4.509 1.79 3.347 

S 2/25/2013 13:39 13.358 4.511 2.103 2.998 

S 2/25/2013 13:40 13.362 4.508 1.87 2.992 

S 2/25/2013 13:41 13.36 4.509 1.815 2.747 

E 3 2/25/2013 13:46 13.421 4.476 2.023 3.191 

E 3 2/25/2013 13:47 13.421 4.472 2.019 3.364 

E 3 2/25/2013 13:48 13.421 4.472 2.048 3.653 

E 3 2/25/2013 13:49 13.42 4.472 2.019 3.632 

E 2 2/25/2013 13:50 13.422 4.466 2.023 3.342 

E 2 2/25/2013 13:51 13.428 4.461 2.018 3.287 

E 2 2/25/2013 13:52 13.421 4.463 1.995 3.592 

E 2 2/25/2013 13:53 13.421 4.46 1.999 3.381 

E 2/25/2013 13:56 13.423 4.45 2.372 3.796 

E 2/25/2013 13:57 13.422 4.452 2.873 3.914 

E 1 2/25/2013 13:58 13.418 4.453 2.316 4.134 

E 1 2/25/2013 13:59 13.421 4.449 1.986 4.062 

N 3 2/25/2013 14:03 13.433 4.427 2.093 4.272 

N 3 2/25/2013 14:04 13.434 4.427 2.072 4.719 

N 3 2/25/2013 14:05 13.433 4.427 2.085 4.709 

N 3 2/25/2013 14:06 13.432 4.425 2.074 4.61 

N 3 2/25/2013 14:07 13.435 4.423 2.165 4.71 1 

N 2 2/25/2013 14:08 13.441 4.419 2.238 4.564 

N 2 2/25/2013 14:09 13.433 4.425 2.198 4.859 

N 2 2/25/2013 14:10 13.432 4.429 2.225 4.884 

N 2 2/25/2013 14:11 13.435 4.429 2.214 5.171 

N 2 2/25/2013 14:12 13.468 4.413 2.353 5.061 

N 1 2/25/2013 14:13 13.47 4.411 2.347 4.97 

N 2/25/2013 14:14 13.471 4.412 2.338 5.223 

N 2/25/2013 14:15 13.471 4.413 2.361 4.712 

N 2/25/2013 14:16 13.47 4.414 2.336 4.665 

N 2/25/2013 14:17 13.47 4.418 2.376 4.994 

Average 13.42 4.46 2.03 3.60 

Delta Air QualifY ServIces 

1845 N. Case Street Sentinel Unit 5 100% NOx-NH3-ROG Compliance.xls 

Orange, California 92865 3/16/2013 

714-279-6777 2:47 PM 
COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentinel-5-CEMS-7S-1 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit: 5 

Performed By: AA, MC, RM, JM 

Cpo 0.99 

Tref: 60 OF 

Stack Area: 143.14 ft' 

Meter Yd: 1.01 4 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H2O) sqrt(dP) of (fps) 

4 0.80 0.8944 726 89.67 

3 0.78 0.8832 728 88.61 

2 0.81 0.9000 729 90.34 

1 0.83 0.9110 727 91.37 

4 0.97 0.9849 729 98.86 

3 1.00 1.0000 730 100.42 

2 1.20 1.0954 729 109.96 

1 1.30 1.1402 728 114.40 

4 0.90 0.9487 730 95.27 

3 1.20 1.0954 731 110.05 

2 1.50 1.2247 730 122.99 

1 1.30 1.1402 729 114.45 

4 0.81 0.9000 730 90.38 

3 0.97 0.9849 731 98.94 

2 1.10 1.0488 730 105.32 

1 1.20 1.0954 729 109.96 

Average 1.0312 1.0155 729.1 101 .94 

Slack Flow Rate: 875.5 kwacfm 

Stack Flow Rate: 349.9 kdscfm 

Dry Gas Meter 

Time Vol. Tm(in) Tm(out) #/Mal l. 

Slart 288.919 69 69 H,O 

72 72 H,O 

End 325.284 72 72 Emply 

70 70 SG 

Total 36.365 70.8 Total 

NOx ppm 

NOx , ppm@ 15% O2 

NOx IbfMMBtu 

NOx Ib/hr 

CO ppm 

CO, ppm @ 15% O2 

CO Ib/hr 

02. % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

1845 N. Case Street 

Orange, California 92865 

714-279-6777 

CT Load MW 

SCR NH3 Injection Ib/hr 

NO, Ib/MMSCF 

CO Ib/MMBlu 

CO Ib/MMSCF 

TEST VARIABLES 

Start Date: 2/25/13 

StartJEnd Time: 16:42 17:48 

Load (MW}/Replicate# 75 1 

Barom . Pressure: 29.60 

Pstack: 2.80 iw9 

Pstack: 29.81 "H9 

MW: 28.27 Ib/lb-moJe 

METHOD 100,1 DATA 

0, CO, NO, CO 

Analyzer Range 20 10 5 10 

Cal Gas Value 18.98 9.62 4.62 9.56 

Pre-Test Direct Zero 0.13 0.12 -0.02 0.03 

Pre-Test Direct Span 18.94 9.73 4.60 9.56 

Pre-Test System Zero 0.17 0.18 -0.01 -0.03 

Pre-Test System Span 18.88 9.74 4.56 9.57 

Post-Test System Zero 0.16 0.13 -0.0 1 0.00 

Post-Test System Span 18.83 9.66 4.55 9.52 

Post-Test Direct Zero 0.13 0.08 -0.01 0.02 

Post-Test Direct Span 18.89 9.68 4.58 9.59 

Average 13.93 4.07 1.54 2.27 

Corr. results 13.98 3.94 1.57 2.28 

Pre-test zero bias 0.2% 0.6% 0.1% -0.5% 

Pre-lest span bias -0.3% 0.1% -0.8% 0. 1% 

Post-test zero bias 0.1% 0.5% 0.0% -0.2% 

Post-test span bias -0.3% -0. 2% -0.4% -0.6% 

Zero drift ~0. 1% ~0.5%, 0.0% 0.3% 

Span drift ~0. 3% 0.8% -0.1% ~0.5% 

METHOD 4,1 DATA 

Jmpingers 

End Start Diff. 

887.8 728.9 158.9 Meter Pressure: 1.5 iwg 

744.5 743.8 0.7 Sample Volume: 35.871 dscf 

630.3 630.2 0.1 H20 Volume: 3.221 scf 

936.1 926.5 9.6 Moisture Content: 8.2 % 

Ir 100 69.3 

RESULTS 

Ref. Meth CEMS 

1.57 1.60 

1.33 1.31 

0.005 0.005 

3.98 3.53 

2.28 2.00 

1.95 1.65 

3.49 2.78 

13.98 13.86 

20,996,712 19,223,000 

- 7,077.7 

-

- 81 

- 137.0 

5.63 - 0.004 -

4.59 -

Sentinel Unit 5 75% NOx- H3~ROG Compliance.xls 

3/16/2013 

2:47 PM 
COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentinel-5-CEMS-7S-2 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit: 5 

Performed By: AA. MC. RM. JM 

Cp: 0.99 

Tref: 60 OF 

Stack Area: 143.14 ft' 

Meter Yd: 1.014 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H,O) sqrt(dP) of (fps) 

4 0.76 0.8718 736 87.99 

3 0.85 0.9220 738 93.13 

2 1.00 1.0000 740 101.10 

1 1.20 1.0954 739 110.70 

4 0.99 0.9950 736 100.42 

3 1.20 1.0954 738 110.65 

2 1.30 1.1402 740 115.27 

1 1.40 1.1832 741 119.67 

4 0.79 0.8888 742 89.93 

3 0.92 0.9592 743 97.09 

2 1.00 1.0000 742 101.18 

1 1.20 1.0954 739 110.70 

4 0.57 0.7550 740 76.33 

3 0.73 0.8544 743 86.48 

2 0.88 0.9381 741 94.88 

1 0.83 0.9110 740 92.10 

Average 0.9635 0.9816 739.9 99.23 

Stack Flow Rate: 852.2 kwacfm 

Stack Flow Rate: 332.9 kdscfm 

Ory Gas Meier 

Time Vol. Tm(in) T m(oul) #/Matl. 

Slart 325.617 65 66 H,O 

66 66 H,O 

End 359.658 65 65 Emply 

69 69 SG 

Tolal 34.041 66.4 Tolal 

NOx ppm 

NO, . ppm @ 15% 0, 

NOx IbfMMBtu 

NOx Ibfhr 

CO ppm 

CO, ppm @ 15% O2 

CO Iblhr 

°2% 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

1845 N. Case Street 

Orange . California 92865 

714-279-6777 

CT Load MW 

SCR NH3 Iniection Iblhr 

NO, IblMMSCF 

CO IblMMBlu 

CO IblMMSCF 

TEST VARIABLES 

Start Date: 2125113 

StartlEnd Time: 18:07 19:14 

Load (MW)IReplicate# 75 2 

Baram. Pressure: 29.60 

Pstack: 2.80 iwg 

Pstack: 29.81 "Hg 

MW: 28.12 Ib/lb-mole 

METHOD 100.1 DATA 

0, CO, NO, CO 

Analyzer Range 20 10 5 10 

Cal Gas Value 18.98 9.62 4.62 9.56 

Pre-Test Direct Zero 0.13 0.08 -0.01 0.02 

Pre-Test Direct Span 18.89 9.68 4.58 9.59 

Pre-Test System Zero 0.16 0.13 -0.01 0.00 

Pre-Test System Span 18.83 9.66 4.55 9.52 

Post·Test System Zero 0.17 0.16 ·0.01 -0.03 

Post-Test System Span 18.83 9.71 4.56 9.60 

Post-Test Direct Zero 0.11 0.11 -0.02 0.00 

Post-Test Direct Span 18.87 9.72 4.58 9.59 

Average 13.97 4.04 2.00 4.11 

Carr. results 14.04 3.92 2.03 4.11 

Pre-test zero bias 0,1% 0.5% 0.0% -0.2% 

Pre-lest span bias -0.3% -0.2% -0.4% -0 ,6% 

Post-test zero bias 0.3% 0.5% 0.2% -0.3% 

PosHest span bias -0.2% -0.1% ·0.4% 0.1% 

Zero drift 0.1% 0.4% 0.0% -0.3% 

Span drift 0.0% 0.5% 0.1%, 0.8% 

METHOD 4.1 DATA 

Impingers 

End Start Diff. 

855.5 687.9 167.6 Meter Pressure: 1.5 iwg 

659.7 658.5 1.2 Sample Volume: 33.858 dscf 

578.7 578.5 0.2 H20 Volume: 3.561 scf 

956.3 948.7 7.6 Moisture Content: 9.5 % 

Ir 100 76.6 

RESULTS 

Ref. Meth CEMS 

203 1.80 

1.75 1.49 

0.006 0.006 

4.92 4.18 

4.11 3.50 

3.54 2.96 

5.97 4.96 

14.04 13.88 

19.973.905 19.294.000 

- 7.085.4 

-

- 80 

- 128.8 

6.94 - 0.008 - 8.33 -

Sentinel Unit 5 75% NOx-NH3-ROG Compliance.xls 

3116120 13 

2:47 PM 
REFERENCE METHOD 1-MINUTE AVERAGE DATA 

Port Point Date Time CO, CO O2-ln NOx-ln CO-I n THe-In 

N 3 2/25/2013 16:43 4.078 0.725 

N 3 2/25/2013 16:44 4.077 0.702 

N 3 2/25/2013 16:45 4.078 0.694 

N 3 2/25/2013 16:46 4.079 0.664 

N 2 2/25/2013 16:49 4.091 1.54 0.668 

N 2 2/25/2013 16:50 4.092 1.573 0.67 1 

N 2 2/25/2013 16:51 4.09 1.607 0.684 

N 2 2/25/2013 16:52 4.082 1.601 0.687 

N 1 2/25/2013 16:53 4.085 1.549 0.688 

N 2/25/2013 16:54 0.661 

N 2/25/2013 16:55 0.653 

N 2/25/2013 16:56 0.678 

0.703 

E 3 2/25/2013 17:01 13.936 4.082 1.441 1.218 

E 3 2/25/2013 17:02 13.938 4.082 1.514 2.267 

E 3 2/25/2013 17:03 13.922 4.091 1.548 3.948 

E 3 2/25/2013 17:04 13.95 4.075 1.6 3.035 

E 2 2/25/2013 17:05 13.936 4.084 1.595 2.309 

E 2 2/25/2013 17:06 13.917 4.095 1.537 3.619 

E 2 2/25/2013 17:07 13.914 4.094 1.51 6.581 

E 2 2/25/2013 17:08 13.951 4.073 1.629 3.401 

E 2 2/25/2013 17:09 13.942 4.076 1.536 2.946 

E 2/25/2013 17:10 13.926 4.082 1.534 5.491 

E 2/2512013 17:11 13.937 4076 1.647 2.426 

E 212512013 17:12 13.896 4.098 1.457 3.241 

E 212512013 17:13 13.899 4.094 1.472 3.699 

E 1 2125/2013 17:14 13.91 4.089 1.509 3.078 

S 3 212512013 17:17 13.984 4.044 1.513 3.001 

S 3 212512013 17:18 13.969 4.052 1.622 3.082 

S 3 212512013 17:19 13.962 4.053 1.542 2.355 

S 3 2/2512013 17:20 13.958 4.051 1.619 2.369 

S 3 2/2512013 17:21 13.948 4.053 1.536 2.554 

S 2 2/2512013 17:22 13.942 4.054 1.531 2.227 

S 2 2/2512013 17:23 13.936 4.058 1.469 2.733 

S 2 2125/2013 17:24 13.93 4.059 1.556 2.409 

S 2 2125/2013 17:25 13.922 4.061 1.525 2.326 

S 2 2125/2013 17:26 13.917 4.064 1.458 2.941 

S 2125/2013 17:27 13.927 4.06 1.438 2.733 

S 2/2512013 17:28 13.919 4.064 1.455 2.564 

S 212512013 17:29 13.935 4.051 1.456 2.546 

S 2125/2013 17:30 13.962 4.036 1.44 2.548 

S 212512013 17:31 13.946 4.04 1.421 2.478 

W 3 2/2512013 17:34 13.92 4.052 1.656 2.524 

W 3 2/2512013 17:35 13.926 4.047 1.665 2.634 

W 3 212512013 17:36 13.915 4.055 1.661 2.516 

W 3 212512013 17:37 13.918 4.052 1.681 2.359 

W 2 2125/2013 17:40 13.913 4.057 1.511 2.27 

W 2 212512013 17:41 13.912 4.055 1.556 2.435 

W 2 2/2512013 17:42 13.917 4.048 1.497 2.896 

W 2 2/2512013 17:43 13.907 4.052 1.539 3.051 

W 1 2/2512013 17:44 13.903 4.051 1.567 2.649 

W 2125/2013 17:45 13.894 4.055 1.579 2.646 

W 212512013 17:46 13.902 4.049 1.518 2.738 

W 212512013 17:47 13.904 4.048 1.473 2.853 

W 2125/2013 17:48 13.915 4.041 1.492 2.975 

Average 13.93 4.07 1.54 2.27 13.68 28.31 81.68 

Dlllta AIr QualifY SIIIVlclIS 

1845 N. Case Street Sentinel Unit 5 75% NOx-NH3-ROG Compliance.xls 

Orange, California 92865 3/16/2013 

714-279-6777 2:48 PM 
REFERENCE METHOD 1-MINUTE AVERAGE DATA 

Port Point Date Time 0, CO, NO. CO O2-ln NOx-ln CO-In THe-In 

W 3 2/25/2013 18:08 13.937 4.04 2.126 4.251 

W 3 2/25/2013 18:09 13.947 4.038 2.101 3.658 

W 3 2/25/2013 18:10 13.952 4.036 2.073 3.615 

w 3 2/25/2013 18:11 13.957 4.037 2.122 3.131 

W 3 2/25/2013 18:12 13.965 4.034 2.053 4.695 

w 2 2/25/2013 18:13 13.97 4.031 2.077 4.112 

W 2 2/25/2013 18:14 13.97 4.032 2.066 4.058 

w 2 2/25/2013 18:15 13.981 4.027 2.161 5.381 

W 2 2/25/2013 18:16 13.977 4.027 2.174 4.788 

W 2 2/25/2013 18:17 13.987 4.018 2.367 5.039 

W 2/25/2013 18:18 13.992 4.014 2.373 4.506 

w 2/25/2013 18:19 13.989 4.017 2.404 4.539 

W 2/25/2013 18:20 14.005 4.008 2.342 5.498 

w 2/25/2013 18:21 14.01 4.007 2.394 5.505 

W 2/25/2013 18:22 14.003 4.009 2.319 6.592 

5 3 2/25/2013 18:26 13.965 4.042 1.704 3.83 

5 3 2/25/2013 18:27 13.946 4.054 1.669 4.092 

5 3 2/25/2013 18:28 13.946 4.051 1.683 3.543 

5 3 2/25/2013 18:29 13.946 4.054 1.606 3.81 

5 3 2/25/2013 18:30 13.939 4.061 1.762 3.352 

5 2 2/25/2013 18:31 13.941 4.058 1.575 4.058 

5 2 2/25/2013 18:32 13.95 4.055 1.579 3.613 

5 2 2/25/2013 18:33 13.947 4.056 1.552 3.997 

5 2 2/25/2013 18:34 13.944 4.058 1.621 3.586 

5 2 2/25/2013 18:35 13.95 4.054 1.627 2.545 

5 1 2/25/2013 18:36 13.975 4.042 1.464 3.411 

5 1 2/25/2013 18:37 13.962 4.049 1.528 3.1 

5 1 2/25/2013 18:38 13.964 4.049 1.503 3.58 

5 1 2/25/2013 18:39 13.953 4.057 1.542 3.958 

E 3 2/25/2013 18:44 13.929 4.073 1.929 4.45 

E 3 2/25/2013 18:45 13.927 4.07 1.929 3.036 

E 3 2/25/2013 18:46 13.937 4.064 1.941 3.552 

E 3 2/25/2013 18:47 13.939 4.059 1.98 3.325 

E 2 2/25/2013 18:48 13.938 4.061 1.917 3.48 

E 2 2/25/2013 18:49 13.945 4.056 1.763 3.029 

E 2 2/25/2013 18:50 13.959 4.048 1.743 3.518 

E 2 2/25/2013 18:51 13.959 4.048 1.71 1 4.164 

E 2/25/2013 18:54 13.975 4.037 1.546 3.023 

E 2/25/2013 18:55 13.98 4.034 1.516 3.51 

E 2/25/2013 18:56 13.976 4.035 1.54 3.434 

E 1 2/25/2013 18:57 13.971 4.038 1.545 3.563 

N 3 2/25/2013 19:00 13.986 4.027 2.226 4.076 

N 3 2/25/2013 19:01 13.987 4.029 2.228 3.91 1 

N 3 2/25/2013 19:02 13.982 4.032 2.23 4.232 

N 3 2/25/2013 19:03 13.981 4.034 2.255 5.123 

N 3 2/25/2013 19:04 13.981 4.034 2.309 5.437 

N 2 2/25/2013 19:05 13.99 4.022 2.464 5.903 

N 2 2/25/2013 19:06 13.991 4.025 2.545 4.53 

N 2 2/25/2013 19:07 13.989 4.026 2.421 5.164 

N 2 2/25/2013 19:08 13.999 4.019 2.498 4.999 

N 2 2/25/2013 19:09 13.997 4.02 2.507 3.638 

N 2/25/2013 19:10 14.018 4.006 2.536 4.167 

N 2/25/2013 19: 11 14.008 4.012 2.636 4.484 

N 2/25/2013 19:12 14.004 4.013 2.683 4.502 

N 2/25/2013 19:13 14.004 4.013 2.732 4.301 

N 2/25/2013 19:14 14 4.016 2.638 4.817 

Average 13.97 4.04 2.00 4.11 13.67 27.29 132.88 

Della Air Quality Services 

1845 N. Case Street Sentinel Unit 5 75% NOx-NH3-ROG Compliance.xls 

Orange, California 92865 3/16/2013 

7 14-279-6777 2:48 PM 
COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentinel-5-CEMS-50-1 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit: 5 

Performed By: AA, MC, RM, JM 

Cp: 0.99 

Tref: 60 of 

Stack Area: 143.1 4 ft' 

Meter y o;!: 1.014 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H2O) sqrt(dP) of (Ips) 

4 0.67 0.8185 764 83.71 

3 0.73 0.8544 766 87.45 

2 0.84 0.9165 769 93.92 

1 0.82 0.9055 768 92.76 

4 0.46 0.6782 769 69.50 

3 0.58 0.7616 770 78.07 

2 0.63 0.7937 771 81.40 

1 0.69 0.8307 770 85.16 

4 0.56 0.7483 772 76.78 

3 0.59 0.7681 774 78.87 

2 0.67 0.8185 777 84.15 

1 0.78 0.8832 775 90.72 

4 0.36 0.6000 775 61.64 

3 0.41 0.6403 777 65.83 

2 0.48 0.6928 778 71.26 

1 0.47 0.6856 776 70.45 

Average 0.6002 0.7748 771 .9 79.48 

Stack Flow Rate: 682.6 kwacfm 

Stack Flow Rate: 259.7 kdscfm 

Dry Gas Meter 

Time Vol. Tm(in) T m(out) #/Mati . 

Start 423.639 69 70 H, O 

72 72 H,O 

End 461.418 73 73 Empty 

70 71 SG 

Total 37.779 71 .3 Total 

NO~ ppm 

NOx , ppm@ 15% O2 

NO. Ib/MMBtu 

NO. Ib/hr 

CO ppm 

CO, ppm@ 15% O2 

CO Ib/hr 

O2 % 

Slack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

1845 N. Case Street 

Orange, California 92865 

7 14-279-6777 

CT Load MW 

SCR NH3 Injection Ib/hr 

NO. Ib/MMSCF 

CO Ib/MMBtu 

CO Ib/MMSCF 

TEST VARIABLES 

Start Date: 2/26/13 

Start/End Time: 8:30 9:37 

Load (MW)/Replicate# SO 1 

Barom . Pressure: 29.47 

Pstack: 2.80 iwg 

Pstack: 29.68 "Hg 

MW: 28 .16 Ib/lb-mole 

METHOD 100.1 DATA 

0, CO, NO. CO 

Analyzer Range 20 10 5 10 

Cal Gas Value 18.98 9.62 4.62 9.56 

Pre-Test Direct Zero 0.11 0.07 -0.03 -0.04 

Pre-Test Direct Span 18.95 9.68 4.60 9.55 

Pre-Test System Zero 0.16 0.11 -0.03 0.03 

Pre-Test System Span 18.96 9.65 4.55 9.66 

Post-Test System Zero 0.15 0.11 -0.01 0.05 

Post-Test System Span 18.85 9.64 4.57 9.65 

Post-Test Direct Zero 0.13 0.07 -0.02 0.05 

Post-Test Direct Span 18.91 9.66 4.60 9.58 

Average 14.13 3.90 2.05 0.51 

Carr. results 14.15 3.83 2.09 0.47 

Pre-lest zero bias 0.2% 0.4% -0.1% 0.7% 

Pre-test span bias 0.0% ·0.4% -1.0% 1.1% 

Post-test zero bias 0.1% 0.4% 0.2% -0.1% 

Post-test span bias -0.3% -0.2% -0.7% 0.7% 

Zero drift 0.0% 0.0% 0.4% 0.2% 

Span drift -0.6% -0.1% 0.4% -0.2% 

METHOD 4.1 DATA 

Impingers 

End Start Ditt. 

895.2 727 .2 168.0 Meter Pressure: 1.5 iwg 

744.8 744 .3 0.5 Sample Volume: 37.068 dscl 

629.8 629.3 0.5 H20 Volume : 3.728 scI 

947.3 936.1 11 .2 Moisture Content: 9.1 % 

Ir 100 80.2 

RESULTS 

ReI. Meth CEMS 

2.09 1.60 

1.83 1.41 

0.007 0.005 

3.95 2.86 

0.47 0.20 

0.41 0.13 

0.53 0.00 

14.15 14.04 

15,579,523 15,000,000 

- 5.384 

-

- 55 

- 103 

7.34 -

0.001 - 0.96 -

Sentinel Unit 5 50% NOx-NH3-ROG Compliance.xls 

3/16/2013 

2:48 PM 
COMPLIANCE TEST 

DATA AND WORKSHEET 

CPV Sentinel-5-CEMS-50-2 

TEST CONSTANTS 

Station: CPV Sentinel 

Unit: 5 

Performed By: AA. MC. RM. JM 

Cp: 0.99 

Tref: 60 of 

Stack Area: 143.1 4 ft' 

Meter Yd: 1.014 

METHOD 2.1 DATA 

dP Temp Vel. 

Point (in. H,O) sqrt(dP) of (Ips) 

4 0.38 0.6164 774 63.30 

3 0.49 0.7000 776 71 .94 

2 0.45 0.6708 776 68.94 

1 0.36 0.6000 775 61.64 

4 0.61 0.7810 776 80.26 

3 0.66 0.8124 778 83.56 

2 0.72 0.8485 779 87.31 

1 0.78 0.8832 777 90.80 

4 0.65 0.8062 775 82 .82 

3 0.81 0.9000 776 92.49 

2 0.84 0.9165 774 94.11 

1 0.88 0.9381 774 96.33 

4 0.47 0.6856 773 70 .37 

3 0.56 0.7483 775 76 .87 

2 0.64 0.8000 776 82 .21 

1 0.66 0.8124 774 83.42 

Average 0.6123 0.7825 775.5 8040 

Stack Flow Rate: 690.5 kwacfm 

Stack Flow Rate: 261.8 kdscfm 

Dry Gas Meter 

Time Vol. T m(in) T m(out) #/Matl. 

Start 462.644 78 78 H,O 

74 75 H,O 

End 499.270 75 75 Empty 

72 72 SG 

Total 36.626 74.9 Total 

NO~ ppm 

NO~ , ppm@ 15% O2 

NO, Ib/MMBtu 

NO, Ib/hr 

CO ppm 

CO, ppm@ 15% O2 

CO Ib/hr 

O2 % 

Stack Flow dscfh 

CT Fuel Flow hscfh 

Turbine Water Injection gpm 

CT Load MW 

SCR NH3 Injection Ib/hr 

'vV'''vvv 

1845 N. Case Street 

Orange. California 92865 

714-279-6777 

NO, Ib/MMSCF 

CO IblMMBtu 

CO Ib/MMSCF 

TEST VARIABLES 

Start Date: 2/26/13 

Start/End Time: 10:00 11 :09 

Load (MW)/Replica1e# 50 2 

Baram. Pressure: 29.47 

Pstack: 2.80 iwg 

Pstack: 29.68 "Hg 

MW: 28.16 Ih/lb-mole 

METHOD 100.1 DATA 

0, CO, NO, CO 

Analyzer Range 20 10 5 10 

Cal Gas Value 18.98 9.62 4.62 9.56 

Pre-Test Direct Zero 0.13 0.07 -0.02 0.05 

Pre-Test Direct Span 18.91 9.66 4.60 9.58 

Pre-Test System Zero 0.15 0.11 -0.01 0.05 

Pre-Test System Span 18.85 9.64 4.57 9.65 

Post-Test System Zero 0.16 0.18 -0.01 -0.02 

Post-Test System Span 18.83 974 4.56 9.62 

Post-Test Direct Zero 0.13 0.13 -0.01 0.04 

Post-Test Direct Span 18.87 9.75 4.59 9.60 

Average 14.07 3.98 2.40 0.51 

Corr. results 14.13 3.86 2.43 0.49 

Pre-test zero bias 0.1% 0.4% 0.2% -0. 1% 

Pre-test span bias -0.3% -0.2% -0.7% 0.7% 

Post-test zero bias 0.2% 0.5% 0.1% -0.6% 

PosHest span bias -0.2% -0.1% -0.7% 0.2% 

Zero drift 0.0% 0.7% 0.0% -0,7% 

Soan drift -0.1% 1.0% -0.2% -0.3% 

METHOD 4.1 DATA 

Impingers 

End Start Diff. 

855.1 687.7 167.4 Meter Pressure: 1.5 iwg 

658.2 657.2 1.0 Sample Volume: 35.693 dscl 

579.0 578.7 0.3 H20 Volume : 3,607 scf 

1012.1 1003.2 8.9 Moisture Content: 9.2 % 

Ir 100 77.6 

RESULTS 

Ref. Meth CEMS 

2.43 1.80 

2.12 1.56 

0.008 0.006 

4.63 3.38 

0.49 0.20 

0.43 0.17 

0.56 0.00 

14.13 14.02 

15.706.947 15.008.000 

- 5.400 

-

- 55 

- 103 

8.58 - 0.001 -

1.01 -

Sentinel Unit 5 50% NOx-NH3-ROG Compliance.xls 

311612013 

2:48 PM 
REFERENCE METHOD 1-MINUTE AVERAGE DATA 

Port Point Date Time 0, CO, NO, CO 02-ln NOx-ln CO-In THC-In 

W 3 2/26/2013 8:31 14.211 3.9 1.789 0.52 14.21 25.975 54.795 3.638 

W 3 2/26/2013 8:32 14.208 3.901 1.793 0.547 14.208 25.974 54.967 3.641 

W 3 2/26/2013 8:33 14.203 3.902 1.834 0.544 14.208 26.055 54.372 3.61 

W 3 2/26/2013 8:34 14.214 3.894 1.84 0.542 14.207 26.033 54.419 3.627 

W 2/26/2013 8:37 14.201 3.89 2.188 0.52 14.208 26.17 53.632 3.591 

W 2/26/2013 8:38 14.214 3.879 2.071 0.506 14.208 26.173 53.644 3.517 

W 2/26/2013 8:39 14.199 3.883 2.11 0.513 14.208 26.297 53.477 3.47 

W 2/26/2013 8:42 14.206 3.87 2.365 0.481 14.208 26.182 53.502 3.591 

W 2/26/2013 8:43 14.183 3.874 2.38 0.496 14.196 26.191 53.144 3.568 

W 2/26/2013 8:44 14.185 3.872 2.471 0.478 14.193 26.25 52.732 3.487 

W 2/26/2013 8:45 14.179 3.871 2.511 0.479 14.194 26.313 52.189 3.428 

5 3 2/26/2013 8:48 14.147 3.887 1.828 0.374 14.17 26.468 50.903 3.274 

S 3 2/26/2013 8:49 14.145 3.887 1.688 0.378 14.165 26.513 51 .299 3.368 

S 3 2/26/2013 8:50 14.148 3.883 1.735 0.364 14.179 26.651 50.379 3.232 

S 3 2/26/2013 8:51 14.143 3.885 1.768 0.337 14.162 26.757 49.824 3.151 

S 3 2/26/2013 8:52 14.132 3.89 1.964 0.345 14.165 26.861 49.405 3.059 

S 2 2/26/2013 8:53 14.127 3.893 1.751 0.3 14.161 27.023 48.783 3.02 

5 2 2/26/2013 8:54 14.123 3.896 1.704 0.286 14.154 27.269 47.667 2.939 

5 2 2/26/2013 8:55 14.099 3.91 1.779 0.271 14.134 27.476 46.625 2.757 

5 2 2/26/2013 8:56 14.098 3.911 1.819 0.241 14.124 27.805 45.339 2.695 

27 

8:58 

S 2/26/2013 8:59 1.961 0.237 14.13 27.842 44.088 2.547 

5 2/26/2013 9:00 1.63 0.283 14.128 26.933 47.536 2.854 

S 2/26/2013 9:01 1.654 0.316 14.109 26.422 50.461 3.175 

5 2/26/2013 9:02 1.688 0.36 14.126 26.148 52.456 3.362 

E 2/26/2013 9:05 14.12 3.899 1.748 0.624 14.141 26.039 53.54 3.621 

E 2/26/2013 9:06 14.107 3.905 1.739 0.63 14.134 25.998 53.496 3.529 

E 2/26/2013 9:07 14.095 3.912 1.723 0.647 14.117 26.038 53.654 3.59 

E 2/26/2013 9:08 14.102 3.91 1.744 0.636 14.125 26.039 53.328 3.554 

E 2 2/26/2013 9:11 14.097 3.911 1.79 0.62 14.116 26 .039 53.327 3.378 

E 2 2/26/2013 9:12 14.089 3.916 1.842 0.62 14.111 26.091 52.996 3.444 

E 2 2/26/2013 9:13 14.095 3.913 1.825 0.628 14.119 26.059 53.063 3.521 

E 2 2/26/2013 9:14 14.093 3.916 1.731 0.662 14.12 26.034 53 .025 3.586 

E 1 2/26/2013 9:15 14.093 3.916 1.674 0.674 14.117 26.072 53.076 3.547 

E 1 2/26/2013 9:16 14.089 3.917 1.708 0.705 14.115 26.044 53.122 3.52 

E 2/26/2013 9:17 14.096 3.914 1.691 0.68 14.128 26.016 53 .347 3.618 

E 2/26/2013 9:18 14.103 3.91 1.696 0.691 14.132 26.026 53.36 3.614 

N 3 2/26/2013 9:24 14.12 3.902 2.298 0.597 14. 13 26.02 53.319 3.634 

N 3 2/26/2013 9:25 14.122 3.899 2.274 0.581 14.133 25.986 53.621 3.625 

N 3 2/26/2013 9:26 14.123 3.899 2.295 0.578 14.138 26.024 53.18 3.588 

N 3 2/26/2013 9:27 14.119 3.901 2.358 0.572 14.133 26.043 53.329 3.599 

N 2 2/26/2013 9:28 14. 106 3.907 2.601 0.557 14.121 26.097 52.986 3.566 

N 2 2/26/2013 9:29 14.106 3.909 2.567 0.579 14.126 26.055 52.921 2.997 

N 2 2/26/2013 9:30 14.102 3.912 2.595 0.574 14.113 26.08 52.752 3.43 

N 2 2/26/2013 9:31 14.102 3.912 2.542 0.576 14.117 26.056 52 .974 3.443 

N 2 2/26/2013 9:32 14.1 3.913 2.539 0.581 14.113 26.033 53.323 3.486 

N 2/26/2013 9:33 14.107 3.91 2.725 0.531 14.125 26.04 53.032 3.437 

N 2/26/2013 9:34 14.104 3.912 2.84 0.537 14.111 26.025 52 .975 3.422 

N 2/26/2013 9:35 14.107 3.912 2.773 0.53 14.11 26.004 53.404 3.459 

N 2/26/2013 9:36 14.099 3.915 2.825 0.555 14.108 25.948 53.415 3.517 

N 2/26/2013 9:37 14.102 3.91 4 2.828 0.566 14.112 25.904 54 .118 3.522 

Average 14.13 3.90 2.05 0.51 14.15 26.32 52.12 

Della Air Quality Services 

1845 N. Case Streel Sentinel Unit 5 50% NOx·NH3·ROG Compliance.xls 

Orange, California 92865 3/16/2013 

714-279-6777 2:48 PM 
REFERENCE METHOD 1-MINUTE AVERAGE DATA 

Port Point Date Time 0, CO 02-ln NOx~ln THC-In 

W 3 2/26/2013 10:01 14.077 14.052 25.316 3.952 

W 3 2/26/2013 10:02 14.062 14.044 4.024 

W 3 2/26/2013 10:03 14.057 14.039 4.04 

w 3 2/26/2013 10:04 14.04 14.035 3.686 

W 2 2/2612013 10:07 14.059 3.947 2.591 0.608 14.038 25.875 52.678 3.48 

W 2 2/26/2013 10:08 14.056 3.949 2.553 0.637 14.041 25.925 52 .567 3.509 

W 2 2/26/2013 10:09 14.073 3.942 2.562 0.607 14.055 25.999 51.727 3.298 

W 2 2/26/2013 10:10 14.083 3.942 2.459 0.595 14.059 25.846 52.463 3.433 

w 1 2/26/2013 10:11 14.067 3.949 2.566 0.595 14.058 25.848 52.853 3.504 

w 1 2/26/20 13 10:12 14.072 3.949 2.564 0.607 14.056 25.887 52.603 3.446 

W 2/26/2013 10:13 14.091 3.941 2.7 0.552 14.062 25.835 53.211 3.471 

W 2/26/2013 10:14 14.067 3.955 2.831 0.559 14.044 25.881 52.765 3.37 

S 3 2/26/2013 10:20 14.054 3.968 1.947 0.438 14.034 26.011 52.383 3.46 

S 3 2/26/2013 10:21 14.042 3.976 1.989 0.445 14.02 25.997 52.894 3.556 

S 3 2/26/2013 1022 14.038 3.98 1.952 0.429 14.01 1 26.008 52.165 3.388 

S 3 2/26/2013 10:23 14.04 3.983 1.925 0.421 14.013 25.986 51 .964 3.322 

S 2 2/26/2013 10:24 14.04 3.982 1.88 0.454 14.016 25.898 53.23 3.607 

S 2 2/26/2013 10:25 14.041 3.982 1.834 0.353 14.03 25.934 53.279 3.684 

S 2 2/26/2013 10:26 14.037 3.987 1.848 0.339 14.015 25.942 53.32 3.263 

S 2 2/26/2013 10:27 14.04 3.988 1.815 0.322 14.014 25.958 52.914 3.464 

S 2/26/2013 10:30 14.032 3.997 2.037 0.343 14.001 26.087 52.209 3.454 

S 2/26/2013 10:31 14.026 4 1.952 0.327 13.991 26.082 51.881 3.383 

S 2/26/2013 10:32 14.038 3.994 1.852 0.287 14.006 26.009 51 .848 3.309 

S 1 2/26/2013 10:33 14.038 3.995 1.864 0.322 14.007 25.986 52 .28 3.361 

E 3 2/26/2013 10:38 14.061 3.988 2.382 0.577 14.02 25.876 52 .895 3.551 

E 3 2/26/2013 10:39 14.072 3.984 2.276 0.557 14.029 25.838 53.538 3.59 

E 3 2/26/20 13 10:40 14.074 3.984 2.294 0.568 14.028 25.895 52.921 3.393 

E 3 2/26/2013 10:41 14.061 3.99 2.36 0.581 14.01 25.965 52.318 3.013 

E 3 2/26/2013 10:42 14.075 3.986 2.429 0.565 14.028 25.903 52.544 2.718 

E 2 2/26/2013 10:43 14.089 3.979 2.588 0.551 14.034 25.914 52.46 3.108 

E 2 2/26/2013 10:44 14.088 3.977 2.59 0.548 14.033 25.902 52.459 3.219 

E 2 2/26/2013 10:45 14.078 3.98 2.611 0.559 14.026 25.917 53.233 3.627 

E 2 2/26/2013 10:46 14.088 3.973 2.603 0.542 14.035 25.915 53.047 3.515 

E 2 2/26/2013 10:47 14.087 3.973 2.725 0.548 14.034 25.932 52.77 3.403 

E 1 2/26/2013 10:48 14.089 3.969 2.9 0.52 14.036 25.927 52.998 3.548 

E 2/26/2013 10:49 14.087 3.968 2.762 0.494 14.031 25.94 52.075 3.243 

E 2/26/2013 10:50 14.091 3.964 2.894 0.476 14.037 26.009 51 .393 3.035 

E 2/26/2013 10:51 14.089 3.967 2.921 0.489 14.031 26.031 51 .119 3.135 

E 2/26/2013 10:52 14.065 3.981 2.937 0.491 14.01 26.095 50.237 3.021 

N 3 2/26/2013 10:55 14.069 3.986 2.319 0.536 14.016 26.03 50 .096 3.038 

N 3 2/26/2013 10:56 14.057 3.994 2.331 0.515 14.004 26.058 49.941 2.961 

N 3 2/26/2013 10:57 14.063 3.993 2.368 0.531 14.01 26.011 50.829 3.177 

N 3 2/26/2013 10:58 14.074 3.991 2.357 0.533 14.024 26.067 50.033 2.994 

N 2 2/26/2013 11 :01 14.081 3.995 2.658 0.486 14.02 26.066 49.799 2.97 

N 2 2/26/2013 11 :02 14.083 3.993 2.572 0.504 14.024 26.05 50.11 3.01 

N 2 2/26/2013 11 :03 14.088 3.995 2.664 0.485 14.03 26.106 49.595 2.992 

N 2 2/26/2013 11 :04 14.089 3.993 2.656 0.495 14.034 26.014 50.111 3.02 

N 2/26/2013 11 :05 14.085 4.001 2.691 0.479 14.025 26.05 50.318 3.013 

N 2/26/2013 11 :06 14.082 4.001 2.711 0.51 14.024 26.109 50.881 3.338 

N 2/26/2013 11 :07 14.084 4.006 2.941 0.5 14.017 26.065 50.857 3.386 

N 2/26/2013 11 :08 14.083 4.004 2.866 0.538 14.023 26.07 50.118 3.086 

N 2/26/2013 11 :09 14.085 4.006 2.771 0.501 14.022 26.045 50.128 3.062 

Average 14.07 3.98 2,40 0,51 14,03 25,94 52,18 

OllIla Air QualilY SlIrvlclIS 

1845 N, Case Street Sentinel Unit 5 50% NOx-NH3-ROG Compliance.xls 

Orange, California 92865 3/16/2013 

714-279-6777 2:48 PM 
Appendix C.2.3 One Minute Data Logger Data 

R5210729 C-6 
Date Time 

0 , 

% 

CO, 

% 

2/25/2013 7:44:00 AM 1L...,;:,0.,,'4,:,...._;0.;::03,;2'-1 

2/25/2013 7:45:00 AM 14.55 7805 

2125/2013 7:46:00 AM 19.018 9.711 

2125/2013 7:47:00 AM I 19.022 9.623 

212512013 7:48:00AM 11.639 5.769 

2125/2013 7:49:00AM 10.105 5.055 

2125/2013 7:50:00 AM 1,.....;,;::0.",0;;;4;-...;:;5.;;;05;;3,...., 

2125/2013 7:51 :00 AM '-:'';'7.':;:496;;;;--~'.';'73;i8~ 

NO~ CO 

PPM PPM 

·0.005 ·0.02 

-0015 -0.037 

·0.021 J -0.017 

-0.022 -0.031 

·0.027 I -0.014 

2.331 7.471 

4.543 9.971 

4.558 9.542 

2125/2013 7:52:00 AM 20.915 0.082 4.596 10.059 

2/25/2013 7:53:00 AM 20.928 0.079 4.604 4.889 

2/25/2013 7:54:00 AM 20.941 0.079 4.599 4.451 

2125/2013 7:55:00AM 20.941 0.078 4.576 4.314 

2125/2013 7:56:00 AM 20.941 0.079 4.574 1.234 

2125/2013 7:57:00 AM 20.936 0.076 4.567 0.657 

2125/2013 7:58:00 AM 20.926 0.075 0.417 0.646 

2125/2013 7:59:00 AM 20.939 0.075 0.001 0.644 

2125/2013 8:00:00 AM 20.942 0.076 2.738 0.659 

2/25/2013 8:01 :00 AM 20.933 0.076 3.457 0.681 

2/25/2013 8:02:00 AM 20.932 0.079 3.445 3.964 

2125/2013 8:03:00 AM 20.941 0.078 3.452 0.723 

2/25/2013 8:04:00AM 20.941 0.079 2.175 0.638 

2125/2013 8:05:00 AM 20.942 0.079 -0.013 0.629 

212512013 8:06:00 AM 20.942 0.078 -0.024 0.621 

2125/2013 8:07:00 AM 20.942 0.079 -0.015 0.606 

2/25/2013 8:08:00 AM 20.941 0.079 1.548 0.596 

2/25/2013 8:09:00 AM 20.941 0.079 4.589 0.581 

2/25/2013 8:10:00 AM 20.937 0.079 4.596 0.581 

2/25/2013 8:11 :00 AM 20.932 0.08 4.601 0.57 

2125/2013 8:12:00 AM 20.922 0.08 4.603 0.569 

2/25/2013 8:13:00 AM 20.917 0.081 2.837 0.57 

2/2512013 8:14:00 AM 20.916 0.081 2.462 0.547 

212512013 8:15:00 AM 20.917 0.081 2.53 0.546 

212512013 8:16:00 AM 20.915 0.081 2.531 0.546 

2125/2013 8:17:00 AM 20.903 0.08 1.8 0.543 

2125/2013 8:18:00 AM 20.892 0.08 0.007 0.495 

2/25/2013 8:19:00 AM 20.893 0.082 0.005 0.477 

2/25/2013 8:20:00 AM 20.893 0.082 0.012 0.483 

2125/2013 8:21 :00 AM 20.893 0.083 0.014 0.486 

2125/2013 8:22:00 AM 20.893 0.084 0.017 0.483 

212512013 8:23:00 AM 20.894 0.085 0.013 0.474 

212512013 8:24:00 AM 20.941 0.083 0.005 0.459 

2125/2013 8:25:00 AM 20.942 0.083 0.002 0.457 

2125/2013 8:26:00 AM 20.942 0.082 -0.007 0.459 

2/25/2013 8:27:00 AM 20.908 0.084 -0.007 0.446 

2/25/2013 8:28:00 AM 20.477 1.539 -0.005 0.448 

2125/2013 8:29:00 AM 19.004 9.576 -0.005 -0.104 

2125/2013 8:30:00 AM rl""1;';9:;;0;;;0";2-""9;;;6;;;0';'~"';-0;;;0;;;':;:6"" -0.187 

2125/201 3 8:31:00AM 16.767 8.202 0.387 -0.17 

2125/2013 8:32:00AM 0.355 0.077 4.552 0.155 

2125/2013 8:33:00 AM rl-:i-0~'64~-""0::'.0i::5;-i'---:4:;;5~8i:9--::0':i2';'74:-" 

2125/2013 8:34:00AM 0.144 0.046 3.142 1.771 

2125/2013 8:35:00 AM 0.138 0.044 -0.007 9.395 

2125/2013 8:36:00 AM 0.138 0.042 ·0.02 9.781 

2125/2013 8:37:00 AM 0.138 0.043 ·0.025 9.781 

2/25/2013 8:38:00 AM 0.138 0.044 1.272 8.64 

2/25/2013 8:39:00 AM 0.138 0.043 4.568 0.422 

2125/2013 8:40:00 AM 3.124 0.05 4.005 0.17 

2125/2013 8:41 :00 AM 20.684 0.088 0.083 0.01 

212512013 8:42:00 AM 20.832 0.092 0.034 0.012 

2125/2013 8:43:00 AM 20.842 0.092 0.013 5.33 

2125/2013 8:44:00 AM 20.852 0.092 0.01 9.424 

0, 

% 

NO~ CO THC 

PPM PPM PPM 

0.022 0.336 7.294 

27.37 39.861 7.428 

48.025 232.184 4.905 

42.059 1 241.1321 1.56 

16.902 186.927 1.406 

0.022 131 .9 0.872 

·0.045 1 132.885 1 0.87 

·0.055 99.753 0.758 

0.442 

0.432 

02lC02lCO Cal Zero 

N2INOx Mode 

02lC02lCO Car High 

N2INO Mode 

NO/NOx Mode 

02lC02lCO Mid 

N2INO Mode; CO Car High 

0.063 

12.161 

18.929 

18.929 

13.488 

10.015 

10.014 

4.955 

0.071 

0.057 

0.042 

0.46 

0.043 

0.043 

0.043 

0.043 

2.537 

20.725 

20.865 

2.773 

4.686 

4.61 

1.726 

0.07 

0.067 

2.272 

0.15 

0.432 NO/NOx Mode; CO Mid;THC Cal Zero 

4.585 

4.581 

4.577 

0.494 

-0.031 

2.8 

3.462 

3.458 

4.322 

25.7 NO/NO Mode 

·0.01 26.954 

0.035 27.325 

0.036 27.135 N02lNO Mode 

-0.036 26.494 

10.453 

20.865 3.449 

0.19 

0.265 

0.265 

0.269 

0.261 

0.26 

0.265 

0.311 

0.538 

0.341 

0.315 

0.587 

0.035 

O.OOg 

0.446 

0.436 N02/NOx Mode 

0.431 

20.819 2.362 0.431 

20.741 ·0.029 3.04 

20.744 -0.03 25.892 NOx Cal Zero 

20.766 ·0.037 25.704 

20.767 12.449 15.293 

20.774 38.842 3.478 

20.865 41.701 0.445 

19.962 28.837 0.434 

9.591 

0.08 

0.068 

0.402 

0.048 

0.042 

0.042 

0.042 

0.043 

0.043 

0.043 

0.293 

0.125 

0.043 

0.042 

0.201 

0.106 

0.042 

0.043 

0.043 

0.043 

0.317 

42.361 

24.648 

23.586 

23.858 

0.434 NOx Cal High 

0.43 

0.434 THC Cal Zero 

0.86 

23.867 0.175 17.088 NOx Mid 

17.224 0.Q18 20.377 

0.1 ·0.017 33.127 

0.051 -0.023 86.849 

0.031 -0.045 87.535 

0.019 ·0.043 89.53 

0.009 -0.013 88.98 

0.344 -0.045 89.824 

0.574 8.203 60.41 

0.018 -0.038 24.715 

0.005 ·0.038 24.155 

0.215 -0.044 23.619 

0.414 

0.012 

0.007 

·0.001 

0.004 

0.779 

3.392 53.496 

·0.044 87.68 

-0.045 86.785 02/C02 bias 

-0.047 85.56 

-0.047 85.078 

1.521 64.889 NOx bias 

0.045 0.015 2.943 21 .898 

0.519 0.995 0.135 0.431 

0.109 0.541 9.675 22.615 CO bias 

0.044 0.011 0.226 44.658 

0.043 0.003 0.238 45.123 

7.298 14.652 33.888 42.87 

13.217 30.175 165.265 39.858 

13.238 30.707 155.668 34.372 

13.239 31 .045 151.591 31 .152 CO Cal Zero 

13.239 31.137 145.34 23.29' 

13.244 31.005 163.322 22.337 
Date Time 

0, 

% 

CO, 

% 

2125/2013 8:45:00 AM 20.851 0.095 

2125/2013 8:46:00 AM 20.855 0.096 

2125/2013 8:47:00 AM 20.864 0.096 

2125/2013 8:48:00 AM 20.866 0.098 

212512013 8:49:00 AM 20.867 0.1 

2/2512013 8:50:00 AM 20.867 0.102 

2/25/2013 8:51 :00 AM 20.87 0.104 

2/25/2013 8:52:00AM 20.868 0.105 

NO, 

PPM 

0.018 

0.011 

o 

-0.004 

0.008 

0.006 

0.007 

-0.001 

CO 

PPM 

9.492 

9.526 

9.565 

9.571 

7.05 

4.506 

4.488 

2.176 

0, 

% 

NO, 

PPM 

CO 

PPM 

THC 

PPM 

13.239 31 .292 143.83 22.272 

13.231 31.403 150.242 26.525 

13.227 31.41 139.437 27.382 

13.242 31 .641 137.5 29.439 CO Cal High 

13.246 31 .338 136.107 24.705 

13.234 31.724 128.409 24.886 

13.24 31.248 142.487 25.669 CO Mid 

13.227 31 .545 136.666 26.748 

2125/2013 8:53:00AM 19.294 4.391 0.176 0.211 13.245 31 .385 148.156 31 .123 

2/25/2013 8:54:00 AM 19.001 9.637 -0.003 -0.251 13.242 31.433 143.93 28.775 

2/25/2013 8:55:00 AM 1"1"'1"'9;; .0"'0';'1 -....:;;9:;;6"6---:-0"' . .0"0"'9..., -0.235 13.243 31.43 146.417 29.948 02/C02 bias 

2125/2013 8:56:00 AM 8.511 3.988 2.433 -0.123 13.247 31.494 144.405 29.968 

2125/2013 8:57:00 AM 0.178 0.103 4.576 0.212 13.24 31 .413 151.061 16.342 

2125/2013 8:58:00 AM 1"1-:i'0';'14:i8:-~0i:'0:':i9~2~-'4::'5i:8r--';;0;;;2i53~ 13.246 31.462 165.249 0.975 NOx bias 

2125/2013 8:59:00 AM 0.137 0.088 4.44 0.301 13.244 31 .635 148.688 0.924 

2125/2013 9:00:00 AM 0.138 0.088 0.069 3.811 13.248 31.315 161.292 0.964 

2125/2013 9:01:00AM 0.138 0.088 -0.016 7.074 16.888 18.624 131.847 0.865 

2125/2013 9:02:00 AM 0.137 0.089 -0.008 9.814 20.908 0.861 7.278 0.453 

2/25/2013 9:03:00 AM 0.137 0.088 -0.009 9.86 20.927 0.613 0.559 0.431 

2125/2013 9:04:00 AM 0.137 0.088 -0.02 9.849 20.925 0.507 0.384 0.433 CO bias 

2125/2013 9:05:00 AM 7.007 0.105 

2125/2013 9:06:00 AM 0.805 0.091 

2/25/2013 9:07:00 AM 0.137 0.091 

2/25/2013 9:08:00AM 14.459 0.124 

2125/2013 9:09:00 AM 20.859 0.14 

2125/2013 9:10:00AM 20.88 0.141 

2/25/2013 9:11:00AM 20.888 0.143 

2/25/2013 9:12:00 AM 20.902 0.143 

2/25/2013 9:13:00AM 20.916 0.145 

2/25/2013 9:14:00 AM 20.916 0.145 

2/25/2013 9:15:00 AM 20.917 0.1 46 

2125/2013 9:16:00 AM 20.917 0.146 

2125/2013 9:17:00 AM 20.916 0.146 

2/25/2013 9:18:00 AM 20.916 0.147 

2/25/2013 9:19:00AM 20.917 0.145 

2125/2013 9:20:00 AM 20.918 0.145 

2125/2013 9:21 :00 AM 20.922 0.146 

2125/2013 9:22:00 AM 20.926 0.146 

2125/2013 9:23:00 AM 20.928 0.147 

2125/2013 9:24:00AM 20.932 0.148 

2125/2013 9:25:00 AM 20.94 0.149 

2/25/2013 9:26:00AM 20.939 0.151 

2/25/2013 9:27:00AM 20.94 0.151 

2/25/2013 9:28:00 AM 20.94 

2125/2013 9:29:00 AM 20.938 

2125/2013 9:30:00 AM 20.933 

2125/2013 9:31 :00 AM 20.932 

2125/2013 9:32:00 AM 20.929 

2125/2013 9:33:00 AM 20.929 

2125/2013 9:34:00 AM 14.366 

2125/2013 9:35:00 AM 

2125/2013 9:36:00 AM 

2/25/2013 9:37:00 AM 

13.298 

13.279 

13.272 

2/25/2013 9:38:00 AM 13.264 

2125/2013 9:39:00 AM 13.254 

2125/2013 9:40:00 AM 13.271 

2125/2013 9:41:00 AM 13.273 

2125/2013 9:42:00 AM 13.272 

2125/2013 9:43:00 AM 13.284 

2125/2013 9:44:00 AM 13.272 

2125/2013 9:45:00 AM 13.261 

2125/2013 9:46:00 AM 13.247 

0.153 

0.155 

0.157 

0.157 

0.158 

0.159 

3.989 

4.509 

4.516 

4.521 

4.525 

4.53 

4.523 

4.519 

4.522 

4.515 

4.523 

4.526 

4.534 

0.001 

-0.012 

-0.019 

0.001 

o 

0.009 

0.001 

-0.004 

o 

-0.006 

-0.003 

-0.003 

-0.004 

-0.002 

-0.006 

-0.006 

-0.004 

-0.002 

o 

-0.002 

0.005 

0.009 

o 

0.004 

0.003 

0.001 

0.001 

0.004 

0.002 

4.862 

5.411 

5.411 

5.411 

5.411 

5.411 

2.716 

2.369 

2.256 

2.24 

2.238 

2.203 

2.182 

7.685 20.923 0.423 0.463 0.431 

5.048 20.914 0.379 0.459 0.432 

4.782 20.923 0.313 0.457 0.432 

4.55 20.93 0.242 0.26 0.432 

1.968 20.922 0.245 0.54 0.435 

0.45 20.928 0.182 0.287 0.94 

0.434 20.928 0.148 0.263 0.344 

0.436 20.926 0.131 0.138 0.437 

0.43 20.917 0.147 0.287 0.437 

0.45 20.914 0.132 0.361 0.436 

0.433 20.916 0.106 0.315 0.437 

0.159 20.91 0.125 0.386 0.436 

0.418 20.912 0.103 0.362 0.434 

0.453 20.915 0.086 0.338 0.435 

0.453 20.916 0.061 0.258 0.433 

0.446 20.917 0.066 0.212 0.433 

0.434 20.914 0.083 0.363 0.434 

0.441 20.921 0.068 0.311 0.434 

0.437 16.773 15.017 29.195 0.529 

0.445 13.633 29.371 156.943 0.952 

0.448 18.901 0.946 43.031 0.576 

0.438 18.978 0.246 -0.323 0.434 

0.441 18.978 0.191 -0.373 0.43 

0.45 18.978 0.156 -0.376 0.432 

0.445 

0.452 

0.448 

0.442 

0.445 

2.995 

4.93 

4.856 

5.06 

5.739 

6.393 

6.109 

3.552 

1.578 

1.477 

1.356 

1.35 

1.993 

18.978 

10.494 

0.112 

0.313 

0.135 

2.913 

4.781 

35.336 

-0.42 

3.714 

1.597 

4.499 

0.434 02 bias 

0.445 

0.439 

0.447 

0.055 

0.042 

0.462 

0.042 

4.329 

41.924 

41.954 

0.063 

0.036 

0.432 NOx bias 

0.438 

12.345 95.601 0.752 

0.132 1 240.1991 1.226 

8.769 235.73 1.212 

13.195 30.3 176.326 1.021 

13.216 30.287 179.263 3.083 

13.238 30.443 172.535 4.364 

13.217 33.348 106.051 3.909 

13.217 34.074 36.378 3.211 

13.228 33.749 33.781 3.141 

13.216 34.086 31.81 3.703 

13.21 33.98 29.573 5.745 

13.203 33.044 50.429 9.621 

CO bias 
Date Time 

0, 

% 

212512013 9"7:00 AM 13.247 

212512013 9"8:00 AM 13.246 

212512013 9"9:00 AM 13.247 

212512013 9:50:00 AM 13.239 

212512013 9:51:00AM 13.237 

212512013 9:52:00 AM 13.242 

212512013 9:53:00 AM 13.243 

212512013 9:54:00 AM 13.247 

212512013 9:55:00AM 13.247 

212512013 9:56:00 AM 13.247 

212512013 9:57:00 AM 15.057 

212512013 9:58:00 AM 15.262 

co, 

% 

4.533 

4.536 

4.536 

4.54 

4.54 

4.54 

4.538 

4.536 

4.536 

4.535 

3.422 

3.455 

212512013 9:59:00 AM 13.247 4.535 

212512013 10:00:00 AM 13.448 4.417 

21251201310:01:00AM 13.643 4.311 

21251201310:02:00AM 13.642 4.311 

212512013 10:03:00 AM 13.624 4.323 

212512013 10:04:00 AM 13.604 4.342 

212512013 10:05:00 AM 15.922 2.962 

212512013 10:06:00 AM 16.613 2.609 

212512013 10:07:00 AM 15.807 3.072 

212512013 10:08:00 AM 14.966 3.565 

212512013 10:09:00 AM 14.067 4.089 

212512013 10:10:00 AM 13.533 4.393 

212512013 10:11 :00 AM 13.543 4.387 

212512013 10:12:00AM 13.569 4.376 

212512013 10:13:00 AM 13.564 4.381 

212512013 10:14:00 AM 13.547 4.394 

212512013 10:15:00 AM 13.536 4.4 

212512013 10:16:00AM 13.58 

212512013 10:17:00AM 13.572 

212512013 10:18:00AM 13.589 

212512013 10:19:00AM 13.593 

212512013 10:20:00 AM 13.582 

212512013 10:21 :00 AM 13.569 

212512013 10:22:00AM 13.573 

212512013 10:23:00 AM 13.567 

212512013 10:24:00 AM 13.584 

212512013 10:25:00AM 13.574 

212512013 10:26:00 AM 13.582 

212512013 10:27:00 AM 13.576 

212512013 10:28:00 AM 13.567 

212512013 10:29:00 AM 13.566 

212512013 10:30:00 AM 13.571 

212512013 10:31:00AM 13.556 

212512013 10:32:00AM 13.568 

212512013 10:33:00 AM 13.556 

2/25/2013 10:34:00 AM 13.555 

212512013 10:35:00AM 13.552 

212512013 10:36:00 AM 13.558 

212512013 10:37:00 AM 13.555 

212512013 10:38:00 AM 13.556 

212512013 10:39:00 AM 13.558 

212512013 10:40:00 AM 13.556 

21251201310:41:00AM 13.556 

212512013 10:42:00 AM 13.547 

212512013 10"3:00 AM 13.551 

212512013 10:44:00 AM 13.545 

212512013 10:45:00 AM 13.547 

212512013 10:46:00 AM 13.548 

212512013 10"7:00AM 13.549 

212512013 10:48:00AM 13.547 

4.384 

4.389 

4.385 

4.386 

4.394 

4.4 

4.399 

4.404 

4.399 

4.403 

4.4 

4.4 

4.401 

4.401 

4.4 

4.401 

4.394 

4.396 

4.396 

4.395 

4.392 

4.392 

4.393 

4.393 

4.394 

4.395 

4.4 

4.395 

4.398 

4.394 

4.391 

4.389 

4.391 

NO, 

PPM 

2.248 

2.247 

2.237 

2.231 

2.223 

2.236 

2.27 

2.236 

2.283 

2.296 

1.852 

1.326 

1.934 

1.964 

1.975 

1.705 

1.656 

1.653 

1.082 

0.364 

0.73 

0.649 

1.708 

2.195 

2.022 

1.986 

1.965 

2.009 

1.97 

1.964 

2.007 

1.967 

1.952 

2.79 

2.314 

2.029 

1.956 

1.948 

1.956 

1.96 

1.955 

1.952 

1.942 

1.962 

1.94 

1.974 

1.968 

1.971 

1.961 

1.976 

1.966 

1.948 

1.969 

1.959 

1.959 

1.958 

1.949 

1.978 

1.976 

1.994 

2.002 

1.973 

CO 

PPM 

2.453 

2.7 

2.164 

2.179 

2.251 

3.083 

2.53 

2.401 

2.535 

3.997 

3.777 

2.291 

3.354 

3.886 

3.938 

3.853 

3.541 

2.592 

1.547 

0.37 

0.262 

0.661 

0.675 

2.744 

5.065 

4.72 

4.43 

2.938 

1.188 

2.609 

1.773 

1.14 

1.345 

1.671 

2.091 

3.863 

4.391 

4.293 

3.623 

3.469 

3.143 

2.808 

3.266 

3.392 

3.189 

2.808 

3.127 

2.979 

2.73 

2.83 

2.783 

3.124 

3.303 

2.759 

3.011 

3.141 

3.416 

3.14 

3.02 

2.978 

2.802 

3.035 

0, 

% 

NO, 

PPM 

CO 

PPM 

THe 

PPM 

13.213 32.771 69.75 13.209 

13.2 32.897 84.543 15.989 

13.204 33.341 60.032 11.414 

13.19 33.212 59.83 11.385 

13.192 32.989 61.019 11.584 

13.194 32.599 95.135 17.962 

13.207 32.99 76.389 14.475 

13.21 32.929 67.275 12.766 

13.201 32.647 75.966 14.412 

13.206 31.555 131.992 24.878 

13.209 31.745 134.045 25.17 

13.214 31.778 142.049 26.673 

13.206 32.021 120.D78 22.6 

13.635 30.212 135.847 25.529 

13.991 28.873 114.339 21.543 

13.979 28.835 112.473 21.197 

13.979 29.205 107.298 20.213 

13.92 30.683 70.368 13.339 

14.519 29.448 40.529 7.755 

16.889 29.868 26.238 5.092 

16.04 28.182 22.487 4.399 

15.268 22.274 50.362 9.593 

14.338 27.763 35.847 6.871 

13.89 29.206 76.345 14.449 

13.905 28.598 152.17 28.601 

13.923 28.832 137.661 25.889 

13.927 28.928 126.926 23.862 

13.908 30.73 86.6 16.388 

13.892 31.108 23.665 4.645 

13.94 29.521 65.889 12.498 

13.946 30.871 46.747 8.926 

13.945 30.734 22.231 4.38 

13.94 30.355 28.615 5.547 

13.916 30.538 39.189 7.532 

13.941 29.868 48.02 9.178 

13.936 28.832 103.554 19.511 

13.936 28.915 124.12 23.337 

13.94 29.068 120.384 22.731 

13.95 29.18 94.655 17.901 

13.93 29.52 93.436 17.737 

13.918 29.818 82.72 15.64 

13.921 29.713 69.03 13.118 

13.929 29.427 85.163 16.11 

13.933 29.539 90.179 17.044 

17.716 29.68 82.407 15.654 

13.916 29.829 68.172 12.926 

20.426 3.595 38.49 7.318 

19.702 0.562 0.511 0.196 

18.369 3.234 16.547 3.211 

14.161 27.711 47.424 9.079 

14.011 29.102 67.25 12.775 

14.02 28.89 68.597 13.049 

14.015 28.866 89.59 17.056 

14.004 29.331 67.045 12.763 

14.013 29.034 72.013 13.701 

13.995 29.05 73.849 14.014 

14.016 28.763 81.028 15.383 

13.974 29.211 82.526 15.654 

13.388 31.617 75.508 14.376 

13.365 31.839 84.966 16.125 

13.362 31.966 74.145 14.112 

13.36 31.831 80.413 15.251 
Date Time 

0, 

% 

CO, 

% 

212512013 10:49:00AM 13.543 4.396 

212512013 10:50:00AM 13.547 4.392 

212512013 10:51 :00AM 13.545 4.395 

212512013 10:52:00AM 13.541 4.401 

212512013 10:53:00 AM 13.544 4.401 

212512013 10:54:00AM 13.545 4.401 

212512013 10:55:00AM 13.551 4.4 

212512013 10:56:00AM 13.542 4.405 

212512013 10:57:00AM 13.533 4.41 

212512013 10:58:00 AM 13.518 4.421 

212512013 10:59:00 AM 13.495 4.434 

212512013 11 :00:00 AM 13.499 4.434 

212512013 11:01:00AM 16.274 2.839 

212512013 11:02:00AM 13.545 4.418 

2I251201311 :03:00AM 13.529 4.423 

212512013 11 :04:00 AM 13.533 4.42 

212512013 11 :05:00 AM 13.533 4.42 

212512013 11:06:00 AM 13.525 4.426 

212512013 11:07:00 AM 13.515 4.435 

212512013 11:08:00 AM 13.486 4.45 

212512013 11 :09:00 AM 13.473 4.458 

212512013 11 :10:00 AM 17.351 2.153 

212512013 11 :11:00AM 20.814 0.256 

212512013 11 :12:00 AM 20.808 0.259 

NO, 

PPM 

1.976 

1.949 

1.947 

1.923 

1.926 

1.945 

1.924 

1.944 

1.894 

1.886 

1.79 

1.835 

1.131 

1.906 

1.915 

1.925 

1.931 

1.898 

1.906 

1.779 

1.793 

0.903 

-0.004 

0.002 

CO 

PPM 

3.312 

3.66 

3.69 

3.667 

3.954 

3.592 

3.798 

3.41 

4.026 

4.363 

4.219 

4.042 

2.587 

4.365 

4.423 

4.692 

4.232 

4.171 

4.37 

3.694 

4.009 

2.766 

0.313 

0.231 

212512013 11:13:00AM 20.828 0.25 -0.008 0.215 

212512013 11:14:00AM 20.068 1.004 0.001 0.247 

212512013 11 :15:00 AM 18.88 9.783 -0.004 -0.233 

212512013 11:16:00AMI 18.928 9.818 -0.01 -0.413 

21251201311:17:00AM 6.664 3.122 2.846 -0.266 

212512013 11 :18:00 AM!"I ~0':'16:i:2i-~0;;;';;23;;;5'---:4~5~7~4--:i0'i.0:i22:i--, 

212512013 11 :19:00 AM 0.215 0.226 2.236 1.42 

212512013 11 :20:00 AM 0.186 0.233 0.003 4.441 

212512013 11 :21 :00 AM 4.844 1.713 0.809 5531 

212512013 11 :22:00 AM 0.139 0.224 -0.004 9.452 

212512013 11:23:00 AM 0.133 0.223 -0.003 I 9.631 

212512013 11 :24:00 AM 16.468 8.968 3.268 9.604 

212512013 11:25:00 AM 18.943 9.845 4.6 9.565 

212512013 11 :26:00 AM~I :;18~~95~:::9;~84~8~::~4ri5~9~7:::~9~5;48;::: 212512013 11 :27:00 AM 4.227 3.464 1.535 5.057 

212512013 11 :28:00 AM 0.126 0.202 -0.006 0.028 

0, 

% 

NO, 

PPM 

CO 

PPM 

THC 

PPM 

13.347 31 .67 89.503 17.025 

13.347 31.408 100.174 19.06 

13.347 31.424 107.21 20.315 

13.342 31 .638 98.802 18.778 

13.35 31 .614 112.799 21 .379 

13.348 31.726 99.812 18.967 Start 100% PM 

13.361 31 .664 108.93 20.663 

13.351 31 .855 91.935 17.519 

13.352 31 .262 114.574 21.732 

13.34 31.297 128.513 24.341 

13.34 31.204 127.289 24.074 

13.34 31.519 128.913 24.409 

13.342 31 .199 118.833 22.488 

13.34 31.154 142.679 26.971 

13.342 31 .227 132.363 25.052 

13.341 31 .143 143.16 27.097 

13.342 31 .31 125.134 23.7 

13.34 31.446 120.665 22.881 

13.34 31.36 132.607 25.115 

13.34 31.486 109.476 20.741 

13.321 31.472 129.449 24.481 

13.336 31 .372 120.646 22.814 

13.332 31.604 127.245 24.03 

13.327 32.11 92.484 17.506 

13.334 31 .969 95.852 18.15 

13.33 32.233 85.414 16.213 

13.338 31 .993 84.521 16.098 

13.327 32.065 89.417 17.02 021C02 b;as 

13.336 31.95 91.62 17.354 

13.33 32.134 88.108 16.77 NOx bias 

15.412 21 .677 75.109 14.224 

18.924 0.878 6.979 1.411 

18927 0675 -0417 0.033 

18.928 

8.208 

0.078 

0.231 

0.566 I -0.441 0.039 

21 .427 0.451 0.291 

41 .884 0.147 I 0.303 

25.09 32.062 6.232 

02 bias 

CO bias 

NOx bias 

0.045 0.42 230.888 43.478 Span Oirect 

0.043 0.322 1 240.3891 45.152 CO b;as 

12.956 29.085 237.241 44.666 

212512013 11 :29:00 AM 0.113 0.202 -0.011 -0.032 18.927 42.051 240.469 45.25 Direct Span 

212512013 11 :30:00 AM .... ~0.~1i:'13'-~0;;;.::-20~2~-;.0:'0:::1~3'--:i-O'i.0~2:i-5 ..... 

212512013 11 :31 :00 AM 5.95 2.044 0.751 0.345 

212512013 11:32:00 AM 13.505 4.445 2.172 3.299 

212512013 11:33:00 AM 13.522 4.447 2.231 3.399 

212512013 11 :34:00 AM 13.519 4.452 2.211 3.764 

212512013 11 :35:00 AM 13.519 4.454 2.257 3.892 

212512013 11 :36:00 AM 13.521 4.45 2.215 3.458 

212512013 11 :37:00 AM 13.526 4.447 2.211 3.719 

212512013 11 :38:00 AM 13.528 4.446 2.206 3.499 

212512013 11 :39:00 AM 13.517 4.453 2.188 3.752 

212512013 11:40:00 AM 13.513 4.456 2.198 4.326 

212512013 11 :41 :00 AM 13.525 4.449 2.268 4.375 

212512013 11:42:00 AM 13.535 4.443 2.288 4.314 

212512013 11 :43:00 AM 13.534 4.441 2.343 4.551 

212512013 11 :44:00 AM 13.534 4.438 2.363 4.426 

212512013 11 :45:00 AM 13.536 4.435 2.347 4.328 

212512013 11 :46:00 AM 13.557 4.422 2.41 4.311 

212512013 11 :47:00 AM 13.557 4.42 2.409 4.156 

2I251201311 :48:00AM 13.558 4.42 2.423 4.708 

212512013 11 :49:00 AM 13.555 4.419 2.436 3.834 

212512013 11 :50:00 AM 13.577 4.409 2.47 3.786 

5.653 

0.048 

0.042 

0.041 

7.903 

13.253 

11 .913 140.418 26.425 DirectZero 

0.052 

0.029 

0.01 

16.449 

31.497 

0.513 

-0.036 

-0.037 

20.967 

100.633 

0.189 

0.096 

0.086 Direct Zero 

4.072 

19.07 Start RATA 1/100% Camp 

13.266 31 .872 86.682 16.474 

13.265 31.684 96.799 18.335 

13.265 31 .833 89.33 16.951 

13.258 31.625 94.569 17.898 

13.262 31.367 104.728 19.81 

13.259 31 .536 103.008 19.506 

13.265 31.447 97.844 18.544 

13.262 31.431 106.686 20.196 

13.261 31 .517 103.26 19.57 

13.262 31 .59 100.414 19.008 

13.263 31.714 98.174 18.603 

13.263 31 .634 92.032 17.443 

13.262 31 .373 109.373 20.658 

13.26 32.105 83.721 15.883 

13.265 31.916 81 .262 15.431 
O2 CO2 NOx 

Dale Time % % PPM 

21251201311:51:00AM 14.759 3.722 1.651 

21251201311 :52:00AM 13.505 4.447 1.847 

21251201311:53:00AM 13.504 4.448 1.816 

21251201311 :54:00AM 13.498 4.45 1.829 

212512013 11 :55:00 AM 13.51 4.448 1.824 

21251201311 :56:00AM 13.5 4.454 1.822 

212512013 11 :57:00 AM 13.504 4.451 1.845 

212512013 11 :58:00AM 13.499 4.454 1.813 

21251201311:59:00AM 13.497 4.459 1.835 

212512013 12:00:00 PM 13.515 4.45 1.722 

212512013 12:01:00 PM 13.519 4.449 1.711 

212512013 12:02:00 PM 13.521 4.449 2.345 

212512013 12:03:00 PM 13.519 4.45 1.821 

212512013 12:04:00 PM 13.536 4.438 1.69 

212512013 12:05:00 PM 13.55 4.431 1.584 

212512013 12:06:00 PM 13.548 4.429 1.588 

212512013 12:07:00 PM 13.555 4.421 1.571 

212512013 12:08:00 PM 13.554 4.419 1.569 

212512013 12:09:00 PM 17.841 1.908 0.66 

212512013 12:10:00 PM 13.584 4.426 2.058 

212512013 12:11:00 PM 13.496 4.434 2.047 

212512013 12:1 2:00 PM 13.494 4.432 2.052 

212512013 12:13:00 PM 13.5 4.433 2.049 

212512013 12:14:00 PM 13.501 4.431 2.022 

212512013 12:15:00 PM 13.5 4.432 2.055 

212512013 12:16:00 PM 13.499 4.433 2.046 

212512013 12:17:00 PM 13.493 4.435 2.06 

212512013 12:18:00 PM 13.493 4.436 2.108 

212512013 12:19:00 PM 13.493 4.437 2.034 

212512013 12:20:00 PM 13.488 4.436 2.07 

212512013 12:21:00 PM 13.489 4.437 2.057 

212512013 12:22:00 PM 13.492 4.438 2.032 

212512013 12:23:00 PM 13.495 4.436 2.041 

212512013 12:24:00 PM 13.496 4.436 2.044 

212512013 12:25:00 PM 13.487 4.439 1.978 

212512013 12:26:00 PM 13.484 4.443 1.969 

212512013 12:27:00 PM 16.731 2.485 1.179 

212512013 12:28:00 PM 15.24 3.519 1.599 

212512013 12:29:00 PM 13.496 4.436 2.184 

212512013 12:30:00 PM 13.486 4.44 2.172 

212512013 12:31 :00 PM 13.495 4.435 2.219 

212512013 12:32:00 PM 13.487 4.44 2.159 

212512013 12:33:00 PM 13.492 4.436 2.158 

212512013 12:34:00 PM 13.49 4.436 2.188 

212512013 12:35:00 PM 13.48 4.441 2.161 

212512013 12:36:00 PM 13.483 4.436 2.186 

212512013 12:37:00 PM 13.473 4.44 2.154 

212512013 12:38:00 PM 13.49 4.429 2.268 

212512013 12:39:00 PM 13.503 4.423 2.388 

212512013 12:40:00 PM 13.494 4.431 2.373 

212512013 12:41 :00 PM 13.496 4.43 2.413 

212512013 12:42:00 PM 13.5 4.43 2.439 

CO 

PPM 

2.736 

2.819 

3.058 

3.1 93 

3.398 

2.962 

2.952 

2.825 

3.538 

3.224 

3.005 

3.023 

3.234 

3.086 

3.289 

3.487 

3.139 

3.1 

1.747 

2.961 

3.76 

3.521 

3.397 

3.432 

3.647 

3.845 

3.618 

3.648 

3.831 

3.834 

4.119 

3.966 

3.757 

3.62 

3.653 

3.852 

3.05 

2.451 

3.933 

4.255 

3.802 

4.132 

4.142 

3.684 

3.907 

4.091 

3.927 

4.394 

4.263 

4.108 

3.857 

3.784 

0, NO, CO THC 

% PPM PPM PPM 

13.263 32.257 70.69 13.434 

13.265 32.048 70.128 13.325 

13.263 32.057 76.546 14.508 

13.265 31.926 80.231 15.216 

13.266 31 .745 87.538 16.581 

13.265 32.116 74.96 14.238 

13.265 32.111 75.371 14.306 

13.265 32.1 27 69.49 13.203 

13.265 31 .643 92.754 17.524 

13.265 31.984 88.117 16.679 

13.27 31.965 79.201 15.026 

13.267 31 .858 85.258 16.139 

13.266 31.838 90.274 17.092 

13.273 31 .919 83.509 15.786 

13.274 31.703 87.508 16.588 

13.271 31.497 103.009 18.469 

13.275 31.916 88.61 4 13.575 

13.28 31 .872 89.411 9.86 

13.269 31.887 81.894 8.744 

13.268 31 .849 92.658 0.824 

13.266 31 .835 98.568 0.843 

13.267 31.915 90.359 0.816 

13.266 32.126 88.954 0.811 

13.267 31 .896 85.723 0.8 

13.267 31.825 92.859 0.823 

13.267 31.81 101.432 0.853 

13.266 31 .919 89.662 0.812 

13.266 31.941 91.068 0.817 

13.266 31 .74 94.64 0.832 

13.267 31 .769 97.998 0.84 

13.266 31.514 106.941 0.87 

13.265 31 .841 104.004 0.86 

13.266 31.845 93.293 0.827 

13.266 32.024 88.065 0.808 

13.264 31 .81 91.531 0.819 

13.265 31.744 100.784 0.85 

13.257 31.624 96.224 0.836 

13.253 31.657 106.907 0.87 

13.241 31 .84 94.822 0.83 

13.245 31.606 102.844 0.857 

13.251 32.031 92.529 0.825 

13.242 31 .552 95.518 0.832 

13.246 31.813 99.135 0.846 

13.242 31 .934 82.956 0.796 

13.24 31.689 90.536 0.828 

13.237 31 .769 99.143 0.859 

13.223 31.665 89.675 0.827 

13.22 31.432 103.417 0.877 

13.218 31 .795 98.566 

13.212 31.808 88.389 

13.193 32.043 82.753 

13.202 31 .989 78.578 

212512013 12:43:00 PM 13.505 4.428 2.407 3.757 13.201 32.056 82.572 

0.854 

0.823 

0.804 

0.791 

0.804 

0.755 

0.782 

0.771 

212512013 12:44:00 PM 17.243 2.188 1.233 2.474 13.194 32.18 68.53 

212512013 12:45:00 PM 19.751 1.736 0.009 0.333 13.174 32.085 78.707 

21251201312:46:00PM 18.803 9.82 -0.011 -0.208 13.181 31.973 73.704 

212512013 12:47:00 PM~I :1~848~2~5:::9~~84~9~::~-~0~0;1::: -0.465 13.171 31 .631 85.044 

212512013 12:48:00 PM 6.743 3.374 2.811 -0.318 13.173 31 .657 88.164 

212512013 12:49:00 PM rl....;;0."1'"55:--0;;;."25"'1;..........:4;;;.5;;6,;2-....;-0".0;.;1.;;2..., 13.136 31 .792 94.035 

212512013 12:50:00 PM 0.138 0.242 4.577 0.025 0.817 5.015 40.25 

212512013 12:51 :00 PM 0.142 0.239 1.755 7.492 0.063 0.86 0.975 

212512013 12:52:00 PM 0.128 0.237 -0.007 10.381 0.044 0.712 0.065 

0 .807 Q2IC02 bias 

2.266 

6.888 NOx bias 

1.271 

0.539 

0.534 
Date Time 

0, 

% 

CO, 

% 

NO. CO 

PPM PPM 

212512013 12:53:00 PM 0.112 0.235 -0.009 9.603 

212512013 12:54:00 PM 0.112 0.236 -0.009 9.592 

212512013 12:55:00 PM 12.513 7.593 3.237 9.561 

212512013 12:56:00 PM 18.874 9.859 4.614 9.544 

212512013 12:57:00 PM 18.887 9.863 4.603 9.544 

212512013 12:58:00 PMI"1-;8"i.8'i:92,--';;9.'o86:;'--'4-;.5:l;98i--'i:9.;:554"" 

21251201312:59:00PM 3.383 1.753 1.304 4.391 

212512013 1:00:00 PM 0.125 0.206 -0.Q16 0.004 

212512013 1 :01 :00 PM 1~0~1i':1'i-4-~0.'::20~3:----i-0~.0~1~5--'-0;:':::02~5"" 

212512013 1:02:00 PM 4.979 1.132 0.251 0.132 

212512013 1:03:00 PM 13.424 4.459 

212512013 1:04:00 PM 13.427 4.462 

212512013 1:05:00 PM 13.424 4.465 

212512013 1:06:00 PM 13.422 4.466 

212512013 1:07:00 PM 13.425 4.462 

212512013 1 :08:00 PM 13.422 4.466 

212512013 1 :09:00 PM 13.422 4.465 

212512013 1 :10:00 PM 13.426 4.462 

212512013 1 :11 :00 PM 13.432 4.456 

212512013 1:12:00 PM 13.434 4.455 

212512013 1:13:00 PM 13.435 4.456 

212512013 1:14:00 PM 13.437 4.453 

212512013 1:15:00 PM 13.451 4.448 

212512013 1:16:00 PM 13.462 4.445 

212512013 1:17:00 PM 13.455 4.448 

212512013 1:18:00PM 13.466 4.446 

212512013 1:19:00 PM 13.458 4.45 

212512013 1 :20:00 PM 13.465 4.448 

212512013 1:21 :00 PM 17.086 2.34 

212512013 1:22:00 PM 13.431 4.48 

212512013 1:23:00 PM 13.396 4.49 

212512013 1:24:00 PM 13.394 4.492 

212512013 1:25:00 PM 13.396 4.487 

212512013 1:26:00 PM 13.405 4.483 

212512013 1:27:00 PM 13.395 4.488 

212512013 1:28:00 PM 13.394 4.49 

212512013 1:29:00 PM 13.393 4.493 

212512013 1:30:00 PM 13.395 4.489 

212512013 1 :31 :00 PM 13.396 4.487 

212512013 1:32:00 PM 13.396 4.486 

212512013 1:33:00 PM 13.391 4.493 

212512013 1:34:00 PM 13.382 4.497 

212512013 1 :35:00 PM 13.38 4.498 

212512013 1:36:00 PM 13.385 4.494 

212512013 1 :37:00 PM 13.375 4.499 

212512013 1 :38:00 PM 13.358 4.509 

212512013 1:39:00 PM 13.358 4.511 

212512013 1 :40:00 PM 13.362 4.508 

212512013 1:41 :00 PM 13.36 4.509 

212512013 1:42:00 PM 13.359 4.511 

212512013 1:43:00 PM 17.153 2.27 

212512013 1:44:00 PM 13.503 4.46 

212512013 1:45:00 PM 13.431 4.467 

212512013 1:46:00 PM 13.421 4.476 

212512013 1:47:00 PM 13.421 4.472 

212512013 1:48:00 PM 13.421 4.472 

212512013 1:49:00 PM 13.42 4.472 

212512013 1 :50:00 PM 13.422 4.466 

212512013 1:51 :00 PM 13.428 4.461 

212512013 1:52:00 PM 13.421 4.463 

212512013 1 :53:00 PM 13.421 4.46 

1.822 

1.783 

1.784 

1.764 

1.802 

1.762 

1.767 

1.689 

1.698 

1.716 

1.706 

1.689 

1.6 

1.622 

1.625 

1.609 

1.616 

1.606 

0.838 

1.963 

1.948 

1.982 

1.995 

1.994 

1.977 

1.952 

1.98 

1.975 

1.979 

1.965 

2.661 

2.417 

1.992 

1.991 

1.902 

1.79 

2.103 

1.87 

1.815 

2.029 

0.969 

2.072 

2.054 

2.023 

2.019 

2.048 

2.019 

2.023 

2.018 

1.995 

1.999 

3.105 

3.065 

3.191 

3.218 

3.208 

2.924 

3.104 

3.255 

2.758 

2.712 

2.727 

2.598 

2.915 

2.774 

2.744 

2.698 

2.725 

2.646 

1.659 

2.762 

3.099 

3.125 

2.657 

2.898 

2.55 

3.265 

3.398 

3.114 

3.181 

3.002 

3.304 

3.145 

2.975 

2.865 

2.803 

3.347 

2.998 

2.992 

2.747 

2.921 

2.231 

2.565 

3.293 

3.191 

3.364 

3.653 

3.632 

3.342 

3.287 

3.592 

3.381 

0, 

% 

0.044 

0.044 

0.541 

0.044 

0.044 

0.044 

0.043 

0.38 

0.045 

0.343 

0.041 

0.041 

0.358 

0.041 

0.041 

0.041 

0.041 

0.041 

0.041 

0.083 

0.223 

0.043 

NO. 

PPM 

0.613 

0.519 

1.925 

0.41 

0.354 

0.307 

0.247 

1.311 

0.229 

1.096 

0.177 

0.15 

1.126 

0.14 

0.128 

0.121 

0.098 

0.081 

0.087 

0.098 

0.721 

0.049 

CO 

PPM 

0.039 

0.015 

THC 

PPM 

0.529 

0.527 CO bias 

3.009 18.213 

0.42 86.098 

-0.008 87.051 

0.016 87.026 Direct Span 

-0.038 85.408 

1.083 83.936 

1.563 53.977 Direct Zero 

2.184 49.766 

1.4 27.749 

-0.027 26.016 Start RATA 2/100% Comp 

3.352 17.51 1 

-0.006 0.528 

-0.036 0.528 ITHC Cal Zero 

-0.032 0.528 

-0.036 0.529 

-0.038 0.529 

-0.033 0.531 

-0.032 0.529 

1.442 37.617 

-0.041 85.33 

0.043 -0.003 -0.035 85.861 Inlet Direct Zero 

16.004 29.813 92.87 86.426 

18.877 41.043 239.859 87.097 

18.891 41 .966 240.032 87.325 THCCa l Hi9h 

18.898 42 240.53 86.955 Inlet Oirect Span 

11 .638 

0.068 

0.318 

0.042 

0.041 

8.419 

18.747 

18.753 

18.773 

5.823 

0.063 

0.169 

0.041 

0.041 

28.746 

0.206 

0.943 

0.107 

0.086 

0.152 

0.096 

0.086 

0.081 

25.699 

41 .398 

207.607 56.707 

11.601 I 50.144 ITHCMid 

1.444 51 .343 

1.219 29.407 

-0.034 27.006 ITHC Low 

5.893 25.966 

2.061 2.591 

-0.442 

-0.448 

1.872 

0.167 

0.528 

0.528 02 bias 

1.459 

31 .097 13.517 

0.532 NOx bias 

0.574 

0.214 218.056 1.519 

0.1 13 1 239.681 I 1.318 CO bias 

6.715 13.989 208.82 1.535 

13.158 31.476 86.641 11.425 

13.166 31.871 78.138 10.889 

13.167 31 .696 78.288 11 .152 

13.166 31 .514 102.921 16.472 

13.167 31.759 91 .063 14.348 

13.177 31.844 92.159 13.703 

13.174 32.053 84.414 13.84 

13.169 31 .899 86.564 11.392 Start 100% Inlet 1 

13.222 31 .672 112.699 20. 174 

13.228 32.141 90.605 13.901 

13.238 31 .935 91 .776 13.546 

13.222 32.089 89.572 13.523 

13.228 31 .931 93.747 13.572 

13.226 31.766 107.986 17.991 

13.225 31.774 104.488 16.79 

13.229 32.276 96.743 17.478 

13.236 31 .849 92.459 13.093 

13.234 31 .872 107.244 17.981 

13.235 32.105 96.412 15.117 
Date Time 

0, 

% 

CO2 NO. 

% PPM 

2125/2013 1 :54:00 PM 13.421 4.456 1.992 

2/25/2013 1 :55:00 PM 13.42 4.459 2.67 

2125/2013 1 :56:00 PM 13.423 4.45 2.372 

2125/2013 1 :57:00 PM 13.422 4.452 2.873 

212512013 1:58:00PM 13.418 4.453 2.316 

2125/2013 1 :59:00 PM 13.421 4.449 1.986 

2125/2013 2:00:00 PM 15.447 3.138 1.423 

2125/2013 2:01 :00 PM 16.032 3.062 1.345 

212512013 2:02:00 PM 13.432 4.433 2.109 

2125/2013 2:03:00 PM 13.433 4.427 2.093 

2125/2013 2:04:00 PM 13.434 4.427 2.072 

2125/2013 2:05:00 PM 13.433 4.427 2.085 

2125/2013 2:06:00 PM 13.432 4.425 2.074 

212512013 2:07:00 PM 13.435 4.423 2.165 

2125/2013 2:08:00 PM 13.441 4.419 2.238 

2125/2013 2:09:00 PM 13.433 4.425 2.198 

212512013 2:10:00 PM 13.432 4.429 2.225 

212512013 2:11 :00 PM 13.435 4.429 2.214 

2/2512013 2:12:00 PM 13.468 4.413 2.353 

2125/2013 2:13:00 PM 13.47 4.411 2.347 

2125/2013 2:1 4:00 PM 13.471 4.412 2.338 

212512013 2:15:00 PM 13.471 4.413 2.361 

2125/2013 2:16:00 PM 13.47 4.414 2.336 

2/25/2013 2:17:00 PM 13.47 4.418 2.376 

2125/2013 2:18:00 PM 15.683 5.365 1.351 

2125/2013 2:19:00 PM rl-':':18~7;';9~~9';'8~0~1-~-0;'-0;;;1;-:'-' 

2125/2013 2:20:00 PM 12.656 4.557 1.492 

2125/2013 2:21 :00 PM 5.787 0.24 3.259 

2/25/2013 2:22:00 PM 2.348 0.222 4.037 

CO 

PPM 

3.745 

4.011 

3.796 

3.914 

4.1 34 

4.062 

3.484 

2.111 

4.121 

4.272 

4.719 

4.709 

4.61 

4.711 

4.564 

4.859 

4.884 

5.171 

5.061 

4.97 

5.223 

4.712 

4.665 

4.994 

0, 

% 

NO, 

PPM 

CO 

PPM 

THC 

PPM 

13.237 31 .613 112.715 18.696 

13.235 31.718 126.421 24.097 

13.24 31.614 117.941 20.576 

13.235 31 .657 120.94 21.366 

13.235 31 .543 132.363 25.266 

13.236 31.606 128.853 23.348 

13.237 31.717 126.057 22.628 

13.244 31.641 122.806 21.886 

13.237 31 .894 121 .067 21.509 

13.239 31.601 121.429 20.913 

13.244 31.434 140.325 27.342 

13.241 31.481 139.348 26.949 

13.242 31.484 137.057 27.342 

13.238 31 .511 134.614 25.957 

13.238 31 .661 126.546 23.533 

13.241 31.408 138.64 26.066 

13.236 31 .46 139.746 27.438 

13.233 31 .316 147.359 29.057 

13.239 31.595 139.357 26.33 

13.24 31.46 135.808 25.478 

13.238 31.432 143.631 27.138 

13.24 31 .85 127.992 24.822 

13.239 31.539 124.184 21.194 

13.234 31 .647 134.887 25.781 

3.552 13.237 31 .645 128.197 24.006 

-0.323 13.232 31.723 129.313 23.821 02lC02 b;as 

-0.345 13.243 31.688 122.395 21 .376 

0.011 13.243 31 .864 118.4 21.828 

0.029 13.244 31 .764 113.616 20.204 

2125/2013 2:23:00 PM 0.164 0.215 4.546 0.01 

212512013 2:24:00 PM rl ~0-i-'3:::6;-~0';'.2;;,,:-i3;-~4~5;':4~7--;i0::;0::-'60"1 13.24 31.522 130.806 23.799 

13.242 31 .711 130.366 26.408 NOx bias 

2/25/2013 2:25:00 PM 0.123 0.214 2.206 6.397 13.242 31.543 125.878 22.221 

2125/2013 2:26:00 PM 0.818 0.216 

2/25/2013 2:27:00 PM 3.711 0.221 

2125/2013 2:28:00 PM 3.362 0.474 

2/25/2013 2:29:00 PM 0.689 0.367 

2/25/2013 2:30:00 PM 0.234 0.25 

2125/2013 2:31 :00 PM 7.414 5.173 

2125/2013 2:32:00 PM 18.86 9.837 

2/2512013 2:33:00 PM 18.888 9.838 

2/25/2013 2:34:00 PM 10.877 5.981 

2125/2013 2:35:00 PM 0.138 0.195 

212512013 2:36:00 PM 0.112 0.193 

2125/2013 2:37:00 PM 10.461 3.598 

2125/2013 2:38:00 PM 13.428 4.459 

2/25/2013 2:39:00 PM 13.428 4.465 

212512013 2:40:00 PM 13.434 4.465 

2125/2013 2:41 :00 PM 13.433 4.465 

2/25/2013 2:42:00 PM 13.433 4.467 

2/25/2013 2:43:00 PM 13.434 4.462 

2125/2013 2:44:00 PM 13.435 4.462 

212512013 2:45:00 PM 13.464 4.453 

2125/2013 2:46:00 PM 13.469 4.455 

2/25/2013 2:47:00 PM 13.471 4.455 

2125/2013 2:48:00 PM 17.83 1.908 

212512013 2:49:00 PM 13.485 4.482 

212512013 2:50:00 PM 13.423 4.49 

2/25/2013 2:51 :00 PM 13.423 4.493 

2125/2013 2:52:00 PM 13.423 4.495 

2125/2013 2:53:00 PM 13.428 4.492 

2125/2013 2:54:00 PM 13.426 4.495 

2125/2013 2:55:00 PM 13.421 4.499 

-0.011 10.779 13.244 31.449 138.596 26.812 

-0.015 10.367 13.245 31 .799 125.339 23.201 

0.14 8.114 13.25 31.875 115.261 20.669 

0.162 9.012 13.24 31.988 106.056 18.479 

0.004 9.514 13.244 31 .77 113.355 19.028 CO b;as 

2.265 9.514 13.244 31.766 119.043 21.83 

4.574 9.56 13.241 31 .558 126.106 22.8 

4.572 9.568 13.251 31.54 137.317 26.493 

3.306 8.581 13.239 31.967 111 .624 20.321 

-0.005 0.586 13.238 31 .776 118.53 20.881 

-0.013 -0.03 13.237 31.785 113.923 16.96 

1.136 1.521 13.237 31 .822 116.196 19.806 

1.688 3.975 13.232 31.615 130.787 24.786 Start RATA 3 

1.681 4.045 13.227 31.672 131 .945 25.055 

1.721 3.301 13.233 32.057 101.912 16.239 

1.734 3.759 13.234 31 .825 119.184 22.129 

1.672 3.756 13.233 31 .844 120.751 22.033 

1.658 

1.638 

1.532 

1.541 

1.513 

0.614 

2.737 

2.049 

1.927 

1.926 

1.919 

2.227 

3.001 

3.388 

3.674 

3.319 

3.343 

3.489 

1.835 

3.322 

3.911 

4.086 

4.143 

4.394 

4.249 

4.511 

12.992 31.662 

18.534 2.632 

18.83 0.833 

8.762 19.993 

0.073 41.921 

0.046 41.915 

109.21 

46.758 

-0.36 

1.698 

0.495 

0.046 

16.582 77.182 

19.124 

8.815 

0.528 0 2 bias 

2.214 

0.561 

0.53 NOx bias 

0.176 1.303 

0.042 

0.042 

0.575 

0.132 

0.041 

0.042 

0.487 238.531 1.315 

0.386 I 239.954 I 1.317 CO b;as 

1.296 240.035 1.319 

0.956 72.033 28.041 

0.081 0.075 48.247 THC M;d 

0.062 -0.037 47.673 Direct Zero 
Date Time 

0, 

% 

co, 

% 

NO~ CO 

PPM PPM 

2125/2013 2:56:00 PM 13.421 4.496 2.1 54 4.1 79 

2125/2013 2:57:00 PM 13.405 4.51 1.636 4.231 

2125/2013 2:56:00 PM 13.396 4.516 1.734 4.656 

2125/2013 2:59:00 PM 13.396 4.519 1.763 4.721 

2125/2013 3:00:00 PM 14.766 3.662 1.457 4.362 

2125/2013 3:01 :00 PM 15.54 3.324 1.342 2.661 

2125/2013 3:02:00 PM 13.442 4.462 1.961 4.279 

2125/2013 3:03:00 PM 13.44 4.462 1.959 4.392 

2125/2013 3:04:00 PM 13.443 4.46 2.97 4.529 

2/25/2013 3:05:00 PM 13.436 4.463 2.116 4.274 

2/25/2013 3:06:00 PM 13.446 4.475 2.095 4.461 

2/25/2013 3:07:00 PM 13.437 4.477 4.432 4.1 43 

2/25/2013 3:06:00 PM 13.436 4.476 2.141 4.131 

2125/2013 3:09:00 PM 13.433 4.476 1.932 4.417 

2125/2013 3:10:00 PM 13.432 4.46 1.653 4.364 

2125/2013 3:11 :00 PM 13.435 4.474 1.902 4.445 

2125/2013 3:12:00 PM 14.241 3.969 2.046 4.03 

2125/2013 3:13:00 PM 15.651 3.113 1.639 2.645 

2125/2013 3:14:00 PM 13.439 4.465 1.925 4.494 

212512013 3:15:00 PM 13.441 4.461 1.67 4.496 

212512013 3:16:00 PM 13.435 4.463 2.541 4.631 

2125/2013 3:17:00 PM 13.435 4.464 1.624 4.44 

2125/2013 3:16:00 PM 13.434 4.462 1.699 4.559 

2125/2013 3:19:00 PM 13.434 4.464 2.56 4.577 

2125/2013 3:20:00 PM 13.435 4.456 1.747 4.747 

2/25/2013 3:21:00 PM 13.44 4.454 1.576 4.291 

2/25/2013 3:22:00 PM 13.445 4.45 1.556 4.06 

2/25/2013 3:23:00 PM 13.462 4.441 1.512 4.099 

2/25/2013 3:24:00 PM 15.267 6.526 1.456 3.247 

2/25/2013 3:25:00 PM 1...;1.;;6;;;.60;5,--....;;9 .. . .;;6~16:---.:-0,:.:0;,:;1:;,2..., -0.305 

2/25/2013 3:26:00 PM 6.136 4.026 2.515 -0.341 

2/25/2013 3:27:00 PM 1"1 ~0;;.;;15"'5--;;0.':;23~3;---;4:'i5"'6~6--i:-0:';0:;"3.., 

2/25/2013 3:26:00 PM 0.195 0.237 2.743 2.066 

2/2512013 3:29:00 PM 0.137 0.214 -0.015 9.312 

2125/2013 3:30:00 PM 0.112 0.21 -0.017 9.562 

212512013 3:31 :00 PM 16.062 6.49 3.169 9.551 

2125/2013 3:32:00 PM '"1""1"6';'; .6"9;;'3 -""9:;..6;::2;,1-.....;4C:6~0"3-..... 9;;.5.;;39;,-, 

2125/2013 3:33:00 PM 3.677 2.076 1.492 5.355 

2125/2013 3:34:00 PM 0.12 0.177 -0.Q16 0.051 

2125/2013 3:35:00 PM 1"1 ~0':'11:"2;--""0;;.1:'7;-;4--""-0';-0;;;2;';1--i-O;-;0;';3':'1" 

2125/2013 3:36:00 PM 9.763 3.395 1.271 1.211 

2125/2013 3:37:00 PM 13.431 4.432 2.07 3.341 

2125/2013 3:36:00 PM 13.433 4.43 2.09 3.266 

2/25/2013 3:39:00 PM 13.441 4.426 2.102 3.343 

2/25/2013 3:40:00 PM 13.436 4.426 2.067 3.107 

2/25/2013 3:41 :00 PM 13.451 4.423 2.145 3.666 

2/25/2013 3:42:00 PM 13.459 4.421 2.192 3.42 

2125/2013 3:43:00 PM 13.466 4.42 2.195 3.626 

2125/2013 3:44:00 PM 13.466 4.419 3.109 3.704 

2125/2013 3:45:00 PM 13.47 4.417 2.547 3.356 

2125/2013 3:46:00 PM 13.47 4.416 2.247 3.713 

2125/2013 3:47:00 PM 15.536 3.209 1.493 2.606 

2125/2013 3:46:00 PM 13.464 4.421 1.676 3.107 

2125/2013 3:49:00 PM 13.435 4.429 1.659 3.614 

212512013 3:50:00 PM 13.442 4.425 1.66 3.441 

2125/2013 3:51 :00 PM 13.444 4.423 1.664 3.44 

2125/2013 3:52:00 PM 13.444 4.422 1.65 3.56 

2125/2013 3:53:00 PM 13.475 4.406 1.626 4.066 

2/25/2013 3:54:00 PM 13.463 4.4 1.565 4.275 

2/25/2013 3:55:00 PM 13.474 4.406 1.577 2.375 

2/25/2013 3:56:00 PM 13.507 4.39 1.477 2.95 

2/25/2013 3:57:00 PM 13.496 4.394 1.46 2.755 

0 , 

% 

1.661 

16.794 

16.927 

14.69 

13.243 

13.242 

13.241 

13.24 

13.239 

13.234 

13.241 

13.233 

13.227 

13.226 

13.23 

13.226 

13.216 

13.22 

13.216 

13.222 

13.215 

13.212 

13.216 

13.216 

13.215 

13.212 

13.206 

13.21 

13.202 

13.195 

13.165 

13.173 

13.176 

NO, 

PPM 

0.721 

40.203 

41 .914 

33.669 

30.992 

31.063 

31.411 

31.263 

31.309 

31.494 

31 .303 

31.66 

31.594 

31.4 

31.409 

31.501 

31.604 

31.374 

31.536 

31.444 

31.543 

31 .525 

31.423 

31 .353 

31 .304 

31 .347 

31.501 

31.337 

31.606 

31.962 

34.731 

32.966 

31.612 

CO 

PPM 

-0.032 

152.557 

240.233 1 

190.336 

152.296 

154.953 

141 .814 

142.71 

150.353 

139.452 

149.106 

136.5 

129.611 

146.741 

144.505 

146.392 

135.411 

146.02 

145.192 

140.221 

147.156 

136.034 

145.627 

145.914 

155.929 

152.761 

146.302 

152.578 

145.642 

146.942 

41.922 

47.656 

131 .97 

THe 

PPM 

26.461 

26.61 

31 .247 Direct Span 

33.939 

31.926 Start 100% Inlet 2 

32.997 

26.472 

26.462 

31.979 

27.902 

31.075 

26.445 

24.556 

30.267 

29.333 

26.233 

23.261 

29.502 

29.231 

27.95 

30.936 

25.632 

29.429 

26.637 

31.943 

31.215 

29.7 

31 .719 

24.672 

26.579 02/C02 bias 

6.679 

3.458 NOx bias 

26.701 

13.194 31.934 126.467 23.59 

13.1 65 32.566 109.94 19.341 CO b;as 

13.1 93 32.696 61.707 11.056 

13.183 32.636 89.456 13.593 Direct Span 

13.179 32.756 65.436 11.342 

13.192 32.632 79.34 10.965 

13.189 32.61 86.583 13.195 Direct Zero 

13.166 32.554 93.269 14.232 

13.193 32.533 95.099 14.604 Start RATA 4 

13.201 32.66 66.219 12.336 

13.166 32.751 92.759 14.693 

13.165 32.794 79.165 10.471 

13.196 32.419 99.646 15.543 

13.197 32.743 88.045 13.575 Start 75% PM, RATA 5, Comp 1 

13.213 32.411 101.974 15.512 

13.206 32.619 99.24 14.746 

13.21 32.695 64.162 10.611 

13.212 32.55 99.165 16.133 

13.212 32.693 62.359 10.939 

13.214 32.179 97.412 14.726 

13.216 32.042 121.713 21 .541 

13.216 32.364 105.935 16.543 

13.227 32.261 100.473 15.694 

13.226 32.166 110.443 17.276 

13.256 31.396 123.512 21.611 

13.252 31.724 140.126 26.461 

13.236 33.041 69.632 6.339 

13.242 32.537 63.594 12.049 

13.244 32.74 76.926 10 
Dale Time 

0, 

% 

21251201 3 3:56:00 PM 17.615 

2/25/2013 3:59:00 PM 13.494 

2/25/2013 4:00:00 PM 13.435 

2125/2013 4:01 :00 PM 13.433 

2125/2013 4:02:00 PM 13.432 

212512013 4:03:00 PM 13.433 

212512013 4:04:00 PM 13.433 

2/2512013 4:05:00 PM 13.422 

2/25/2013 4:06:00 PM 13.421 

2/25/2013 4:07:00 PM 

2/25/2013 4:08:00 PM 

2/25/2013 4:09:00 PM 

2125/2013 4:10:00 PM 

2125/2013 4:11 :00 PM 

212512013 4:12:00 PM 

2125/2013 4:13:00 PM 

2125/2013 4:14:00 PM 

13.422 

13.426 

16.646 

13.49 

13.479 

13.473 

13.474 

13.479 

CO, 

% 

NO, 

PPM 

1.994 0.622 

4.432 1.776 

4.433 1.664 

4.434 1.666 

4.431 1.652 

4.436 1.65 

4.435 1.664 

4.446 1.716 

4.446 1.725 

4.446 1.731 

4.443 1.733 

2.47 0.965 

4.402 1.96 

4.405 1.913 

4.407 1.935 

4.405 1.964 

4.402 1.699 

2125/2013 4:15:00 PM 13.476 4.4 1.916 

2/25/2013 4:16:00 PM 13.463 4.396 1.937 

2125/2013 4:17:00 PM 13.46 4.396 1.922 

2125/2013 4:16:00 PM 13.461 4.392 1.956 

2125/2013 4:19:00 PM 13.46 4.392 1.935 

2125/2013 4:20:00 PM 16.479 7.676 0.647 

CO 

PPM 

1.633 

3.169 

4.973 

5.022 

4.851 

4.885 

4.988 

4.567 

4.847 

4.67 

4.642 

2.882 

4.457 

4.906 

4.726 

4.652 

4.76 

4.523 

4.722 

4.671 

4.857 

4.978 

2.552 

0, 

% 

NO, 

PPM 

CO 

PPM 

THC 

PPM 

13.24 32.576 84.913 11.247 

13.242 32.016 108.937 17.493 

13.246 31.491 142.727 28.227 

13.262 31.475 144.997 26.246 

17.394 7.551 79.462 14.296 

18.889 0.912 0.103 0.528 

18.903 0.736 

6.779 19.844 

0.075 41.72 

0.145 17.042 

0.041 0.494 

0.041 0.39 

13.474 31.362 

18.941 41 .937 

11.127 24.054 

-0.445 

2.195 

0.625 

74.471 

236.539 

1 240.369 1 

234.596 

241.2651 

199.003 

0.528 02 bias 

1.786 

0.532 NOx bias 

1.152 

1.312 

1.32 CO bias 

5.536 

32.959 Direct Span 

28.746 

0.058 0.095 6.519 29.152 

L..,;:;0.;:;04-::1;,-......,;0:;..0;,4:;.9,........,,; -0;;;.0~3;;4,.-11 25.467 Direct Zero 

11 .109 23.721 61.544 27.428 

13.265 31 .305 147.557 30.256 

13.265 31.315 153.389 30.671 

13.266 31.482 154.394 31.781 

13.27 31.443 157.731 32.664 

13.266 31 .351 162.9 34.524 

2125/2013 4:21:00 PM 16.661 9.736 -0.01 -0.413 13.265 31.26 167.495 34.494 

212512013 22:00PMrl""1ii6'i.6:i:6':"4-""9~.7~4i'i3""'-_~0'i:0-i-1-' -0.463 13.577 31 .156 112.905 23.056 021C02bias 

2/25/2013 4:23:00 PM 6.562 4.207 2.402 -0.341 13.75 29.955 32.261 1.536 

2/25/2013 4:24:00 PM rl ~0-:-16;;6;--""0':'.1~7;;'6,....--i4;;'.5;';5~6---i-O:':.0;';2i6-' 13.742 29.946 32.13 1.452 NOx bias 

2/25/2013 4:25:00 PM 0.139 0.163 1.5 4.429 

2/25/2013 4:26:00 PM 0.137 0.156 -0.013 9.467 

2/25/2013 4:27:00 PM 0.137 0.151 -0.02 9.569 

2125/2013 4:26:00 PM 12.636 7.779 3.546 9.57 

2125/2013 4:29:00 PM rl""1ii8'i9;';3~9-""9;-.7;:3;:i2""'--i4"5"'96:;;--n9';:5'<55;:--' 

2125/2013 4:30:00PM 7.438 2.816 1.511 4.793 

2125/2013 4: 31 :00 PM rl"'"'o .~12:;';9;---i0~. ;,11i'i7,....-...,_0:i'. 0i::1;";7"-°0';. 0;:;25~ 

2125/2013 4:32:00 PM 8.595 2.577 0.675 0.133 

2/25/2013 4:33:00 PM 13.944 4.08 1.332 0.609 

2/25/2013 4:34:00 PM 13.942 4.083 1.361 0.677 

2125/2013 4:35:00 PM 13.943 4.081 1.384 0.676 

2/25/2013 4:36:00 PM 13.938 4.085 1.416 0.65 

212512013 4:37:00 PM 13.939 4.081 1.422 0.67 

2125/2013 4:38:00 PM 13.935 4.083 1.463 0.671 

2125/2013 4:39:00 PM 13.94 4.079 1.46 0.668 

2125/2013 4:40:00 PM 13.929 4.066 1.429 0.674 

2/25/2013 4:41 :00 PM 13.938 4.063 1.44 0.685 

2125/2013 4:42:00 PM 13.938 4.082 1.468 0.692 

2/25/2013 4:43:00 PM 13.941 4.076 1.432 0.725 

2/25/2013 4:44:00 PM 13.948 4.077 1.432 0.702 

2125/2013 4:45:00 PM 13.949 4.078 1.479 0.694 

2125/2013 4:46:00 PM 13.952 4.079 1.467 0.664 

212512013 4:47:00 PM 13.944 4.082 1.531 0.682 

2125/2013 4:48:00 PM 13.942 4.086 1.531 0.653 

2125/2013 4:49:00 PM 13.932 4.091 1.54 0.668 

2/25/2013 4:50:00 PM 13.931 4.092 1.573 0.671 

2/25/2013 4:51:00 PM 13.929 4.09 1.607 0.684 

2/25/2013 4:52:00 PM 13.936 4.082 1.601 0.687 

2/25/2013 4:53:00 PM 13.927 4.085 1.549 0.688 

2125/2013 4:54:00 PM 13.915 4.09 1.557 0.661 

212512013 4:55:00 PM 13.933 4.078 1.572 0.653 

212512013 4:56:00 PM 13.933 4.077 1.564 0.678 

2/25/2013 4:57:00 PM 13.939 4.075 1.626 0.703 

2/25/2013 4:58:00 PM 17.013 2.302 0.644 0.46 

13.721 30.091 31.665 

13.712 30.151 30.625 

13.705 30.055 31.695 

13.69 30.132 31 .495 

13.724 29.666 32.064 

13.724 29.84 32.684 

13.726 29.663 32.733 

13.726 29.669 33.111 

13.717 29.69 32.653 

13.705 29.626 32.911 

13.703 29.602 32.967 

13.695 29.652 32.379 

13.702 29.732 33.033 

13.696 29.794 32.606 

13.696 29.775 32.984 

13.693 29.795 32.681 

13.706 29.721 32.961 

13.696 29.751 33.007 

13.696 29.606 33.589 

13.697 29.536 33.969 

13.69 29.671 33.647 

13.697 29.749 32.81 

13.705 29.637 33.262 

13.697 29.909 33.032 

13.666 30.003 32.166 

13.69 29.939 32.352 

13.692 29.604 32.503 

13.694 29.695 32.783 

13.696 29.667 33.011 

13.686 29.76 32.712 

13.689 29.67 33.243 

13.69 29.634 33.213 

13.686 29.656 33.519 

13.669 29.774 33.121 

1.32 

1.224 

1.288 CO bias 

1.263 

1.187 Direct Span 

1.27 

1 .299 Direct Zero 

1.305 

1.31 

1.323 

1.274 

1.236 

1.236 

1.242 

1.26 

1.256 

1.269 

1.3 

1.334 

1.127 

1.276 

1.2 

1.276 

1.285 

1.245 

1.226 

1.259 

1.305 

1.286 

1.034 

1.249 

1.3 

1.31 

1.291 
Date Time 

0, 

% 

CO, 

% 

2125/2013 4:59:00 PM 13.976 4.066 

2125/2013 5:00:00 PM 13.943 4.075 

2/25/2013 5:01 :00 PM 13.936 4.082 

2125/2013 5:02:00 PM 13.938 4.082 

2125/2013 5:03:00 PM 13.922 4.091 

212512013 5:04:00 PM 13.95 4.075 

212512013 5:05:00 PM 13.936 4.084 

2125/2013 5:06:00 PM 13.917 4.095 

2/25/2013 5:07:00 PM 13.914 4.094 

2/25/2013 5:08:00 PM 13.951 4.073 

2/25/2013 5:09:00 PM 13.942 4.076 

2/25/2013 5:10:00 PM 13.926 4.082 

2125/2013 5:11 :00 PM 13.937 4.076 

212512013 5:12:00 PM 13.896 4.098 

2125/2013 5:13:00 PM 13.899 4.094 

2125/2013 5:14:00 PM 13.91 4.089 

2125/2013 5:15:00 PM 16.423 2.639 

2125/2013 5:16:00 PM 13.995 4 .043 

2125/2013 5:17:00 PM 13.984 4.044 

2125/2013 5:18:00 PM 13.969 4.052 

2125/2013 5:19:00 PM 13.962 4.053 

2125/2013 5:20:00 PM 13.958 4.051 

2125/2013 5:21 :00 PM 13.948 4.053 

2125/2013 5:22:00 PM 13.942 4.054 

2125/2013 5:23:00 PM 13.936 4.058 

2125/2013 5:24:00 PM 13.93 4.059 

2/25/2013 5:25:00 PM 13.922 4.061 

2/25/2013 5:26:00 PM 13.917 4.064 

2125/2013 5:27:00 PM 13.927 4.06 

2125/2013 5:28:00 PM 13.919 4.064 

2/25/2013 5:29:00 PM 13.935 4.051 

212512013 5:30:00 PM 13.962 4.036 

2125/2013 5:31 :00 PM 13.946 4.04 

2125/2013 5:32:00 PM 16.574 2.528 

2125/2013 5:33:00 PM 13.933 4.051 

2125/2013 5:34:00 PM 13.92 4.052 

2/25/2013 5:35:00 PM 13.926 4.047 

2/25/2013 5:36:00 PM 13.915 4.055 

2125/2013 5:37:00 PM 13.918 4.052 

2125/2013 5:38:00 PM 13.912 4.057 

212512013 5:39:00 PM 13.931 4.046 

212512013 5:40:00 PM 13.913 4.057 

2/2512013 5:41 :00 PM 13.912 4.055 

2125/2013 5:42:00 PM 13.917 4.048 

2125/2013 5:43:00 PM 13.907 4.052 

2/25/2013 5:44:00 PM 13.903 4.051 

2125/2013 5:45:00 PM 13.894 4.055 

2125/2013 5:46:00 PM 13.902 4.049 

2125/2013 5:47:00 PM 13.904 4.048 

2125/2013 5:48:00 PM 13.915 4.041 

NO. CO 

PPM PPM 

1.517 0.631 

1.503 0.696 

1.441 1.218 

1.514 2.267 

1.548 3.948 

1.6 3.035 

1.595 2.309 

1.537 3.619 

1.51 6.581 

1.629 3.401 

1.536 2.946 

1.534 5.491 

1.647 2.426 

1.457 3.241 

1.472 3.699 

1.509 3.078 

0.919 1.883 

1.554 2.176 

1.513 3.001 

1.622 3.082 

1.542 2.355 

1.619 2.369 

1.536 2.554 

1.531 2.227 

1.469 2.733 

1.556 2.409 

1.525 2.326 

1.458 2.941 

1.438 2.733 

1.455 2.564 

1.456 2.546 

1.44 2.548 

1.421 2.478 

0.918 1.681 

1.655 2.153 

1.656 2.524 

1.665 2.634 

1.661 2.516 

1.681 2.359 

1.638 2.491 

1.51 2.24 

1.511 2.27 

1.556 2.435 

1.497 2.896 

1.539 3.051 

1.567 2.649 

1.579 2.646 

1.518 2.738 

1.473 2.853 

1.492 2.975 

0 , 

% 

NO. 

PPM 

CO 

PPM 

THC 

PPM 

13.691 29.674 33.13 1.252 

13.689 29.704 33.516 1.309 

13.688 28.463 41 .207 2.024 

13.687 27.701 71.101 10.42 

13.685 26.712 123.374 30.1 4 

13.689 27.689 100.711 23.1 12 

13.693 27.785 72.875 10.73 

13.689 26.521 110.932 21.442 

13.694 25.673 225.779 81 .745 

13.714 27.766 116.863 32.157 

13.708 26.852 86.307 11 .17 

13.699 26.669 190.801 70.574 

13.697 27.962 74.883 10.8 

13.701 27.135 110.518 25.963 

13.71 26.977 138.202 29.882 

13.713 27.516 110.547 24.607 

13.718 27.841 92.486 19.16 

13.706 28.078 80.259 14.296 

13.72 27.418 102.717 22.114 

13.699 27.793 109.676 27.348 

13.69 28.204 80.813 14.654 

13.689 28.104 79.719 12.924 

13.686 27.925 90.479 18.145 

13.671 28.144 79.137 12.728 

13.674 27.679 101.743 21.706 

13.667 28.296 88.295 17.6 

13.662 27.996 82.882 12.791 

13.642 27.888 112.174 27.104 

13.652 28.269 100.626 21 .77 

13.656 28.386 91.159 18.496 

13.663 28.197 91.532 16.168 

13.673 28.047 92.869 19.363 

13.665 28.035 88.355 16.139 

13.659 28.001 87.594 16.008 

13.66 28.134 82.299 12.997 

13.662 28.053 86.238 13.728 

13.661 27.923 89.766 16.703 

13.658 28.202 88.493 16.288 

13.662 28.257 80.77 13.795 

13.66 28.355 86.225 15.182 

13.669 28.239 85.498 15.589 

13.662 28.249 82.497 12.878 

13.655 28.228 86.747 16.289 

13.653 27.637 107.764 23.561 

13.649 27.794 119.515 28.895 

13.642 27.89 97.697 19.286 

13.636 28.04 98.146 20.246 

13.637 27.988 95.553 18.149 

13.636 27.957 101.789 21.721 

13.638 27.858 110.665 25.255 

2125/2013 5:49:00 PM 16.717 7.969 0.428 1.636 16.585 10.586 79.948 18.774 

2/25/2013 5:50:00 PM 1 18.826 9.662 -0.009 -0.42 18.817 0.819 0.875 0.532 02lC02 b;as 

2/25/2013 5:51 :00PM 6.933 3.318 2.779 -0.305 7.38 22.894 0.063 0.717 

2/25/2013 5:52:00 PM LI _0~.;;15;;6~.....;0",.1;.;2:;;9_....;4;;5:;;5;3_...:;.0.:;;0;01;-_0~.;07:;2;-....;.4;,;1:;:92;;3;-....,;;0,:.0,:;92;;,-_.,:0,;;5;;;3,..-1INOX b;as; THC Zero 

2/25/2013 5:53:00 PM 0.139 0.119 1.267 4.959 0.179 13.468 95.445 1.533 

2/25/2013 5:54:00PM 0.137 0.113 -0.014 9.524 0.043 0.5 1240.7931 1.321 COb;as 

212512013 5:55:00 PM 12.322 6.943 3.031 9.569 13.798 31.423 238.053 10.103 

212512013 5:56:00 PM 1 18.891 9.68 4.575 9.586 18.887 41.964 241 .671 1 42.23 D;rect Span 

212512013 5:57:00 PM 7.043 2.758 1.507 3.798 4.739 9.941 132.472 47.349 

2125/2013 5:58:00 PM 0.128 0.084 ·0.01 0.021 0.047 0.089 0.446 47.325 Direct Zero 

2125/2013 5:59:00 PM L-:1':i2';;. 7ii69:;-......;2:':.0~4~3---:;0"i96~2 -"";'1 ;';1;;'73i:-~0;';~12~5~""";0:':2:i2~5-~0':i.9::;'68i:-r.4~7;:6ii3-i-4'THC Md 

2/25/2013 6:00:00 PM 13.94 4.024 2.022 4.878 7.11 12.169 29.305 46.553 
Date Time 

0, 

% 

co, 

% 

2125/2013 6:01 :00 PM 13.94 4.028 

2/25/2013 6:02:00 PM 13.931 4.037 

2/25/2013 6:03:00 PM 13.923 4.044 

2/25/2013 6:04:00 PM 13.918 4.048 

2125/2013 6:05:00 PM 13.923 4.047 

2125/2013 6:06:00 PM 13.919 4.051 

212512013 6:07:00 PM 13.926 4.047 

2125/2013 6:08:00 PM 13.937 4.04 

2125/2013 6:09:00 PM 13.947 4.038 

2/25/2013 6:10:00 PM 13.952 4.036 

2/25/2013 6:11 :00 PM 13.957 4.037 

2/25/2013 6:12:00 PM 13.965 4.034 

212512013 6:13:00 PM 13.97 4.031 

2125/2013 6:14:00 PM 13.97 4.032 

2125/2013 6:15:00 PM 13.981 4.027 

212512013 6:16:00 PM 13.977 4.027 

2125/2013 6:17:00 PM 13.987 4.018 

2/25/2013 6:18:00 PM 13.992 4.014 

2/25/2013 6:19:00 PM 13.989 4.017 

2/25/2013 6:20:00 PM 14.005 4.008 

2/25/2013 6:21 :00 PM 14 .01 4.007 

2125/2013 6:22:00 PM 14.003 4.009 

2125/2013 6:23:00 PM 15.606 3.095 

2125/2013 6:24:00 PM 13.957 4.047 

2125/2013 6:25:00 PM 13.952 4.049 

2125/2013 6:26:00 PM 13.965 4.042 

2125/2013 6:27:00 PM 13.946 4.054 

2125/2013 6:28:00 PM 13.946 4.051 

2125/2013 6:29:00 PM 13.946 4.054 

2125/2013 6:30:00 PM 13.939 4.061 

2125/2013 6:31:00 PM 13.941 4.058 

2125/2013 6:32:00 PM 13.95 4.055 

2125/2013 6:33:00 PM 13.947 4.056 

2/25/2013 6:34:00 PM 13.944 4.058 

2125/2013 6:35:00 PM 13.95 4.054 

2/25/2013 6:36:00 PM 13.975 4.042 

2125/2013 6:37:00 PM 13.962 4.049 

2125/2013 6:38:00 PM 13.964 4.049 

2125/2013 6:39:00 PM 13.953 4.057 

2125/2013 6:40:00 PM 13.959 4.056 

2125/2013 6:41 :00 PM 17.623 1.95 

212512013 6:42:00 PM 13.958 4.065 

2125/2013 6:43:00 PM 13.941 4.065 

2125/2013 6:44:00 PM 13.929 4.073 

2125/2013 6:45:00 PM 13.927 4.07 

2/25/2013 6:46:00 PM 13.937 4.064 

2/25/2013 6:47:00 PM 13.939 4.059 

2125/2013 6:48:00 PM 13.938 4.061 

2125/2013 6:49:00 PM 13.945 4.056 

2125/2013 6:50:00 PM 13.959 4.048 

212512013 6:51:00 PM 13.959 4.048 

2125/2013 6:52:00 PM 13.973 4.039 

2125/2013 6:53:00 PM 13.985 4.033 

2/25/2013 6:54:00 PM 13.975 4.037 

2125/2013 6:55:00 PM 13.98 4.034 

2125/2013 6:56:00 PM 13.976 4.035 

2125/2013 6:57:00 PM 13.971 4.038 

2125/2013 6:58:00 PM 16.105 2.807 

2125/2013 6:59:00 PM 13.988 4.028 

2/25/2013 7:00:00 PM 13.986 4.027 

2/25/2013 7:01 :00 PM 13.987 4.029 

2125/2013 7:02:00 PM 13.982 4.032 

NO, 

PPM 

1.984 

2.077 

2.099 

2.1 72 

2.097 

2.077 

2.13 

2.126 

2.101 

2.073 

2.122 

2.053 

2.077 

2.066 

2.161 

2.174 

2.367 

2.373 

2.404 

2.342 

2.394 

2.319 

1.479 

1.76 

1.751 

1.704 

1.669 

1.683 

1.606 

1.762 

1.575 

1.579 

1.552 

1.621 

1.627 

1.464 

1.528 

1.503 

1.542 

1.558 

0.74 

1.785 

1.821 

1.929 

1.929 

1.941 

1.98 

1.917 

1.763 

1.743 

1.711 

1.57 

1.475 

1.546 

1.516 

1.54 

1.545 

1.514 

2.371 

2.226 

2.228 

2.23 

CO 

PPM 

5.704 

5.461 

5.093 

3.439 

3.89 

4.027 

4.092 

4.251 

3.658 

3.615 

3.131 

4.695 

4.112 

4.058 

5.381 

4.788 

5.039 

4.506 

4.539 

5.498 

5.505 

6.592 

4.068 

4 

3.139 

3.83 

4.092 

3.543 

3.81 

3.352 

4.058 

3.613 

3.997 

3.586 

2.545 

3.411 

3.1 

3.58 

3.958 

3.559 

2.149 

3.124 

4.038 

4.45 

3.036 

3.552 

3.325 

3.48 

3.029 

3.518 

4.164 

3.891 

3.832 

3.023 

3.51 

3.434 

3.563 

2.442 

3.447 

4.076 

3.911 

4.232 

0, 

% 

NO, 

PPM 

CO 

PPM 

THe 

PPM 

13.611 25.957 173.494 59.382 

13.614 26.775 167.059 55.904 

13.612 27.222 153.095 53.875 

13.628 27.896 91.171 16.939 

13.62 27.649 115.873 33.554 

13.624 27.634 113.386 27.535 

13.638 27.499 114.897 27.545 Start RATA 6, 75% Comp 2 

13.637 27.501 128.534 37.402 

13.637 27.957 105.656 24.068 

13.645 27.757 105.183 24.16 

13.64 27.9791.29517.453 

13.637 27.097 137.682 38.679 

13.646 27.687 125.064 37.872 

13.645 27.245 116.939 23.386 

13.634 27.022 158.212 55.423 

13.645 27.051 134.997 37.394 

13.634 27.277 144.683 45.059 

13.64 27.469 127.58 34.108 

13.647 27.387 122.363 32.32 

13.674 26.944 153.763 47.271 

13.673 27.008 148.903 46.836 

13.672 26.396 191 .851 69.635 

13.671 27.409 154.403 48.498 

13.678 27.233 133.921 36.426 

13.67 27.668 108.498 26.741 

13.669 27.129 123.438 32.65 

13.658 27.195 141.787 42.107 

13.658 27.463 120,47 33.607 

13.659 27.314 127.516 31.41 

13.663 27.791 111.864 27.817 

13.668 27.131 141.516 41 .028 

13.666 27.397 136.648 39.71 

13.671 26.953 145.966 43.619 

13.671 27.713 145.205 45.046 

13.676 27.695 90.56 16.303 

13.665 26.947 133.097 37.854 

13.666 27.529 120.643 32.116 

13.675 26.746 134.826 36.218 

13.67 27.225 168.149 60.741 

13.676 27.106 140.356 40.062 

13.68 27.231 155.751 52.461 

13.67 27.811 125.055 34.898 

13.675 26.968 138.377 38.134 

13.669 27.402 163.573 50.486 

13.663 27.819 100.88 22.365 

13.679 27.512 119.466 30.408 

13.679 27.469 117.471 29.746 

13.676 27.67 118.43 30.617 

13.684 27.784 105.976 26.189 

13.687 27.135 123.956 32.219 

13.682 27.121 151.759 47.979 

13.677 26.908 142.532 32.119 

13.672 27.271 149.028 50.111 

13.664 27.526 118.916 29.723 

13.658 27.097 140.496 40.872 

13.661 27.184 132.137 38.902 

13.658 27.078 142.495 39.054 

13.667 27.672 117.138 31 .886 

13.682 27.844 102.065 23.562 

13.669 27.427 119.332 31.007 

13.672 27.656 115.167 31 .314 

13.669 27.239 123.049 30.887 
Date Time 

212512013 7:03:00 PM 

212512013 7:04:00 PM 

212512013 7:05:00 PM 

212512013 7:06:00 PM 

212512013 7:07:00 PM 

212512013 7:08:00 PM 

212512013 7:09:00 PM 

212512013 7:10:00 PM 

212512013 7:11 :00 PM 

212512013 7:12:00 PM 

212512013 7:13:00 PM 

212512013 7:14:00 PM 

212512013 7:20:00 PM 

212512013 7:21 :00 PM 

212512013 7:22:00 PM 

0, 

% 

13.981 

13.981 

13.99 

13.991 

13.989 

13.999 

13.997 

14.018 

14.008 

14.004 

14.004 

14 

0.139 

0.137 

0.116 

212512013 7:23:00 PM 15.377 

212512013 7:24:00 PM 1 18.87 

2125/2013 7:25:00 PM 3.557 

212512013 7:26:00 PM 0.121 

212512013 7:27:00PMI 0.114 

2125/2013 7:28:00 PM 0.59 

2/25/2013 7:29:00 PM 13.628 

2/25/2013 7:30:00 PM 13.941 

2/25/2013 7:31 :00 PM 13.944 

2125/2013 7:32:00 PM 13.937 

2125/2013 7:33:00 PM 13.936 

2125/2013 7:34:00 PM 13.943 

CO, 

% 

2125/2013 7:35:00 PM 13.948 4.043 

2125/2013 7:36:00 PM 13.967 4.035 

2125/2013 7:37:00 PM 13.964 4.039 

2125/2013 7:38:00 PM 13.993 4.02 

2/25/2013 7:39:00 PM 14.006 4.011 

2125/2013 7:40:00 PM 14.001 4.016 

2/25/2013 7:41:00 PM 16.043 2.847 

212512013 7:42:00 PM 13.951 4.059 

212512013 7:43:00 PM 13.933 4.064 

212512013 7:44:00 PM 13.93 4.068 

2125/2013 7:45:00 PM 13.935 4.065 

212512013 7:46:00 PM 13.942 4.062 

2/2512013 7:47:00 PM 13.939 4.064 

2125/2013 7:48:00 PM 13.951 4.06 

2125/2013 7:49:00 PM 13.962 4.057 

2125/2013 7:50:00 PM 13.977 4.047 

2125/2013 7:51 :00 PM 13.966 4.048 

2125/2013 7:52:00 PM 13.979 4.034 

2125/2013 7:53:00 PM 17.644 1.902 

2125/2013 7:54:00 PM 13.982 4.03 

2125/2013 7:55:00 PM 13.928 4.038 

2125/2013 7:56:00 PM 13.922 4.035 

2125/2013 7:57:00 PM 13.921 4.031 

2/25/2013 7:58:00 PM 13.931 4.02 

2125/2013 7:59:00 PM 13.907 4.031 

2125/2013 8:00:00 PM 13.88 4.043 

212512013 8:01:00 PM 13.885 4.042 

2125/2013 8:02:00 PM 13.894 4.039 

2125/2013 8:03:00 PM 13.898 4.041 

212512013 8:04:00 PM 16.815 2.284 

NO, 

PPM 

2.255 

2.309 

2.464 

2.545 

2.421 

2.498 

2.507 

2.536 

2.636 

2.683 

2.732 

2.638 

2.531 

-0.006 

-0.01 

CO 

PPM 

5.123 

5.437 

5.903 

4.53 

5.164 

4.999 

3.638 

4.167 

4.484 

4.502 

4.301 

4.817 

2.401 

9.331 

9.601 

0, 

% 

13.682 

13.669 

13.67 

13.677 

13.671 

13.681 

13.678 

13.681 

13.683 

13.673 

13.671 

13.68 

0.201 

0.043 

0.044 

NO, 

PPM 

26.909 

26.741 

26.74 

27.507 

26.81 

27.257 

27.859 

27.223 

27.251 

27.294 

27.3 

27.237 

26.23 

CO THC 

PPM PPM 

153.709 50.058 

162.845 53.593 

171.992 60.157 

135.745 43.931 

151.445 45.771 

153.155 52.136 

104.003 25.381 

121 .309 32.989 

128.817 37.274 

132.717 37.129 

123.021 24.585 

135.996 37.342 

29.736 1.14 

0.534 231.154 1.301 

0.402 1 241.4231 1.326 

2.312 9.606 12.807 26.717 237.516 6.86 

CO bias 

4.582 9.59 18.851 41.878 241.4281 34.1 Direct Span 

1.412 5.751 9.335 19.671 176.492 33.597 

-0.014 0.223 0.054 0.103 2.469 46.192 

-0.015 0.004 0.042 0.069 -0.034 46.982 Direct Zero 

-0.016 -0.009 0.042 0.067 -0.036 47.399 

1.874 

2.204 

2.204 

2.277 

2.359 

2.271 

2.418 

2.38 

2.454 

2.67 

2.599 

2.456 

1.559 

1.765 

1.709 

1.787 

1.79 

1.821 

1.757 

1.65 

1.585 

1.474 

1.568 

1.502 

0.731 

1.909 

1.935 

1.901 

1.93 

1.931 

1.744 

1.813 

1.784 

1.807 

1.883 

1.074 

2.14 

3.777 

3.652 

4.011 

3.544 

3.381 

3.566 

4.186 

3.904 

4.355 

4.661 

5.587 

3.107 

3.149 

3.62 

3.742 

3.842 

4.199 

3.969 

3.899 

3.298 

3.393 

3.242 

3.975 

2.614 

3.614 

3.678 

3.368 

4.342 

3.297 

4.765 

3.913 

4.016 

4.654 

3.792 

3.003 

8.822 

9.93 

9.935 

9.923 

9.926 

9.935 

16.933 51.26 47.737 

22.411 131.5251 48.073 ITHC Mid 

23.62 132.821 47.944 Start RATA 7 

23.724 132.805 41 .434 

23.729 133.153 25.926 

23.723 133.001 1 20.835 tntet Mid 

12.726 25.191 115.929 24.194 

13.65 27.111 115.398 30.988 

13.649 27.378 106.315 24.457 

13.663 27.334 122.363 34.242 

13.662 27.061 123.656 33.059 

13.662 26.987 156.538 53.016 

13.666 27.459 112.328 26.412 

13.659 27.663 108.734 28.235 

13.655 27.1 9 115.077 30.474 

13.648 27.233 128.346 36.611 

13.65 27.023 127.531 33.747 

13.653 26.911 135.724 39.682 

13.662 27.3 137.056 43.6 

13.657 27.27 136.01 42.247 

13.663 27.39 117.319 33.298 

13.664 27.1 6 128.432 37.508 

13.668 27.258 122.618 30.292 

13.673 26.559 149.841 18.53 

13.679 26.504 169.118 1.09 

13.665 27.069 138.475 0.984 

13.656 27.61 116.828 0.917 

13.649 27.503 104.743 0.881 

13.648 27.064 135.797 0.977 

13.657 27.531 99.98 0.86 

13.641 26.499 152.62 1.035 

13.633 27.39 131 .603 0.963 

13.641 27.107 128.062 0.953 

13.65 26.977 151.985 1.023 

13.66 27.506 123.403 0.933 

13.667 27.469 122.129 0.933 
Dale Time 

0, 

% 

CO, 

% 

2/25/2013 6:05:00 PM 16.399 2.693 

2/25/2013 6:06:00 PM 13.965 4.01 

2125/2013 6:07:00 PM 13.954 4.015 

2/25/2013 6:06:00 PM 13.964 4.012 

212512013 6:09:00 PM 13.956 4.013 

2125/2013 6:10:00 PM 13.961 4.001 

2/2512013 6:11 :00 PM 13.996 3.991 

2125/2013 6:12:00 PM 14.007 3.966 

2/2512013 6:13:00 PM 14.01 3.966 

2/25/2013 6:14:00 PM 14.009 3.99 

2/25/2013 6:15:00 PM 14.036 3.976 

NO, 

PPM 

1.479 

2.361 

2.355 

2.323 

2.299 

2.605 

2.564 

2.722 

2.691 

2.599 

2.562 

CO 

PPM 

1.556 

4.056 

4.71 

4.513 

5.929 

3.266 

5.563 

4.651 

4.527 

4.554 

4.271 

0, 

% 

NO, 

PPM 

CO 

PPM 

THC 

PPM 

13.662 27.74 110.636 0.694 

13.657 27.502 116.553 0.921 

13.664 27.359 136.606 0.967 

13.66 26.665 131.065 0.961 

13.659 26.759 162.627 1.131 

13.659 26.053 91.354 0.633 

13.657 26.449 153.732 1.033 

13.669 27.457 137.446 0.961 

13.676 27.256 124.202 0.941 

13.665 27.456 126.664 0.952 

13.676 27.261 110.75 0.695 

2/25/2013 6:16:00 PM 16.179 7.267 1.047 3.171 13.663 27.367 119.764 0.922 

2/25/2013 6:17:00 PM I 16.623 9.665 -0.004 -0.345 13.654 27.556 119.627 0.923 02lC02 bias 

2/25/2013 6:16:00 PM ,;;;6.:';94:;;1'--;4,.3;.;6;:;2_--;2"i.2"'6,;.5 __ --;:0:'; .3:;44", 13.655 27.233 121.567 0.932 

2125/2013 6:19:00 PM I 0.16 0.146 4.551 -0.017 13.666 27.035 150.315 1.025 NOxbias 

212512013 6:20:00 PM 0.137 0. 133 1.51 4.377 13.66 27.265 114.091 0.906 

2125/2013 6:21:00 PM 0.137 0.129 -0.005 9.469 13.661 26.622 126.17 0.947 

2125/2013 6:22:00 PM 0.114 0.126 -0.Q1 9.591 13.655 27.181 137.397 0.984 CO bias 

2125/2013 6:23:00 PM 9.514 2.91 1.559 6.639 13.656 27.613 115.43 0.911 

2125/2013 6:24:00 PM 13.972 4.006 2.313 3.769 13.667 27.563 102.264 0.666 Start RATA 6 

2125/2013 6:25:00 PM 13.967 4.013 2.227 4.319 13.67 27.15 121.662 0.931 

2125/2013 6:26:00 PM 13.965 4.014 2.16 5.074 13.671 26.679 153.905 1.037 

212512013 6:27:00 PM 13.965 4.016 2.379 4.092 13.675 27.625 120.491 0.926 

212512013 6:26:00 PM 13.991 4.009 2.215 4.626 13.672 26.626 137.326 0.962 

2125/2013 6:29:00 PM 13.991 4.01 2.261 3.966 13.669 27.374 121.665 0.926 

2/25/2013 6:30:00 PM 14.037 3.964 2.366 5.402 13.666 26.179 145.357 1.007 

2/25/2013 6:31 :00 PM 14.042 3.96 2.424 5.935 13.674 26.714 176.576 1.114 

2/25/2013 6:32:00 PM 14.045 3.979 2.437 4.316 13.676 26.695 115.326 0.91 

2/25/2013 6:33:00 PM 14.049 3.96 2.523 4.256 13.676 27.33 125.321 0.942 

2125/2013 6:34:00 PM 17.556 1.959 1.045 2.04 13.675 26.679 116.039 0.913 

2/25/2013 6:35:00 PM 14 4.029 1.656 4.62 13.664 26.237 195.475 1.176 

212512013 6:36:00 PM 13.965 4.026 1.761 3.659 13.675 27.447 136.069 0.976 

212512013 8:37:00 PM 13.964 4.039 1.569 5.613 13.656 25.256 201 .3 1.191 

2125/2013 6:36:00 PM 13.962 4.04 1.619 6.594 13.653 25.664 245.317 1.34 

2125/201 3 6:39:00 PM 13.976 4.031 1.767 3.159 13.642 26.044 111.92 0.697 

2125/2013 6:40:00 PM 13.941 4.047 1.657 4.969 13.636 26.003 170.429 1.066 

2/25/2013 6:41 :00 PM 13.954 4.043 1.599 4.006 13.626 27.465 156.169 1.044 

2/25/2013 6:42:00 PM 13.943 4.046 1.566 3.027 13.625 27.66 119.673 0.92 

2/25/2013 6:43:00 PM 13.946 4.042 1.522 2.906 13.63 27.601 112.331 0.904 

2/25/2013 6:44:00 PM 13.977 4.027 1.541 2.752 13.652 27.729 102.792 0.672 

212512013 6:45:00 PM 13.96 4.029 1.466 3.034 13.653 27.504 115.225 0.91 

212512013 6:46:00 PM 16.567 2.527 0.963 1.663 13.662 26.251 77.399 0.762 

212512013 6:47:00 PM 13.964 4.041 1.642 2.106 13.656 26.071 66.575 0.753 

2125/2013 6:46:00 PM 13.94 4.046 1.796 2.261 13.66 27.949 67.615 0.752 

2/25/2013 6:49:00 PM 13.946 4.041 1.77 3.265 13.672 27.46 102.063 0.666 

2/25/2013 8:50:00 PM 13.948 4.042 1.649 2.406 13.661 27.635 71.064 0.763 

2125/2013 6:51:00 PM 13.943 4.041 1.757 3.746 13.659 27.011 121.73 0.931 

2125/2013 6:52:00 PM 13.936 4.046 1.765 4.063 13.656 26.677 122.199 0.932 

2125/2013 6:53:00 PM 13.93 4.05 1.626 5.53 13.653 26.392 176.342 1.112 

212512013 6:54:00 PM 13.939 4.041 1.925 3.594 13.659 27.466 114.521 0.904 

2125/2013 6:55:00 PM 13.93 4.049 1.63 4.046 13.651 26.631 126.663 0.954 

2125/2013 6:56:00 PM 13.916 4.056 1.656 4.591 13.636 27.209 152.695 1.034 

2/25/2013 6:57:00 PM 16.065 2.72 1.267 2.97 13.631 27.445 109.474 0.669 

2/25/2013 6:56:00 PM 14.297 3.931 2.103 3.639 13.636 27.105 140.264 0.992 

2125/2013 6:59:00 PM 13.976 4.015 2.337 4.237 13.626 27.027 124.654 0.939 

2/25/2013 9:00:00 PM 13.962 4.012 2.193 5.044 13.645 26.63 157.669 1.049 

2125/2013 9:01:00 PM 13.96 4.014 2.256 4.127 13.636 27.153 124.401 0.94 

2125/2013 9:02:00 PM 13.977 4.016 2.293 4.725 13.643 26.653 143.457 

2125/2013 9:03:00 PM 13.99 4.006 2.453 3.36 13.654 27.665 94.629 0.642 

2125/2013 9:04:00 PM 14.015 3.969 2.733 3.645 13.653 27.675 109.01 0.69 

2125/2013 9:05:00 PM 14.016 3.966 2.734 4.069 13.651 27.426 106.617 0.667 

2125/2013 9:06:00 PM 14.024 3.962 2.563 4.545 13.666 26.94 130.126 0.957 
Date Time 

0, 

% 

CO, 

% 

NO, 

PPM 

CO 

PPM 

0 , 

% 

NO, 

PPM 

CO 

PPM 

THC 

PPM 

2/25/2013 9:07:00 PM 14.024 3.98 2.511 5.705 13.655 26.808 165.793 1.073 

2125/2013 9:08:00 PM 16.931 8.195 0.669 1.68 13.648 27.978 84.596 0.807 

2125/2013 9:09:00 PM rl"",i-i8~.8:;:0';'8-""9;;;6:ii8;;5~-i_0;:;.0;::0:;8"" -0.41 13.65 27.435 104.085 0.872 02lC02 bias 

2125/2013 9:10:00 PM .... ;i5.'4n'04:f-.....,2;;;.5f.3;.:4---;3;.,.1;;7;;5 ..... -0.267 13.634 27.473 110.216 0.89 

2125/2013 9:11:00 PM I 0.1 5 0.137 4.563 0 13.638 26.871 138.523 0.986 NOx bias 

2125/2013 9:12:00 PM .... ;i0':-,:::38;-.....,0;;;=',2;;7:--:,~.06~5-~5~2~96;;-' 13.643 27.119 132.545 0.968 

2125/2013 9:13:00 PM 0.138 0.123 -0.009 9.529 13.636 27.226 121.097 0.928 

212512013 9:14:00 PM 0.114 0.12 -0.008 9.614 13.638 26.268 150.276 1.026 CO bias 

2125/2013 9:15:00 PM 6.303 1.99 1.038 8.096 13.64 27.553 138.887 0.986 

2125/2013 9:16:00 PM 13.946 3.995 2.274 4.216 13.643 27.177 116.544 0.914 Start RATA 9 

2125/2013 9:17:00 PM 13.974 4.004 2.383 4.205 13.648 27.564 126.024 0.944 

2/25/2013 9:18:00 PM 13.986 4.003 2.368 4.35 13.653 26.79 122.895 0.934 

2125/2013 9:19:00 PM 13.987 3.999 2.276 4.509 13.658 27.486 132.637 0.964 

212512013 9:20:00 PM 13.991 3.995 2.387 3.258 13.66 27.498 86.381 0.811 

212512013 9:21 :00 PM 13.993 3.996 2.272 4.736 13.652 27.158 132.84 0.967 

2125/2013 9:22:00 PM 14.009 3.985 2.548 3.372 13.655 27.377 86.842 0.817 

2125/2013 9:23:00 PM 13.999 3.99 2.305 5.56 13.646 26.769 156.071 1.043 

2125/2013 9:24:00 PM 13.994 3.993 2.342 3.048 13.644 27.881 81.229 0.798 

2125/2013 9:25:00 PM 14.001 3.989 2.281 4.16 13.661 26.423 113.541 0.902 

2125/2013 9:26:00 PM 16.622 2.484 1.426 3.723 13.646 27.68 140.308 0.991 

2125/2013 9:27:00 PM 13.997 4.004 2.26 2.202 13.644 28.047 61 .251 0.731 

2/25/2013 9:28:00 PM 13.985 4.01 2.1 33 3.79 13.645 27.351 109.529 0.891 

2125/2013 9:29:00 PM 13.988 4.008 2.121 3.772 13.654 27.342 107.763 0.884 

2125/2013 9:30:00 PM 13.988 4.009 2.158 3.727 13.655 27.355 109.19 0.889 

2125/2013 9:31:00 PM 13.988 4.013 2.25 3.738 13.645 27.42 108.624 0.889 

2125/2013 9:32:00 PM 13.991 4.009 2.261 3.644 13.644 27.578 99.792 0.861 

2125/2013 9:33:00 PM 14.011 3.994 2.531 3.238 13.642 27.667 89.717 0.826 

2125/2013 9:34:00 PM 14 3.998 2.535 4.624 13.635 26.996 135.141 0.972 

2125/2013 9:35:00 PM 14.003 3.996 2.536 3.658 13.635 27.727 102.606 0.867 

2125/2013 9:36:00 PM 13.991 4.001 2.325 5.794 13.628 26.238 163.094 1.066 

2125/2013 9:37:00 PM 16.748 2.411 1.473 3.274 13.633 27.638 122.634 0.934 

212512013 9:38:00 PM 13.991 4.01 2.307 4.905 13.618 26.58 149.804 1.023 

2125/2013 9:39:00 PM 13.987 4.007 2.475 3.372 13.621 27.713 98.404 0.854 

2125/2013 9:40:00 PM 13.97 4.015 2.265 5.337 13.612 26.684 147.129 1.012 

2125/2013 9:41:00 PM 13.976 4.015 2.567 3.337 13.618 28.087 93.567 0.833 

2/25/2013 9:42:00 PM 13.981 4.012 2.329 4.152 13.626 26.739 111 .361 0.896 

2125/2013 9:43:00 PM 13.987 4.007 2.307 5.404 13.637 27.074 178.226 1.117 

2125/2013 9:44:00 PM 13.989 4.005 2.337 3.14 13.646 27.874 79.948 0.793 

2125/2013 9:45:00 PM 13.989 4.002 2.268 5.16 13.636 26.192 142.504 0.997 

2/25/2013 9:46:00 PM 13.994 4.001 2.42 5.084 13.629 27.464 155.107 1.04 

2125/2013 9:47:00 PM 13.99 4.004 2.295 3.642 13.63 27.445 92.427 0.835 

2125/2013 9:48:00 PM 16.37 2.632 1.445 3.185 13.622 27.053 126.177 0.944 

2125/2013 9:49:00 PM 13.992 4.01 2.2 4.649 13.631 26.705 138.83 0.986 

2125/2013 9:50:00 PM 13.988 4.011 2.232 4.472 13.634 27.129 128.291 0.952 

2125/2013 9:51 :00 PM 13.987 4.012 2.201 4.87 13.635 26.647 141.553 0.996 

2/25/2013 9:52:00 PM 13.989 4.012 2.362 4.044 13.641 27.21 118.328 0.92 

2/25/2013 9:53:00 PM 13.986 4.018 2.284 5.287 13.643 26.564 156.556 1.045 

2125/2013 9:54:00 PM 13.99 4.015 2.472 4.961 13.634 27.175 139.725 0.99 

212512013 9:55:00 PM 13.991 4.011 2.479 5.336 13.638 27.108 142.269 0.997 

2125/2013 9:56:00 PM 13.989 4.016 2.397 5.647 13.636 26.878 155.142 1.041 

2125/2013 9:57:00 PM 13.989 4.018 2.478 5.228 13.646 26.85 145.101 1.005 

2/25/2013 9:58:00 PM 13.978 4.027 2.461 5.273 13.643 27.18 150.469 1.026 

2125/2013 9:59:00 PM 15.861 6.982 1.152 3.698 13.637 26.923 149.136 1.022 

2/25/2013 10:00:00 PM,.I..:..;,;;8;;:8.:........;9;;;6;;;9;:;4~-i-0;,.0;;;0,;6.., -0.295 13.634 26.443 176.069 1.108 02/C02 bias 

2125/2013 10:01:00 PM 11.207 5.535 1.728 -0.37 13.645 26.631 175.172 1.107 

2125/2013 10:02:00 PMfl nO.-;;177:5'.....,0;;;.1;-;5oi8:--4 •. :f. 53f--;;0;; _ .0;,;2;3' 13.643 27.574 135.509 0.974 NOx bias 

2125/2013 10:03:00 PM 0.138 0.14 1.576 4.267 13.639 28.283 86.188 0.814 

2125/2013 10:04:00 PM 0.138 0.132 -0.008 9.503 13.667 27.937 89.77 0.83 

2125/2013 10:05:00 PM 0.122 0.128 -0.016 9.6 

2125/2013 10:06:00 PM 14.992 8.719 3.868 9.604 

2125/2013 1 0:07:00 PMrl""';';8;;.8"'8;-'-"':;9;".7:=--":;4;;.5~6;;3--;;9;;;.5;;75"'" 

2/25/2013 10:08:00 PM .... ;i5.-;',0n'4;-....,,;'.77'2;;,--:,'i.0;;i0'i-8--;-3~.8 .. ,4~ 

14.216 26.993 63.109 

15.398 27.391 51.061 

16.716 29.415 51.927 

16.691 28.855 68.063 

0.736 CO bias 

0.699 

0.703 Direct Span 

0.753 
0 , CO, NO, CO 0 , NO, CO THC 

Date Time % % PPM PPM % PPM PPM PPM 

2/25/2013 10:09:00 PM! 0.122 0.098 -0.009 0.029 16.694 28.548 74.348 0.775 Direct Zero 

2/25/2013 10:10:00 PM 8.378 4.462 2.404 2.43 16.704 28.288 77.744 0.786 

2/25/2013 10:11 :00 PM 10.005 5.122 2.531 4.497 16.698 28.256 79.103 0.792 

2125/2013 10:12:00 PM! 10.005 5.121 2.526 4.488 16.692 28.264 79.276 0.788 Direct Mid 
O2 CO2 NOx CO O2 NOx CO 

Date Time % % PPM PPM % PPM PPM 

2126/2013 7:48:00 AM LI +.0~1 i:i12':-....,0".0~7,.;4_....,-0"0;::3;:;1,.-_-~0;,;0:;;36~....,0~."::04ii3':-.....;0;;.04~1,....~-0;;.0:;:36~ 212612013 7:49:00AM 11 .787 7.054 -0.037 4.215 11.486 -0.Q15 91.745 

2126/2013 7:50:00 AM .-:1:.;8.;;9;;:34,;....-;9".6~8;;:2;.-t.....;-0;;;.O;;:3:,;84-:;9;,:.4;,86;;-....,1;;:8.;;.96;;:9:o-1h-0;;;,,036;,;-+;2,,3:;:8::;96;:,4:-, 

THC 

PPM 

4.056 N2INOx Mode;02lC02/CO Cal Zero 

0.962 

1.44 N21NO Mode 

2126/2013 7:51:00 AM L...,1.;;8'i9~5;;2_...,9".6::;8;;;2~ 3.818 9.552 18.997 3.675 240.491 1.445 02/C02/CO Cal High 

2126/20137:52:00AM 14178 7138 46 9558 14668 4649 231.023 1.412 

2126/2013 7:53:00 AM 101.523 "1-0::"."98"'7:-1INo/NOx Mode; THC Cal Zero 

2126/2013 7:54:00 AM 54.628 0.831 021C021CO Mid 

212612013 7:55:00AM 36.505 71 .537 NO/NO Mode 

2126/2013 7:56:00 AM 20.814 

2126/2013 7:57:00 AM 20.832 

0.141 2.138 0.361 

0.138 -0.002 0.3 

2126/2013 7:58:00 AM 20.844 0.137 2.839 0.297 

2126/2013 7:59:00 AM 20.853 0.138 3.465 0.287 

2126/2013 8:00:00 AM 20.875 0.138 0.798 0.29 

212612013 8:01 :00 AM 20.889 0.137 -0.027 0.295 

2126/2013 8:02:00 AM 20.892 0.138 3.665 0.288 

0.067 2204 

0.047 I -0.027 

0.043 2.936 

0.051 I 3.495 

0.719 0.933 

0.061 -0.033 

0.042 27.323 

52.983 89727 

132.268 90.121 N02/NO Mode 

132.565 I 85.076 CO Mid 

80.615 I 84.574 IN021NOx Mode; THC Cal High 

1.304 83.8 

3.079 54.054 NOx Cal Zero 

0.308 48.77 ITHC Mid 

2/26/2013 8:03:00 AM 20.896 0.137 4.595 0.292 0.424 40.232 

41 .91 5 

42.021 

1.076 50.399 

2126/2013 8:04:00 AM 20.902 0.136 4.599 0.305 0.046 

212612013 8:05:00 AM 20.906 0.135 2.897 0.295 0.042 

2126/2013 8:06:00 AM 20.904 0.136 2.506 0.296 4.435 

1.223 

0.058 

27.915 NOx Cal High 

26.633 INOx Inlet Cal High;THC l ow 

25.237 3.186 25.395 

2126/2013 8:07:00AM 19.882 0.138 2.531 0.85 14.21 23.74 49.218 6.529 NOx Mid 

2126/2013 8:08:00 AM 0.556 0.094 0.597 10.782 0.879 23.906 1160.917 2.762 NOx Inlet Mid 

2126/2013 8:09:00 AM 0.155 0.092 -0.018 9.955 0.054 6.291 240.738 1.448 

2126/2013 8:10:00AM 0.137 0.091 -0.032 9.664 0.044 0.153 1240.7641 1.446 CO bias 

212612013 8:11 :00AM 3.304 1.99 -0.03 9.158 4.177 0.122 234.617 1.425 

2126/2013 8:12:00 AM .-:1,;:8,;;.8;;:6:;.8_-i9".6:;;2,,1,.-.....;-0,..0:;;3;,:3..., 1.013 .....,1;,:;8:;; .9.,3;--:;0.:;:09,;;8;-, 41.785 0.941 

2126/2013 8:13:00 AM 1 .._1;.8;i.9:':5;-7_-i9~.6;.,4;:;7_....,-::'-0.i:03i--' -0.387 ~1;;,8.;i;97ii7_-i:0,,:08~4::-, -0.34 0.682 021C02 bias 

2/26/2013 8:14:00 AM 7.544 3.631 2.61 -0.273 8.249 21 .112 -0.22 0.789 

2/26/2013 8: 15:00 AM 1..-0'".;.15,;,9:-.....;0"'.1'"0;,;9--;4:;.5::,4"9-..;,0.;;0;;,31::-.....;0;;.0;;7;;2:..-...:;4"'1."58;,;2;;-....,0;;.06;;....., 0.651 NOx bias 

2126/2013 8:16:00AM 14.02 0.124 1.607 0.1 89 9.861 31 .05 20.017 

2126/2013 8:17:00AM 20.852 0.13 0.003 0.282 14.19 25.285 57.163 

2126/2013 8:18:00 AM 20.868 0.129 -0.008 0.276 14.207 25.352 57.461 

2/26/2013 8:19:00AM 20.871 0.127 -0.011 0.265 14.204 25.435 57.287 

2/26/2013 8:20:00 AM 20.864 0.127 -0.012 0.285 14.208 25.495 57.097 

2126/2013 8:21 :00 AM 20.875 0.127 0.001 0.29 14.213 25.536 56.988 

212612013 8:22:00 AM 20.867 0.135 -0.017 0.304 14.223 25.521 57.089 

212612013 8:23:00 AM 20.866 0.135 -0.014 0.282 14.213 25.682 56.649 

2126/2013 8:24:00 AM 15.001 3.525 1.371 0.384 14.225 25.788 55.488 

2126/2013 8:25:00 AM 14.222 3.897 1.549 0.552 14.217 25.743 56.129 

2126/2013 8:26:00 AM 14.226 3.895 1.696 0.512 14.23 26.499 53.319 

2126/2013 8:27:00 AM 14.217 3.901 1.718 0.458 14.215 26.644 48.031 

212612013 8:28:00 AM 14.211 3.903 1.551 0.541 14.211 25.842 54.798 

212612013 8:29:00 AM 14.214 3.903 1.728 0.551 14.208 25.902 55.262 

212612013 8:30:00AM 14.205 3.904 1.789 0.541 14.208 25.961 55.059 

2126/2013 8:31 :00AM 14.211 3.9 1.789 0.52 14.21 25.975 54.795 

2126/2013 8:32:00 AM 14.208 3.901 1.793 0.547 14.208 25.974 54.967 

2/26/2013 8:33:00 AM 14.203 3.902 1.834 0.544 14.208 26.055 54.372 

212612013 8:34:00AM 14.214 3.894 1.84 0.542 14.207 26.033 54.419 

2126/2013 8:35:00 AM 14.216 3.888 1.873 0.524 14.217 26.111 53.975 

2126/2013 8:36:00AM 14.215 3.888 2.065 0.522 14.208 26.08 54.076 

2/26/2013 8:37:00 AM 14.201 3.89 2.188 0.52 14.208 26.17 53.632 

2126/2013 8:38:00AM 14.214 3.879 2.071 0.506 14.208 26.173 53.644 

2126/2013 8:39:00 AM 14.199 3.883 2.11 0.513 14.208 26.297 53.477 

2126/2013 8:40:00AM 14.2 3.88 2.146 0.515 14.208 26.307 53.042 

212612013 8:41 :00AM 14.212 3.871 2.329 0.494 14.208 26.223 53.658 

2/26/2013 8:42:00AM 14.206 3.87 2.365 0.481 14.208 26.182 53.502 

2126/2013 8:43:00 AM 14.183 3.874 2.38 0.496 14.196 26.191 53.144 

2126/2013 8:44:00AM 14.185 3.872 2.471 0.478 14.193 26.25 52.732 

2126/2013 8:45:00AM 14.179 3.871 2.511 0.479 14.194 26.313 52.189 

212612013 8:46:00AM 16.714 2.426 1.331 0.375 14.179 26.386 51 .679 

2126/2013 8:47:00 AM 14.169 3.881 1.757 0.332 14.178 26.516 51 .069 

1.659 

3.957 

3.959 

3.901 

3.874 

3.874 

3.893 

3.858 

3.662 

3.727 

3.522 

2.932 

3.612 

3.688 

3.68 Start 50% PM/COMP 

3.638 

3.641 

3.61 

3.627 

3.559 

3.569 

3.591 

3.517 

3.47 

3.444 

3.571 

3.591 

3.568 

3.487 

3.428 

3.316 

3.285 
Date Time 

212612013 8:48:00 AM 

212612013 8:49:00 AM 

212612013 8:50:00 AM 

2126/2013 8:51 :00 AM 

2126/2013 8:52:00 AM 

2126/2013 8:53:00 AM 

2126/2013 8:54:00 AM 

2126/2013 8:55:00 AM 

212612013 8:56:00 AM 

2126/2013 8:57:00 AM 

2126/2013 8:58:00 AM 

2126/2013 8:59:00 AM 

212612013 9:00:00 AM 

212612013 9:01 :00 AM 

2126/2013 9:02:00 AM 

2126/2013 9:03:00 AM 

2126/2013 9:04:00 AM 

212612013 9:05:00 AM 

212612013 9:06:00 AM 

2126/2013 9:07:00 AM 

2126/2013 9:08:00 AM 

2126/2013 9:09:00 AM 

2126/2013 9:10:00 AM 

2126/2013 9: 11 :00 AM 

212612013 9:12:00 AM 

212612013 9: 13:00 AM 

2126/2013 9:14:00AM 

2126/2013 9:15:00AM 

2126/2013 9:16:00AM 

2126/2013 9:17:00 AM 

2126/2013 9:18:00 AM 

212612013 9:19:00 AM 

2126/2013 9:20:00 AM 

2126/2013 9:21 :00 AM 

212612013 9:22:00 AM 

2126/2013 9:23:00 AM 

212612013 9:24:00 AM 

2126/2013 9:25:00 AM 

212612013 9:26:00 AM 

212612013 9:27:00 AM 

2126/2013 9:28:00 AM 

212612013 9:29:00 AM 

212612013 9:30:00 AM 

2126/2013 9:31 :00 AM 

2126/2013 9:32:00 AM 

2126/2013 9:33:00 AM 

212612013 9:34:00 AM 

212612013 9:35:00AM 

O2 

% 

14.147 

14.1 45 

14.148 

14.143 

14.132 

14.127 

14.123 

14.099 

14.098 

14.108 

14.107 

14.091 

14.092 

14.079 

14.083 

18.803 

14.183 

14.12 

14.1 07 

14.095 

14.102 

14.1 

14.095 

14.097 

14.089 

14.095 

14.093 

14.093 

14.089 

14.096 

14.103 

14.1 

17.561 

14.178 

14.111 

14.11 9 

14.12 

14.122 

14.123 

14 .1 19 

14.106 

14.106 

14 .102 

14.102 

14.1 

14.107 

14.104 

14.1 07 

CO2 

% 

NO, CO 

PPM PPM 

3.887 1.828 0.374 

3.887 1.688 0.378 

3.883 1.735 0.364 

3.885 1.768 0.337 

3.89 1.964 0.345 

3.893 1.751 0.3 

3.896 1.704 0.286 

3.91 1.779 0.271 

3.911 1.819 0.241 

3.905 1.907 0.259 

3.907 1.883 0.231 

3.919 1.961 0.237 

3.915 1.63 0.283 

3.925 1.654 0.316 

3.921 1.688 0.36 

1.205 0.512 0.311 

3.892 1.76 0.531 

3.899 1.748 0.624 

3.905 1.739 0.63 

3.912 1.723 0.647 

3.91 1.744 0.636 

3.912 1.826 0.642 

3.912 1.82 0.639 

3.911 1.79 0.62 

3.916 1.842 0.62 

3.913 1.825 0.628 

3.916 1.731 0.662 

3.916 1.674 0.674 

3.917 1.708 0.705 

3.914 1.691 0.68 

3.91 1.696 0.691 

3.912 1.763 0.674 

1.906 0.889 0.52 

3.897 2.42 0.485 

3.904 2.33 0.585 

3.901 2.292 0.591 

3.902 2.298 0.597 

3.899 2.274 0.581 

3.899 2.295 0.578 

3.901 2.358 0.572 

3.907 2.601 0.557 

3.909 2.567 0.579 

3.912 2.595 0.574 

3.912 2.542 0.576 

3.913 2.539 0.581 

3.91 2.725 0.531 

3.912 2.84 0.537 

3.912 2.773 0.53 

212612013 9:36:00AM 14.099 3.915 2.825 0.555 

212612013 9:37:00 AM 14.102 3.914 2.828 0.566 

2126/2013 9:38:00 AM 16.066 6.961 1.28 0.226 

2126/2013 9:39:00 AM '"!""1~8"i84~6~-i:9"i.6~36i--_-ii0'i:0:-1 -, -0.4 

O2 

% 

14.17 

14.165 

14.179 

14.162 

14.165 

14.161 

14.154 

14.134 

14.124 

14.145 

14.147 

14.13 

14.128 

14.109 

14.126 

14.122 

14.139 

14.141 

14.134 

14.117 

14.125 

14.125 

14.121 

14.116 

14.1 11 

14.119 

14.1 2 

14.117 

14.115 

14.128 

14.132 

14.125 

14.123 

14.121 

14.122 

14.133 

14.13 

14.133 

14.138 

14.133 

14.121 

14.126 

14.113 

14.117 

14.113 

14.125 

14.111 

14.11 

NO, 

PPM 

26.468 

26.513 

26.651 

26.757 

26.861 

27.023 

27.269 

27.476 

27.805 

27.872 

28.031 

27.842 

26.933 

26.422 

26.148 

26.121 

26.038 

26.039 

25.998 

26.038 

26.039 

26.012 

26.04 

26.039 

26.091 

26.059 

26.034 

26.072 

26.044 

26.016 

26.026 

26.078 

26.051 

26.016 

26.025 

25.996 

26.02 

25.986 

26.024 

26.043 

26.097 

26.055 

26.08 

26.056 

26.033 

26.04 

26.025 

26.004 

CO 

PPM 

50.903 

51.299 

50.379 

49.824 

49.405 

48.783 

47.667 

46.625 

45.339 

44.517 

44.401 

44.088 

47.536 

50.461 

52.456 

52.863 

53.326 

53.54 

53.496 

53.654 

53.328 

53.47 

53.392 

53.327 

52.996 

53.063 

53.025 

53.076 

53.122 

53.347 

53.36 

53.054 

52.9 

53.163 

53.234 

53.44 

53.319 

53.621 

53.18 

53.329 

52.986 

52.921 

52.752 

52.974 

53.323 

53.032 

52.975 

53.404 

14.108 25.948 53.415 

14.112 25.904 54.118 

16.083 14.593 42.392 

18.875 0.58 0.971 

THC 

PPM 

3.274 

3.368 

3.232 

3.151 

3.059 

3.02 

2.939 

2.757 

2.695 

2.601 

2.638 

2.547 

2.854 

3.175 

3.362 

3.454 

3.501 

3.621 

3.529 

3.59 

3.554 

3.605 

3.586 

3.378 

3.444 

3.521 

3.586 

3.547 

3.52 

3.618 

3.614 

3.608 

3.551 

3.61 

3.632 

3.646 

3.634 

3.625 

3.588 

3.599 

3.566 

2.997 

3.43 

3.443 

3.486 

3.437 

3.422 

3.459 

3.517 

3.522 

3.278 

0.665 02lC02 bias 

2126/2013 9:40:00AM 5.148 2.398 3.254 -0.241 5.537 26.578 -0.014 0.709 

2126/2013 9:41 :00 AM '"!....;:,0."1 '"52 ..... -0;;..;,1 0;;;8:--.....;4~;::57:,;--.,;0;;;04;.:9,.....-;;.0"07:;;1:-....:;4:;;1 'i:.

84.;,9 ..... ....,0:;,.0"56:,;...-.;;0;.;.6:::52;:...,!NOX bias 

2126/2013 9:42:00AM 0.14 0.099 2.002 3.403 0.192 20.387 56.906 0.883 

2126/2013 9:43:00 AM 0.137 0.095 -0.017 9.461 0.044 0.368 237.799 1.434 

2126/2013 9:44:00 AM 0.137 0.093 -0.017 9.649 0.044 0.278 ! 241.362! 1.446 CO bias 

212612013 9:45:00AM 13.36 6.836 2.69 9.611 14.316 31 .067 238.414 2.345 

212612013 9:46:00 AM '"!"'1:':8~9"09~-"'9;;'6"'5;;8:---"'4;::.6;;;04"""-';;9;';5"'78;'---:1;';8;;.9;;'2;;'9-":;4"'1.'i:94';'4;-"';2;'4;;1"6"'78';"! 28.791 Direct Span 

212612013 9:47:ooAM 7.434 2.857 1.484 3.949 4.799 10.541 133.921 45.233 

2126/2013 9:48:00 AM! 0.128 0.07 -0.018 0.054 0.049 0.038 0.545 45.165 !Direct Zero; THC Mid 
Date Time 

212612013 9:49:00 AM 

212612013 9:50:00 AM 

212612013 9:51 :00 AM 

2126/2013 9:52:00 AM 

2126/2013 9:53:00 AM 

2/26/2013 9:54:00 AM 

212612013 9:55:00 AM 

212612013 9:56:00 AM 

2126/2013 9:57:00 AM 

2126/2013 9:58:00 AM 

0, 

% 

11 .323 

14.089 

14.088 

14.086 

14.083 

14.092 

14.096 

14.076 

14.051 

14.066 

2126/2013 9:59:00 AM 14.057 

2/26/2013 10:00:00AM 14.069 

212612013 10:01 :00 AM 14.077 

212612013 10:02:ooAM 14.062 

2126/201310:03:ooAM 14.057 

2126/2013 10:04:00 AM 14.04 

2126/2013 10:05:ooAM 14.049 

2126/2013 10:06:ooAM 14.058 

21261201310:07:ooAM 14.059 

21261201310:08:ooAM 14.056 

2126/2013 10:09:ooAM 14.073 

2126/2013 10:10:00AM 14.083 

2126/2013 10:11:00AM 14.067 

2/26/2013 10:12:ooAM 14.072 

21261201310:13:ooAM 14.091 

2126/201310:14:ooAM 14.067 

2126/2013 10:15:00AM 14.088 

2126/2013 10:16:00AM 17.256 

2126/2013 10:17:00AM 14.079 

212612013 10:18:00AM 14.058 

2126/201310:19:ooAM 14.059 

2126/201310:20:00AM 14.054 

2126/201310:21:00AM 14.042 

2126/201310:22:00AM 14.038 

2126/201310:23:00AM 14.04 

2126/201310:24:00AM 14.04 

2126/201310:25:ooAM 14.041 

2126/2013 10:26:ooAM 14.037 

2126/201310:27:00AM 14.04 

2126/201310:28:00AM 14.026 

2126/2013 10:29:00AM 14.033 

2126/2013 10:30:00 AM 14.032 

2126/201310:31:ooAM 14.026 

2126/201310:32:ooAM 14.038 

2126/2013 10:33:00AM 14.038 

2126/2013 10:34:00AM 15.775 

2/26/2013 10:35:ooAM 15.031 

21261201310:36:ooAM 14.08 

2126/201310:37:ooAM 14.056 

2126/2013 10:38:00AM 14.061 

2126/2013 10:39:00AM 14.072 

2126/2013 10:40:ooAM 14.074 

212612013 10:41 :ooAM 14.061 

212612013 10:42:00 AM 14.075 

21261201310:43:00AM 14.089 

2126/201310:44:00AM 14.088 

2/26/2013 10:45:00AM 14.078 

2/26/2013 10:46:00 AM 14.088 

212612013 10:47:00 AM 14.087 

212612013 10:48:00 AM 14.089 

2126/201310:49:00AM 14.087 

co, 

% 

3.216 

3.926 

3.932 

3.938 

3.938 

3.929 

3.927 

3.937 

3.945 

3.939 

3.943 

3.938 

3.936 

3.941 

3.945 

3.954 

3.954 

3.948 

3.947 

3.949 

3.942 

3.942 

3.949 

3.949 

3.941 

3.955 

3.943 

2.124 

3.954 

3.965 

3.964 

3.968 

3.976 

3.98 

3.983 

3.982 

3.982 

3.987 

3.988 

3.994 

3.993 

3.997 

4 

3.994 

3.995 

3.001 

3.43 

3.978 

3.99 

3.988 

3.984 

3.984 

3.99 

3.986 

3.979 

3.977 

3.98 

3.973 

3.973 

3.969 

3.968 

NO, 

PPM 

1.571 

2.18 

2.319 

2.227 

2.202 

2.17 

2.192 

2.393 

2.386 

2.284 

2.264 

2.263 

2.313 

2.286 

2.317 

2.28 

2.199 

2.359 

2.591 

2.553 

2.562 

2.459 

2.566 

2.564 

2.7 

2.831 

2.701 

1.263 

1.893 

1.858 

1.807 

1.947 

1.989 

1.952 

1.925 

1.88 

1.834 

1.848 

1.815 

1.957 

2.022 

2.037 

1.952 

1.852 

1.864 

1.575 

1.964 

2.418 

2.507 

2.382 

2.276 

2.294 

2.36 

2.429 

2.588 

2.59 

2.611 

2.603 

2.725 

2.9 

2.762 

CO 

PPM 

0.193 

0.597 

0.594 

0.619 

0.627 

0.596 

0.58 

0.628 

0.62 

0.666 

0.656 

0.634 

0.622 

0.721 

0.677 

0.655 

0.633 

0.621 

0.608 

0.637 

0.607 

0.595 

0.595 

0.607 

0.552 

0.559 

0.581 

0.383 

0.43 

0.447 

0.406 

0.438 

0.445 

0.429 

0.421 

0.454 

0.353 

0.339 

0.322 

0.288 

0.302 

0.343 

0.327 

0.287 

0.322 

0.312 

0.408 

0.582 

0.574 

0.577 

0.557 

0.568 

0.581 

0.565 

0.551 

0.548 

0.559 

0.542 

0.548 

0.52 

0.494 

0, 

% 

2.981 

14.022 

5.972 

0.061 

0.043 

0.043 

0.043 

0.043 

0.043 

0.043 

NO, 

PPM 

3.427 

25.31 

12.844 

0.293 

0.23 

0.197 

0.165 

0.148 

0.131 

0.114 

CO 

PPM 

1.914 

45.264 

42.25 

1.46 

0.279 

0.281 

0.279 

0.278 

0.276 

0.273 

THe 

PPM 

44.669 

14.026 

9.845 

44.354 

44.981 

45.507 

45.687 

45.821 

45.936 !THe Mid 

45.86 

8.805 14.02 16.019 37.918 

14.034 25.274 54.292 4.097 Start 50% COMP 

14.052 25.316 55.364 3.952 

14.044 

14.039 

14.035 

14.035 

14.037 

14.038 

14.041 

14.055 

14.059 

14.058 

14.056 

14.062 

14.044 

14.059 

14.041 

14.045 

14.034 

14.039 

14.034 

14.02 

14.011 

14.013 

14.016 

14.03 

14.015 

14.014 

13.989 

14.009 

14.001 

13.991 

14.006 

25.369 56.202 

25.549 55.571 

25.709 54.178 

25.792 54.498 

25.834 53.178 

25.875 52.678 

25.925 52.567 

25.999 51.727 

25.846 52.463 

25.848 52.853 

25.887 52.603 

25.835 53.211 

25.881 52.765 

25.812 54.297 

25.868 54.532 

25.92 53.301 

25.915 53.632 

25.92 53.316 

26.011 52.383 

25.997 52.894 

26.008 52.165 

25.986 51.964 

25.898 53.23 

25.934 53.279 

25.942 53.32 

25.958 52.914 

26.094 51 .824 

26.054 52.129 

26.087 52.209 

26.082 51.881 

26.009 51 .848 

14.007 25.986 52.28 

13.997 25.967 52.253 

14.004 26.015 52.011 

14.03 25.915 52.513 

14.004 25.992 52.359 

14 .02 25.876 52.895 

14.029 25.838 53.538 

14.028 25.895 52.921 

14.01 25.965 52.318 

14.028 25.903 52.544 

14.034 25.914 52.46 

14.033 25.902 52.459 

14.026 25.917 53.233 

14.035 25.915 53.047 

14.034 25.932 52.77 

14.036 25.927 52.998 

14.031 25.94 52.075 

4.024 

4.04 

3.686 

4.046 

3.577 

3.48 

3.509 

3.298 

3.433 

3.504 

3.446 

3.471 

3.37 

3.664 

3.923 

3.59 

3.732 

3.649 

3.46 

3.556 

3.388 

3.322 

3.607 

3.684 

3.263 

3.464 

3.27 

3.348 

3.454 

3.383 

3.309 

3.361 

3.385 

3.343 

3.352 

3.416 

3.551 

3.59 

3.393 

3.013 

2.718 

3.108 

3.219 

3.627 

3.515 

3.403 

3.548 

3.243 
Date Time 

0, 

% 

CO, 

% 

2126/2013 10:50:00AM 14.091 3.964 

212612013 10:51 :00 AM 14.089 3.967 

2126/2013 10:52:00AM 14.065 3.981 

2126/2013 10:53:00 AM 17.444 2.041 

2126/2013 10:54:00AM 14.075 3.986 

212612013 10:55:00AM 14.069 3.986 

212612013 10:56:00 AM 14.057 3.994 

212612013 10:57:00AM 14.063 3.993 

212612013 10:58:00AM 14.074 3.991 

212612013 10:59:00AM 14.059 3.998 

212612013 11 :00:00 AM 14.085 3.99 

212612013 11 :01:00AM 14.081 3.995 

212612013 11 :02:00AM 14.083 3.993 

212612013 11 :03:00 AM 14.088 3.995 

212612013 11 :04:00 AM 14.089 3.993 

2126/2013 11:05:00AM 14.085 4.001 

NO, 

PPM 

2.894 

2.921 

2.937 

1.341 

2.349 

2.319 

2.331 

2.368 

2.357 

2.327 

2.525 

2.658 

2.572 

2.664 

2.656 

2.691 

CO 

PPM 

0.476 

0.489 

0.491 

0.318 

0.462 

0.536 

0.515 

0.531 

0.533 

0.518 

0.516 

0.486 

0.504 

0.485 

0.495 

0.479 

O2 NO~ CO 

% PPM PPM 

14.037 26.009 51 .393 

14.031 26.031 51.119 

14.01 26.095 50.237 

14.002 26.069 50.1 

14 26.039 50.122 

14.016 26.03 50.096 

14.004 26.058 49.941 

14.01 26.011 50.829 

14.024 26.067 50.033 

14.009 26.061 49.976 

14.023 26.066 49.926 

14.02 26.066 49.799 

14.024 26.05 50.11 

14.03 26.106 49.595 

14.034 26.014 50.111 

14.025 26.05 50.318 

212612013 11 :06:00 AM 14.082 4.001 2.711 0.51 14.024 26.109 50.881 

212612013 11 :07:00 AM 14.084 4.006 2.941 0.5 14.017 26.065 50.857 

212612013 11 :08:00AM 14.083 4.004 2.866 0.538 14.023 26.07 50.118 

212612013 11 :09:00 AM 14.085 4.006 2.771 0.501 14.022 26.045 50.128 

212612013 11 :10:00 AM 17.135 8.308 0.597 0.304 16.935 8.545 38.073 

212612013 11:11:00AM'"1 ~18~.8:::3~~9~.7;':3:i9:--:-0;".0;f,0~8;--' -0.447 18.752 0.542 0.333 

212612013 11 :12:00AM 9.636 4.958 2.088 -0.36 10.536 15.036 -0.175 

THC 

PPM 

3.035 

3.135 

3.021 

3.024 

3.03 

3.038 

2.961 

3.177 

2.994 

2.841 

2.974 

2.97 

3.01 

2.992 

3.02 

3.013 

3.338 

3.386 

3.086 

3.062 

2.238 

0.654 02/C02 bias 

0.675 

2126/2013 11 :13:00 AM LI ~0-:,15:::8:-~0~~18;:;1:-~4:,:.5::5-::8_--:,-0:,:.0::;:2::,2 __ 0:,:,.::08:-:3:--:;4:;,1::50~5:--;;'0;'.0:i'56:,;-_-:0-:.6;:57,-,INOX bias 

21261201311 :14:00AM 0.138 0.166 1.018 5.437 0.214 13.254 97.513 1.01 

212612013 11 :15:00 AM 0.127 0.161 -0.017 9.553 0.044 0.312 240.052 1.444 

21261201311:16:00AM 0.112 0.158 -0.019 9.615 0.044 0.242 1240.6961 1.444 CO bias 

21261201311:17:00AM 14.579 6.516 2.813 9.597 14.71 30.079 236.998 2.368 

2126/2013 11 : 18:00 AM '"1""1;';8:': .8"'7"'4 -""9"'. 7;;,54;;;--..;4;:.;.5;;94;;....-.;;9;; .5.;;95 ..... ~1i::8;;,.8;"75,,........;;4.,.1 .';;88"'6;--:2"'4';;0';; .6';;22;;"1 26.528 Direct Span 

212612013 11:19:ooAM 8.11 3.397 1.752 4.21 5.79 12.342 141 .69 44.863 

212612013 11 :20:00 AMI 0.127 0.133 -0.013 0.037 0.048 0.036 1.131 44.882 Direct Zero 

212612013 11 :21 :00AM 13.484 0.176 1.355 3.03 5.294 11 .246 29.783 45.206 

212612013 11 :22:00 AM 20.669 0.197 2.493 7.277 9.954 23.815 91.666 45.585 

212612013 11 :23:00 AM 20.692 0.195 2.548 4.745 9.962 23.796 68.275 42.218 NOX/02 Direct Mid 

212612013 11 :24:00 AM 18.886 1.337 1.422 4.339 4.878 12.975 131 .055 1.211 

212612013 11 :25:ooAM 14.106 3.989 2.636 4.513 0.053 0.189 1 132.6631 1.087 

212612013 11 :26:00 AM 14.088 3.993 2.554 3.053 0.444 1.075 97.408 32.528 

21261201311:27:00AM 14.073 4.005 2.588 0.55 0.042 0.13 1.594 78.425 

212612013 11:28:00AM 14.064 4.007 2.614 0.531 

212612013 11 :29:00 AM 14.065 4.008 2.599 0.538 

212612013 11 :30:00 AM 14.087 4.001 2.513 0.533 

212612013 11 :31 :00 AM 14.081 4.005 2.505 0.539 

21261201311 :32:00AM 14.057 4.014 2.715 0.53 

212612013 11 :33:00 AM 14.068 4.01 2.673 0.538 

21261201311:34:00AM 14.059 4.014 2.652 0.532 

2126/2013 11 :35:00 AM 14.067 4.01 2.619 0.546 

212612013 11 :36:00 AM 14.065 4.011 2.653 0.55 

212612013 11 :37:00 AM 14.047 4.019 2.648 0.508 

212612013 11 :38:00 AM 14.071 4.011 2.624 0.518 

212612013 11 :39:00 AM 14.071 4.011 2.65 0.512 

2126/2013 11 :40:00 AM 14.052 4.019 2.596 0.521 

212612013 11:41:00AM 14.052 4.017 2.642 0.528 

212612013 11 :42:00 AM 14.049 4.019 2.567 0.525 

212612013 11 :43:00 AM 14.05 4.02 2.601 0.525 

212612013 11 :44:00 AM 14.054 4.015 2.578 0.546 

212612013 11 :45:00 AM 14.063 4.013 2.616 0.498 

212612013 11 :46:00AM 14.069 4.008 2.522 0.525 

2126/2013 11 :47:00 AM 14.067 4.009 2.532 0.491 

212612013 11 :48:00AM 14.065 4.007 2.526 0.481 

2126/2013 11 :49:00 AM 14.075 4.004 2.592 0.506 

212612013 11 :50:00AM 14.053 4.009 2.583 0.501 

0.042 0.11 -0.029 

0.042 0.091 -0.03 

0.302 0.205 -0.027 

0.298 1.173 2.648 

0.042 0.07 0.271 

0.042 0.066 0.25 

10.011 16.186 19.143 

14.006 25.554 51.032 

14.019 25.693 51.085 

14.006 25.81 51 .079 

14.028 25.87 50.57 

14.03 25.921 50.226 

14.017 25.96 50.384 

14.018 25.992 50.144 

14.011 26.013 50.025 

14.017 26.031 50.245 

14.018 26.081 50.091 

14.032 26.083 49.626 

14.034 26.066 49.629 

14.033 26.05 49.745 

14.034 26.063 49.886 

14.037 26.077 49.595 

14.026 26.15 49.302 

78.845 

81 .284 

84.144 

62.061 

49.039 

48.875 

35.516 

3.985 

3.702 

3.687 

3.462 

3.283 

3.33 

3.246 

3.232 

3.355 

3.322 

3.226 

3.2 

3.215 

3.21 

3.164 

3.078 

CO Direct Mid 
Date Time 

0, 

% 

2126/20131151:00AM 14.055 

2126/201311:52:00AM 14.048 

2/26/2013 11 :53:00 AM 14.046 

2126/2013 11:54:00 AM 14.037 

2126/2013 11 :55:00 AM 14.036 

2126/201311:56:00AM 14.029 

2126/2013 11 :57:00 AM 14.031 

2126/2013 11 :58:00 AM 14.028 

2126/2013 11 :59:00 AM 14.03 

2126/2013 12:00:00 PM 14.026 

2126/2013 12:01 :00 PM 14.025 

2126/2013 12:02:00 PM 14.024 

2126/2013 12:03:00 PM 14.028 

2126/2013 12:04:00 PM 14.03 

212612013 12:05:00 PM 14.029 

212612013 12:06:00 PM 14.021 

2/26/2013 12:07:00 PM 14.024 

2126/2013 12:08:00 PM 14.018 

2/26/2013 12:09:00 PM 14.025 

2126/2013 12:10:00 PM 14.024 

2126/2013 12:11 :00 PM 14.016 

212612013 12:12:00 PM 14.013 

2126/2013 12:13:00 PM 14.026 

2126/2013 12:14:00 PM 14.013 

2126/2013 12:15:00 PM 14.012 

2126/2013 12:16:00 PM 14.013 

2/26/2013 12:17:00 PM 14.023 

2/26/2013 12:18:00 PM 14.017 

2/26/2013 12:19:00 PM 14.022 

2126/2013 12:20:00 PM 14.051 

2126/2013 12:21 :00 PM 14.061 

212612013 12:22:00 PM 14.055 

212612013 12:23:00 PM 14.05 

2126/2013 12:24:00 PM 14.054 

2126/2013 12:25:00 PM 14.055 

2/26/2013 12:26:00 PM 14.073 

2/26/2013 12:27:00 PM 14.085 

2/26/2013 12:28:00 PM 14.098 

2126/201312:29:00PM 14.11 

212612013 12:30:00 PM 14.106 

212612013 12:31 :00 PM 14.108 

212612013 12:32:00 PM 14.109 

2126/2013 12:33:00 PM 14.118 

2/26/2013 12:34:00 PM 14.118 

2126/2013 12:35:00 PM 14.109 

2126/2013 12:36:00 PM 14.108 

2126/2013 12:37:00 PM 14.107 

2126/2013 12:38:00 PM 14.939 

2/26/2013 12:39:00 PM 18.841 

2126/2013 12:40:00 PM 7.485 

2126/2013 12:41 :00 PM 0.149 

2126/2013 12:42:00 PM 0.12 

2/26/201312:43:00PM 0.112 

2126/2013 12:44:00 PM 10.958 

2/26/2013 12:45:00 PM 18.896 

2126/2013 12:46:00 PM 12.772 

2126/2013 12:47:00 PM 10.02 

212612013 12:48:00 PM 10.027 

co, 

% 

4.004 

4.006 

3.998 

4 

3.999 

3.997 

3.994 

3.994 

3.993 

3.994 

3.995 

3.997 

3.995 

3.995 

3.994 

3.997 

3.995 

4 

4 

4.002 

4.006 

4.012 

4.006 

4.014 

4.017 

4.019 

4.013 

4.015 

4.021 

4.016 

4.012 

4.016 

4.015 

4.013 

4.014 

4.006 

3.998 

3.99 

3.983 

3.987 

3.987 

3.989 

3.984 

3.983 

3.989 

NO. 

PPM 

2.493 

2.606 

2.533 

2.625 

2.627 

2.51 

2.525 

2.539 

2.557 

2.433 

2.62 

2.552 

2.435 

2.471 

2.524 

2.479 

2.456 

2.522 

2.399 

2.4 

2.49 

2.512 

2.5 

2.501 

2.611 

2.526 

2.386 

2.441 

2.549 

2.554 

2.52 

2.591 

2.581 

2.574 

2.596 

2.54 

2.447 

2.444 

2.56 

2.638 

2.634 

2.56 

2.521 

2.508 

2.666 

co 

PPM 

0.476 

0.521 

0.509 

0.488 

0.486 

0.467 

0.476 

0.487 

0.477 

0.479 

0.463 

0.479 

0.503 

0.478 

0.502 

0.486 

0.528 

0.509 

0.494 

0.485 

0.525 

0.494 

0.505 

0.513 

0.528 

0.535 

0.512 

0.497 

0.518 

0.503 

0.525 

0.509 

0.505 

0.526 

0.507 

0.512 

0.531 

0.501 

0.514 

0.511 

0.509 

0.527 

0.508 

0.528 

0.507 

0 , 

% 

NO. 

PPM 

CO 

PPM 

14.028 26.15 49.026 

14.016 26.185 48.857 

14.023 26.193 48.705 

14.01 26.178 49.562 

14.004 26.292 48.511 

14.002 26.255 48.1 93 

14.001 26.251 48.309 

14 26.268 48.087 

14 26.264 48.024 

13.999 26.292 47.915 

13.992 26.267 47.732 

13.992 26.202 47.903 

13.99 26.2 48.033 

13.998 26.158 48.06 

13.995 26.159 48.221 

13.991 26.217 47.89 

13.996 26.132 48.246 

13.992 26.17 48.576 

13.998 26.18 47.937 

13.996 26.133 48.152 

13.986 26.167 48.551 

13.985 26.197 48.039 

13.999 26.102 48.782 

13.99 26.14 48.804 

13.985 26.185 48.644 

13.986 26.162 48.65 

13.998 26.127 48.493 

19.097 8.707 29.095 

20.418 0.285 1.772 

20.408 0.207 0.421 

20.393 0.166 0.216 

20.373 0.137 0.134 

20.368 0.12 0.129 

20.358 0.103 0.128 

20.343 0.099 0.127 

20.343 0.084 0.125 

20.343 0.083 0.125 

20.343 0.077 0.12 

20.343 0.068 0.126 

20.343 0.058 0.131 

20.343 0.061 0.134 

20.327 0.059 0.131 

20.299 0.057 0.13 

20.293 0.056 0.132 

20.287 0.048 0.127 

3.989 2.685 0.492 20.269 0.045 

0.042 

0.044 

0.046 

0.047 

0.043 

0.044 

0.044 

0.038 

0.039 

0.046 

0.035 

0.043 

0.126 

0.126 

0.13 

0.13 

0.127 

0.133 

0.131 

0.128 

0.129 

0.135 

0.1 3 

0.128 

0.131 

3.989 2.572 0.501 20.247 

5.691 1.775 0.615 20.235 

'-9"'."'72"'6:---""0."'006""''' -0.309 20.219 

3.754 -0.012 -0.317 20.203 

0.165 -0.012 o 20.194 

0.133 0.424 0.07 20.174 

0.121 -0.006 0.185 20.17 

5.943 -0.015 0.166 20.169 

9.757 -0.018 0.165 20.1 48 

6.591 -0.016 0.163 20.144 

5.176 -0.022 0.159 20.145 

5.176 -0.022 0.156 20.145 

THe 

PPM 

3.001 

3.003 

3.035 

3.453 

3.061 

2.832 

2.842 

2.853 

2.88 

2.887 

2.812 

2.845 

2.845 

2.904 

2.899 

2.862 

2.402 

2.586 

2.787 

2.867 

3.04 

2.947 

3.073 

3.112 

3.103 

3.051 

3.014 

2.657 

6.053 

5.339 

6.433 

3.585 

2.964 

3.209 

5.997 

3.177 

1.864 

0.986 

0.708 

0.654 

0.654 

0.655 

0.656 

0.652 

0.654 

0.651 

0.654 

0.653 

0.656 02lC02 bias 

0.655 

0.653 Zero bias 

0.653 

0.653 Direct Zero 

0.653 

0.656 Direct Span 

0.655 

0.65 Mid 

0.653 
Appendix C.3 Ammonia Data by SCAQMD Method 207.1 

R521 0729 C-l 
AMMONIA TEST RESULTS SUMMARY 

Client Gemma Parameter 

Location CPV Sentinel Fuel 

Unit 5 Data By 

Test Number CPV Sentinel-5-NH3-1 06-1 CPV Sentinel-5-NH3-106-2 

Reference Temperature, F 60 60 

Test Date 2/25/2013 2/25/2013 

Test Method SCAQMD 207.1 SCAQMD 207.1 

Sample Train 1-P&M 1-P&M 

Meter Calibration Factor 1.014 1.014 

Stack Area (sq It) 143.14 143.14 

Sample Time (Min) 60 60 

Barometric Pressure (in Hg) 29.60 29.60 

Start Time 11:35 13:04 

Stop Time 12:43 14:17 

Meter Volume (acf) 43.642 36.161 

Meter Temperature (F) 76.3 75.3 

Meter Pressure (iwg) 1.50 1.50 

Liquid Volume (ml) 99.7 83.2 

Stack 02 (%) 13.54 13.50 

Stack NOx (ppm) @ 15% 02 1.70 1.65 

Unit Load MW 106 106 

Fuel Flow Rale, hsclh 8,746 8,742 

Standard Sample Volume (SCF) 42.803 35.370 

Moisture Fraction 0.098 0.099 

Stack Flow Rale (dsclm , 60 of) 416,170 393,969 

Stack Flow Rate (dsclm , 70 of) nla nla 

Gas Constant (It-Ibl/lb-mole-R) 1545.33 1545.33 

Standard Pressure (lbfllt2) 2116.224 2116.224 

Molecular Weight NH3 (Ib/lb-mole) 17 17 

Specilic Molar Volume (lt3/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) 3995.65 3437.99 

Mass NH3 (mg) 3.996 3.438 

Mass NH3 (Ib) 8.80E-06 7.57E-06 

PPM NH3 (Ilue cas) 4.6 4.8 

PPM NH3_@ 02 Correction 3.68 3.81 

Ib/hr 5.14 5.06 

Ib/MMscl fuel 5.87 5.79 

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, MC, RM , JM 

Averace Limit 

13.52 

1.68 

4.7 

3.75 5 

5.10 

5.8330 
AMMONIA TEST RESULTS SUMMARY 

Client Gemma Parameter 

Location CPV Sentinel Fuel 

Unit 5 Data By 

Test Number CPV Sentinel-5-NH3-81-1 CPV Sentinel-5-NH3-80-2 

Reference Temperature, F 60 60 

Test Date 2/25/2013 2/25/2013 

Test Method SCAOMD 207.1 SCAOMD 207.1 

Sample Train 1-P&M 1-P&M 

Meter Calibration Factor 1.01 4 1.014 

Stack Area (sq ft) 143.14 143.14 

Sample Time (Min) 60 60 

Barometric Pressure (in Hg) 29.60 29.60 

Start Time 16:42 18:07 

Stop Time 17:48 19:14 

Meter Volume (act) 36.365 34.041 

Meter Temperature (F) 70.8 66.4 

Meter Pressure (iwg) 1.50 1.50 

Liquid Volume (ml) 69.3 76.6 

Stack 02 (%) 13.98 14.04 

Stack NOx (ppm) @ 15% 02 1.33 1.75 

Unit Load MW 81 80 

Fuel Flow Rate, hscfh 7,078 7,085 

Standard Sample Volume (SCF) 35.871 33.858 

Moisture Fraction 0.082 0.095 

Stack Flow Rate (dscfm, 60 of) 349,945 332,898 

Stack Flow Rate (dscfm, 70 of) n/a n/a 

Gas Constant (ft-Ibfllb-mole-R) 1545.33 1545.33 

Standard Pressure (lbf/ft2) 2116.224 2116.224 

Molecular Weight NH3 (Ib/lb-mole) 17 17 

SpeCific Molar Volume (ft3/lb-mole) 379.50 379.50 

Mass Conversion (Ib/ug) 2.20E-09 2.20E-09 

02 Correction Factor (%) 15 15 

Mass NH3 (ug/sample) 1893.24 1278.55 

Mass NH3 (mg) 1.893 1.279 

Mass NH3 (Ib) 4.17E-06 2.82E-06 

PPM NH3 (flue qas) 2.6 1.9 

PPM NH3.@ 02 Correction 2.21 1.60 

Ib/hr 2.44 1.66 

Ib/MMscf fuel 3.45 2.35 

NH3 EQUATIONS: 

ppm NH3 = (mass NH3· Gas Const • RefTemp· 106 )/(Sample vol. • Press· MW) 

ppm NH3 @ 02 correction = ppm· (20.9-02 Corr)/(20.9-%02) 

NH3 

natural gas 

AA, MC, RM, JM 

Average Limit 

14.01 

1.54 

2.2 

1.91 5 

2.05 

2.8984 
AMMONIA TEST RESULTS SUMMARY 

Client Gemma Parameter 

Location CPV Sentinel Fuel 

Unit 5 Data By 

Test Number CPV Sentinel-5-NH3-55-1 CPV Sentinel-5-NH3-55-2 

Relerence Temperature, F 60 60 

Test Date 2/26/2013 2/26/2013 

Test Method SCAOMD 207.1 SCAOMD 207.1 

Sample Train 1-P&M 1-P&M 

Meter Calibration Factor 1.014 1.014 

Stack Area (sq It) 143.14 143.14 

Sample Time (Min) 60 60 

Barometric Pressure (in Hg) 29.47 29.47 

Start Time 8:30 10:00 

Stop Time 9:37 11 :09 

Meter Volume (acf) 37.779 36.626 

Meter Temperature (F) 71 .3 74.9 

Meter Pressure (iwg) 1.50 1.50 

Liquid Volume (ml) 80.2 77.6 

Stack 02 (%) 14.15 14.13 

Stack NOx (ppm) @ 15% 02 1.83 2.12 

Unit Load MW 55 55 

Fuel Flow Rate, hsclh 5,384 5,400 

Standard Sample Volume (SCF) 37.068 35.693 

Moisture Fraction 0.091 0.092 

Stack Flow Rate (dsclm , 60 of) 259,659 261 ,782 

Stack Flow Rate (dsclm, 70 of) nla nla 

Gas Constant (It-Ibl/lb-mole-R) 1545.33 1545.33 

Standard Pressure (lbl/lt2) 2116.224 2116.224 

Molecular Weight NH3 (Ib/lb-mole) 17 17 

Specific Molar Volume (lt3/1b-mole) 379.50 379.50 

Mass Conversion (Ib/ug) 2.20E-09 2.20E-09 

02 Correction Factor (%) 15 15 

Mass NH3 (ug/sample) 549.19 587.91 

Mass NH3 (mg) 0.549 0.588 

Mass NH3 (Ib) 1.21 E-06 1.29E-06 

PPM NH3 (flue gas) 0.7 0.8 

PPM NH3 @ 02 Correction 0.64 0.71 

Ib/hr 0.51 0.57 

Ib/MMsclluel 0.94 106 

NH3 EQUATIONS: 

ppm NH3 = (mass NH3' Gas Const' ReI Temp' 106 )/(Sample vol. • Press' MW) 

ppm NH3 @ 02 correction = ppm' (20.9-02 Corr)/(20 .9-%02) 

NH3 

natural gas 

AA, MC, RM , JM 

Average Limit 

14.14 

1.97 

0.8 

0.67 5 

0.54 

1.0004 
""0..-.,. DeI/a~ __ 

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: (10v\tI\t\ LOCATION:>K~"-Itvd.­

DATE: 1. -Z~(1 'l 

RUN NO: > -'2/ $ ell-- ,\j 1-\1, - ~;? - I \CMI't \ 

OPERATOR: I }'" 

METERBOX~N~O~:~j~P~ == ________ __ 

METER IIH@: I· g b·? 

METER Yd: I' I <-( 

STACK AREA, FT~ I~ ('f ' 

TRAVERSE POINTS, MIN/POINT: c;;(i z.. 

IIH= "jA X LIP: 

Probe ondition, pre/post test: i/ ../ 

Silica Gel Expanded, YIN: N 

Filter Condition after T est:-

7

- /--+""'Ir----

Check Weight:, ___ -"'-

Meter LIP 

Point Time Volume, ft3 in, H,O 

,J 'S 1I 1,~ i <;6. -'1r'&. L-i" LZ. 

Z 11'\ " :3 /, (& 

i \\~) ;.I I I <"" 

0 \1 '<" If) iio. <\<,\S' II / ' </ 

\ 7 I I \ ')-., I ( .... :l . ('\~\) 1"1' I,.::' 

" Xl S-g I? /' '-, 

I 1"0"> ;?, I ,' 

() ( "",{ I ':It,, u'\'l I / '1 

I' 7 \ I .. i IY" ~-"!. "i <," (/ 

1- '.1,(" 'I (,7 

I 111\ :;I (, q 

D 1.11 \, 1\7 .. :5"\ I iL 7 

If ~ \ i 'l-'h 1 ' \ I, )"'1 <I /' / 

2- I t\'\ J / 7, 

, Ihl ,} / J 

,(j 11.""1 L,JL c"ln , (/ 

, 

Average: 

\ " 

AMBIENT TEMPERATURE: 5- rp 

BAROMETRIC PRESSURE-: -oiU--; 'I ::"? --------

ASSUMED MOISTURE: __ -'-"'--'---' '7.'''o _______ _ 

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

O,IIV fh\C" QIO,2-7l"67 

PITOT TUBE COEFF, Cp:--"~'-'I "'~'\-,-,,-_______ _ 

PROBE ID NO/MATERIAL:...clr"',"'4.....;>l S(!LC _______ __ 

PROBELENGTH:.~~ ~,-~---------- NOZZLE ID NO/ MATERIAL:_'-'.'.-,"' ________ __ 

NOZZLE DIAMETER: __ --""<'If:-i<-' ________ __ FILTER NOITYPE: ,I, /, 

PRE-TEST LEAK R=-A'""'T"'E=-:-: -"""""-'\--'-""k--'C:-::F""M""@"'"""""- , ,-::---'-in-, 7H;--g-, -

POST-TEST LEAK RATE: : :, C' 1- CFM@ ",- in, Hg, 

..3:..- 0 i ,v 11 / ~01 7 '1>, S- 7,-(1,L 

> R~i' l-..t b 3D, 0 ("2-q;, ~ 

'cl { ['7, q L{ 6.cj ~lJ v 

l (~ "OJ \t 0,0 I 0 () 

PITOT LEAK CHECK - PRE: f / POST ~~" _ __ 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN~ 

SAMPLER ~ "-

SAMPLE CUSTODIAN~ Total: _________________ _ 

IIH 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, H,O 

T),.)- ..ILl).. '" I "" ko 'l ', 1;\ )0 '!'<:: ,c;,' 

77'7 

'7') l f 

7J2 I . ) '72 (( -bCf(l;lr 11 IX ';"<> 

1'5 

?,b 

7') (/ 

I ' '\: "7 "7' 5' 6? 1>=> 'I \ ,, ·0 -7,<-

--; ? L" 

-7 '3 "I , ,S 7-~ /71.{ n . ( '{ s-: ~', c. 

'--'7 ___ 

/'; \ 

J '-

Comments: ____________________________________________________________________________________________________________________ __ 

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

DS834049 

Master Document StoragelFormslDatasheetslField Datasheets 
I 

Oe/1a1J.. 

... .,...".--

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: }' \' V I (I AMBIENT TEMPERATURE:_,fS"'''=-r ,--___ ___ _ 

LOCATIO : '-;UV't ",1<- \ BAROMETRIC PRESSURE :--i2<;o,-oi--'-''''----____ __ _ 

DATE: Z.I,,-{( \ 

RUN NO 2 1'5"0<-- ",,( t - "'=>- '--

OPERATOR: }", ) 

ASSUMED MOISTURE: ~ Q'1. ~,1r\4 1-- PITOT TUBE COEFF, C""p'--: -c, =-"..;",:-'-'----------

PROBE 10 NO/MATERIAL:.~';-:,-, · ~<-, ' ,-,,---<'",-,"' ______ _ 

METER BOX No:-":-'C-:',"-, ______ _ 

METER 6H@: \ '<,. " 

METERYd: ~- ~A-------

STACK AREA, FT': 1,2- I-I. 

TRAVERSE POINT"'S"', >-,M~IN+I=PO'::--:-:-IN7.:T:-: --:"=-' {I-,-

PROBE LENGTH::-:-:o!:,.'::'=_---:;;;,--_______ _ 

NOZZLE 10 NOI MATERIAL:--,'-'''-1'''A- -'--_______ _ 

NOZZLE DIAMETER:_----'1V""0"'''-''----________ _ 

FI L TER NOfTYPE:==---'-N"'I:-':i:'----::-c==_--,---_-:-"77_ 

PRE·TEST LEAK RATE: : "" c 'S- CFM@ 1-' in. Hg. 

6H= /VI J,- X 6P: / ./ 

Probe Cbndition, prelpost test:_v-,-' __ _ 

Silica Gel Expanded, YIN : 00 

Filter Condition after Test:--''''ii{.,,----

Check Weight: 7 

POST· TEST LEAK RATE: ~-<O.:-; CFM@ '" in. Hg. 

PITOT LEAK CHECK· PRE: ./' POST: .r'" 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN ,/V'6L--

SAMPLER 5M SAMPLEC~U~S~T~O IA ~-,~ --

Meter 6P 6H Stack Probe Filter Imp, Out 

Point Time Volume, ft3 in, H,O in, H,O Temp, OF Temp, OF Temp, OF Temp, OF 

II'- '-, hJ.\ Zol\ 1,lt\ '" {, ,.;;. 1 • -:;- 7 '? {, 'v ( r" 1\1 f 't - \:iY 

, 11" 'I .) I. ') '7') 7 , nit "- /. <-f '7 ;. -;- \ 

' J I ~ 1'\ - \) ,b?-I II /, (.. -' J c... I 

7 " 11 2--: 'h t.,;<./. .j , 7_ I ." ~ J 7 I (,.,2, 

v p,z. 1- '7 i /? "l? "'- i , f);' 7 ;) I 0 -, ~l..) I I , / 1...111...- '! n , ~\L. I { " "1 ", i i 

Imp. # Contents Post· Test· Pre·Test = Difference 

0,1 ,\/ ill >O~ "6 S'6,7 b'63,b 

L O,I'V 1-1,50'1 0b'--!,Q b..SJ:7 r; 02, 2 

l ~~~ ,nq, '1 ')-71~ 

:L (,0, qt.r'b,1 q i.-f 0,1 

\..1'1.. !'ll. \-/ " 0 lUll 

Total: _____________ _ 

Meter Temp, OF Vacuum 0, P. static 

In Out in. Hg. % in, H,O 

l~ 1b :>-0 1 ~ 

\ 

1y " 11 <) ,) 

~ "-. I ~"'1 Ht·5'>L LI I, / I , , ''1 -( '.' I I V 110 1" 1'1< "0 

1 1 7~ "- h I ' :.,L 'If I I 1 

I [ ,'J'-I ,1 [, " };l/ I I 

) "s't' }.,I.il ;& ,-(~ I I I 

Ai 'Z-- ;:" \ ~.I'I <, (. ,::; I ~ '7 7 I U 1'1 1<; ! \~ " 

v ,yo, -) ). <- "1 ; ,~ \ 

\ 1'1 17 ? I c 1-,'1 

:1 11411 ~.( ·"I. 1 7., 1 I I 1~, I \ \ , 

I V \ \ 

Average: " J " .1. 

Comments: ______________________________________________________________________________________________________________ _ 

,I last revision 1/25/2013 Page __ of __ 

05834049 

Master Document 5toragelFormslDatasheetslFieid Datasheets 
Delta/j. 

.. ...-. ........ ,-

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: '-1C:;MI\\fILOCATION:YN\ N3 ___ 

DATE: 1-(7.\ lit, 

RUN NO: <, -., fe, < - "':1\-3 'TO;; - \ gmA ~ OPERATOR: ,,/'''' -

METER BOX NO:"I'--(,,"--"'----_____ _ 

METER ll :._--"'!."'";'-~ _ _ _____ _ 

METER Yd:::-:->I.:., ' ' "' .:.L---;-,-,--_ _ __ _ 

STACK AREA, FT': i"" IL!, 

TRA VE RS E POI NT:'Sc-, L::M"'I N'-,-/ "'O"'I N:>: -==-: <-, ! z..-

llH= V / . .l- X llP: • /" 

Probe Condition, pre/post test:;, ~ 

Silica Gel Expanded, Y/N:_ --c.. 'v_,,--- -

Filter Condition after Test: y?" 

Check Weight: ,Z 

Meter llP 

Point Time Volume. ft' in. H2O 

/V " \\" '12- 1.XJ .'11'' -.I .p.Ll 

L I 10,7 ; .' ? v"' 

I 1 (',-z.. ;). ·SI 

G If. <; 1 ?-SW. , l(1 I .., ~ ...... ;, 

I~ " i &;')<>1 l. 'LY. rL'i , ! ,I"i 7 

Z- 171.0 '-i --; I u 

1 I '1," t ., , 2-

.9 1 1 I '-{ ')·=-7·IA( I I ., 

.> 

~ " n 1,,' '1"'71(,1 ;,L ~ '7 ' 

7, "2-1 .", j . z.. 

I 11 'o , ,. \ 

0 17)\ ';;1 b. il'? -/ I' "2. 

,J " 11 "7 $I~1. \3 ,/ , V'.,? f 

1, 11Z,:) -, tf'J 

, 11 4 l, 2- I · I 

11 11'1 S ':-:..::. "S . .1-;1 / t, :lAveraQe: 

AMBIENT TEMPERATURE :._ 6,,: " ,--______ _ _ 

BAROMETRIC PRESSURE: .... "''-'-.'T(.,,~,-----_____ _ 

ASSUMED MOISTURE: ~ 117% 

PITOT TUBE COEFF, C:-p-: "":;,-:c,-'''''---'-'''--"'''----- ---

PROBE ID NO/MATERIAL,..: i&?=:o;S"-~-""'-.;--"Q'----____ _ _ 

PROBE LENGTH: & • 

NOZZLE ID NO/ M"A-=T-=E""R"'IA--L-:u-,'''''l''''<\--- ---- --

NOZZLE DIAMETER:---;;cNTiC-f_' ___ _ ___ __ _ 

FILTER NOfTYPE: JC(~ PRE· TEST LEAK RA=T"'Ec': -: "", ;-. . ,::O--- C"'F""M-;C@;OC-- I -:=E~----'"----;. H7 g-.-

POST·TEST LEAK RATE: :{ ./ .. u~ CFM@ , " in. Hg. 

PITOT LEAK CHECK· PRE: ~ POST: 7 

Imp. # Contents Post-Test· Pre·Test = Difference 

(nV 11,) 0'1 1) '3 1.1' 7 ~ 'iVi 

'L o·tlv' \1, S0'11'l'l.> '7 "/J .1;, 

., e""'r 1--, 630. 3 00.2. 

7 

q 210.5- l >-Cn, if)1,. 1 

Lit- pr: It'1.-U [00 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN, ,-,-,!.~ __ 

SAMPLER >6 

SAMPLE CUSTODIAN ... 6-"-",,L-_ _ _ Total: ____ _ ____ _ 

llH Stack Probe Filter Imp. Out Meter Temp. OF Vacuum 0 2 P. static 

in. H2O Temp. OF Temp. OF Temp, OF Temp, OF In Out in. HQ. % in. H2O 

·~ 726 I vr A 1./ (!J.. 00 "\ 1-"'1 ht' l ,>", • <: Y 

72t., , 7i-~ , 

72... 7 I 

i .~ ;129 (, ,::; It "7 <- y .", I 

·7 "-c I 

72... </ I 72 ~ 1 

\, . '/~. , 'S'-:{ '1Z-. ,

'- "0 I 

7 },/ I 

7;:' v I 

72-'1 I 

( . , -'''u 57 ,:> l~ ')0 I .-'f -; I ~~ -t<r. ~ ].:;". , ~'- 1 .,.....,.:; t } I 

"' .. '1 ~I I II / I , 1 ! .,.... \'.1 

'0... 

Comments: ____________________________________________________________________________________________________________ ___ 

Date of last revision 1/25/201 3 Page _ _ of __ 

DS834049 

Master Document Storagel Formsl Datasheetsl Field Datasheets 
DelIa~ .... ---

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: ( -eN, (",(1 

LOCATION: ,, ' Nil"',", l 

DATE: '-11S:J./) 

RUN NO::;:;: , \ -s;)<., ~ -tvh-] l.i: - 2.... 

OPERAToR: ~ ________ _ 

METER BOX NO:..,'!;-,,f """-'-_____ _ 

METER "' H@:--,\~,-, '(,-, . ,'-______ _ 

METER Yd: I E':\ cl 

STACK ARE""A7",*F"'i9 : -,-yAY-·"-1 ."1----, -

TRAVERSE POINTS, MIN/POINT: 'S ( ( L., 

H~ r",j( ~ X 6P: / / ' 

Probe Condition, pre/post test_-:-+, __ _ 

Silica Gel Expanded, YIN: t-J 

Filter Condition after Test: .. J( 

Check Weight ./ 

- > AMBIENT TEMPERATURE: ') (; 

BAROMETRIC PRESSURE-: ,,'-"'-------

~ ASSUMED MOISTURE: __ --'I.!-",=--____________ _ 

. PITOT TUBE COEFF, CP:'--LO",,"o..·-i-' --,-;c:;-------

\0 PROBE ID NO/MATERIAL j;t:», .. ?"'., .... 4..ct..:,. .. "' ,>(' _______ _ 

PROBE LENGTH:="C'='=--:--;-________ _ 

NOZZLE ID NO/ MATERIAL:..:."'.:.1¥1>"--_______ -'-

NOZZLE DIAMETER: __ .!.: r>'j, 1;::1.l _ _______ _ 

FILTER NOITYPE:==--"c{ii';7.c;::J..- =----===-___ ,--,-,-_ 

PRE-TEST LEAK RATE: : I' .,)\ CFM@ 1£ in. Hg. 

POST-TEST LEAK RATE: : .. ,." h, CFM@ \ "" in. Hg. 

PITOT LEAK CHECK - PRE: ,/ POST: L---' 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN ,'1 v 

SAMPLER V1 SAMPLEC U~S~T~0~D IA~N~--

Imp. # Contents Post-Test - Pre,Test ~ Difference 

_\ ,W II, Jt'1 '65'), ~ (,'07,Q 

~ a·IN I~ r,t}y (, 5"1, 7 105'1> _.5'_ ..,--

I /1"_ l t:.~p"j 7 '1<6,::;' ,4"T~(/1 ,)71, '> 

"I ~ G 1S(,) ? '1'6 _, 7 __ 

L IL ,lr. ).1,0 __ _ \ 00 __ _ 

Total: ______________ _ 

Meter 6P 6H Stack Probe Filter Imp. Out Meter Temp, OF Vacuum 0 2 P. static 

Point Time Volume, fI' in. H20 in. H20 Temp, OF Temp, OF Temp, OF Temp, OF In Out in. Hg. % in. H20 

>J <., 1~"1 .?zr_i"t7 ' 7~ l " 7J(., " 1'''- "II~ ~-Y' c" 'Or", ::>.,,," ·, -7· -;> d/2... .• ,<",c, 1:7""1 

I I i I 1 ,2. ( , t' J ?<r',') , \ 

o I~Z<" -~ , It.\' , /,2- ,/,yc, I I 

c:, L \ { 'I " .;.;; ),,"'tllI i,l '~, ", 1 . " ? 3 b I I '"5'5" i, b /.::,-' ::, . 2, '1.- ''i ',.7 / . 7_ '7J .cr I 

I lOs' r, '7 '7",;> I I 

o " ,-\ ,) <''1"2 'j''\~ I I' '-i '7 ~ I I ,e;; '1, I"'I?, ,'-Il'l'\~ <j ,., q 1·5' -7 <{2. ( "-4 ./.:/;-- Co( :",;' 

1. 'is 4'1 f ,"1 Z. 7'-1'" , 1 \~':;2.. :I- / . U '7cr 2-. 

v \~ ,J /." :'!, 1;~ ~ I 1,2-7:?<7 I 

rv '> \ ':/\- "1 '·'0,' I'\Z 'f l'f '57 \. '> lYb ' c-"'\, ~\ 1:."'- '> " 

"' 1'10'" (., . 7, ?t',- :s 

I 1"1-/'" 7-- ,.,C; '7"r / 

,? k'l l cJ >S'l. ,,,' I ,[<;:~ '7'1'6 , 'I ~ 

- ~ 1'>" '" II 

Average: \. /' 

Comments: ____________________________________________________________________________________________________________ ___ 

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

D5834049 

Master Document 5toragelFormslDatasheetsl Fieid Datasheets 
WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: '/jd'/I""~ 4-

LOCATION: '> N'O" ,,&iDATE: 2{ "'-<>!J, ~ 

RUN NO:t:.-.;-!,-1'Z -,.j '"', - s;.:;> - \ 

OPERATOR: ~ 

METERBOX·~N~O~:~\~'~~------

METER LlH@:_i-::-i~-j(,Tij-' ______ _ 

METER Yd: \ . 0 ''1 STACKARE~A~,~F~T2r:~+'~~-~~'----,---

TRAVERSE POINTS, MIN/POINT: ;, ( Ii!.-

LlH: /'J/ ,,,,. X LIP: _ /' 

Prob;aQ;;d;tion, pre/post test:....!:V; .."f.V __ _ 

Silica Gel Expanded, YIN: N 

Filter Condition after Test: fJi!i' 

Check Weight: Z 

Meter LIP 

Point Time Volume, ft3 in, H2O 

,r.,) ;~ ,-..~ ~~ .Irl:. 'tZ; "1 --4 ' ~ 1 

1- lli ,_) 2 ' i 3 

1 03L\ ,:10 '2 ·84 

IJ c,-:i'\ '5' 7, ,0 ~'\ , ~ ~;' 

'> 1 (J ~4'1 'i-'~~ ,.c )<'1. '-I . If 12 ~ c 1"2.- .;:. ·r S' , 

, [;'3~7 ? Ie'} 

o <;.~,?1-- LNZ '{Ir I · itI( I ~ 

~ -~ (.,,-\,:, '-I 'i yz. <{ I '" '-i J j(d 

L ::)''1'"".,) \ '~ erA " ~ 

1 /"}:"\ \q -;z.. · (07 

.;, ~);'\ \ \ L~'St . . ':"'''5 I i ./~ 

1/ ; O-P:l. u.. ~\ . -;? .... '-{" ·-i ·30 

1-- "'11.1 '3 · 41 ; eLl'll. :2 · '-I < . 

o ''117 "f{" I,1 \ ~ I . --1-, 

Average: 

AMBIENT TEMPERATURE: hi" 

BAROMETRIC PRESSURE :--,",-- , ,;-'u. i ::-,~~~~~~~~~~~~~~= ASSUMED MOISTURE: .~ 'l ('" PITOT TUBE COEFF, C'''p-: o:-"',<~;-;"':;;=----------

PROBE ID NO/MATERIAL :..>\2~:x~?,> '5 'O P~ ______ _ 

PROBE LENGTH: (, , NOZZLE ID NO/ M"A"'T::':E'=R-IA:-:-L-:7>- ...jT"i 'l'l'a---------

~1~~~~EN~~~~~~R :--Mi.:Kft/rl"',-------------

PRE-TEST LEAK RATE: : ,Q, ":,, CFM@ '> in, Hg, 

POST-TEST LEAK RATE: :", "''f' CFM@ ' " in, HQ. 

PITOT LEAK CHECK - PRE: ,___ POST: ,/ 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN k\ -:-(---

SAMPLER ''''' SAMPLEC~U~S~T~O~D~IA~N~J~~'C--

LlH Stack Probe Filter Imp, Out 

in, H2O Temp, OF Temp, OF Temp. OF Temp, OF 

\' 7 V-> '-I '\/' '\- IVj/L ~-.l 

1(,; (, i 

'1 t,,) l) 1 

7 (pl(, I 

i ,', '') b<- I 

1 'I <> '" 

711 

/1 () 

\ . ':; "'17). /,00 

1Jq 

777 

/'l~ 

\. '" "71, I C' ( 

777 I 

"77 , 

!7 (, 

\ V I ! 

V 

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

\ /l,I/J H] iO'f <6'15', L l''J 7. ?-- --

~ O,IN liz SO'I 7'i1,CP J"14,3 

') t--1 ~++ 6'2,/,'6 b 2-''1.} 

'-1 > ' L'J qn ,) q 36. t 

~tt DJ. \71,.0 iOO 

Total: _________________ __ 

Meter Temp, OF Vacuum 0, P. static 

In Out in, Hg, % in, H2O 

I,/,'" ID ',;:",v .,.7. X 

-'1z. TL :s_o 

~ I ) .-,'~ 'I."" 

0", '\ <;-:'" 

i 

'-\ 1 

"'V 

Comments: ____________________________________________________________________________________________________________________ __ 

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

D5834049 

Master Document 5toragelFormslDatasheetsl Fieid Datasheets 
WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: ( j?'I1""" f-lLOCATION: r~d 1 e. i 

DATE: Z 12.!-,' (I . 

RUN NO:)-,> J>1f..- -tJltj-S;::> -1-

OPERATOR: S/., METERBOX7N~0~::17t~ -,~ __________ _ 

METER dH@:-'Ic:..':-S"..""' C' ______ __ 

METER Yd:=+" ~I i:r---=,.---,"'---- STACK AREA, FT : I y·'z·1 q TRA VE RSE POI NT~S,-J, ~M~I N7,,/P;';:0~I:-;No;cT:-s-==-7h/c;

H~ vl->- X dP: / ~ probeco;;d;tion, pre/post te sl:-,~V,--__ 

Silica Gel Expanded, YIN: fJ 

Filter Condition after T eSI: __ 1.:"'71\:.-__ Check Weight: ,/ 

Meter dP 

Point Time Volume, ft' in. H,O 

"..J 3 \C'), ., LH,'U,-! '1 '-i 30 

l. lO-Q '> ., 

-" _c/l1 , 10\0 :... ,4S 

<;, 10 ,< '{l l l':' I . , ( -

') 'J.. \~ '-<'), '\ '1 \, 't f ( . i 

i u2~ , o t.v f.£J 

I \c ~~ 'A - J_ 

"D Vel"';:' ~'" I . 1'\ L I . I (./. 

p; " 1. ,',7 ~ti, \1.\'--- /; .I..~ 

i_I ,11 L ~ , f'\ f 

i " d'-I''{ ,1 Y Li 

" J;:"' , _ Wi':) . , '3 () I , v.v . 

oJ " i ,0:' 'j- ltC', ",. I ~ 0 

" '1"7 

i- 1::>9' .. , 'y ~ 

, \ I D't / w'-! 

" I ,')'~ ' ............ '-'\ I .... 11) J (~0 

AveraQe: 

AMBIENT TEMPERATURE: bY" 

BAROMETRIC PRESSURE:-: ~::,-:,';- \ -. -:-::7;---------

ASSUMED MOISTURE:.-c-:--::-=::J'!'--'-PJjlo'----------

PITOT TUBE COEFF, Cp :~ 

PROBE ID NO/MATERIAl;J.QQi<?l=II _______ __ 

PROBE LENGTH: b NOZZLEIDNO M~A~T~E R~IA~L-:-'~ {~~----------

NOZZLE DIAMETER: __ --'-'/c:;.,'i.;:,,'--________ __ FILTER NOfTYPE: ;vl !>-

PRE-TEST LEAK R::-A:-:T;:;E:-: -'-: "',,-. ~"'<=---C"'F;o;M::-@=-"/----,--in--,. H:-:-g-.-

POST-TEST LEAK RATE: :t •. ·J " -( CFM@ i'- in. Hg. 

PITOT LEAK CHECK - PRE: , / POST:~ 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN,...:..:,M"'C=-___ 

SAMPLER cl /VI 

SAMPLEC~U~S~T~O~D~IA:-;N~}{AL,----

dH Stack Probe Filter Imp. Out 

in. H,O Temp, OF Temp, OF Temp, OF Temp, OF 

\. S- 77« tll ~ f'.,.',A 0'\ 77 (> 

7?w 1 

77<; \ . c:: '77c.- I , ~ S 

'/ i~ 1 

1'7/ I 

7 "77 I 

\ ,<;,"" """7-) I (,'! 

''11 6 I .kt7:1"'i-. 

'77if .1 

''''/' 1./ \ l 71:-" I (. '-\ 

-., -,'- I 

...... -~ 

'" ... .,t \ 

\ 1 

" 

Imp. # Contents Post-Test - Pre-Test ~ Difference 

0l.v 1-1, SO,! 1,55',/ b'61,7 

L o IIJHJ"i.1 {,5"'O.l b 51, Z. 

;. f;: .... ? 't--.-t $'1«,0 :;'-71" 1 

cl (.&1. 1012, 1 : (?03,Z- -

l(L ~'i- It,U / vO 

Total: _______________ _ 

Meter Temp, OF Vacuum 0 , P. static I 

In Out in. Hg. % in. H,O 

-Ii It '><:J -r1. ... 

...l. 

'l 'J. J.S ,s.-.o 

15'">, -) s :S . :> --

~ ~-"\-

' IL /12 '5:. ? 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 1/25/20 13 Page __ of __ 

D5834049 

Master Document 5toragelFormslDatasheetslFieid Datasheets 
llellab. ""_ ......... - ... 

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: /;'g",,"'fr 

LOCATIOW' SIe /V"t,,j oil 

DATE: && -s-I(l 

RUN NO:&~ ;CTI:- .........,b-~ fr> 

OPERATOR: ,--.. 

METERBOXNO:.~\f~ ____________ __ 

METER dH@:.,-"I .... 3''' ,0''-____________ _ 

METE R Y :=-:-"" S":i'~------------­ STACK AREA, FT : 

TRA VEI~ E POI NTO=S"-, M:-::-:-I NC::/P"'O"'I N"'T=-:£.JJiO -:--'-'--

dH= N XdP: 

Probe Condition, pre/post test:. _______ _ 

Silica Gel Expanded. Y/N:. _________ __ 

Filter Condition after Test: __________ _ 

Check Weight: _________ __ 

Meter dP 

Point Time Volume, ft3 in. H2O 

I 

/ /~ 

/ \ /M 'M.j 

Y /A. p 

v"'\ / 

AMBIENT TEMPERATURE: _______________ _ 

BAROMETRIC PRESSURE: ________________ _ 

ASSUMED MOISTURE: PITOT TUBE COEFF. C'-p-: ------------

PROBE ID NO/MATERIAL: ... -l6'> = "'{"-_____________ __ 

PROBE LENGTH: NOZZLEIDNO ~A~T=E~R~IA:--L-:-Al~ZrA----------

NOZZLE DIAMETER: __ -<..:: Ml-'111' -'--________ _ 

FILTER NOfTYPE: 

PRE-TEST LEAK R"'A:-::T"'E"': -: ,-.2-. ,"";-~C=cF=:M""@-=-· · --C'in-. H""g-.-

POST-TEST LEAK RATE: : CFM@ in. Hg. 

PITOT LEAK CHECK - PRE: (/ POST: ____ _ 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN 

dH Stack 

SAMPLER 

SAMPLEC~U~S~T~O~D~IA~N~---

Probe Filter Imp. Out 

in. H2O Temp, OF Temp, OF Temp, OF Temp, OF 

..- ,....-.., / 

/' ./,( ~/ IV ,- \/4 / \ r: l\j , 

/\ ("-.."--1 \ \ , 

, 

II /' 

;1/ 

JI--r ~ 

\ ~ 

1I.1d'7' ,~ 

Y..J9\V 

K / 

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

0·( 14250,( 7 n 4 "1:33.1"'" 

,l", o· I Hl.5oy 7 't 7, I -;"(7.( 

~ ~I:'t I 

Co)2 b (/32.'( 

..:J..., 5;1 Ge( ")31,f, -'!32 .Y 

/ {;1D,..-.Q l R.. 

Total: _________________ __ 

Meter Temp, OF Vacuum 02 P. static 

In Out in. Hg. % in. H2O 

Comments: _ _________________________________________________________ _ 

Date of last revision 1/25/2013 Page __ of __ DS834049 

Master Document StoragelFormslDatasheetslField Datasheets 
AMMONIA ELECTRODE CALIBRATION CURVE 

:Sample Koom 

NH3 concentration log NH3 concentration Electrode potential Temperature Temperature 

(~g NH31 ml as N) (mV) (C) (C) 

1 0.000 97.6 22.5 22.5 

5 0.699 59.4 22.5 22.5 

20 1.301 24.9 22.5 22.5 

100 2.000 -15.5 22.5 22.5 

Ammonia Electrode Calibration Curve y = -56.6126x + 98.2126 

2/27/2013 

R2 = 0.9998 

120.0 

::;- 100.0 

.S- 80.0 OJ 

'" c: 60.0 

-

" 0 

Q. 40.0 

"C " 

0 20.0 ~ 

-

" 0.0 

iij " 

-20.1) 00 0.500 1.000 1.500 ~O 2. 00 

-40.0 

logarithm of the concentration of ammonia (~g NH,I ml as N) 

slope 

y-intercept 

Concentration 

(~g NH, I ml as N) 

1 

5 

20 

100 

Calculation: 

-56.6126 

98.2126 

Value LR line 

1.0252 

4.8482 

19.7237 

102.0022 

Regression Line: P=M·log( g of NH,I ml as N)+B 

Difference 

0.0252 

-0.1518 

-0.2763 

2.0022 

Measured Concentration of Ammonia (C) in ~g 1 ml NH, as N: C=10,P,81/M 

where P = electrode potential, M= slope (must be -57±3) and B= intercept 

% Difference 

2.5229 

-3.0356 

-1 .3817 

2.0022 

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 

Unit 5 100% 

SCAQMD 207.1 

2/26/2013 

2/27/2013 

RF 

y= -56.6126 x+ 98.2126 

0.9998 

P Cone. 

mV g NH3/ml as N 

28 ug NH3/ ml as N 16.2 

repeat 28 ug NH3/ml as N 16.1 

1-NH3 -100-1 56.4 

repeat 1- NH3 -100-1 56.8 

2-NH3 -100-1 59.4 

repeat 2- NH3 -100-1 59.2 

spike 2-NH3100-1 19.5 

repeat spike 19.3 

28 NH3/ml as N 16.1 

repeat 28 ug NH3/ml as N 16.1 

Reagent Blank 153.4 

repeat ReaQent Blank 153.7 

Field Blank 145.6 

repeat Field Blank 146.2 

DI H20 Blank 151.7 

Repeat DI H20 Blank 152.1 

28 NH3/ml as N 17.2 

repeat 28 ug NH3/ml as N 17.3 

Notes: 

Measured Concentration of Ammonia (C) in )..lg NH3 I mt as N 

C= 1 O(P-B}/M 

P = electrode potential (mV), M=slope and B=intercept 

28.097 

28.212 

5.477 

5.389 

4.848 

4.888 

24.568 

24.769 

28.212 

28.212 

0.106 

0.105 

0.146 

0.142 

0.114 

0.112 

26.977 

26.868 

Average Measured Ammonia Concentration (Cavg) = (C1 + C2)/2 

where C1 , C2 results from duplicate analyses (l1g NH3/ml as N) 

Cavg (~g NH,Iml as NH3) = Cavg (~g NH31 ml as N)' 17.03/14.01 

Ilg NH3 I sample = Cavg (J.l.g NHy'ml 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 lSA unless otherwise indicated. 

Sample PH and Temperatures can be found on the laboratory datasheet. 

C avg as N 

28.154 

5.433 

4.868 

24.668 

28.212 

0.1053 

0.1438 

0.1126 

26.923 

Maximum samples (including blanks) between 28 ug/ml check standard is 5 samples 

analyzed in duplicate. 

TV C avg as NH3 ~g NH,I 

(ml) sample 

NA 34.223 NA 

605 6.604 3995.651 

581 5.917 3437.992 

NA 29.986 NA 

NA 34.293 NA 

NA 0.128 NA 

405 0.175 70.781 

NA 0.137 NA 

NA 32.726 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/ 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 ReaQent 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 5 100% 

SCAQMD 207.1 

2/26/2013 

2/27/2013 

RF 

% recovery 

NA 

NA 

NA 

103.45 

NA 

NA 

NA 

NA 

NA 

spike: 100 ml sample + 2 ml (1000 I1g NH3/ 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 (l1g NH,I ml as N) 

RPD 

% 

-0.41 

1.63 

-0.81 

-0.81 

0.00 

1.22 

2.44 

1.63 

0.41 

RPA 

% 

0.552 

NA 

NA 

NA 

0.756 

NA 

NA 

NA 

-3.848 

Relative Percent Difference (RPD) = (C1-C2)/ Cavg *100 (must be 5% or less) 

Relative Percent Accuracy (RPA) (must be 10% or less) 

RPA = (Cavg-theoretical value of standard)/ theoretical value of standard * 100 
Oell811 

Ai, Qwli.., $....;.;.,. ," 

AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project#: _______ District Method: SCAQMD 207.1 Sample Date: '4/ /13 

Client/Location: SeD1.ioe. ( 

Sample Location: U/);t 

Calibration Date: A I /13 Analysis Date z./ /13 

Test #'s: 1()6 % 

Calibration Curve: V= -5'."l~ .Y~·9r.)./ Z f Analyst's Initials: R 7 ) 

Sample 

Standard Check: 

28 ~g NH,Iml 

Repeat 28 

/- Jlf/, -/bO ~ I 

2,. NI/, - /(;0 - I 

2fAl/./, 

field MCMK 

Electrode 

Potential 

(mV) 

It. 2, 

It. ( 

sc..'1 

S'(,.J' 

59· 'I 

J9·~ 

19-3 

It. ( 

Jf... r 

/53.Q 

/5~, 1 

/45. (, 

/.5:/.1-

}Sl.t 

TV 

(ml) 

{,6S 

5JI 

Cone. 

fl9 NH3 -

N 1 ml 

U·C/i7-

S. ~/11 

2.f. 212.. 

U.212. 

o. l OS 

D./4~ 

O./J..(1... 

D. III.( 

0, (! 1.. 

Cavg 

(fl9 NH3 

- N 1 ml-) 

5. 'f33 

21; 2,12.. 

().IDS 3 

o. jJ/3f' 

O.lllc:. 

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 1 ml) = 10 (P-S}/M 

P = electrode potential, B = y·intercept and M = slope 

fl9 NH31 

sample 

3975. ~ 

Commentsl Temp/pH 

Percent Recovery: 

Cavg = average result of duplicate analyses (fl9 NH3 - N 1 mil = (C1+C2)/2 

fl9 NH31 sample = Cavg* 17.03/14.01 * TV 

mg 1 sample = fl9 Isample .,. 1000 

ppm NH3 = mg NH3/sampie x 1Nmstd x 1/454000 x SV/17 x 106 

Della/). "' ''-''t'""'"'"' ............. 

Date of last revision 12/5/2008 

DS834059 

Master Document StoragelFormslDatasheetslLab Forms 
Dellal1 

""O""ljtys...;. .......... _ ..... 

AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project #: ________ District Method: SCAQMD 207.1 Sample Date: 212~ 113 

ClienULocation: 5e.01. t 1\ ~ t Calibration Date: :z.lh113 Analysis Date: 2/2.:;-/13 

Sample Location: Uf)/t: ~ Calibration Curve: ________ ~Analyst's Initials: R?: 

Test #'s: P,j 1. R2: _____ _ 

Sample Electrode TV Cone. Cavg fig NH31 Commentsl Temp/pH 

Potential (ml) fig NH3- (fig NH3 sample 

(mV) N 1 ml - N 1 ml) 

Standard Check: Percent Recovery: 

28 I-lg NH,Iml /7.2- 2&. 'in 

Repeat 28 /7.1 2'.~"f 2(,.'113 

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·8YM 

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 NH3/sampie x 1Nmstd x 1/454000 x SV/17 x 106 

Della/:). 

.----- DS834059 

Date of last revision 12/5/2008 Master Document StoragelFormslDatasheetslLab Forms 
AMMONIA ELECTRODE CALIBRATION CURVE 

Sample Room 

NH3 concentration log NH3 concentration Electrode potential Temperature Temperature 

g NH,I ml as N) (mV) (C) (C) 

1 0.000 97.6 22.5 22.5 

5 0.699 59.4 22.5 22.5 

20 1.301 24.9 22.5 22.5 

100 2.000 -15.5 22.5 22.5 

Ammonia Electrode Calibration Curve y = -56.6126x + 98.2126 

2/27/2013 R' = 0.9998 

120.0 

:;- 100.0 

.§. 80.0 .. 

~ 60.0 

g 

0 

D- 40.0 .. 

"C 20.0 0 

--() 

.. 0.0 

jjj 

-20!J·( 00 0.500 1.000 1.500 ~O 2. 00 

-40.0 

logarithm of the concentration of ammonia (~g NH,I ml as N) 

slope 

y-intercept 

Concentration 

(~g NH,I ml as N) 

1 

5 

20 

100 

Calculation: 

-56.6126 

98.2126 

Value LR line 

1.0252 

4.8482 

19.7237 

102.0022 

Regression Line: P;M'log(~g of NH,t ml as N)+B 

Difference 

0.0252 

-0.1518 

-0.2763 

2.0022 

Measured Concentration of Ammonia (C) in ~g 1 ml NH, as N: C;10(P,81/M 

where P ; electrode potential, M; slope (must be -57±3) and B; intercept 

% Difference 

2.5229 

-30356 

-1.3817 

2.0022 

All standards were prepared in O,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 [nitials: 

Calibration Curve: 

R' 

Sample 

Sentinel 

Unit 4 75% 

SCAQMD 207.1 

2/26/2013 

2/27/2013 

RF 

y= -56.6126 x+ 96.2126 

0.9996 

P Conc. 

mV ~g NH3/ml as N 

28 ug NH3/ ml as N 16.2 

repeat 28 UQ NH3/ml as N 16.2 

1~NH3 -75-1 73.2 

repeat 1- NH3-75-1 73.6 

2-NH3 -75-1 63.2 

repeat 2- NH3 -75-1 63.1 

spike 2-NH3 75-1 23.1 

repeat spike 22.9 

28 NH3/ml as N 16.2 

repeat 28 ug NH3/ml as N 16.2 

Reagent Blank 153.4 

repeat Reagent Blank 153.7 

Field Blank 145.6 

repeat Field Blank 146.2 

DI H20 Blank 151.7 

Repeat DI H20 Blank 152.1 

28 NH3/ml as N 17.2 

repeat 28 uq NH3/ml as N 17.3 

Notes: 

Measured Concentration of Ammonia (C) in f.l9 NH3! ml as N 

C= 1 O{P-B)IM 

P = electrode potential (mV), M=slope and 8=intercept 

26.097 

26.097 

2.766 

2.699 

1.642 

1.649 

21.222 

21.395 

26.097 

26.097 

0.106 

0.105 

0.146 

0.142 

0.114 

0.112 

26.977 

26.666 

Average Measured Ammonia Concentration (Cavg) = (C1 + C2)/2 

where C1, C2 results from duplicate analyses (119 NH3/ml as N) 

Cav9 ("9 NH,Iml as NH3) = Cav9 ("9 NH31 ml as N)' 17.03/14.01 

119 NH31 sample = Cav9 (119 NH3/ml as NH3) * TV 

Used 100 ml of samples and standards with 2 ml ISA and constant stirrin9 rate. 

AI! solutions turned blue and remained blue with ISA unless otherwise indicated. 

Sample PH and Temperatures can be found on the laboratory datasheet. 

e avg as N 

26.097 

2.732 

1.645 

21.306 

26.097 

0.1053 

0.1436 

0.1126 

26.923 

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 34.154 NA 

570 3.321 1693.236 

570 2.243 1276.547 

NA 25.902 NA 

NA 34 .154 NA 

NA 0.126 NA 

405 0.175 70.761 

NA 0.137 NA 

NA 32.726 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 Reaqent Blank 

Field Blank 

repeat Field Blank 

DI H20 Blank 

Repeat DI H20 Blank 

28 NH3/ml as N 

repeat 28 ua NH3/ml as N 

Notes: 

Sentinel 

Unit 4 75% 

SCAQMD 207.1 

2/26/2013 

2/27/2013 

RF 

% recovery 

NA 

NA 

NA 

101.39 

NA 

NA 

NA 

NA 

NA 

spike: 100 ml sample + 2 ml (1000 ftg 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,t ml as N) 

RPD 

% 

000 

2.44 

-0.41 

-0.81 

0.00 

1.22 

2.44 

1.63 

0.41 

RPA 

% 

0.347 

NA 

NA 

NA 

0.347 

NA 

NA 

NA 

-3.848 

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: 212(/1$ 

Client/Location: SeDt!' oe ( Calibration Date: ~ ht/l3 Analysis Date: Z./zi/13 

Sample Location: Una; 5" Calibration Curve:Y:-s,. ,12' X= +94'.:Z I Z E Analyst's Initials: R 7 

75C>/~ 2 c,.-.L> Test #'s: __ ..:....:::'-'''<...: <v=---__ R: o. -"7 fSample Electrode TV Cone. Cavg fl9 NH31 Commentsl Temp/pH 

Potential (ml) fl9 NH3- (fl9 NH3 sample 

(mV) N Iml - N I ml") 

Standard Check: Percent Recovery: 

28 ~g NH,Iml It. 2- 2f.617 

Repeat 28 It.l. 2~,09l )f·697-

/- /If./, -75 - I 7.n. 2.1ft, 

&~ct I ,.v~ 75 - I 1.H- 5"10 2.C,C;, 2.7H. /f'l3. 2. pI-I <. 2. T::z;.S( 

2.. NI/, - "15 - I f3·1.. I.S't!.. 

1.Q~c:t 2}/#' 75 - I 8-3·\ 5"10 ;. 'i'f7 /.H5 lUFfS: 1>/./ c..l. T= 22.5" ( 

5 £)iKe.2. AlII, 75" - I 23·' 2.{.~1.2. 

RU'ld 5IJ/K, 22. '1 21.3'15 2.1· 3o.r re. {a-vetc/ :- /6' ~V o 

2.fAlIL I~· 2.., n011 

Ig&>~[ 2f N'~ 1&'.2.. 2~.O11 ]f..on 

12<:: ,,,,,.J p,/rrr../( /5Y( o./or, A It 50b f i CI>t.5 

~ ~d R (J. /53,.7- {)./OS O./{)5 ~ ~k( c..t 

Ii eJ d /l. / ""'/<. /~s.~ o.!'-/~ 22.S-° (.. 

'a:ALd fA /'f/,.7.. 0·/1../2- o'/1.3~ 

f)/J ~ 6 I?J{CYlK. /S/.T D. III{ 

N. '.42~:I: fi lAo t3 J K. /$7.. .\ 0./12- {).II2.£ 

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·BI/M 

P = electrode potential, B = y·intercept and M = slope 

Cavg = average result of duplicate analyses (fl9 NH3 - N I ml) = (C1+C2)/2 

fl9 NH31 sample = Cavg* 17.03/14.01 * TV 

mg I sample = flg Isample + 1000 

ppm NH3 = mg NH3/sampie x 1Nmstd x 1/454000 x SV/17 x 106 

Del/a!1 

---- DS834059 

Date of last revision 12/5/2008 Master Document Storage\Forms\Datasheets\Lab Forms 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project #: ________ District Method: SCAQMD 207.1 Sample Date: :? /~" 113 

ClienULocation Se.ct t 1\ e.1 Calibration Date: .2.12? /13 Analysis Date 2/21-/13 

Sample Location: Uf\,'t 5" Calibration Curve: _________ ,Analyst's Initials: R:t 

Test #'s: 75:0/0 R': ------

Sample Electrode TV Cone. Cavg fl9 NH31 Commentsl Temp/pH 

Potential (ml) fl9 NH3- (fl9 NH3 sample 

(mV) N 1 ml - N 1 mil 

Standard Check: Percent Recovery: 

28 ~g NH3/ml /7.2. 2(... '17 7 

Repeat 28 )7.3 2e,. fe-I" 2(.,. y2J 

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 1 ml) = 10 (P·BVM 

P = electrode potential, B = y-intercept and M = slope 

Cavg = average result of duplicate analyses (fl9 NH3 - N 1 ml) = (C1+C2)/2 

flg NH31 sample = Cavg' 17.03/14.01 • TV 

mg 1 sample = fl9 Isample .,. 1000 

ppm NH3 = mg NH,tsample x 1Nmstd x 1/454000 x SV/17 x 10' 

Delfa/j. 

-----.- DS834059 

Date of last revision 12/5/2008 Master Document StoragelFormslDatasheetslLab Forms 
AMMONIA ELECTRODE CALIBRATION CURVE 

::>amp,e Koom 

NH3 concentration log NH3 concentration Electrode potential Temperature Temperature 

(Mg NH31 ml as N) (mV) (C) (C) 

1 0.000 97.6 22.5 22.5 

5 0.699 59.4 22.5 22.5 

20 1.301 24.9 22.5 22.5 

100 2.000 -15.5 22.5 22.5 

Ammonia Electrode Calibration Curve y = -56.6126x + 98.2126 

2/27/2013 

R2 = 0.9998 

120.0 

:> 100.0 

-S 80.0 C; 

~ 60.0 

$ 

0 

0- 40.0 Q) 

" 0 20.0 ~ 

~ 

... 

Q) 0.0 

iii 

-20Jj.( 00 0.500 1.000 1.500 ~O 2. 00 

-40.0 I 

logarithm of the concentration of ammonia ("g NH, 1 ml as N) 

slope 

V-intercept 

Concentration 

(Mg NH31 ml as N) 

1 

5 

20 

100 

Calculation: 

-56.6126 

98.2126 

Value LR line 

1.0252 

4.8482 

19.7237 

102.0022 

Regression Line: P=M'log(M9 of NH,J ml as N)+B 

Difference 

0.0252 

-0.1518 

-0.2763 

2.0022 

Measured Concentration of Ammonia (C) in Mg 1 ml NH, as N: C=10(P-BjIM 

where P = electrode potential, M= slope (must be -57±3) and B= intercept 

% Difference 

2.5229 

-3.0356 

-1.3817 

2.0022 

All standards were prepared in 0.04N H2S04 and allowed to equilibrate to room temperature. 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS CALCULATION 

ClienU Location: 

Sample Location: 

District Method: 

Sample Date: 

Analysis Date: 

Analyst's Initials: 

Calibration Curve: 

R' 

Sample 

Sentinel 

Unit 5 50% 

SCAQMD 207.1 

2/26/2013 

2/27/2013 

RF 

y= -56.6126x+ 98.2126 

0.9998 

P Conc. 

mV )19 NH3/ml as N 

28 ug NH3/ ml as N 16.3 

reoeat 28 ua NH3/ml as N 16.4 

1-NH3-5D-l 100.8 

reoeat 1- NH3-50-1 101.1 

2-NH3 -50-1 102.9 

reDeat 2- NH3 -50-1 103.3 

spike 2-NH3 50-1 24.5 

reneat snike 24.2 

28 NH3/ml as N 16.2 

repeat 28 uo NH3/ml as N 16.2 

Reagent Blank 153.4 

rene at Reanent Blank 153.7 

Field Blank 145.6 

reoeat Field Blank 146.2 

DI H20 Blank 151.7 

ReDeat DI H20 Blank 152.1 

28 NH3/ml as N 17.3 

reoeat 28 UD NH3/ml as N 17.2 

Notes: 

Measured Concentration of Ammonia (C) in )19 NH3! ml as N 

C= 1 O(P-8)/M 

P = electrode potential (mV), M=slope and B=intercept 

27.983 

27.870 

0.900 

0.889 

0.826 

0.813 

20.047 

20.293 

28.097 

28.097 

0.106 

0.105 

0.146 

0.142 

0.114 

0.112 

26.868 

26.977 

Average Measured Ammonia Concentration (Cavg) = (C1 + C2)/2 

where C1, C2 results from duplicate analyses (J.19 NH3/m! as N) 

Cavg (~g NH,tml as NH3) = Cavg (~g NH31 ml as N)' 17.03/14.01 

J.19 NH31 sample = Cav9 (J.19 NHiml 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. 

e avg as N 

27.926 

0.895 

0.820 

20.170 

28.097 

0.1053 

0.1438 

0.1126 

26.923 

Maximum samples (including blanks) between 28 ug/ml check standard is 5 samples 

analyzed in duplicate. 

TV C avg as NH3 ~g NHJI 

(ml) sample 

NA 33.946 NA 

505 1.088 549.190 

590 0.996 587.912 

NA 24.518 NA 

NA 34.154 NA 

NA 0.128 NA 

405 0.175 70.781 

NA 0.137 NA 

NA 32.726 NA 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS QUALITY CONTROL 

ClienV Location: 

Sample Location: 

District Method: 

Sample Date: 

Analysis Date: 

Analyst's Initials: 

Sample 

28 ug NH31 ml as N 

repeat 28 ug NH3/ml as N 

1-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 5 50% 

SCAQMD 207.1 

2/26/2013 

2/27/2013 

RF 

% recovery 

NA 

NA 

NA 

100.70 

NA 

NA 

NA 

NA 

NA 

spike: 100 ml sample + 2 ml (1000 I"g NH31 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 (fig NH,t ml as N) 

RPD 

% 

0.41 

1.22 

1.63 

-1 .22 

0.00 

1.22 

2.44 

1.63 

-0.41 

RPA 

% 

-0.263 

NA 

NA 

NA 

0.347 

NA 

NA 

NA 

-3.848 

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: ?,/zt,./13 

ClienULocation: SeD-/.ioe.f Calibration Date: ~ ht/l3 Analysis Date: Z./J,+/<3 

Sample Location: u!)a; 5 Calibration Curve:V=-Y..611f X=+"1<f',.2IZt; Analyst's Initials: R7 

Test#'s: $0% R': 0.9'1'1[' , ----=-~-=----

Sample Electrode TV Cone. Cavg ~g NH31 Commentsl Temp/pH 

Potential (ml) ~g NH3- (~g NH3 sample 

(mY) N Iml - N I mil 

Standard Check: Percent Recovery: 

28 IJg NH,tml 

It3 27·9'f3 

Repeat 28 It .ll 2;;·);7-0 n·. t;zCr 

1- JlI/, - So - I 160·" D.900 

/0,tci / #~ 50 - \ /6/.1 sos D. ff7 ().f%- 5 t

/9. I pH < 2. T::22.sc 

Z·NI/, - .50 - I /02 . ., 6·f1.~ 

f<L~c.t Z##' 50 - I /(')~ .~ 590 0.f/3 D. no sH·9 /J/-/ < 2.... T=' 22. S' ( 

Sj),'lft.. 2.. AlII, 5D - I 21.(.r:; 2e>, /)L{':fDb" ,.I. 5IJ,'KL 2L(.2.. lb,273 2(!)·/70 re.. {avetl/ :: 100 < 

2fAl/J. IC·2. Zf. on 

2 AO/_t v 1 f. HI/., If,. 2. 2f;097- 2f.M7 

h: ".11-1. P, /0Yt.i<. 18.1./ D./Orr A I { soL-l:i 011,5 

h ~d R /!.. /~<,·1 D./OS J~~ -Le..s·kJ c. t 

lie.(d f>..lfMl<. }I{s.c, D·Nf, 22So 

(.. 

R(fit,-t f IJ. It.{ r,. 1- D-/'{1- D. J'-{3~ 

lilll ~ 6 /3{CH-,K. {~/.1 D-I/I{ 

1M ~4-1:: /Y /Ao t3 J K.. /5Z. I 0.111- O. {1M. 

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)/M 

P = electrode potential, B = y-intercept and M = slope 

Cavg = average result of duplicate analyses (~g NH3 - N 1 ml) = (C1+C2)/2 

~g NH31 sample = Cavg· 17.03/14.01 • TV 

mg I sample = ~g Isample .,. 1000 

ppm NH3 = mg NH,tsample x 1Nmstd x 1/454000 x SV/17 x 106 

!!P!@A 

Date of last revision 12/5/2008 

DS834059 

Master Document StoragelFormslDatasheetslLab Forms 

~ 
AMMONIA BY ION SELECTIVE ELECTRODE ANALYSIS 

Project #: ________ District Method: SCAQMD 207.1 Sample Date: 2. 1)4/13 

ClienULocation: Se.at,' 1\ ~ I Calibration Date: 2..1z':j11.~ Analysis Date: 2 IH / 13 

Sample Location: U()/t!l Calibration Curve: _________ Analyst's Initials: R:lTest #'s: .50 70 fJ 1.. R': _____ _ 

Sample Electrode TV Cone. Cavg ~g NH31 Commentsl Temp/pH 

Potential (ml) ~g NH3- (~g NH3 sample 

(mV) N 1 ml - N 1 ml) 

Standard Check: Percent Recovery: 

28 I-Ig NH,Iml (n 2(.· fC fRepeat 28 1'7.2... 2t,.977- )(,·923 

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-BVM 

P = electrode potential, B = y-intercept and M = slope 

Cavg = average result of duplicate analyses (~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 NH3/sampie x 1Nmstd x 1/454000 x SV/17 x 10' 

Oe//a/j, 

.--.--- DS834059 

Date of last revision 12/5/2008 Master Document StoragelFormslDatasheetslLab Forms 
Appendix C.4 SOx by SCAQMD Method 307.91 

R521 0729 C-8 
Parameter 

so, 

Units 

Ib/MMBtu 

Ib/MMsef 

gr H2S/100sef 

Max Result Limit 

0.00002 

0.017 

0.006 

0.06 

0.67 

0.25 

Rule 

40 CFR 60 

Rule 2011 

SCAQMD Permit B61 .1 
Sent inel Unit 5 Fuel Analysis and Sulfur Cales.xls 

Sulfur 

Client 

Facility 

Unit 

Gemma 

Sentinel 

5 

Sentinel - -5 fuel -1&2 

Fuel Sulfur HHV 

Content, (BTU/ft3@ 

ppmv 60F) MW (H2S) MW(S02) 

Result 0.1 1026.8 34.00 64.00 

Limit 

Reference 

gr/100 scI = ppmv luel/10'6 x MW (H2S)/SV x gr/lb x 100 

Ib/10"6 sef = ppmv fue1/10"6 x MW (H2S)/SV x 10"6 

Ib-S02lMMBtu = ppm lue1/10'6 x MW (S02)/SV/HHV x 10'6 

(~peeilie 

Molar 

Volume@6 

OF) 

379.5 

grnb gr-H2S/100 sci 

7.000 0.006 

0.25 

SCAQMD 

Permit, 

861 .1 

lbsH2S/MMscl 

0.009 

0.690 

Rule 2011 

IbS02lMMBtu 

0.00002 

0.06 

40 CFR 60 

4/15/2013 

2: 26 PM 
Client 

Facility 

Unit 

Load, MW 

106 

Gemma 

Senlinel 

5 

Fuel Sulfur 

Content, ppm 

10.1 

Sentine l Unit 5 Fuel Analy sis and Sulfur Cales . xls 

SOx 

Sentinel-5-Fuel-1 &2 

Specific 

Molar Slack Flow 

Volume Rate Fuel Flow 

(SV), (Qsd19), Rate, 

dscf/lb-mol dscfm hscf/h 02 Ib/hr, S02 ppmv 

379.5 405,070 8744 13.52 0.01475 0.004 

S021b/hr = (sulfur ppmv)/10"6 x (MW S02)/SV x hscf/hr x 100 scl/hscf 

ppm S02 = Ib/hr x SV/MW x 1/Qsd19 x 10"6/60 

S02, 

ppmv@ Ib/MMscf15% 02 Fuel 

0.003 0.017 

Load, Stack fiow rate, fuel fiow and 02 average of data collected in conjuction with NOxiCO tests at 100% load condition 

4/15120 13 

2 , 26 PM 
Client 

Facility 

Unit 

Carbons 

1 

2 

2 

3 

3 

4 

4 

4 

4 

4 

4 

4 

5 

5 

6 

Gemma 

Sentinel 

5 

Compound 

Hydrogen 

Carbon Dioxide 

Carbon Monoxide 

Nitrogen 

Oxvaen 

Methane 

t:thylene 

Ethane 

Propane 

Propylene 

SODutane 

n-Butane 

1-Butene 

Isobutylene 

t-2-Butene 

c-2-Butene 

1,3-Butadiene 

sopentane 

n-Pentane 

HexaneSt-'IUS 

Compound 

Total Reduced Sulfur 

FUEL F-FACTOR CALCULATIONS 

Sentinel-5-Fuel-1 &2 

1 2 Average 

detect? 1 MOLE % detect? 1 MOLE % detect? MOLE % 

< 0.001 < 0.001 

0.321 0.321 

< 0.001 < 0.001 

3.261 3.261 

0.007 0.007 

90.772 90.772 

< 0.001 < 0.001 

4.803 4.803 

0.670 0.670 

< 0.001 < 0.001 

0.042 0.042 

0.083 0.083 

< 0.001 < 0.001 

< 0.001 < 0.001 

< 0.001 < 0.001 

< 0.001 < 0.001 

< 0.001 < 0.001 . 

0.009 0.009 

0.009 0.009 

0.023 0.023 

detect? 1 ppm detect? 1 ppm detect? ppm 

10.1 1 0.1 

Note: Results from one sample. One of the duplicate samples obtained a leak and was compromised. 
FUEL F-FACTOR CALCULATIONS 

Client Gemma Unit 5 

Facility Sentinel 

Sentinel-5-Fuel-1 &2 

SPECIES MW MOLE % MW*% HHV BTU/SCF C H 0 N 

CO2 44 0.321 14.13 0.04 0.00 0.10 0.00 

CO 28 0.001 0.03 321.0 0.003 0.00 0.00 0.00 0.00 

N2 28 3.261 91.35 0.00 0.00 0.00 0.91 

O2 32 0.007 0.22 0.00 0.00 0.00 0.00 

C, 16 90.772 1456.2 1012.0 918.61 10.89 3.63 0.00 0.00 

C2 30 4.804 144.45 1773.0 85.17 1.15 0.29 0.00 0.00 

C3 44 0.671 29.59 2524.0 16.94 0.24 0.05 0.00 0.00 

C4 58 0.130 7.54 3271 .0 4.25 0.06 0.01 0.00 0.00 

Cs 72 0.018 1.30 3998.0 0.72 0.01 0.00 0.00 0.00 

C6+ 86 0.023 1.98 4743.0 1.09 0.02 0.00 0.00 0.00 

Ave. 1 Total 100.01 1641.09 1026.79 12.38 3.99 0.00 0.00 

Weight, % 99.74 75.42 24.32 0.00 0.00 

GasMW 16.41 

Btu/scf= 1027 @60F 

Btu/scf= 1043 @68F 

Btu/lb.= 23,744 

Ib'/scf= 0.0432 

Fd"(60)= 8,458 (02 Based) 

Fd"(68)= 8,588 

Fc"(60)= 1,004 (C02 Based) 

Fc"(68)= 1,020 

Calculations: 

Fd"(68) = 1 0'6' [3.64 • (H%) + 1.53 • (C%) + 0.14 • (N%) - 0.46 • (0%)] 1 HHV, Btu/lb 

Fd"(60) = Fd"(68) • 520 R 1528 R 

Fc"(68) = 10' 6' [0.321 • (C%)] 1 HHV, Btu/lb 

Fc"(60) = Fc"(68) • 520 R 1 528 R 
Sentinel Unit 5 Fuel Analysis and Sulfur Cales.xls 

F-Summary 

Client 

Facility 

Unit 

Gemma 

Sentinel 

5 

Sentinel-5-Fuel-1 &2 

GasMW 16.41 

Btu/set= 1,027 

Btu/set= 1,043 

Btu/lb.= 23,744 

Ib.Jset= 0.04324 

Fd"(60)= 8,458 

Fd"(68)= 8,588 

Fe"(60)= 1 ,004 

Fe"(68)= 1,020 

4/15/2013 

2:26 PM 
Parameter Method No. 

Fixed Gases ASTM D1945/1946 

HHV ASTM D3588 

Sulfur 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 Matrix 
Appendix C.5 ROG by Modified SCAQMD Method 25.3 

R521 0729 C-9 
Client/location Gemma CPV Sentinel 

Unit 5 

Sample location Stack 

Test No. S-S/STK-ROG-100-1A 

Date 2/25/2013 

Test Method Modified SCAQMD 25.3 

Sample Time (HH :MM) 1 :13 

Start Time 13:04 

Stop Time 14:17 

Stack 0, (%) 13.54 

Results 

Canister NMNEOC (ppm) 0.62 

ROG, ppm' 0.62 

ROG, ppm @ 15% 0, 0.50 

RPO', % - 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 POL 

Reference Temp (F) 60 

Data By AA, MC, RM, JM 

S-S/STK-ROG-100-1 B Average 

2/25/2013 

Modified SCAQMD 25.3 

1 :13 

13:04 

14:17 

13.54 

0.66 

0.66 0.64 

0.53 0.51 

- 3.1% 
Client/location Gemma GPV Sentinel 

Unit 5 

Sample location Stack 

Test No. S-5/STK-ROG-75-1A 

Date 2/25/2013 

Test Method Modified SGAOMD 25.3 

Sample Time (HH :MM) 1:08 

Start Time 16:42 

Stop Time 17:50 

Stack O2 (%) 13.98 

Results 

Canister NMNEOC (ppm) 0.58 

ROG, ppm' 0.58 

ROG, ppm @ 15% O2 0.49 

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 POL 

Reference Temp (F) 60 

Data By AA, MG, RM, JM 

S-5/STK-ROG-7S-1 B Average 

2/25/2013 

Modified SGAOMD 25.3 

1:08 

16:42 

17:50 

13.98 

0.61 

0.61 0.60 

0.52 0.51 

- 2.5% 
Client/location Gemma CPV Sentinel 

Unit 5 

Sample location Stack 

Test No. S-5/STK-ROG-50-1A 

Date 2/26/2013 

Test Method Modified SCAOMD 25.3 

Sample Time (HH:MM) 1:08 

Start Time 8:30 

Stop Time 9:38 

Stack 0, (%) 14.15 

Results 

Canister NMNEOC (ppm) 0.62 

ROG, ppm' 0.62 

ROG, ppm @ 15% 0, 0.54 

RPD', % - 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 pal 

Reference Temp (F) 60 

Data By AA, MC, RM, JM 

S-5/STK-ROG-50-1 B Average 

2/26/2013 

Modified SCAOMD 25.3 

1:08 

8:30 

9:38 

14.15 

0.73 

0.73 0.68 

0.64 0.59 

- 8.1% 
SCAQMD METHOD 25.3 

EVACUATED CANISTER SAMPLING DATA 

Client/Facility: Oe vt--\. .~ 7 7 ") ~c c- ~ I,,", Oate: ___ C7" ___ J __ ----=:-' ___ _ 

Unit/Location: 5 S-.?IA.-'-'r,\.,J Performed By:---.:c?"'-..:....:..,4-/.'f ____ _ 

4"'"5 d'- Probe Material_--=----_'--______ Probe Length __ ? _______ _ 

Connecting Tubing Material ___ ----- ___ ,Connecting Tubing Length, _____ _ 

~~ / ~c Barometric Pressure,_ ----'o<- =----_7 _. __ ,==-_ Ambient Temperature ___ J... \ --<, _ _ _ 

Test No. ;5 -5js1K -!?Ofr-fOo -fA S-S/#rlo-II?cJ&- ,,./J,,. ,- ~ 

Vial 10 rJfI- f\fft 

Canister 10 "'5"2, '/ j i 5 

Time Vacuum Time Vacuum TinlIe Vacuum 

Pre-Test Leak Start 

Check 1Q(u 50 10/0 3u \ 

Pre-Test Leak Stop IJ 2-0 30 ( 1)2u " , 

Check J(.-J 

Sample N Start 13 0 '-( Collection 5v ( 36 'I 30 

G 5~,+ nz-v 2:[ (37-U r3Z J 

<5 S'fM 1- i 'JL{, J V (?'i') eN] 

tv je, ~r !,{ o1 Ix{ 1'-1 01 I 'Iv? 

Sample Stop 

Collection /'In ( u Iff? /1 

Post -Test Leak Start 

Check i {n. ( J fy l?..- If 

Post-Test Leak Stop ('-{ 32- Check t V flf) 2.- II 

Line Rinse 

Volume / ./ ,..- /' \ 

\ 

Comments: _____ ______ ____ _________ _ 

Della/1 ,.,o_"s-;, .. , __ ... 

Date of last revision 11/13/08 

DS834043 

Master Document Storage\Forms\Datasheets\Field Datasheets 
SCAQMD METHOD 25.3 

EVACUATED CANISTER SAMPLING DATA 

Client/Facility: GevIA MOl - Se"",L~ \ Oate:_--=C2.-: _ - _2_ '5_ -_2D __'_'...::"2:;, ==--_ 

Unit/Location: 5- skc/< Performed By _-'r<c....:...c'--.l..-___ _ 

Probe Material_----=5=--.=:: 5 _____ Probe Length tfOilrr-rf/-e S 

Connecting Tubing Material, ___ ------ __ Connecting Tubing Length, ___ ..--- __ _ 

Barometric Pressure __ 2- L·----'Y=-.L __ ,Ambient Temperature· __ ...::(;--'f .... · "",2 __ _ 

Test No. 

Vial 10 

Canister 10 

Pre-Test Leak 

Check 

Pre-Test Leak 

Check 

Sample 

Collection 

Sample 

Collection 

Start 

Stop 

Start 

Stop 

Post -Test Leak Start 

Check 

Post-Test Leak Stop 

Check 

Line Rinse 

Volume 

Time Vacuum 

(Mc(' 1J; 

( 7 

175'0 / 0 

Iv 

If I cJ 

/ / 

i 

! 

/ 

Time Vacuum Time Vacl,lum 

/(/)~ / 

/ 

/ 

/'7 / ~ j 

/ 

I / 

I 

I 

11<) 0 II I 

(gou II / 

II 

/' / 

Comments: _______________________ _ 

Date of last revision 11/13/08 

DS834043 

Master Document StoragelFormslDatasheetslField Datasheets 
SCAQMD METHOD 25,3 

EVACUATED CANISTER SAMPLING DATA 

() ,A <"" i' / 'lr ..., t;; c /3- ClientlFacility: lY--ew"v, c ,) ...... LhHe Oate: __ =-"" __ .?-________ _ 

UnitlLocation:_..;:5=---___ Sl-er __ C'_ k:' _' __ Performed BY:_--LI'f---"'<'<cc;1 __ J.-f -'-__ _ 

Probe Material ___ ----=-S'--"5'=---____ Probe Length __ -'1!(;l i _____ _ 

Connecting Tubing Material ___ ,,-/ __ Connecting Tubing Length, __ ""'/"-----

Barometric Pressure_---=,,')=---'1_,_C( -'-. ' '1=---_~Ambient Temperature __ --'y"-' -,-~2,,- ' __ _ 

Test No, S- S/.<;!i<. - ~c&--5 p.. S -Skit. RVb- -5 a·lt 

Vial 10 NT\- NI\, 

Canister 10 /7 .;L It! ~ 

Time Vacuum Time Vacuum Tme Vacuum 

Pre-Test Leak Start 

Check 0&'/2- 2'1 " Ii /2- :2.<; 

Pre-Test Leak Stop 

Check P[j 2- 2-- 2; (/ ?7-J-- 2-'1 

Sample Start 0630 2-') Collection III ti?Jo 2-9 

&: tJ lb <1'1 ,;2,/ {/ [3 'I "7 2.,5' 

5' ()9 0 (;J 11 09'-'3 2-2. 

i.f) 0"1.; c.) 1<1 i/'".-J () 1& 

Sample Stop 

Collection 01:; 0 w 1)73 J I] 

Post -Test Leak Start t7 '1 '-f ~ Check /0 0'1'1 r 1'2. 

Post-Test Leak Stop 0755 (u "755 /) Check \ 

\ 

Line Rinse ./ V / ' 

Volume \ ,.------ /" 

I 

Comments: _________________________ _ 

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 5 

\30219 

3/5/2013 

On February 27, 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 lD Lab No. Initial Pressure 

(mmHg) 

S5/Stk-VOC-100-IA 130219-61285 476.4 

S5/Stk-VOC-100-IB 130219-61286 445.0 

S5/Stk-VOC-75-1 A 130219-61287 506.3 

S5/Stk-VOC-75-IB 130219-61288 479.7 

S5/Stk-VOC-50-IA \30219-61289 473.4 

S5/Stk-VOC-50-1B 130219-61290 403.7 

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 ppmV (as 

Propane) as dictated by the lowest point in the calibration curve. All results were detected below this level 

and therefore reported as <PQL. 

I 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. 

Marcus Hueppe 

Laboratory Director 

This report consists of 41 pages. CertHlca t l ' f . l. l7 

Page 1 

1534 Eastman Ave., Ste. A • Ventura, • CA 93003 @ www.aaclab.com. (805) 650-1642 • FAX (805) 650-1644 
® lAce Atmospheric Analysis & Consulting, Inc, 

SAMPLE RECEIPT / LOG-IN REPORT 

AAe Proiect 130219 Received By: J. Zachman 

Sample Project Desc Clients ID Matrix Sampling Sampled By Sample # Analysis 

Receipt Date Daterrime Requested 

2/2712013 Delta Air Quality SS/Stk-VOC-IOO Summa 2/2S/20 13 Client 6128S SCAQMD 2S.3M 

lOIS 

-IA Canister 

Gemma. Sentinel S 

2/27/2013 Delta Air Quality SS/Stk-VOC-I 00 Summa 2/2S120 13 Client 61286 SCAQMD 2S.3M 

lOIS -IB Canister 

Gemma, Sentinel S 

2127/2013 Delta Air Quality SS/Stk-VOC-7S- Summa 212S12013 Client 6 1287 SCAQMD 2S.3M 

lOI S IA Canister 

Gemma, Sentinel S 

212712013 Delta Air Quality SS/Stk-VOC-7S- Summa 2/2S/2013 Client 61288 SCAQMD 2S.3M 

lOIS IB Canister 

Gemma, Sentinel S 

2/27/2013 Delta Air Quality SS/Stk-VOC-SO- Summa 2/26/2013 Client 61289 SCAQMD 2S.3M 

lOIS IA Canister 

Gemma, Sentinel S 

212712013 Delta Air Quality SS/Stk-VOC-SO- Summa 2/26/2013 Client 61290 SCAQMD 2S.3M 

lOIS IB Canister 

Gemma, SentinelS 

TURN AROUND TIME: Normal (lOdays) 

Lab Due Date: 3/612013 Total Samples: 6 

REMARKS: 

Client returned 6 x Summa canisters + 6 x Flows. 

Page 2 
Client: 

Date: 

Delta Air Quality 

2/27/2013 

Canister # 

357 

115 

086 

119 

172 

106 

Atmospheric Analysis & Consulting, Inc, 

CANISTER PRESSURE LOG 

Project No.: 130219 

Sample # Initial Pressure Final Pressure 

61285 476.4 912.3 

61286 445.0 906.8 

61287 506.3 902.4 

61288 479.7 901.0 

61289 473.4 902.7 

61290 403.7 910.5 

1 

Page 3 
c,;zZ'sre /-z-15' It> 

fA I z.? ·7 

'I ; z.t?tJ 

o I -z. fJ<'l 

" 11-'10 

/I.4C # /3021cr 

CHAIN OF CUSTODY 

CLIENT: Sentinel TEST OATE(S): 212512013 212612013 

LOCATION: 5 SAMPLER(S): .:;R"'M'-___________ _ 

SAMPLE LOCATION: Slk PROJECT MANAGER: SF 

TEST METHOD(S): SCAQMD 25.3 DATE DUE: 3/6/2013 

OUTSIDE LAB REQUIRED?: Yes COMPLIANCE TEST? Yes 

ot 0 

212512013 S5/Stk·VOC·101J.1A SCAQMD25.3 an ter # 0(90 ." . 1 

2125/2013 S5/Stk-VOC·100·1 B SCAQMD 25.3 Canister # 0'" 1 

2/25/2013 SSlStk-VOC·75-1A SCAQMD25.3 Canister # 0001> 1 

2125/2013 S5/Stk·VOC·75·1 B SCAQMD 25,3 Canister # 00 119 1 

2126/2013 S5/Stk·VOC·50·1A SCAQMD 25.3 Canister # r-' 01 2- 1 

212612013 S5IStk-VOC-50-1 B SCAQMO 25.3 Canister # t) 1 

ola ampes 6 

eagent: 

eagent ot s: 

I oe«!~ : /' 

6. 

z I ;111;;;;/ ~ z;; I ;; ~A 
Results 

Page 5 
Atmospheric Analysis & Consulting, Inc . 

LABORATORY ANALYSIS REPORT 

CLIENT 

PROJECT NO. 

MATRIX 

UNITS 

Client ID 

S5/Stk-VOC-100-1A 

SS/Stk-VOC-100-1B 

S5/Stk-VOC-75-1A 

SS/Stk-VOC-75-1 B 

SS/Stk-VOC-50-1A 

SS/Stk-VOC-50-IB 

Delta Air Quality Services, Inc. 

130219 

Air 

ppmC 

Tank Vol Liters 

LabID# 

(VT.nk) 

130219-61285 6.00 

130219-61286 6.00 

130219-61287 6.00 

130219-61288 6.00 

130219-61289 6.00 

130219-61290 6.00 

SCAQMD 25.3 Modified 

Initial Return Final 

Pressure Pressure Pressure 

mmHg (P;) mmHg(P,) mmHg (Pr) 

0.0 476.4 912.3 

0.0 445.0 906.8 

0.0 506.3 902.4 

0.0 479.7 901.0 

0.0 473.4 902.7 

0.0 403.7 910.5 

* 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# Oxygen CO 

S5/Stk-VOC-100-1A 130219-61285 13.6 <PQL 

SS/Stk-VOC-IOO-IB 130219-61286 13.5 <PQL 

S5/Stk-VOC-75-1A 130219-61287 14.0 <PQL 

S5/Stk-VOC-7S-IB 130219-61288 14.0 <PQL 

SS/Stk-VOC-SO-1A 130219-61289 14.1 <PQL 

S5/Stk-VOC-SO-IB 130219-61290 14.2 <PQL 

Fixed Gases have been normalized to 100% on a dry weight baSIS 

Sample Vol. 

(L) (VS.mpl,) 

3.76 

3.51 

4.00 

3.79 

3.74 

3. 19 

CO2 

5.6 

5.3 

5.0 

5.1 

5.0 

5.0 

Tank Dil 

Factor 

(DFT.nk) 

1.91 

2.04 

1.78 

1.88 

1.91 

2.26 

I 

SAMPLING DATE : 2/25,26/2013 

RECEIVING DATE : 02/27/2013 

ANALYSIS DATE : 03/04,05n013 

REPORT DATE : 03/05/2013 

Total 

PQL NMNEOC* 

<PQL 0.62 

<PQL 0.66 

<PQL 0.58 

<PQL 0.61 

<PQL 0.62 

<PQL 0.73 

~L-..-~ Marcus Hueppe 

1534 Eastman Ave., Ste. A • Ventura, • CA 93003 * (805) 650-1 642 • FAX (805) 650-1644 

Laboratorv 0l'rector Page 6 

• WWW.3acab.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) 

CrcA = Average of analysis results from chromatograms, ppmv (as Propane) 

DFrank = Dilution factor reSUlting from tank pressurization upon receipt (PrlPr) 

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 Control/Quality Assurance Report 

Date Analyzed : 03/05/2013 

Analyst : ZG 

Units : G/o 

1- QDenine: Continuin2: Calibration Verification - SeA MD25.125.3 

I AA C ID I Anal~ te I 0 , N, 

Spike Cone 10.46 19.6 

CCV Result 10.46 21.01 

% Ree- * 100.0 107. 1 

AACID 0, N, 

MB NO NO 

IflL - a b oratory' C ontro ISik&D p • uplicate - SC A QM , D 25.1,25.3 

AACID . .<\nalyte N, CO, 

Sample Cofl(' 0.0 0.0 

Spike Con(' 19.6 10.3 

Lab Contrul LCS Result 20.7 10.6 

Standal"ds LCSD Result 19.1 9.8 

LCS % Rcc "" IOS.7 103.7 

L e SJ) % Ret '" 97.2 95.2 

% RPD""" 8.4 8.6 

IV -Sample & Sam pIe ill uplicate - SCAQM D 25.125.3 

AAC ID Analyte 0, N, 

Sampl. 6. 1 34.8 

130219·61290 Sample Dup 6.0 34.S 

Mcan 6. 1 34.6 

% RPD ..... 1.S 0.' 

V ·Matrix ~ike & DUDlie.te . SCAQMIl25.1 25.3 

I AACID I Analyte I N, CO, 

Sample Cone 17.3 1.1 

Spike Cone 9.2 10.3 

MS Result 28.0 11.8 

130219·61290 MSDR~uJt 27. 1 11.3 

MS % Rec *'" 1\6.7 104.7 

MSD %Rec"'· 106.1 100.3 

%RPD "'*'" 9.6 4.3 

VI - Closing Continuine: Calibration Verific ation - SCAQMD 25.125.3 

I AACID 

CCV 

• Must be 85-115% 

.. Must be 75-125% 

... fust be < 15% 

ND '" Not Dejected 

I Ana1lte 

Spike Cone 

Resu1t 

% Ref'" 

L '" Ius thlln Reporting Limit 

II 0, I N, 

10.46 19.6 

9.98 20.0 

9S.S 102.2 

CO, 

10.3 

10.54 

102.8 

co, 

NO 

CH. 

0.0 

9.9 

10.2 

9.2 

102.7 

92.9 

10.0 

CO, 

2.2 

2.0 

2.1 

8.6 

CH, 

0.0 

9.9 

10.2 

9.9 

102.8 

100. 1 

2.6 

I CO, 

10.3 

10.2 

99. 3 

I 

Instrument ID 

Calb Date 

TCD#1 

04/13/2012 

Repo rting Limit: (tl % 

CH. 

9.9 

10. 18 

102.5 

CH. 

NO 

CO 

0.0 

10.3 

10.6 

9.6 

102.6 

93.0 

9.8 

CH, 

0.0 

0.0 

0.0 

0.0 

CO 

0.0 

10.3 

10.6 

10.3 

102.9 

99.6 

3.3 

CH. I 

9.9 

9.6 

97.0 

Marcus Hueppe 

Laboratory Director 

CO 

10.3 

10.56 

102. 1 

co 

NO 

CO 

0.0 

0.0 

0.0 

0.0 

CO 

10.3 

10. 1 

97.4 

I 

Page 9 

1534 Eastman Ave., Ste. A • Ventura, • CA 93003 www.aaclab.com • (805) 650-1642 • FAX (805) 650·1644 
Atmospheric Analysis & Consulting, Inc. 

SCAQMD Method 25.1,3 Quality Control/Quality Assurance Report 

Date Analyzed 

Analyst 

03/0412013 

ZG 

1- Openine: Calibration Verification Standard 

I AAC1D I Analyte I Concentration 

O·CV NMNEOC 0.27 

O-CV dp NMNEOC 0.27 

O-CV tp NMNEOC 0.27 

11- Method Blank 

AAC ID Analytc Result 

MB NMNEOC ND 

III - Matrix SDike & Duplicate 

AAC lD .-\nalylc 

Sample 

Concentnttion 

I 130220-61291 I NMNEOC /I 0.00 

IV - 1 ppm Backfl u sh Standa r s d 

A,\ClD Analyte Result 

Backflush 1 NMNEOC 1.003 

Backflush 2 NMNEOC 0.985 

Backflush 3 NMNEOC 0.937 

I Result 

0.257 

0.253 

0.251 

Spike 

Added 

I 54.35 

"/0 Recovery "'* 

92.3 

90.6 

86.2 

v -Bracketed Closing Calibration Verification Standards 

AAC ID Ana lyte I Concentration I Result 

C-CV Low 

C-CV High 

• Must be 90-110% 

•• Must be 80-120% 

*** Must be 75-125% 

  Must be < 25% 

** *** Must he < 10% 

NMNEOC 

NMNEOC 

0.27 0.293 

2.72 2.48 

I % Recovery *' I 

94.6 

93.1 

92.4 

MS 

Result 

I 43.36 I 

% Recovery ." I 

107.8 

91.3 

MSD 

Result 

45.38 I 

Instrument ID: FID#4 

Units: PPMV 

Calibration Date: 

MS MSD 

% Rec ... • % Ret orr .. 

79.8 I 83.5 

Marcus Hueppe 

Laboratory Director 

111012013 

% RPD** U 

I 4.5 

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 : 03/04/2013 

Analyst: : ZG 

s amplole upllcr a t e ana1 . lysIs RPO' 

I AACID I Result I Result UU!! 

130220-61291 <PQL <PQL 

130220-61292 <PQL <PQL 

130219-61285 <PQL <PQL 

130219-61286 <PQL <PQL 

130219-61287 <PQL <PQL 

130219-61288 <PQL <PQL 

1302 19-61289 <PQL <PQL 

130219-61290 <PQL <PQL 

130228-6133 0 <PQL <PQL 

130228-61331 <PQL <PQL 

130228-61332 <PQL <PQL 

130228-61333 <PQL <PQL 

130239-61413 <PQL <PQL 

130239-61414 <PQL <PQL 

I Qualit,r Assurance Criteria 

Cone. (ppmv) %RPD 

1-3 S20 

4-6 Sl5 

7- 12 <12 

13-30 <10 

31 -50 < 5 

s 

I 

Instrument ID: 

Units: 

FID#4 

PPM V 

Calibration Date: 1/1012013 

I %RPD I 

NA 

NA 

NA 

NA 

NA 

NA 

NA 

NA 

NA 

NA 

NA 

NA 

NA 

NA 

Marcus Hueppe 

Laboratory Director 

Page 11 

1534 Eastman Ave., Ste. A • Ventura, • CA 93003 * www.aaclab.com · (805) 650-1642 • FAX (805) 650-1644 
Raw Data 

Page 12 
Chrom Perfect Chromatogram Report 

130219-61285 

600 

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0 4 6 8 10 12 

Time - Minutes 

Sample Name = 130219-61285 

Instrument = TCD #1 

Raw File Name = C:ICPDATAllnst#01120131030513.0006.raw 

Method File Name = C ICPDATAllnst#01120131030513.0006.bnd 

Calibration File Name = C:ICPDATAl lnst#01120131030513.0006.bnd 

Peak # Ret. Time Name Amount Amt % 

1 7. 03 Oxygen-MS5A 6.501 13.578 

2 9.16 Nitrogen-MS5A 38.736 80'.905 

3 9.55 C02-Q bond 2.642 5.518 

Total Area = 685342.7 Total Height = 98875.56 

Printed on 31512013 8:0244 AM 

14 

« 

~ 

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16 18 20 22 

Date Taken (end) = 315120 13 741 :29 AM 

Dilution Factor = 1 

Area Area % Type Width 

89079 12.998 BB 0.09 

564546 82.374 SBB 0.11 

31 718 4.628 TBB 0.20 

Total Amount = 47.87892 

24 

Page 13 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130219-61285 dp 

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·100 

0 4 6 8 10 12 

Time - MillJles 

Sample Name = 130219-61285 dp 

Instrument = TCD #1 

Raw File Name = C:ICPDATAllns!#01120131030513.0007.raw 

Method File Name = C:ICPDATAllnst#01\20131030513 0007 bnd 

Calibration File Name = C:ICPDATAllnst#01\20131030513.0007.bnd 

Peak # Ret. Time Name Amount Amt% 

1 7.04 Oxygen-MSSA 5.897 13.573 

2 9.16 Nitrogen-MS5A 35. 117 80.832 

3 9.55 C02-Q bond 2.431 5.595 

Total Area = 621786 Total Height = 92023.47 

Printed on 3/5/2013 8:06:05 AM 

14 

::i 

"' " • :;; 

" w 

16 18 20 22 

Date Taken (end) = 3/5/2013 7:58:58 AM 

Dilution Factor = 1 

Area Area % Type Width 

80802 12.995 BB 0.09 

24 

51 1802 82.312 SBB 0.11 

29182 4.693 TBB 0.20 

Total Amount = 43.44465 

Page 14 Page 1 of 1 

2"1"1..-\\3 
Chrom Perfect Chromatogram Report 

130219-61 286 

600 

500 

400 

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Time - Minutes 

Sample Name = 130219-61286 

Instrument:; TCD # 1 

Raw File Name = C:ICPDATAl lns!#011201 3103051 3.0010.raw Date Taken (end) = 3/5/2013 922:29 AM 

Method File Name = C:ICpmethodsl lnst#0112012ID1945-D1946-3C.MET Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #01 \20 12ID1945-D1946-3C-041312-standard.CAL 

Peak # Ret Time Name Amount Amt % Area Area % Type Width 

1 7.03 Oxygen-MS5A 6.159 13.509 84401 12.929 BB 0.09 

2 9.16 Nitrogen-MS5A 36.970 81.084 538805 82 .536 SBB 0.11 

3 9.55 C02-Q bond 2.466 5.408 29602 4.535 TBB 0.19 

Total Area = 6528086 Total Height = 95549.37 Total Amount = 45.59514 

Printed on 3/5/20139:23:24 AM Page 15 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130219-81286 dp 

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I I U ,; " " u w W W 

-100 

, 0 2 4 6 8 10 12 14 16 18 20 22 24 

Time - Minutes 

Sample Name = 130219-61286 dp 

Instrument = TeO #1 

Raw File Name = C:ICPDATAl lns!#01120131030513.0011 .raw Date Taken (end) = 3/5/2013 9:45:33 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 6.140 13.532 84142 12.948 BB 0.09 

2 9.16 Nitrogen-MS5A 36.838 81 .178 536875 82.616 BV 0.11 

3 9.55 C02-Q bond 2.401 5.291 28826 4.436 VB 0.19 

Total Area = 649842.3 Total Height = 95267.48 Total Amount = 45.37908 

Printed on 3/5/2013 9:51:02 AM Page 16 Page 1 of 1 
600 

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Sample Name = 130219-61287 

Instrument::: TeO #1 

Chrom Perfect Chromatogram Report 

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14 

.. 

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16 18 20 22 

Raw File Name = C:ICPDATAllnst#01120131030513_0012_raw Date Taken (end) = 315/2013 10:03:33 AM 

Method File Name = C:ICpmethodsllnst #0112012ID1945-D1946-3C.MET Dilution Factor = 1 

Calibration File Name = C:ICpmethodsl lnst #0112012ID1945-D1946-3C-041312-standard_CAL 

Peak # Ret Time Name Amount Amt% Area Area % Type Width 

1 7.03 Oxygen-MS5A 7.357 13.983 100811 13.378 BB 0_09 

2 9.15 Nitrogen-MS5A 42.584 80.935 620620 82.361 SBB 0.11 

3 9.54 C02-Q bond 2.674 5.082 32105 4_261 TBB 0.20 

Total Area = 753534.9 Total Height = 106098.2 Total Amount = 52.6148 

24 

Printed on 3/5/2013 10:03:59 AM Page 17 Page 1 of 1 
Chrom Perfect Chromatogram Report 

--------------------

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Raw File Name = C:ICPDATAllnst#01120131030513.0013.raw Date Taken (end) = 3/5/201310:19:29 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-MSSA 7.308 14.0S4 100136 13.44 1 BB 0.09 

2 9.1 5 Nitrogen-MSSA 42.177 81.1 13 614692 82 .509 BV 0.1 1 

3 9.54 C02-Q bond 2.513 4.833 3017 1 4.0S0 VB 0.20 

Total Area = 744999.4 Total Height = 105646.8 Total Amount = 51 .99781 

24 

Printed on 3/5/201310:19:56AM Page 18 Page 1 of 1 

2s1 3/.,;-/13 
Chrom Perfect Chromatogram Report 

130219-61288 

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Time - Minutes 

Sample Name' 130219·61288 

Instrument = TCD #1 

Raw File Name ' C:ICPDATA\lnst#01120131030513.0014.raw Date Taken (end)' 31512013 10:36:30 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 7.007 14.028 96014 13.421 BB 0.09 

2 9.15 Nitrogen-MS5A 40.432 80949 589263 82.369 SBB 0.11 

3 9.54 C02-Q bond 2.509 5.023 30121 4.210 TBB 0.20 

Total Area' 715398.1 Total Height· 102342.9 Total Amount· 49.948 

Printed on 31512013 10:38:11 AM Page 19 Page 1 of 1 
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Raw File Name = C:ICPDATAllnst#01120131030513.0015.raw Date Taken (end) = 3/5/2013 10:54:06 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 7.03 Oxygen-MS5A 6.978 13.945 95617 13.346 BB 0.09 

2 9.15 Nitrogen-MS5A 40.450 80.839 589522 82.281 SBB 0.11 

3 9.55 C02-Q bond 2.610 5.216 31334 4.373 TBB 0.20 

Total Area = 716472.4 Total Height = 102323.3 Total Amount = 50.03778 

" 

Printed on 3/5/2013 10:55:32 AM Page 20 Page 1 of 1 
600 

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Sample Name: 130219-61289 

Instrument = TCD #1 

Chrom Perfect Chromatogram Report 

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Raw File Name: C:ICPDATAllnst#01120131030513.0016.raw Date Taken (end): 3/5/201311:12:14 AM 

Method File Name: C:ICpmethodsllnst #0112012ID1945-D1946-3C.MET Dilution Factor: 1 

Calibration File Name: C:ICpmethods\lnst #0112012ID1945-D1946-3C-041312-standard.CAL 

Peak # Ret Time Name Amount Amt% Area Area % Type Width 

1 7.03 Oxygen-MS5A 6.828 14.102 93568 13.492 BB 0.09 

2 9.16 Nitrogen-MS5A 39.166 80.885 570814 82.306 SBB 0.11 

3 9.54 C02-Q bond 2,427 5.013 29145 4.202 TBB 0.20 

Total Area: 693526.8 Total Height: 99945.16 Total Amount: 48.4223 

24 

Printed on 3/5/2013 11: 14:54 AM Page 21 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130219-61289 dp 

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Time - Minutes 

Sample Name = 130219-61289 dp 

Instrument = TeO #1 

Raw File Name = C:ICPDATAlinst#01120131030513.0017.raw Date Taken (end) = 3/5/201311:29:01 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 7.03 Oxygen-MS5A 6.916 14. 134 94774 13.522 BB 0.09 

2 9.15 Nitrogen-MS5A 39.582 80.889 576872 82.306 BV 0.11 

3 9.55 C02-Q bond 2435 4.977 29240 4.172 VB 0.20 

Total Area = 700885.5 Total Height = 100880 Total Amount = 48.93388 

Printed on 3/5/2013 1129:28 AM Page 22 Page 1 of 1 
600 

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Sample Name; 130219-61290 

Instrument = TeD #1 

Chrom Perfect Chromatogram Report 

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Raw File Name; C:ICPDATAllnst#01120131030513.0018.raw Date Taken (end) ; 3/5/2013 11 :46:57 AM 

Method File Name; C:ICpmethodsllnst #011201 2ID1945-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 6.120 14.203 83859 13.593 BB 0.09 

2 9.16 Nitrogen-MS5A 34.754 80.659 506509 82.099 SSB 0.11 

3 9.55 C02-Q bond 2.214 5.138 26579 4.308 TBB 0.20 

Total Area; 616946.8 Total Height; 91623.7 Total Amount; 43.08774 

" 

Printed on 3/5/2013 11 :47:25 AM Page 23 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130219-61290dp 

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0 2 4 6 8 10 12 14 16 18 20 22 24 

Time - Minutes 

Sample Name c 130219-61290 dp 

Instrument = TCO #1 

Raw File Name = C:\CPDATA\lnst#01\2013\030513_0019_raw Date Taken (end) c 3/5/2013 12:03:32 PM 

Method File Name c C:\Cpmethods\lnst #01 \2012\D1945-D1946-3C.MET Dilution Factor c 1 

Calibration File Name c C:\Cpmethods\lnst #01 \2012\D1945-D1946-3C-041312-standard.CAL 

Peak # Ret Time Name Amount Amt % Area Area % Type Width 

1 7.03 Oxygen-MS5A 6.027 14_174 82593 13_555 BB 0.09 

2 9.16 Nitrogen-MS5A 34.467 81 .050 502319 82.442 BV 0.11 

3 9.55 C02-Q bond 2.031 4.776 24385 4.002 VB 0.20 

Total Area c 609296.8 Total Height c 90987.09 Total Amount c 42.52512 

Printed on 3/5/2013 12:03:55 PM Page 24 Page 1 of 1 
Chrom Perfect Chromatogram Report --------_._._ ._ ... _-- -----

1600 r ~ 

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Sample Name = 130219-61285 

Instrument = FlO #4 

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130219-61285 

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5.0 

Time · Minutes 

u 

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Z U " z 0 

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6.0 7.0 80 90 

Raw File Name = C:ICPDATAllnst#04120131030413_0014.raw Dale Taken (end) = 3/4/2013 9:25:55 AM 

Method File Name = C:\Cpmethods\lnst #04\2013\Method25.1 ,3J ow.met Dilution Factor = 1 

Calibral ion File Name = C:ICpmelhodsllnsl #0412013IM25.1 ,310w-011013 CAL 

Peak # Ret. Time Name Amount Amt % Area Area % Type Widlh 

1 0.67 0.000 0.000 9682 0.022 BV 0.05 

2 0.86 Carbon Monoxide 10.899 0.501 154370 0.346 W 0. 17 

3 1.05 Methane 9.755 0.449 190509 0.427 VB 0.18 

4 1.94 Carbon Dioxide 2153.096 99.048 44241740 99.200 BB 0.52 

5 5.88 NMNEOC 1 0.038 0.002 2018 0.005 BB 0.36 

Tolal Area = 4.459832E+07 Tolal Height = 1105364 Total Amounl = 2173.787 

Printed on 3/4/20 13 9:48:37 AM Page 25 Page 1 of 1 
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Raw File Name = C:ICPDATAl lnst#04120131030413.0015.raw Date Taken (end) = 31412013 9:42:14 AM 

Method File Name;:;; C:\Cpmethods\lnst #04\2013\Method25.1,3Jow.met Dilution Factor::; 1 

Calibration File Name = C:ICpmethodsllnst #0412013IM25.1 ,3tow-011013.CAL 

Peak # Ret Time Name Amount Amt % Area Area % Type Width 

1 0.87 Carbon Monoxide 10.280 0.475 145608 0.328 BV 0.17 

2 1.05 Methane 9.705 0.448 189546 0.427 VB 0.19 

3 1.92 Carbon Dioxide 2146.096 99.076 44097908 99.242 BB 0.52 

4 5.89 NMNEOC 1 0.033 0.002 1755 0.004 BB 0.36 

Total Area = 4.443482E+07 Total Height = 1101517 Total Amount = 2166.115 

Printed on 31412013 9:48:43 AM Page 26 Page 1 of 1 
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Raw File Name = C:ICPDATAllnst#04120131030413.0016_raw Date Taken (end) = 3/4/2013 956:30 AM 

Method File Name = C:\Cpmethods\lnst#04\2013\Method25.1 ,3Jow.met Dilution Factor = 1 

Calibration File Name = C ICpmethodsllnst #04\2013IM25.1 ,310w-011 013 CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.87 Carbon Monoxide 9_554 0.451 135323 0.311 BV 0. 17 

2 1.05 Methane 9.123 0.430 178174 0.410 VB 0.18 

3 1.94 Carbon Dioxide 2101.174 99.117 43174852 99.275 BB 0.51 

4 5.82 NMNEOC 1 0.037 0.002 1978 0.005 BB 0.42 

Total Area = 4.349032E+07 Total Height = 1099692 Total Amount = 2119.888 

Printed on 3/4/2013 10: 15:40 AM Page 27 Page 1 of 1 
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Raw File Name = C:ICPDATAllnst#04120131030413.0017.raw Date Taken (end) = 3/4/2013 10:11:28 AM 

Method File Name = C:ICpmethodslinst #0412013IMethod25.1 .3Jow.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodslinst #0412013IM25.1.310w-Oll013 CAL 

Peak # Ret. Time Name Amount Ami % Area Area % Type Width 

1 0.87 Carbon Monoxide 9.293 0.439 131618 0.303 BV 0.17 

2 1.05 Methane 8.916 0.421 174133 0.401 VB 0.18 

3 1.92 Carbon Dioxide 2097.610 99.137 43101624 99.289 BB 0.51 

4 5.84 NMNEOC 1 0.053 0.002 2825 0.007 BB 0.35 

Total Area = 4.34102E+07 Total Height = 1099291 Total Amount = 21 15.872 

Printed on 3/4/2013 10:15:45 AM Page 28 
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Raw File Name = C:ICPDATAllnst#04120131030413.Q020.raw Date Taken (end) = 3/412013 10:53:06 AM 

Method File Name = C:\Cpmethods\lnst #04\2013\Method25.1 ,3_fow.met Dilution Factor = 1 

Calibration File Name = CICpmethodsllnst #04\2013IM25.1 ,310w-011 013.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.87 Carbon Monoxide 10.150 0.467 143759 0.323 BV 0.17 

2 1.07 Methane 12.922 0.595 252369 0.566 VB 0.17 

3 1.95 Carbon Dioxide 2149.652 98.936 441 70980 99. 106 BB 0.52 

4 5.84 NMNEOC 1 0.043 0.002 2305 0.005 BB 0.37 

Total Area = 4.456941 E+07 Total Height = 1108920 Total Amount = 2172.767 

Printed on 3/4/201311 :12:54 AM Page 29 Page 1 of 1 
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Raw File Name = C:\CPDATA\lnst#04\2013\030413.0021.raw Date Taken (end) = 31412013 11 :10:36 AM 

Method File Name = C:\Cpmethods\lnst #04\2013\Method25.1 ,3_low.met Dilution Factor;; 1 

Calibration File Name = C:\Cpmethods\lnst #04\2013\M25.1 ,310w-011013.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.87 Carbon Monoxide 6.941 0.414 126633 0.266 BV 0.16 

2 1.06 Methane 12.671 0.596 251365 0.566 VB 0.17 

3 1.95 Carbon Dioxide 2136.365 96.966 43697946 99.142 BB 0.52 

4 5.82 NMNEOC 1 0.036 0.002 2050 0.005 BB 0.39 

Total Area = 4.427799E+07 Total Height = 1106766 Total Amount = 2158.214 

Printed on 3141201311 :12:56AM Page 30 Page 1 of 1 
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Raw File Name = C:ICPDATAllnst#04120131030413.0022.raw Date Taken (end) = 31412013 11 :24:01 AM 

Melhod File Name = C:ICpmethodslinst #0412013IMethod25. 1 , 3_low. met Dilution Factor = 1 

Calibration File Name = C:ICpmelhodslinst #0412013IM25.1 ,310w-011 onCAl 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.87 Carbon Monoxide 8.087 0.381 11 4543 0.263 BV 0.16 

2 1.05 Methane 12.328 0.581 240765 0.553 VB 0.17 

3 1.96 Carbon Dioxide 2100.858 99.036 43168368 99.180 BB 0.51 

4 5.80 NMNEOC 1 0.034 0.002 1798 0.004 BB 0.36 

Tolal Area = 4.352547E+07 Total Height = 1104110 Total Amount = 2121.307 

Printed on 31412013 11 :38:54 AM Page 31 Page 1 of 1 
Chrom Perfect Chromatogram Report 

130219-61288 dp 

1600.-------------------------------------------~------------------------------__, ~ • 

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Raw File Name = C:ICPDATAllnst#04120131030413.0023.raw 

, 

6.0 7.0 80 9.0 

Date Taken (end) = 3/4/201311 :37:34 AM 

Method File Name = C:\Cpmethods\lnst #04\2013\Method2S.1 ,3_low.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0412013\M25.1 ,3Iow-011013.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.87 Carbon Monoxide 7.923 0.374 112225 0.258 BV 0.16 

2 1.05 Methane 12.134 0.573 236970 0.545 VB 0.17 

3 1.90 Carbon Dioxide 2098.037 99.052 43110396 99.192 BB 0.51 

4 5.86 NMNEOC 1 0.033 0.002 1772 0.004 BB 0.36 

Total Area = 4.346136E+07 Total Height = 1103681 Total Amount = 2118.127 

Printed on 3/4/2013 11 :38:59 AM Page 32 Page 1 of 1 
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Raw File Name = C:ICPDATAllns!#04120131030413.0024.raw Date Taken (end) = 31412013 115101 AM 

Method File Name = C:ICpmethodsllnst #0412013IMethod25.1 ,3Jow.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsl lnst #04120131M251 ,310w-01 10 13 CAL 

Peak# Ret. Time Name Amount Amt % Area Area % Type Width 

1 0.88 Carbon Monoxide 14.025 0.669 198640 0.462 BB 0.30 

2 1.97 Carbon Dioxide 2082 .876 99.330 42798864 99.535 BB 0.50 

3 6.26 NMNEOC 1 0.026 0.001 1370 0.003 BB 020 

Total Area = 4.299888E+07 Total Height = 1081921 Total Amount = 2096.926 

Printed on 31412013 12:07 :32 PM Page 33 Page 1 of 1 
1600 

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Raw File Name = C:ICPDATAllns\#04120131030413.0025.raw Date Taken (end) = 3/4/20 13 12:06:13 PM 

Method File Name = C ICpmethodslinst #0412013IMethod25.1 ,3Jow.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodslinst #0412013IM25.1 ,3Iow-Ol 1 onCAl 

Peak # Ret. Time Name Amount Amt % Area Area % Type W idth 

1 0.87 Carbon Monoxide 13.970 0.666 197870 0.460 BB 0.30 

2 1.93 Carbon Dioxide 2084.988 99.333 42842268 99.537 BB 0.50 

3 6.23 NMNEOC 1 0.026 0.001 1398 0.003 BB 0.20 

Total Area = 4.304154E+07 Total Height = 1082516 Total Amount = 2098.985 

Printed on 3/4/20 1312 :07:35 PM Page 34 Page 1 of 1 
1600 

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Sample Name; 130219-61290 

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Raw File Name; C:\CPDATA\inst#04\2013\030413.0026.raw Date Taken (end); 3/4/20131219:11 PM 

Method File Name = C:\Cpmethods\lnst#04\2013\Method25.1,3_low.met Dilution Factor = 1 

Calibration File Name; C:\Cpmethods\inst #04\2013\M25.1 ,310w-011 013.CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.88 Carbon Monoxide 12.524 0.622 177384 0.430 BB 0.29 

2 1.93 Carbon Dioxide 1999.988 99.376 41095688 99.565 BB 0.48 

3 5.97 NMNEOC 1 0.044 0.002 2343 0.006 BB 0.30 

Total Area; 4.127542E+07 Total Height; 1081506 Total Amount; 2012.556 

Printed on 3/4/2013 12:35:03 PM Page 35 Page 1 of 1 
1600 

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130219-61290dp 

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, , 3.0 4.0 5.0 6.0 70 8.0 9.0 

Time - Minutes 

Raw File Name = C:ICPDATAllns1#041201 31030413.0027.raw Date Taken (end) = 3/4/201312:31 :51 PM 

Method File Name = C:ICpmethodsllnst #0412013IMethod25.1 ,3Jow.met Dilution Factor = 1 

Calibration File Name = C:ICpmethodsllnst #0412013\M251 ,310w-Oll 013CAL 

Peak # Ret. Time Name Amount Amt% Area Area % Type Width 

1 0.88 Carbon Monoxide 11 .352 0.565 160791 0.390 BB 0.28 

2 1.84 Carbon Dioxide 1998.254 99,433 41060064 99.605 BB 0,48 

3 6.00 NMNEOC 1 0.040 0.002 2136 0.005 BB 0.31 

Total Area = 4.1 22299E+07 Total Height = 1081180 Total Amount = 2009.647 

Printed on 3/4/201312:35:06 PM Page 36 Page 1 of 1 
Calibration 

Summary 

Page 37 
SCAQMD Method 25.1 125.3 Calibration Curve (GC/FIDITCA #4) 

ANAL YTE: TNMNEOC las 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 158327 5.4 6179.41 2.72 

5.44 6.84 282757 

____ 5.44 ____ 6.84 280611 _Q.8 1517.45_ 5.44 

AvgRT 6.85 RTWindow +/- 0.20 min 

Calibration Verification Standards: 

CCV Retention Time Result (oomv % Rec" 

2.5 ppmv 6.84 2.89 106.3 

2.5 PDmv dp 6.85 2.79 102.5 

Must be +/- 10 % of Theoretical Concentration 

Analysl (Inlilial & dale) ~ ,I \0113 Lab Direclor (Inilial & dale): ~I 

Jd14! ~ 

Analyst: 

Response Area 

(mean) 

6536 

14388 

27611 

64019 

162697 

281684 

Calb. Type 

R2 value: 

Intercept (8) 

Lin Consl (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 

(+1-16 '!o) 

112 

99 

95 

110 

112 

97 

Y=MX+B 

Must be> 0.990 

Included 

00 

<'"l 

<1) 

~ p... 
.. 

~ 

« 

4.E+05 

3.E+05 

3.E+05 

2.E+05 

2.E+05 

1.E+05 

5.E+04 

O.E+OO 1/ 

0.00 

TNMNEOC (as Propane) Plot 

./' V 

* ......... 

/' 

/ 

V 

1.00 2.00 3.00 4.00 

Concentration (ppmv) 

y; 53584.6911 X 

R 2 ; 0.9925 

,/ ~ 

5.00 

I 

6.00 

0-

<'1 

p... 

~ 
Date: 01/10/2013 Analyst: ZG 

Analvte: Conc. MOL #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: GC/FID #4 Units: ppmV 

MOL#2 MOL#3 MOL #4 MOL #5 MOL #6 MOL#7 

0.050 0.054 0.043 0.051 0.056 0.047 

MOL· Method Detection Limit Study per USEPA Guidelines 

MOL MRL 

0.01 6 0.049 MOL (Method Otl ~c ion Limit) (7 replicQf r '$) = StLinda:d Deviation x 3.1" 3 

MRL (Minimum Rp.porting Limit) ~ MOL x 3.0 

Is the spiked concentration < 10 times the calculated MOL 0 N 

Definition: MDL- The minimum concentration of a s ubstance thar can be IdufJtified, measured and reported with a 99% confidence interval, t/Jat 

the ana/y te concentration is greater than lero :tnd is determined from Uw analysis of a sample in a given matrix containing the analyfu. 

Definition : MRL - The smallest measu,red concentration ora s ubstance that can be reliably measured by using a given analytical method. 

o 

""" '" 00 

CO 

>l-. 
Analvte: LOD LOQ Canc./MOL 

NMOC o O~H 0052 3 

Alternative Supporting Calculations 

M%Rec S:N Ratio 

10~ .S) 

.0[1 (Lim it of Detection) Standard O('>li. iiIQ:l )' :'\.0 

LOO (L:mtt of Quantltation)= St-lnd<1rd Dr-~, ~tlo n x 10 

:.,.le" n ·( Rcc -(Mc2n Resf Truo Valuc) y 1 ClO' 't. 

Is the Mean % Ree between 80% and 120%?~ I N 

~onc.!M DL ~ Concentration J MOL 

Is the Conc.lMDL between 2 to 5?{J)1 N 

51qnal to Noisl; Ratio · (MaanlStdDfW) 

Is the signal to Noise Ratio between 2.5 and 10(2)1 N 

Definition: LOD - The lowest concentration that can be determined to be star;stically different from a blank. 

Definition: LOO · The concentration above which quantitative results can be obtained with a specific degree of confidence. 

Analyle: PQL RL 

NMOC 0.104 0.1 04 

Proposed PQL and RL 

Practical Quantitation Limit 

Is the PQl 2 to 5 times higher than the lOa?(Jjf N 

Re portmg limil 

Is the RL equal to or greater than the pal -(5)1 N 

POL (practicdl QU3ntitalion Umit) = Established by the laboratory as~ d on the: above c(liculations 

RL (Rc portinq limit) :. Es.ta bli d by tho laboratory based on the PQl and/or method. 

Definition: POL - The lowest level tl1at can be reliably achieved witllin spocified limits of precision and accuracy during routine laboratory 

operating conditions. In addition, if qllatitating at this level, the lowest point of the calibration curve must be set at this point. 

Comments: 

Analyst (sign & date): $3 \ \ t 0 \ (5 Lab Director (sign & date): 1141# 

-'<t 

.., 

~ 0... 
Appendix C.6 PM by SCAQMD Method 5.1 

R521 0729 C-10 
SCAOMD METHOD 5.1 PARTICULATE TEST DATA SUMMARY 

CUenU1.ocalion. 

Unit 

Sample Location 

Test No. 

Tes! Melhoct 

Dale 

Start Time 

Slap Time 

Sample Train 

Pilot Factor 

MeIer Cal Factor 

Slack Area (SCI It) 

Sample Time (Min) 

Bar Press (In Hg) 

Nozzle Dlam (in) 

Slack Press (iwg) 

Stack Temp (F) 

Vel Head (iwg) 

Stack 02 (%0) 

Stack C02 ~~) 

Meter Vol (acf) 

Meter Temp (F) 

Meier Press (iwg) 

liqUid Vol (ml) 

Sid Sample Vol (SCF) 

Moisture Fraction 

Stack Gas Mol Wt 

Stack Gas Velocity 1ft/sec) 

Stack Flow Rate (waclm) 

Slack Flow Rate (elsctm) 

Isoklnetlc Ratio (%) 

Facility Average Gas Flow (hscfh). 

Facility AI/erage Gas Flow (MMscfh) .. 

Total Weight Gain, mp .. 

Partic ulate Emissions 

Grain Loading . grldscf.. 

Grain Loeding @ 3% 02 . 

Grain Loading@ I S+'. 02 .. 

Grain Loading @ 12% C02. 

Mass Emlss;ons,lblhr1

•• • ....................... ............. . 

Emission Rale.lb/MMSCF 

1) 11 Iblhr per Rule 475 PM limit 

Gemma 

Sentinel 

5 

S·51STK·PM·1QO.l 

SCAOMD 5.1 

212512013 

10.56 

15:20 

12-WCS 

0.84 

0.98 

143.14 

240 

29.60 

0.234 

2.60 

735.8 

1.5209 

13.017 

' .34 187.Q32 

73.9 

1.85 

3916 

177.408 

0.090 

28.22 

105.43 

905.462 

356.867 

99.24 

8747.4 

0.675 

32 

0.0003 

0.0007 

0.0002 

0.0008 

0.85 

0.97 

Reference Temp (F). 60 

Fuel Nat. Gas 

Data By AA 

Average Limits 

2.80 

735.8 

1.5209 

13.5 

4.3 

187.03 

73.9 

1.85 

39 1.6 

177 408 

0.090 

28.22 

105.43 

905.462 

356.867 

99.24 

8747,4 

0.875 

3.2 

0.0003 

0.0007 

0.0002 

0.0008 

0.85 

0.97 

Limits 

0.01 

0.1 

11 

5.71 

Senljo~1 Unil5 100% I'M .. \II 

Summa" l 16 :01) 

3:30 PM 
I ~ 

. .~. I- : 

~ ~ = 

§! r--. 

l- ~ ~ 

I l-I1-, 

~ 

Page I 
pe.lla~ 

SCAQMD METHOD 5.1 PARTICULATE TEST DATA SUMMARY 

ClienULocation. 

UnJl 

Sample l.ocation 

Test No. 

Test Method 

Dale 

Slart Time 

Stop Time 

Sample Train 

Pilot Factor 

Meter Cal Faclor 

Stack Area (sq It) 

Sample Time (Min) 

Bar Press (in Hg) 

Nozzle Diam (in) 

Slack Press (iwg) 

Slack Temp (F) 

Vel Head (iwg) 

Slack 02 (%l 

Slack C02 (%) 

Meier Vol (ad) 

Meter Temp (F) 

Meter Press (iwg) 

Liguld Vol (mt) 

Sid Sample Vol (SCF) 

Moislure Fraction 

Slack Gas Mol Wt 

Slack Gas Velocity (ft/sec) 

Slack Ftow Rate (waclm) 

Stack Ftow Rate (dscfm) 

IsoklneUc Ratio /%) 

FaCility Average Gas Flow (hscfh), 

Facility Average Gas Flow (MMsclh) , 

Total Weight Gain. mg .. 

Particulate Emissions 

Grain Loading, gr/dscl ... 

Grain Loading @ 3% 02 .. . 

Grain Loading@ 15% 02 ... . 

Grain Loading@ 12% ~02 .. . 

Mas!> Emissions, Ib/hr •.•.•• 

Emission Rate. lbIMMSCF 

1) 11 Iblhr per Rule 475 PM Limit 

2) 5·PM lesl resu!ls discarded due to glass and graphite from sampling equipment 

Gemma 

Sentinel 

5 

S-5ISTK-PM-75-1 

SCAOMO S.I 

2125/2013 

16:42 

20:54 

!2-Wes 

0.84 

0 .980 

143.14 

240 

29.60 

0.234 

2.80 

732.7 

1.4524 

14.0 1 

3.91 

182.212 

6<.0 

1.77 

347.6 

176.068 

0.090 

28.18 

102.97 

884 ,360 

349.451 

100.58 

7063.1 

0.706 

3.2 

0.0003 

0.0007 

0.0002 

0.0009 

0 .84 

1.19 

Reference Temp (F). 60 

Fuel Nat Gas 

Data By AA 

Average limits 

2.60 

732.7 

1.4524 

14.0 

3.9 

162.21 

64.0 

1.77 

347 .6 

176,068 

0.090 

28 ,18 

102.97 

884,360 

349,451 

100.58 

7063.1 

0.706 

3.2 

0.0003 

0.0007 

0.0002 

0.0009 

0.84 

1.19 

Limits 

am 

0.' 

5" .71 

Sc," incl Un;1 S 75% PM .. ,I. Summary 

)116nOI) 

3:)0 PM 
1-: 1- . 

, I 

Page I 
... 

Della ( ...... . ~ ' ''-' 

SCAQMO METHOD 5.1 PARTICULATE TEST DATA SUMMARY 

Client/Location. 

Unit 

Sample Locatlon 

Test No. 

Test Method 

Dato 

Start Time 

StOP Time 

Sample Train 

Pilot Faclor 

Meier Cal Factor 

Slack Area (sq ttl 

Sample Time (Min) 

Bar Press (in Hg) 

Nozzle Diam (In) 

Slack Press (iwg) 

Stack Temp (F) 

Vel Head (iwg) 

Siaclot02 (%) 

Slack C02 (% ) 

Melor Vol (aci) 

Meter Temp (F) 

Meier Press (iwgl 

liquid Vol (mil 

Std Sample Vol (SCF) 

Moisture Fraction 

Stack Gas Mol Wt 

Stack Gas Velocity (tusee) 

Stack Flow Rate (wacfm) 

Slack Flow Rate (dscfm) 

Isoklnetic Ratio 1%1 

Facility Average Gas Flow (hscth) .. 

Facility Average Gas Flow (MMsc:fh) .. 

Total Weight Gain. mg. 

Particulate Emissions 

Gram Loading . gr/dscf .. 

Grain Loading @ 3% 02 

Gram Loading @ 15% 02 

Grain Loading@ 12% C02 ... 

MaliS Emissions, Ib/hr' •.......•.•.......••.• 

Emiu lon Ra le. lbIMMSCF 

1) 11 Iblh r per Rule 475 PM limit 

Gemma 

Sentinel 

5 

S-5/STK-PM·SQ· \ 

SCAQMD 5.1 

212612013 

8:30 

12:40 

12-WCS 

0.84 

0.98 

143.14 

'40 

29.47 

0.234 

1.90 

775.5 

0.7267 

14.10 

3.85 

132.322 

71 .1 

0.65 

264 

125.310 

0 .089 

28.18 

74 .37 

638.743 

242.273 

103.26 

5391.5 

0.539 

4.0 

0.0005 

0.0013 

0.0004 

0.0015 

1.02 

1.90 

Reference Tomp (F). 60 

Fuel Nat. Gas 

Dala Bv AA 

Average Limits 

1.90 

775.5 

0.7267 

14.1 

' .9 132.32 

71.1 

0.85 

264.0 

125.310 

0.089 

28.18 

74.37 

638,743 

242 ,273 

103.26 

5391 .5 

0.539 

4.0 

0 .0005 

0.0013 

0.0004 

0.00 15 

1.02 

1.90 

Limits 

0.0 1 

0.1 

11 

5.71 

nli n~l lJ ni l ~;.()% l>M.~ s 

Summary 

.l!l61ZOI3 

k lOI'M 
I l":C 

i i 

I t-

, ~ 

- t- . . 

EI , 

, 

, 

, 

, 

t-: 

~ , 

tI , Page I 
CPV SENTINEL UNIT 5 

PARTICULATE TEST 

STACK O2• CO2 DATA 

Test #: S-5/STK-PM-100-1 

Date: 2/25/2013 

Time: 10:56 15:20 

Load: 106MW 

O2 CO2 

Range 20 10 

Cal Gas 18.98 9.62 

Analyzer Zero 0.14 0.03 

Analyzer Span 19.02 9.62 

Pre-Bias Zero 0.16 0.05 

Pre-Bias Span 19.00 9.60 

Post-Bias Zero 0.16 0.23 

Post-Bias Span 18.81 9.82 

Average Bias Zero 0.16 0.14 

Average Bias Span 18.90 9.71 

Pre-test zero bias 0.1% 0.2% 

Pre-tesl span bias -0.1% -0.2% 

Post-test zero bias 0.1% 2.0% 

Post-test span bias -1.1% 1.9% 

Zero Drift 0.0% 1.8% 

Span Drift -1.0% 2.2% 

Test Results (from data logger average) 

Average 13.46 4.45 

Cal Corrected 13.47 4.34 

O2 CO2 

Date Time % % 

2/25/2013 10:55:00 13.551 4.4 

2/25/2013 10:56:00 13.542 4.405 

2/25/2013 10:57:00 13.533 4.41 

2/25/2013 10:58:00 13.518 4.421 

2/25/2013 10:59:00 13.495 4.434 

2/25/2013 11 :00:00 13.499 4.434 

2/25/2013 11 :02:00 13.545 4.418 

2/25/2013 11 :03:00 13.529 4.423 

2/25/2013 11 :04:00 13.533 4.42 
2/25/2013 11 :05:00 13.533 4.42 

2/25/2013 11 :06:00 13.525 4.426 

2/25/2013 11 :07:00 13.515 4.435 

2/25/2013 11 :08:00 13.486 4.45 

2/25/2013 11 :09:00 13.473 4.458 

2/25/2013 11 :32:00 13.505 4.445 

2/25/2013 11 :33:00 13.522 4.447 

2/25/2013 11 :34:00 13.519 4.452 

2/25/2013 11 :35:00 13.519 4.454 

2/25/2013 11 :36:00 13.521 4.45 

2/25/2013 11 :37:00 13.526 4.447 

2/25/2013 11 :38:00 13.528 4.446 

2/25/2013 11 :39:00 13.517 4.453 

2/25/2013 11 :40:00 13.513 4.456 

2/25/2013 11 :41 :00 13.525 4.449 

2/25/2013 11 :42:00 13.535 4.443 

2/25/2013 11 :43:00 13.534 4.441 

2/25/2013 11 :44:00 13.534 4.438 

2/25/2013 11 :45:00 13.536 4.435 

2/25/2013 11 :46:00 13.557 4.422 

2/25/2013 11 :47:00 13.557 4.42 

2/25/2013 11 :48:00 13.558 4.42 

2/25/2013 11 :49:00 13.555 4.419 

2/25/2013 11 :50:00 13.577 4.409 

2/25/2013 11 :52:00 13.505 4.447 

2/25/2013 11 :53:00 13.504 4.448 

2/25/2013 11 :54:00 13.498 4.45 

2/25/2013 11 :55:00 13.51 4.448 

2/25/2013 11 :56:00 13.5 4.454 

2/25/2013 11 :57:00 13.504 4.451 

2/25/2013 11 :58:00 13.499 4.454 

2/25/2013 11 :59:00 13.497 4.459 

2/25/2013 12:00:00 13.515 4.45 

2/25/2013 12:01 :00 13.519 4.449 

2/25/2013 12:02:00 13.521 4.449 

2/25/2013 12:03:00 13.519 4.45 

2/25/2013 12:04:00 13.536 4.438 

2/25/2013 12:05:00 13.55 4.431 

2/25/2013 12:06:00 13.548 4.429 

2/25/2013 12:07:00 13.555 4.421 

2/25/2013 12:08:00 13.554 4.419 

2/25/2013 12:10:00 13.584 4.426 

2/25/2013 12:11 :00 13.496 4.434 

2/25/2013 12:12:00 13.494 4.432 

2/25/2013 12:13:00 13.5 4.433 

2/25/2013 12:14:00 13.501 4.431 

2/25/2013 12:15:00 13.5 4.432 

2/25/2013 12:16:00 13.499 4.433 

2/25/2013 12:17:00 13.493 4.435 

2/25/2013 12:18:00 13.493 4.436 

2/25/2013 12:19:00 13.493 4.437 
2/25/2013 12:20:00 13.488 4.436 

2/25/2013 12:21 :00 13.489 4.437 

2/25/2013 12:22:00 13.492 4.438 

2/25/2013 12:23:00 13.495 4.436 

2/25/2013 12:24:00 13.496 4.436 

2/25/2013 12:25:00 13.487 4.439 

2/25/2013 12:26:00 13.484 4.443 

2/25/2013 12:29:00 13.496 4.436 

2/25/2013 12:30:00 13.486 4.44 

2/25/2013 12:31:00 13.495 4.435 

2/25/2013 12:32:00 13.487 4.44 

2/25/2013 12:33:00 13.492 4.436 

2/25/2013 12:34:00 13.49 4.436 

2/25/2013 12:35:00 13.48 4.441 

2/25/2013 12:36:00 13.483 4.436 

2/25/2013 12:37:00 13.473 4.44 

2/25/2013 12:38:00 13.49 4.429 

2/25/2013 12:39:00 13.503 4.423 

2/25/2013 12:40:00 13.494 4.431 

2/25/2013 12:41:00 13.496 4.43 

2/25/2013 12:42:00 13.5 4.43 

2/25/2013 12:43:00 13.505 4.428 

2/25/2013 13:03:00 13.424 4.459 

2/25/2013 13:04:00 13.427 4.462 

2/25/2013 13:05:00 13.424 4.465 

2/25/2013 13:06:00 13.422 4.466 

2/25/2013 13:07:00 13.425 4.462 

2/25/2013 13:08:00 13.422 4.466 

2/25/2013 13:09:00 13.422 4.465 

2/25/2013 13:10:00 13.426 4.462 

2/25/2013 13:11 :00 13.432 4.456 

2/25/2013 13:12:00 13.434 4.455 

2/25/2013 13:13:00 13.435 4.456 

2/25/2013 13:14:00 13.437 4.453 

2/25/2013 13:15:00 13.451 4.448 

2/25/2013 13:16:00 13.462 4.445 

2/25/2013 13:17:00 13.455 4.448 

2/25/2013 13:18:00 13.466 4.446 

2/25/2013 13:19:00 13.458 4.45 

2/25/2013 13:20:00 13.465 4.448 

2/25/2013 13:22:00 13.431 4.48 

2/25/2013 13:23:00 13.396 4.49 

2/25/2013 13:24:00 13.394 4.492 

2/25/2013 13:25:00 13.396 4.487 

2/25/2013 13:26:00 13.405 4.483 

2/25/2013 13:27:00 13.395 4.488 

2/25/2013 13:28:00 13.394 4.49 

2/25/2013 13:29:00 13.393 4.493 

2/25/2013 13:30:00 13.395 4.489 

2/25/2013 13:31:00 13.396 4.487 

2/25/2013 13:32:00 13.396 4.486 
2/25/2013 13:33:00 13.391 4.493 

2/25/2013 13:34:00 13.382 4.497 

2/25/20 13 13:35:00 13.38 4.498 

2/25/2013 13:36:00 13.385 4.494 

2/25/2013 13:37:00 13.375 4.499 

2/25/2013 13:38:00 13.358 4.509 

2/25/2013 13:39:00 13.358 4.511 

2/25/2013 13:40:00 13.362 4.508 

2/25/2013 13:41:00 13.36 4.509 

2/25/2013 13:42:00 13.359 4.511 

2/25/2013 13:44:00 13.503 4.46 

2/25/2013 13:45:00 13.431 4.467 

2/25/2013 13:46:00 13.421 4.476 

2/25/2013 13:47:00 13.421 4.472 

2/25/2013 13:48:00 13.421 4.472 

2/25/2013 13:49:00 13.42 4.472 

2/25/2013 13:50:00 13.422 4.466 

2/25/2013 13:51 :00 13.428 4.461 

2/25/2013 13:52:00 13.421 4.463 

2/25/2013 13:53:00 13.421 4.46 

2/25/2013 13:54:00 13.421 4.456 

2/25/2013 13:55:00 13.42 4.459 

2/25/2013 13:56:00 13.423 4.45 

2/25/2013 13:57:00 13.422 4.452 

2/25/2013 13:58:00 13.418 4.453 

2/25/2013 13:59:00 13.421 4.449 

2/25/2013 14:02:00 13.432 4.433 

2/25/2013 14:03:00 13.433 4.427 

2/25/2013 14:04:00 13.434 4.427 

2/25/2013 14:05:00 13.433 4.427 

2/25/2013 14:06:00 13.432 4.425 

2/25/2013 14:07:00 13.435 4.423 

2/25/2013 14:08:00 13.441 4.419 

2/25/2013 14:09:00 13.433 4.425 

2/25/2013 14:10:00 13.432 4.429 

2/25/2013 14:11:00 13.435 4.429 

2/2 5/2013 14:12:00 13.468 4.413 

2/25/2013 14:13:00 13.47 4.411 

2/25/2013 14:14:00 13.471 4.412 

2/25/2013 14:15:00 13.471 4.413 

2/25/2013 14:16:00 13.47 4.414 

2/25/2013 14:17:00 13.47 4.41 8 

2/25/2013 14:38:00 13.428 4.459 

2/25/2013 14:39:00 13.428 4.465 

2/25/2013 14:40:00 13.434 4.465 

2/25/2013 14:41 :00 13.433 4.465 

2/25/2013 14:42:00 13.433 4.467 

2/25/2013 14:43:00 13.434 4.462 

2/25/2013 14:44:00 13.435 4.462 

2/25/2013 14:45:00 13.464 4.453 

2/25/2013 14:46:00 13.469 4.455 
2/25/2013 14:47:00 13.471 4.455 

2/25/2013 14:49:00 13.485 4.482 

2/25/2013 14:50:00 13.423 4.49 

2/25/2013 14:51 :00 13.423 4.493 

2/25/2013 14:52:00 13.423 4.495 

2/25/2013 14:53:00 13.428 4.492 

2/25/2013 14:54:00 13.426 4.495 

2/25/2013 14:55:00 13.421 4.499 

2/25/2013 14:56:00 13.421 4.498 

2/25/2013 14:57:00 13.405 4.51 

2/25/2013 14:58:00 13.396 4.516 

2/25/2013 14:59:00 13.396 4.519 

2/25/2013 15:02:00 13.442 4.482 

2/25/2013 15:03:00 13.44 4.482 

2/25/2013 15:04:00 13.443 4.48 

2/25/2013 15:05:00 13.436 4.483 

2/25/20 13 15:06:00 13.446 4.475 

2/25/2013 15:07:00 13.437 4.477 

2/25/2013 15:08:00 13.436 4.478 

2/25/2013 15:09:00 13.433 4.476 

2/25/2013 15:10:00 13.432 4.48 

2/25/2013 15:11 :00 13.435 4.474 

2/25/2013 15:14:00 13.439 4.465 

2/25/2013 15:15:00 13.441 4.461 

2/25/2013 15:16:00 13.435 4.463 

2/25/2013 15:17:00 13.435 4.464 

2/25/2013 15:18:00 13.434 4.462 

2/25/2013 15:19:00 13.434 4.464 

2/25/2013 15:20:00 13.435 4.458 

Average 13.46 4.45 
CPV SENTINEL UNIT 5 

PARTICULATE TEST 

STACK O2• CO2 DATA 

Test #: S-5/STK-PM-75-1 

Date: 2/25/2013 

Time: 16:42 20:54 

Load: 80MW 

O2 CO2 

Range 20 10 

Cal Gas 18.98 9.62 

Analyzer Zero 0.13 0.12 

Analyzer Span 18.94 9.73 

Pre-Bias Zero 0.17 0.18 

Pre-Bias Span 18.88 9.74 

Post-Bias Zero 0.15 0.14 

Post-Bias Span 18.81 9.69 

Average Bias Zero 0.16 0.16 

Average Bias Span 18.85 9.71 

Pre-test zero bias 0.2% 0.6% 

Pre-test span bias -0.3% 0.1% 

Post-test zero bias 0.1% 0.2% 

Post-test span bias -0.7% -0.5% 

Zero Drift -0.1% -0.4% 

Span Drift -0.4% -0.6% 

Test Results (from data logger average) 

Average 13.95 4.04 

Cal Corrected 14.01 3.91 

O2 CO2 

Date Time % % 

2/25/2013 16:43:00 13.941 4.078 

2/25/2013 16:44:00 13.948 4.077 

2/25/2013 16:45:00 13.949 4.078 

2/25/2013 16:46:00 13.952 4.079 

2/25/2013 16:47:00 13.944 4.082 

2/25/2013 16:48:00 13.942 4.086 

2/25/2013 16:49:00 13.932 4.091 

2/25/2013 16:50:00 13.931 4.092 

2/25/2013 16:51 :00 13.929 4.09 

2/25/2013 16:52:00 13.936 4.082 
2/25/2013 16:53:00 13.927 4.085 

2/25/2013 16:54:00 13.915 4.09 

2/25/2013 16:55:00 13.933 4.078 

2/25/2013 16:56:00 13.933 4.077 

2/25/2013 16:57:00 13.939 4.075 

2/25/2013 16:59:00 13.976 4.066 

2/25/2013 17:00:00 13.943 4.075 

2/25/2013 17:01:00 13.936 4.082 

2/25/2013 17:02:00 13.938 4.082 

2/25/2013 17:03:00 13.922 4.091 

2/25/2013 17:04:00 13.95 4.075 

2/25/2013 17:05:00 13.936 4.084 

2/25/2013 17:06:00 13.917 4.095 

2/25/2013 17:07:00 13.914 4.094 

2/25/2013 17:08:00 13.951 4.073 

2/25/2013 17:09:00 13.942 4.076 

2/25/2013 17:10:00 13.926 4.082 

2/25/2013 17:11:00 13.937 4.076 

2/25/2013 17:12:00 13.896 4.098 

2/25/2013 17:13:00 13.899 4.094 

2/25/2013 17:14:00 13.91 4.089 

2/25/2013 17:16:00 13.995 4.043 

2/25/2013 17:17:00 13.984 4.044 

2/25/2013 17:18:00 13.969 4.052 

2/25/2013 17:19:00 13.962 4.053 

2/25/2013 17:20:00 13.958 4.051 

2/25/2013 17:21 :00 13.948 4.053 

2/25/2013 17:22:00 13.942 4.054 

2/25/2013 17:23:00 13.936 4.058 

2/25/2013 17:24:00 13.93 4.059 

2/25/2013 17:25:00 13.922 4.061 

2/25/2013 17:26:00 13.917 4.064 

2/25/2013 17:27:00 13.927 4.06 

2/25/2013 17:28:00 13.919 4.064 

2/25/2013 17:29:00 13.935 4.051 

2/25/2013 17:30:00 13.962 4.036 

2/25/2013 17:31 :00 13.946 4.04 

2/25/2013 17:33:00 13.933 4.051 

2/25/2013 17:34:00 13.92 4.052 

2/25/2013 17:35:00 13.926 4.047 

2/25/2013 17:36:00 13.915 4.055 

2/25/2013 17:37:00 13.918 4.052 

2/25/2013 17:38:00 13.912 4.057 

2/25/2013 17:39:00 13.931 4.046 

2/25/2013 17:40:00 13.913 4.057 

2/25/2013 17:41 :00 13.912 4.055 

2/25/2013 17:42:00 13.917 4.048 

2/25/2013 17:43:00 13.907 4.052 

2/25/2013 17:44:00 13.903 4.051 

2/25/2013 17:45:00 13.894 4.055 

2125/2013 17:46:00 13.902 4.049 
2/25/2013 17:47:00 13.904 4.048 

2/25/2013 17:48:00 13.915 4.041 

2/25/2013 18:00:00 13.94 4.024 

2/25/2013 18:01 :00 13.94 4.028 

2/25/2013 18:02:00 13.931 4.037 

2/25/2013 18:03:00 13.923 4.044 

2/25/2013 18:04:00 13.918 4.048 

2/25/2013 18:05:00 13.923 4.047 

2/25/2013 18:06:00 13.919 4.051 

2/25/2013 18:07:00 13.926 4.047 

2/25/2013 18:08:00 13.937 4.04 

2/25/2013 18:09:00 13.947 4.038 

2/25/2013 18:10:00 13.952 4.036 

2/25/2013 18:11 :00 13.957 4.037 

2/25/2013 18:12:00 13.965 4.034 

2/25/2013 18:13:00 13.97 4.031 

2/25/2013 18:14:00 13.97 4.032 

2/25/2013 18:15:00 13.981 4.027 

2/25/2013 18:16:00 13.977 4.027 

2/25/2013 18:17:00 13.987 4.018 

2/25/2013 18:18:00 13.992 4.014 

2/25/2013 18:19:00 13.989 4.017 

2/25/2013 18:20:00 14.005 4.008 

2/25/2013 18:21 :00 14.01 4.007 

2/25/2013 18:22:00 14.003 4.009 

2/25/2013 18:24:00 13.957 4.047 

2/25/2013 18:25:00 13.952 4.049 

2/25/2013 18:26:00 13.965 4.042 

2/25/2013 18:27:00 13.946 4.054 

2/25/2013 18:28:00 13.946 4.051 

2/25/2013 18:29:00 13.946 4.054 

2/25/2013 18:30:00 13.939 4.061 

2/25/2013 18:31 :00 13.941 4.058 

2/25/2013 18:32:00 13.95 4.055 

2/25/2013 18:33:00 13.947 4.056 

2/25/2013 18:34:00 13.944 4.058 

2/25/2013 18:35:00 13.95 4.054 

2/25/2013 18:36:00 13.975 4.042 

2/25/2013 18:37:00 13.962 4.049 

2/25/2013 18:38:00 13.964 4.049 

2/25/2013 18:39:00 13.953 4.057 

2/25/2013 18:40:00 13.959 4.056 

2/25/2013 18:42:00 13.958 4.065 

2/25/2013 18:43:00 13.941 4.065 

2/25/2013 18:44:00 13.929 4.073 

2/25/2013 18:45:00 13.927 4.07 

2/25/2013 18:46:00 13.937 4.064 

2/25/2013 18:47:00 13.939 4.059 

2/25/2013 18:48:00 13.938 4.061 

2/25/2013 18:49:00 13.945 4.056 

2/25/2013 18:50:00 13.959 4.048 
2/25/2013 18:51 :00 13.959 4.048 

2/25/2013 18:52:00 13.973 4.039 

2/25/2013 18:53:00 13.985 4.033 

2/25/2013 18:54:00 13.975 4.037 

2/25/2013 18:55:00 13.98 4.034 

2/25/2013 18:56:00 13.976 4.035 

2/25/2013 18:57:00 13.971 4.038 

2/25/2013 18:59:00 13.988 4.028 

2/25/2013 19:00:00 13.986 4.027 

2/25/2013 19:01 :00 13.987 4.029 

2/25/2013 19:02:00 13.982 4.032 

2/25/2013 19:03:00 13.981 4.034 

2/25/2013 19:04:00 13.981 4.034 

2/25/2013 19:05:00 13.99 4.022 

2/25/2013 19:06:00 13.991 4.025 

2/25/2013 19:07:00 13.989 4.026 

2/25/2013 19:08:00 13.999 4.019 

2/25/2013 19:09:00 13.997 4.02 

2/25/2013 19:10:00 14.018 4.006 

2/25/2013 19:11 :00 14.008 4.012 

2/25/2013 19:12:00 14.004 4.013 

2/25/2013 19:13:00 14.004 4.013 

2/25/2013 19:14:00 14 4.016 

2/25/2013 19:30:00 13.941 4.044 

2/25/2013 19:31 :00 13.944 4.047 

2/25/2013 19:32:00 13.937 4.051 

2/25/2013 19:33:00 13.936 4.052 

2/25/2013 19:34:00 13.943 4.046 

2/25/2013 19:35:00 13.948 4.043 

2/25/2013 19:36:00 13.967 4.035 

2/25/2013 19:37:00 13.964 4.039 

2/25/2013 19:38:00 13.993 4.02 

2/25/2013 19:39:00 14.006 4.011 

2/25/2013 19:40:00 14.001 4.016 

2/25/2013 19:42:00 13.951 4.059 

2/25/2013 19:43:00 13.933 4.064 

2/25/2013 19:44:00 13.93 4.068 

2/25/2013 19:45:00 13.935 4.065 

2/25/2013 19:46:00 13.942 4.062 

2/25/2013 19:47:00 13.939 4.064 

2/25/2013 19:48:00 13.951 4.06 

2/25/2013 19:49:00 13.962 4.057 

2/25/2013 19:50:00 13.977 4.047 

2/25/2013 19:51 :00 13.966 4.048 

2125/2013 19:52:00 13.979 4.034 

2/25/2013 19:54:00 13.982 4.03 

2/25/2013 19:55:00 13.928 4.038 

2/25/2013 19:56:00 13.922 4.035 

2/25/2013 19:57:00 13.921 4.031 

2/25/2013 19:58:00 13.931 4.02 
2/25/2013 19:59:00 13.907 4.031 

2/25/2013 20:00:00 13.88 4.043 

2/25/2013 20:01 :00 13.885 4.042 

2/25/2013 20:02:00 13.894 4.039 

2/25/2013 20:03:00 13.898 4.041 

2/25/2013 20:06:00 13.965 4.01 

2/25/2013 20:07:00 13.954 4.015 

2/25/2013 20:08:00 13.964 4.012 

2/25/2013 20:09:00 13.956 4.013 

2/25/2013 20:10:00 13.981 4.001 

2/25/2013 20:11 :00 13.996 3.991 

2/25/2013 20:1 2:00 14.007 3.986 

2/25/2013 20:13:00 14.01 3.986 

2/25/2013 20:14:00 14.009 3.99 

2/25/2013 20:15:00 14.036 3.976 

2/25/2013 20:24:00 13.972 4.006 

2/25/2013 20:25:00 13.987 4.013 

2/25/2013 20:26:00 13.985 4.014 

2/25/2013 20:27:00 13.985 4.016 

2/25/2013 20:28:00 13.991 4.009 

2/25/2013 20:29:00 13.991 4.01 

2/25/2013 20:30:00 14.037 3.984 

2/25/2013 20:31 :00 14.042 3.98 

2/25/2013 20:32:00 14.045 3.979 

2/25/2013 20:33:00 14.049 3.98 

2/25/2013 20:35:00 14 4.029 

2/25/2013 20:36:00 13.985 4.028 

2/25/2013 20:37:00 13.964 4.039 

2/25/2013 20:38:00 13.962 4.04 

2/25/2013 20:39:00 13.978 4.031 

2/25/2013 20:40:00 13.941 4.047 

2/25/2013 20:41 :00 13.954 4.043 

2/25/2013 20:42:00 13.943 4.048 

2/25/2013 20:43:00 13.948 4.042 

2/25/2013 20:44:00 13.977 4.027 

2/25/2013 20:45:00 13.98 4.029 

2/25/2013 20:47:00 13.964 4.041 

2/25/2013 20:48:00 13.94 4.046 

2/25/2013 20:49:00 13.948 4.041 

2/25/2013 20:50:00 13.948 4.042 

2/25/2013 20:51 :00 13.943 4.041 

2/25/2013 20:52:00 13.938 4.046 

2/25/2013 20:53:00 13.93 4.05 

2/25/2013 20:54:00 13.939 4.041 
Average 13.95 4.04 
CPV SENTINEL UNIT 5 

PARTICULATE TEST 

STACK O2 • CO2 DATA 

Test #: 

Date: 

Time: 

Load: 

S-5/STK-PM-50-1 

2/26/2013 

8:30 12:40 

55MW 

O2 

Range 20 

Cal Gas 18.98 

Analyzer Zero 0.11 

Analyzer Span 18.95 

Pre-Bias Zero 0.16 

Pre-Bias Span 18.96 

Post-Bias Zero 0.15 

Post-Bias Span 18.84 

Average Bias Zero 0.15 

Average Bias Span 18.90 

Pre-test zero bias 0.2% 

Pre-test span bias 0.0% 

Post-test zero bias 0.2% 

Post-test span bias -0.6% 

Zero Drift -0.1% 

Span Drift -0.6% 

CO2 

10 

9.62 

0.07 

9.68 

0.11 

9.65 

0.17 

9.73 

0.14 

9.69 

0.4% 

-0.4% 

0.9% 

0.4% 

0.6% 

0.8% 

Test Results (from data logger average) 

Average 14.08 3.96 

Cal Corrected 14.10 3.85 

O2 CO2 

Date Time % % 

2/26/2013 8:31 :00 14.211 3.9 

2/26/2013 8:32:00 14.208 3.901 

2/26/2013 8:33:00 14.203 3.902 

2/26/2013 8:34:00 14.214 3.894 

2/26/2013 8:35:00 14.216 3.888 

2/26/2013 8:36:00 14.215 3.888 

2/26/2013 8:37:00 14.201 3.89 

2/26/2013 8:38:00 14.214 3.879 

2/26/2013 8:39:00 14.199 3.883 

2/26/2013 8:40:00 14.2 3.88 
2/26/2013 8:41 :00 14.212 3.871 

2/26/2013 8:42:00 14.206 3.87 

2/26/2013 8:43:00 14.183 3.874 

2/26/2013 8:44:00 14.185 3.872 

2/26/2013 8:45:00 14.179 3.871 

2/26/2013 8:47:00 14.169 3.881 

2/26/2013 8:48:00 14.147 3.887 

2/26/2013 8:49:00 14.145 3.887 

2126/2013 8:50:00 14.148 3.883 

2/26/2013 8:51 :00 14.143 3.885 

2/26/2013 8:52:00 14.132 3.89 

2/26/2013 8:53:00 14.127 3.893 

2/26/2013 8:54:00 14.123 3.896 

2/26/2013 8:55:00 14.099 3.91 

2/26/2013 8:56:00 14.098 3.911 

2/26/2013 8:57:00 14.108 3.905 

2/26/2013 8:58:00 14.107 3.907 

2/26/2013 8:59:00 14.091 3.919 

2/26/20 13 9:00:00 14.092 3.915 

2/26/2013 9:01:00 14.079 3.925 

2/26/2013 9:02:00 14.083 3.921 

2/26/2013 9:04:00 14.183 3.892 

2/26/2013 9:05:00 14.12 3.899 

2/26/2013 9:06:00 14.107 3.905 

2/26/2013 9:07:00 14.095 3.912 

2/26/2013 9:08:00 14.102 3.91 

2/26/2013 9:09:00 14.1 3.912 

2/26/2013 9:10:00 14.095 3.912 

2/26/2013 9:11 :00 14.097 3.911 

2/26/2013 9:12:00 14.089 3.916 

2/26/2013 9:13:00 14.095 3.913 

2/26/2013 9:14:00 14.093 3.916 

2/26/2013 9:15:00 14.093 3.916 

2/26/2013 9:16:00 14.089 3.917 

2/26/2013 9:17:00 14.096 3.914 

2/26/2013 9:18:00 14.103 3.91 

2/26/2013 9:19:00 14.1 3.912 

2/26/2013 9:21:00 14.178 3.897 

2/26/2013 9:22:00 14.111 3.904 

2/26/2013 9:23:00 14.119 3.901 

2/26/2013 9:24:00 14.12 3.902 

2/26/2013 9:25:00 14.1 22 3.899 

2/26/2013 9:26:00 14.1 23 3.899 

2/26/2013 9:27:00 14.119 3.901 

2/26/2013 9:28:00 14.106 3.907 

2/26/2013 9:29:00 14.106 3.909 

2/26/2013 9:30:00 14.102 3.912 

2/26/2013 9:31 :00 14.102 3.912 

2/26/2013 9:32:00 14.1 3.913 

2/26/2013 9:33:00 14.107 3.91 

2/26/2013 9:34:00 14.1 04 3.912 
2/26/2013 9:35:00 14.107 3.912 

2/26/2013 9:36:00 14.099 3.915 

2/26/2013 9:37:00 14.102 3.914 

2/26/2013 9:50:00 14.089 3.926 

2/26/2013 9:51 :00 14.088 3.932 

2/26/2013 9:52:00 14.086 3.938 

2/26/2013 9:53:00 14.083 3.938 

2/26/2013 9:54:00 14.092 3.929 

2/26/2013 9:55:00 14.096 3.927 

2/26/2013 9:56:00 14.076 3.937 

2/26/2013 9:57:00 14.051 3.945 

2/26/2013 9:58:00 14.066 3.939 

2/26/2013 9:59:00 14.057 3.943 

2/26/2013 10:00:00 14.069 3.938 

2/26/2013 10:01 :00 14.077 3.936 

2/26/2013 10:02:00 14.062 3.941 

2/26/2013 10:03:00 14.057 3.945 

2/26/2013 10:04:00 14.04 3.954 

2/26/2013 10:05:00 14.049 3.954 

2/26/2013 10:06:00 14.058 3.948 

2/26/2013 10:07:00 14.059 3.947 

2/26/2013 10:08:00 14.056 3.949 

2/26/2013 10:09:00 14.073 3.942 

2/26/2013 10:10:00 14.083 3.942 

2/26/2013 10:11 :00 14.067 3.949 

2/26/2013 10:12:00 14.072 3.949 

2/26/2013 10:13:00 14.091 3.941 

2/26/2013 10:14:00 14.067 3.955 

2/26/2013 10:15:00 14.088 3.943 

2/26/2013 10:17:00 14.079 3.954 

2/26/2013 10:18:00 14.058 3.965 

2/26/2013 10:19:00 14.059 3.964 

2/26/2013 10:20:00 14.054 3.968 

2/26/2013 10:21 :00 14.042 3.976 

2/26/2013 10:22:00 14.038 3.98 

2/26/2013 10:23:00 14.04 3.983 

2/26/2013 10:24:00 14.04 3.982 

2/26/2013 10:25:00 14.041 3.982 

2/26/2013 10:26:00 14.037 3.987 

2/26/2013 10:27:00 14.04 3.988 

2/26/2013 10:28:00 14.026 3.994 

2/26/2013 10:29:00 14.033 3.993 

2/26/2013 10:30:00 14.032 3.997 

2/26/2013 10:31 :00 14.026 4 

2/26/2013 10:32:00 14.038 3.994 

2/26/2013 10:33:00 14.038 3.995 

2/26/2013 10:36:00 14.08 3.978 

2/26/2013 10:37:00 14.056 3.99 

2/26/2013 10:38:00 14.061 3.988 

2/26/2013 10:39:00 14.072 3.984 

2/26/2013 10:40:00 14.074 3.984 
2/26/2013 10:41 :00 14.061 3.99 

2/26/2013 10:42:00 14.075 3.986 

2/26/2013 10:43:00 14.089 3.979 

2/26/2013 10:44:00 14.088 3.977 

2/26/2013 10:45:00 14.078 3.98 

2/26/2013 10:46:00 14.088 3.973 

2/26/2013 10:47:00 14.087 3.973 

2/26/2013 10:48:00 14.089 3.969 

2/26/2013 10:49:00 14.087 3.968 

2/26/2013 10:50:00 14.091 3.964 

2/26/2013 10:51 :00 14.089 3.967 

2/26/2013 10:52:00 14.065 3.981 

2/26/2013 10:54:00 14.075 3.986 

2/26/2013 10:55:00 14.069 3.986 

2/26/2013 10:56:00 14.057 3.994 

2/26/2013 10:57:00 14.063 3.993 

2/26/2013 10:58:00 14.074 3.991 

2/26/2013 10:59:00 14.059 3.998 

2/26/2013 11 :00:00 14.085 3.99 

2/26/2013 11 :01 :00 14.081 3.995 

2/26/2013 11 :02:00 14.083 3.993 

2/26/2013 11 :03:00 14.088 3.995 

2/26/2013 11 :04:00 14.089 3.993 

2/26/2013 11 :05:00 14.085 4.001 

2/26/2013 11 :06:00 14.082 4.001 

2/26/2013 11 :07:00 14.084 4.006 

2/26/2013 11 :08:00 14.083 4.004 

2/26/2013 11 :09:00 14.085 4.006 

2/26/2013 11 :25:00 14.106 3.989 

2/26/2013 11 :26:00 14.088 3.993 

2/26/2013 11 :27:00 14.073 4.005 

2/26/2013 11 :28:00 14.064 4.007 

2/26/2013 11 :29:00 14.065 4.008 

2/26/2013 11 :30:00 14.087 4.001 

2/26/2013 11 :31 :00 14.081 4.005 

2/26/2013 11 :32:00 14.057 4.014 

2/26/2013 11 :33:00 14.068 4.01 

2/26/2013 11 :34:00 14.059 4.014 

2/26/2013 11 :35:00 14.067 4.01 

2/26/2013 11 :36:00 14.065 4.011 

2/26/2013 11 :37:00 14.047 4.019 

2/26/2013 11 :38:00 14.071 4.011 

2/26/2013 11 :39:00 14.071 4.011 

2/26/2013 11 :40:00 14.052 4.019 

2/26/2013 11 :41:00 14.052 4.017 

2/26/2013 11 :42:00 14.049 4.019 

2/26/2013 11 :43:00 14.05 4.02 

2/26/2013 11 :44:00 14.054 4.015 

2/26/2013 11 :45:00 14.063 4.013 

2/26/2013 11 :46:00 14.069 4.008 

2/26/2013 11 :47:00 14.067 4.009 

2/26/2013 11 :48:00 14.065 4.007 
2/26/2013 11 :49:00 14.075 4.004 

2/26/2013 11 :50:00 14.053 4.009 

2/26/2013 11:51 :00 14.055 4.004 

2/26/20 13 11 :52:00 14.048 4.006 

2/26/2013 11:53:00 14.046 3.998 

2/26/2013 11 :54:00 14.037 4 

2/26/2013 11 :55:00 14.036 3.999 

2/26/2013 11 :56:00 14.029 3.997 

2/26/2013 11 :57:00 14.031 3.994 

2/26/2013 11 :58:00 14.028 3.994 

2/26/2013 11 :59:00 14.03 3.993 

2/26/2013 12:00:00 14.026 3.994 

2/26/2013 12:01 :00 14.025 3.995 

2/26/2013 12:02:00 14.024 3.997 

2/26/2013 12:03:00 14.028 3.995 

2/26/2013 12:04:00 14.03 3.995 

2/26/2013 12:05:00 14.029 3.994 

2/26/2013 12:06:00 14.021 3.997 

2/26/2013 12:07:00 14.024 3.995 

2/26/2013 12:08:00 14.018 4 

2/26/2013 12:09:00 14.025 4 

2/26/2013 12:10:00 14.024 4.002 

2/26/2013 12:11 :00 14.016 4.006 

2/26/2013 12:12:00 14.013 4.012 

2/26/2013 12:13:00 14.026 4.006 

2/26/2013 12:14:00 14.013 4.014 

2/26/2013 12:15:00 14.012 4.017 

2/26/2013 12:16:00 14.013 4.019 

2/26/2013 12:17:00 14.023 4.013 

2/26/2013 12:18:00 14.017 4.015 

2/26/2013 12:19:00 14.022 4.021 

2/26/2013 12:20:00 14.051 4.016 

2/26/2013 12:21 :00 14.061 4.012 

2/26/2013 12:22:00 14.055 4.016 

2/26/2013 12:23:00 14.05 4.015 

2/26/2013 12:24:00 14.054 4.013 

2/26/2013 12:25:00 14.055 4.014 

2/26/2013 12:26:00 14.073 4.006 

2/26/2013 12:27:00 14.085 3.998 

2/26/2013 12:28:00 14.098 3.99 

2/26/2013 12:29:00 14.11 3.983 

2/26/2013 12:30:00 14.106 3.987 

2/26/2013 12:31 :00 14.108 3.987 

2/26/2013 12:32:00 14.109 3.989 

2/26/2013 12:33:00 14.118 3.984 

2/26/2013 12:34:00 14.118 3.983 

2/26/2013 12:35:00 14.109 3.989 

2/26/2013 12:36:00 14.108 3.989 

2/26/2013 12:37:00 14.107 3.989 
Average 14.08 3.96 
WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: .-, 

L OCA TION ... : -:'"'~oLI="'-:'~ DATE: ...-- .., c.7 

RUN NO: '- cs:; '.. ""'- rJ.-

OPERATOR: ~ 

METER BOX NO: j, C-<../C' 

METER liH@: (- ~ (;,V· :-'> 

METER Yd: . 

STACK AREA, FT ==: _~ '''{=!,-....,..,'7'7"'''''' TRAVERSE POINTS, MIN/POINT: cJ.:t.: 

li H= li P: /' 

Probe Condition, pre/post test: V (/ 

Silica Gel Expanded, YIN: fJ/ 

Filter Condition after Test: _ _ -':7;r-__ _ Check Weight: Z 

Meter liP 

Point TIme Volume, ft' in. H,O 

if (; /115 c.,. 111'-1·7;). c( I , c.; 

S 1/017 .'22.. 11[; I , ? 

'-I 1/ 1 G "VO,~10 I 2-

"I 112" ?3.5',P/'f j. "3 

2. //8y ?:fL. 112- I. 'Z. 

I II "f (., ;r.s-o kv /. z.. 

0 liS 10 !?5(':. ?~" /<.. 

I>J ,;, 1.,207 ~". 7(.'-, J. :z. 1~/7 8~"5 5'7 <.l- i . -.0> ~ 

'/ 1.22.. 7 I8'qO. ?f<, / . "'3 

'? f'L. '3 '7 F:7¥: q"l j . '7 

d /2'-17 fl '-f. 01 /' ¥' 

I /2-57 ,1''12.. , .),/ j. '7 

/::} Ig07 "Ie} 2· 'Y "''-

Average: 

AMBIENT TEMPERATURE: C ~. ' r Imp. # Contents Post-Test - Pre-Test = Difference 

BAROMETRIC PRESSURE: ~C ~_k ASSUMED MOISTURE: ---"-- _ PITOT TUBE COEFF, C'-p-: --- 1"-jff'-. 7{/'7. --;4"'7.-' - - -

PROBE ID NO/MATERIAL: ~ 2- (., S )' 

J 

;::z. 

:J.qq,"L 1'1<;:1 

q '{ b.D "') )'0.2, 

0):. Ii? 0 

or. H1"o 

PROBE LENGTH: G ~ ~ :;? 

NOZZLE ID NO/ MATERIAL:.--::::-'SO::=-.,-7/ ____ _ _ _ 

NOZZLE DIAMETER: ::2 ') if 

FILTER NO/TYPE: 'S"'S"..--'-j7::7:::-'::;Z"''d'''· .----=--- -

3. 

Z. 

T? ...... v 1-/ 

S·h. 

(., 06· '-b I.. C<J.S --

QrJ7. r", "6'" ,·S 

PRE-TEST LEAK RATE: : ~M@ <> in. Hg. 

POST-TEST LEAK RATE:: FM@ in. Hg. 5.«1 f5 Z .Lf:.'~}. \-1, G 

PITOT LEAK CHECK - PRE POST: 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN -'r'"''c..--

SAMPLER iLA 

SAMPLE CUSTODIAN~fV'G~ __ Total: _ ______ _ . __ _ 

liH Stack Probe Filter Imp. Out Meter Temp, OF Vacuum 0 , P. static 

in. H,O Temp, OF Temp, OF Tem ,oF Temp, OF In Out in. HQ. % in. H,O 

/ • ..L. 7] '-/ ,)C h .c) 1)'/- <?i '7... '/ ?I "" . '-/- 7:5(' X . ,r ss ?fa 9'U "2- . '-j 73C .X' X .:;2- xn "7 C '2-

.;) "73 '/ A :x. <'7 10 '7'1 'V-:5 

· if 73i..f' . X J( <)',-/ -;'.0 -7 .'>' '2-

.<., 7:!) .Y-- .;') -1 ' ~ '7 '/' ":J.-

A ./"-- ./'-. .Y X Y 'X 

/. ~ 7~ -::> )( -" <;b 7(/ . ,. -z-. '-' 

/ . S'" 7'5<; )( -t- . 7'1 --;J(v --7' :> '/, .- /. S-- 7:r( "X V S7, 7<"'" 7'1' 2 · ~ / . . ~~ --;")7 V "- S'Lf 7li '7, 2-' ') 

j. Y' 7'3'7 'x ~y -S.(, 7 7.-/ J, u 

~·P\ <'7> £. '>< ')<. S'I 7'{ 77 9.0 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 1/25/2013 Page L Of A DS834049 Master Document Storagel FormslDatasheetsl Field Datasheets 
Dellal1 

... _'-' .... -- WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: G6l:::':"-1 0{ . 

LOCATION: S';;! L, \' 7 DATE: :::d,. kC::; - I::::::::' 

RUN NO: ?'$+k - P":1 - jQ0 - I 

OPERATOR: rfi'0i 

METER BOX NO: \1.... -1.<../( S 

METER L1H@: \ . \0 \P --;z 

METER Yd: D.01av 

STACK AREA, FT': . 

TRAVERSE POINTS, MIN/POINT: IVI ?-q L1H~~XLl : Probe Condition, pre/post test ____ _ 

Silica Gel Expanded, Y/N: _ _ ___ _ 

Filter Condition after Test _____ _ 

Check Weight ___ _____ _ 

Meter 

Point 1 Time 1 Volume, ft' 

lie, C; I i 7;( lP I PI''' ,r . ., I() 

t:; I i;>;'1 G I 90«·1'(7 

r?J) 0 1 q/ ,), Ci'6/ 

1,!1;t./C; 1 CV2-'" ,u,C,C 

o- l~wT.qc:? ~ ,Z["l{ I~ I<..> I Cftfl -; to (,., ;) II t( I V I q,SI2b c/. 

,I ~ IN} u l "I)/ . z.t;<..> 

'7. 1/'f3o 111::;5)'/') i.-

('f "f'() I q (Pf:L 2.0,) 

1'-15'0 Iq 1 0 . qJc" 

r ~ I /S'"clJ I qwif. 6"3 ' 

7 IISlu Iq'n .QSL 

U 1(52.0 I/oo(,?<."( 

~ Aver~ 

comments~ '\ ~ '-I . c,') 1 

Date of last revision 1/25/2013 

LIP 

in. H20 

1 5' 

2... 

'/. &> 

~ "'\ ..... ~ 

r 2-

)(' 

I~{.e 

/' f/-:? 

/'. y? 

i · q 

'7 , 

I Cl 

AMBIENT TEMPERATURE: (... L/ 

BAROMETRIC PRESSURE ---"¢-~Cf .-:"'''' ~- --

ASSUMED MOISTURE: PITOT TUBE COEFF, :--~O;-·-':-:c:)-cV:-;r---

PROBE ID NO/MATERIAL: Jt z- &- 5'"5 

PROBE LENGTH: In t- =:'I NOZZLEIDNO ~A~T=E~R~I~LL-: -L----~-'-h"- ~ 

NOZZLE DIAMETER: ,.KL ~. 

FILTER NO/TYPE: ' 

PRE-TEST LEAK RATE: : CFM@ in. Hg 

POST-TEST LEAK RATE: :<,;.vJ ;;I CFM@ /5 in. Hg /) 

PITOT LEAK CHECK - PRE: POST: vte>-c.£./ 

CHAIN OF CUSTODY: SAMPLE CUSTPPI~N--,t7=--,.".--,,_ 

SAMPLER ,;2~ /9 

L1H 

in. H20 

/' g t . D 

I . 

. '7 J . L.f. 

. t.:; 

x' 

1 

2 . ' 

:;!.. , 

2. , -., 

;2 , </ 

"2 ..::2 

Stack 

Tamo, OF 

7'5 r'.> 

f <;?tQ. 

-("7 <) 

77<?.? 

?v-,-

7~ <> 

x' 

73 "") 

--7}(, 

-,.." '--L 

7-:'7.. 

/ :> "2., 

23..5. 

SAMPLE CUSTODIAN _ _ _ _ 

Probe 

Temo, OF 

y 

'X' 

'X 

x 

..x 

x 

x 

~ 

x 

':LS, 

x 

'Y 

...x 

Filter 

Temp, OF 

x 

...Y' 

x 

.x 

.X 

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Page L of dDS834049 

Master Document StoragelFormslDatasheetsiField Datasheets 
Delta/).. 

"'~--

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: a ·eM,.vt q 

LOCATION;,5ee1d:-A"",-Z 

DATE: ;2, 25 .. ;2-0/3 

RUN NO: 5-.5/Yf/r -P-",:?- ZQ 1 

OPERATOR: ;tlfry - cv1 

METER BOX NO: / ,21- - <..-<-C S 

METER tlH@: / ce &, '3 

METERYd: a·? e,u 

STACK AREA, FT': 142]. \4 

TRAVERSE POINTS, MIN/POINT: Z'jt242 

tlH; I·...L-x tiP: / 

Probe ConditIOn, pre/post test . ......,YiM-_ _ _ Silica Gel Expanded, Y/N:. ___ TV7'7 

AMBIENT TEMPERATURE: Vf:2 

BAROMETRIC PRESSURE-: -;1."'''1''',-:-'''-70,.-'-------

ASSUMED MOISTURE: ~"Ylo PITOTTUBE COEFF, C'-::p:-: -~tfJ'::' . ,?G~<::-:ZT"'------

PROBE ID NO/MATERIAL: .;;2 y GLA.s 5' 

PROBE LENGTH: &;. PT NOZZLEIDNO M~A~T~E IA -:~5~-:-7r--------

NOZZLE DIAMETER:.=·::-~_'f~1i:!c:::---------­ FILTER NO/TYPE: Ss= 17']4 PRE-TEST LEAK R"'A:-:T"'E"': -:: 27~':;;"':-:: «.>7:i;z...c =F::-;M-:-@::::---/CCl-;-:~---,,.--:. H-:-g-.-

POST-TEST LEAK RATE: : CF;t@ = in. Hg. L£<-

PITOT LEAK CHECK - PRE: 6,(JC/.~ POST: 4,\ l 

CHAIN OF CUSTODY: SAMPLE CUShODIAN "" ( rj 

Imp. # Contents Post,Test - Pre-Test; Difference 

, l) f :1, D luo>.j 7 C)'j ,.$" 

1- OJ '1,,0 '53'1,\ i3'2.,b 

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Filter Condition after Test d 

Check Weight. _____ "'IT_ SAMPLER K,"'\ 

SAMPLE C~U-;;S"'T:;:O;;:Dc-IA;c;N:;-M"' >lT/ Total: _____________ _ 

Meter tiP tlH Stack Probe Filter Imp. Out Meter Temp, OF Vacuum 

Point I Time I Volume, ft3 in. H20 in. H20 Temp, OF Temp, OF Temp, OF Temp, OF In lOut in. Hg. 

u) 1", 1 1&<14- 14". '?9'ol (. '1 ;: . '73) ---x )( S'1 ?<? I ?'-"<, I 5 . 0 

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O liZi,q-'\T (0.2. qs<.; 

Average: 

0, 

% 

P. static ' 

in. H20 

7' ..2, go; 

Comments: ____________________________________________________________________________________________________________ __ 

Date of last revision 1/25/2013 page_I of L DS834049 

Master Document StoragelFormslDatasheetslField Datasheets 
Dellal1. "'-- - WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: '\.....,..::' .'C../'" - 'tv ...... '-..'-'1 

LOCATION: 'S>£<"'" , DATE: ..-:2...-

RUN NO: 5C54¥fIV';:- /2-

OPERATOR: ~ ,- Vi?' 

METER BOX NO: I a - : < 

METER 6H@: I , Co (, 3> 

METER Yd: 0 \ v 

STACK AREA, FT ;r: ;:r:iiitt~fi;\lbWJ~'l TRAVERSE POINTS, MIN/POINT: 

=~ : 

Probe Condition, pre/post tesl: ____ _ 

Silica Gel Expanded, Y/N: _____ _ 

Filter Condition after Tesl:. ___ __ _ 

Check Weighl: _ _ ___ ____ _ 

AMBIENT TEMPERATURE: ? A 

BAROMETRIC PRESSURE :_ ::!,? , ~P'-"c.!&",,,-____ _ ASSUMED MOISTURE: 

PITOT TUBE COEFF, C'-"p-: --g,-::--..e"------

PROBE ID NO/MATERIAL: .-/:k:?('p 5''-::' 

PROBE LE NGTH ::-:-=~lje'7:-:,E,:-,-,'L-'--_-:---;-__ ----;=-cNOZZLE ID NO/ MATERIAL: !~ 1 'S:s 

NOZZLE DIAMETER:·--,~25=c '-.3'-.L---------

FILTER NOfTYPE: 

PRE-TEST LEAK R"'A""T;:;E:-:-: - ---,C"'F"'M"'@;;:-- - --,iC'"n""' . H""g-.-

POST-TEST LEAK RATE: :~" V,.:LCFM@ ('-) ,n.fig, /) 

PITOT LEAK CHECK - PRE: POST:-f"?2",, ' ~~"-"=~ 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN-iL.1 __ _ 

SAMPLER 

SAMPLE C"'U"'S"'T"'O"'D:;-IA;-;N.,---

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

-::te: P:t-l---

Total: _ _ __ ________ _ _ 

Meter 6P 6H Stack Probe Filter Imp. Out Meter Temp, OF Vacuum 0 2 P. static 

Point Time Volume, ft' in. H20 in. H20 . Temp, ' F Temp, OF Temp, OF Temp, OF In Out in. Hg. % in. H20 

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Average: 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 1/25/2013 Page~of 2-

DS834049 

Master Document StoragelFormslDatasheetslField Datasheets 

r , 
Del/al1 

... - - .-- WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: G e \V\ ,,1\ OJ 

LOCATION: Sf' ",*,,1\ -e.. \ 

DATE: ::b - &~ - ;J.. a 1..:'2 

~~~~~0I?-1fft; P~0 -5?- METERBOX~N~O~:~\~'~~-~uJ~~C~3r---

METER <'>H@: \ , (p 1R :3 

METERYd: £ .<>'\.20 

STACK AREA, Fr: /"131'1 

TRA VE RS E POI NT~S;--, f.M~1 ~/Pf.Of.I""N"'T-l:-:;O"I-i::-i:77 

<'>H=~<'>P: /' 

Probe Condition, pre/post test:-",/':cr----"--v __ Silica Gel Expanded, YIN: iJ " 

Filter Condition after Test: 7 

Check Weight: <7 

Meter 

Point I Time I Volume, ft' 

11 1\1 c> ~'i5Ju 1,;iDCf ,2(oO:; <J 1 tiN;?] ,;<.Fo -;-'1T f 

UI til', u J;2.1~ , ~v r 

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. U 

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( 8'2--

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AMBIENT TEMPERATURE:._--,W=::,-,'!:"'2Z· --,-,= ____ _ BAROMETRIC PRESSURE: ~~ 'f J 

ASSUMED MOISTURE: 0 

PITOT TUBE COEFF, C-p:-~""· -, iZ"' ,c:(:77'''-------

PROBE ID NO/MATERIAL: ff:;; Gl--AS,S 

PROBE LENGTH: U Pc ~ 

NOZZLE ID NO/ MATERIAL:=".S'----'I'--______ _ 

NOZZLE DIAMETER: ';2 9i 

FILTER NO/TYPE: "rC;;~"""-"'llf:q,;;-Q;:---------

PRE-TEST LEAK RATE: :<'''',,,''bCFM@ Ira in. Hg. UJ 

POST-TEST LEAK RATE: : C~@ in. Hg. ;d 

PITOT LEAK CHECK - PRE: Gtf't1 . POST: 11 Z 

CHAIN OF CUSTODY: SAMPLE USTQDIAN Mk. IJ 

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

\ 011"'-6 %'1,7 J '1.'1. "/, -

1-

- j) r: 11], () 1> l.i;? ,~ 7 Lf'1,(' 

') f ""~ b,: (,01,) :;q <t, 7 

LI , lr] . '132.4 '10'O~ 

Lrt OJ: \.1-,..0 \ uv 

SAMPLER t5.11-<-( SAMPLE CUSTODIAN ?IC Total: _ ______________ _ 

<'>H 

in. H20 

7· Z 

I 2-

/ . v , 9;' 

, '''17 : 02 

'/. 

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71;z... 

775 

77f1 

'11~ 

17& 

'71.'2 

'/. 

'1'7t(~ 

'129; 

.,7"1 

'77 '9, 

'77 ~ 

77 </' 

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Temp, OF 

x 

1 

x 

x 

r· ,~ 

2 

1 

x 

y 

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.;" 

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Temp, OF 

A' 

1 

x 

x 

L. 

.1! 

)(. 

)< 

--=:. 

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Temp, OF In lOut 

2"<, __ I ?! I Vb 

'11 73 1 t::'i 

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in. Hg. 

--'2 

:3 

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2.. 

'2..... 

Y.. 

z.: 

2-

'7 

'2.-.£ 

.:2. 

.3 

0 2 

% 

P. static 

in. H20 

fY,,, 

Comments: ____________________________________________________________________________________________________________________ __ 

Date of last revision 1/25/2013 Page __ I __ of ,;;L.. 

DS834049 

Master Document StoragelFormslDatasheetslField Datasheets 
Della/'). """"'"""-_ ...... 

WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: C -:r.e.v<-C ;,.vt ~ LOCATION: Se.r,",J;:,~ 

DATE: iJ.--;L'i> " <' 

AMBIENT TEMPERATURE: {/ -:> 

BAROMETRIC PRESSURE:,--- -,OZf.q""'". "'</":7::7,,--------

ASSUMED MOISTURE: 

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

RUN NO: _ 5 < - 1''''1.- D 

OPERATOR: 

PITOT TUBE COEFF, C-,-p:,----Q::::-. 'toJ ""0z------- -- '- METERBOX~N~O~:~~r-~c~~----

METER tlH@: (. & & ;. 

METER Yd: 0. q t' rJ 

PROBE ID NO/MATERIAL:_)t£l-o;",2=0""-_ _ ___ ___ _ 

PROBE LENGTH ==:"(/ ---,(;,--,-------=-__;;_- NOZZLE ID NO/ MATERIAL: 5 " ( "?-.5 

NOZZLE DIAMETER:---,-' -<:J-:..;2'--<fL-________ _ 

--- /L 7iH='" --- STACK AREA, FT': 

TRA VE RSE POI NT"'S'-, M=-I N"'/P"'O"'I""NT"":-c"J'""'r""';t,'-f/C7. 

tlH= XtlP: i , 

Probe Condition, pre/post tesl: _____ _ 

Silica Gel Expanded, Y/N: _________ _ 

Filter Condition after T est: _ _ ____ _ 

FILTER NOrTYPE: 

PRE-TEST LEAK R"'A"'T"'Ec-: -: ------,C"'F"'M""@;;:-------,ic-n.--=H7 g-.-

POST-TEST LEAK RATE:Zr2"'" 2cFM@ 1 f-2 in. HlV 

PITOT LEAK CHECK - PRE: POST: 1./ 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN --"'-----

SAMPLER /Z.JJ(' 

Check Weight: ______ _ ___ __ SAMPLE CUSTODIAN, _ __ _ Total: _______ __________ _ 

Meter tlP tlH Stack Probe Filter Imp. Out Meter Temp, OF 

Point I Time I Volume, ft' in. H,O in. H,O Temp, of Temp, of Temp, ~F Temp, of In lOut in. Hg. 

4'-{lTfI)?,1 1213'. ;?ib'2. l --;(ii<J I .7,)-, I 17L! -Ix -I .. - -/\ I "7 '7 I c/o I '70 .2.0 

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Comments: [tV/Of cll<'<l'ill J 0 . ( "j ,2prt f.-It- '" 

0 , 

% 

P. static 

in. H,O 

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Date of last revision 1/25/2013 Page 2.. of L--

DS834049 

Master Document StoragelFormsl DatasheetslField Datasheets 
",,-_ Oe/tal'!t. .. - WET CHEMICAL SAMPLING SYSTEM DATA AND WORKSHEET - STANDARD 

CLIENT: ~;~:r t:..VV\ i4 OJ 

~~~~:I0'i_~~: t, ~ifi~ RUN NO: _ __ ' "f1?\ OPERATOR: ,i v ,Atl 

METER BOX NO: \ 2- _v.-C 

METER t.H@: \, ?i'e:.'? ~~g:~~A, F$:' )~ TRAVERSE POINT:'S:-, 7M"'IN::-I=P"'0""IN':::T:-:--

t.H= _ _ Xt.P: 

Probe Condition, pre/post test: ____ _ 

Silica Gel Expanded, YIN: 

Filter Condition after T est:------

Check Weight: _________ _ 

------- -

Meter t.P 

Point Time Volume, ft3 in, H,O 

7'<Y(,)(0 ,;;L () 

\ 

".- \ __ I 

\. I 

\ 

\ 

AveraQe: 

AMBIENT TEMPERATURE: Imp: # Contents Post-Test - Pre-Test = Difference 

BAROMETRIC PRESSURE: y - 7 

ASSUMED MOISTURE: :~ k~k1 <---.. \ t>l ii, () 1%,0 7 '13, 

k PROBE ID NO/MATERIAL: '2 L I ...L 01 11" 0 7 )0, b "1 SO, b PITOT TUBE COEFF, Cp: ~. i ~ D 

1 

L 

PROBE LENGTH: _ 

NOZZLE ID NOI M:-:A::::TE;:-;R:::- IA:7'L-: --'--'---- --- ') f ""r ~, >'/1, 'i ~1'''i j 

NOZZLE DIAMETER: _ d. ~ d 

FILTER NOITYPE: 5' r - ii7b Ll -C~: "6b'1 ,) 'V$'b,,, 

~~~~i~~i~~~~;i~ :: g~~~ :~ : ~~ : L ~ ~r H~ rJ \ 0 () 

PITOT LEAK CHECK - PRE: POST: 

CHAIN OF CUSTODY: SAMPLE CUSTODIAN ,VI. LSAMPLER 

SAMPLE C:'U"'ScoT""O=CDI

CO' A77N---'/vI-'--'-- C Total: 

t.H Stack Probe Filter Imp: Out Meter Temp, OF 

in: H2O Temp, OF TeI11P, OF Temp, OF Temp, OF In Out 

,'J.,4' '7/",1 )( V <::; 2- 52- c?Z , 

" ..,., 11/ 

~ I Iv' .x---'- u ------- I '\ "- \ ,- ") l - ( ./ '--' 

Vacuum 0, 

in: Hg: % 

P: static 

in, H2O 

Comments: ___________ __________ ________ _____________________________ __ 

Date of last revision 1/25/2013 Page _ _ of __ 05834049 Master Document 5toragelFormslDatasheetslFieid Datasheets 
Oollal1. 

PARTICULATE 

SCAQMD 5.1, WET IMPINGEMENT 

Project # 

ClienVLocation S'M 1. ill .. I 

Sample Location Un,'/::> Water Blank mg/ml 6. OC>2~ 

Sample Date 

Analysis Date 

Analyst Initials 

:z./n/fJ 

Test # :)S'btl(·plt1·/O(>.( MeCl,Blankmg/ml D.W/(, 

Item Number 

1. Glass Fiber Filter Ss-- (Backup Filter) 

11U 

2. Insoluble Solids Filter S5-

pl/ 

3. Impingers and Probe 

Catches 1/37-1 a. Water Fraction 

b. Organic Extraction 1117-0 125 ml MeCI2 

(5 x 25 ml) 

Date of last revision 11/13/08 

Final Tare Gain Aliquot Net Gain Blank based 

Weight Weight Weight Correction (mg/Sample) on Total 

(g) (g) (mg) (ml/ml) Volume (mg) 

O{&2.2- o·(~23 0,0 6,0 ------._-------- -----------------

()./S1'<t 0./:57-'( O·S" ---------------- OS -----------------

~(/~ 

2.2.. 2.3 1.9.0('/1 1.'1.0.515'" ~,z. ~ t '( .r 

2~.~ 2.<I.St;G I 6.~ ~ ,f~.r O.S' 0.2. 

Total Particulate = __ '3=--' L.=-___ ...:m.c:9"-. 

Method of Sample Prep/Notes 

OS834012 

Master Document StoragelFormslOatasheetslLab Forms 
801lal1 

PARTICULATE 

SCAQMD 5.1, WET IMPINGEMENT 

Project # 

ClienULocation Sell 01-. ( 

Sample Location u~ . t. ~ 

Test # .5€ it..... .os·/ 

Item Number 

1. Glass Fiber Filter .s~- (Backup Filter) 

/tl~ 

2. Insoluble Solids Filter SS'-

/ r-76 

3. Impingers and Probe 

Catches mc-" 

a. Water Fraction 

b. Organic Extraction 

125 ml MeCI2 I/~r 

(5 x 25 ml) 

Deltaf1 

.. ""'''' .......... ........ ... 

Date of last revision 11/13/08 

Water Blank mg/ml 

MeCt, Blank mg/ml 

Final Tare 

W~tt W~tt 

D·It:.1.6" O./?2..L. 

6.($2.. 0./55"1 

2.'f.('6~ l."1.'53~{ 

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Sample Date 

0.= 1.~ Analysis Date 

_()>.!.!....oo=:..\'-.:<''----_ Analyst Initials 

)./nil'l 

Gain Aliquot Net Gain Blank based 

Weight Correction (mg/Sample) on Total 

(mQl (ml/ml) Volume (mql 

()'3 ---------------- 0·3 -----------------

0 ·\ ---------------- D.l -----------------

)j30 

~.3 2·3 2.'3 .:---

i'3& 

0.5 

faD 

~ 605 0.2.. i'""36 

Total Particulate = _---')=-._L ____ -'m"'9"--

Method of Sample Prep/Notes 

DS834012 

Master Document StoragelFormslDatasheetslLab Forms 
OollaJ1. 

PARTICULATE 

SCAQMD 5.1, WET IMPINGEMENT 

Project # 

Client/Location 

Sample Location 

Test # 

Item 

1. Glass Fiber Filter 

(Backup Filter) 

2. Insoluble Solids Filter 

3. Impingers and Probe 

Gatches 

a. Water Fraction 

b. Organic Extraction 

125 ml MeGI2 

(5 x 25 ml) 

Oel/a/1 "'-'-'.--

Number 

SS-

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$5-

) 8'(,9 

mC.1 

{{3('~ 

Date of last revision 11/13/08 

Water Blank mg/ml 

MeGl, Blank mg/ml 

Final Tare 

Weight 

(gl 

Weight 

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0'/(.17 () 1(,2 2. 

o.ISS"\ 6.ls~Z 

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Weight 

(mg) 

0·0 

0·0 

j·~1 

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Sample Date 

Analysis Date 

Analyst Initials 

Aliquot Net Gain 

Correction (mg/Sample) 

(mllml) 

6·0 ----------------

0,0 ----------------

Jj9- 3.4 110 

1J!2- 0," 11b 

Blank based 

on Total 

Volume (mg) 

-----------------

------_.----_.---

,.9 

0·2. 

Total Pa rti cu I ate = __ I.f-L.:...:O""---___ --'m.:.:.;;L9 

Method of Sample Prep/Notes 

DS834012 

Master Document StoragelFormslDatasheetslLab Forms 
DClla~ 

PARTICULATE 

SCAQMD 5.1, WET IMPINGEMENT 

Project # 

ClienVLocation 's<!l l.'1-e. , Sample Location Ullie:sTest # !€/st K' PI'I·f.Ij 

Item Number 

1. Glass Fiber Filter $- (Backup Filter) 

11~ 

2. Insoluble Solids Filter !;£-

Jf~f 

3. Impingers and Probe 

Catches (ex,~ 

a. Water Fraction 

b. Organic Extraction 

125 ml MeCI2 If 3(,1.{ (5 x 25 ml) 

IJ 1 {{2-D B( I>f\ '< 1{3P. 

Me. C k 1.3 \ """ I( 1/3(;3 

Date of last revision 11 /13/08 

Water Blank mg/ml D. 6<:> ~ ~ 

MeCl, Blank mg/ml p. """I~ 

Final Tare Gain 

W~tt W~tt Weight 

(m~) 

0 .(r;.(1 o.lr./~ 0 ·0 

O·/5£S O·/!ls'I 6·\ 

1'1.£'101 2Cz.Q; fG. ,.5 

2.,. 'l'f'/5" la,o ~1C."1 0.(, 

~"'.~5S0 li':3S<{3 0·1 

1'1'.14(; ( ). '1. ').(,Sl o·~1 

Sample Date 

Analysis Date 

Analyst Initials 

Aliquot Net Gain 

Correction (mg/Sample) 

(mllm!) 

---------------- 6,0 

---------------- D.( 

S/O 

- 1..5 !lID 

~ 

5::(0 

0.(" SID 

3:32:: 

2. SO 

~ 

Blank based 

on Total 

Volume (mq) 

-----------------

-----------------

/ . 1./ 

C),2..., 

Total Particulate = __ -='Z'-'.--='L=-__ ---'m=-9 

Method of Sample Prep/Notes 

08834012 

Master Document 8toragelFormslDatasheetslLab Forms 
APPENDIX D GENERAL EMISSIONS CALCULATIONS 

R521 0729 D-1 
GENERAL EMISSION CALCULATIONS 

1) Stack Gas Velocity 

A. Stack gas molecular weight, Ib/lb-mole 

MWd", = 0.44 * %CO , + 0.32 * %0 , + 0.28 * %N, 

MWwel = MWdry * (1-Bwo) + 18 * Bwo 

B. Absolute stack pressure, iwg 

Ps = Pbar + Psg 

13.6 

C. Stack gas velocity, ft/sec 

V s = 2.9 * Cp * ..jt,p *.JT. * 

2) Moisture 

A. Sample gas volume, dscf 

V msld = 0.03342 * V m * (Pb", + 

B. Water vapor volume, scf 

v = 0.0472 * V. * Trot 

wsld Ie 528 oR 

29.92 * 28.95 

p. * MWwel 

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 

R5210729 0-2 
QSd 

= Q * (1- B ) * T,ef * Ps 

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 * 106 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- Bwa)O x V, x Ps x Dn' r;,j 

VII. Particulate emissions 

a) Grain loading, gr/dscf 

C = 0.01543 (M.JV m Sid) 

b) Grain loading at 12% CO2, gr/dscf 

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 

[b / l0 Btu = ex 7000gr x F x 20.9 _ %02 

R521 0729 D-3 
Nomenclature: 

As 

Bwo 

C12%C02 

C3%02 

C 

Cp 

On 

F 

H 

HHV 

I 

Mn 

M; 

MW 

Mw; 

o 

P 

Pbar 

Ps 

P sg 

Q 

Qws 

QSd 

SV 

Tm 

T ref 

Ts 

Vs 

V ic 

Vm 

Vmstd 

VWStd 

Yd 

R521 0729 

= 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: 

S02: 64 

NO,: 46 

CO: 28 

HC: 16 

= sample time, min. 

= average velocity head, iwg = (..{i;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, 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 

0-4 
APPENDIX E CHAIN OF CUSTODY 

R5210729 E-1 
CHAJN OF CUSTODY 

CLIENT: Sentinel TEST DATE(S): 2125/2013 212612013 

LOCATION: 5 SAMPLER(S): -"S"S ___________ _ 

SAMPLE LOCATION: Stk PROJECT MANAGER: BF 

TEST METHOD(S): SCAQMD 207.1 DATE DUE: 3/6/2013 

OUTSIDE LAB REQUIRED?: No 

DATE TEST# 

212512013 $5/Stk·NH3- FB Blank 

,)/""''lni':l S5/Stk.NH3-1 

2125/2013 

212512013 

212512013 

212612013 

2126/2013 

SS/Stk-NH3-1 ~'''C'''' . ~'u ... 

2/25/2013 S5/~ ~nk 

Method 

CAQMD 20' 

:AQMD20' 

:AQM[ 

~AOMr. .... . 

CA 

Probe, line , 

be, 

ine . Impingers 

ine ! Impingers 

COMPLIANCE TEST? 

RM 

Yes 

ICOMMENTS 

0.1 N H2S04 

H2SO4 

H2S04 

• I " H2S04 

.1 N H2S04 

,04 

ina, Impingers rvl IU' I I,. n..:;:)v .. 

" ., "2S04 " 

8 

RE~S~:: DAT~~ I ~c~n==t=;-~ATE7TlME- )Jt;.;C(? .112JJn ::qo/tj~2 ,3 &-""2) 

R ,-- -. _ 1- I'L i , / I I . 

Rl'fIIA 

o 
CHAIN OF CUSTODY 

CLIENT: Sentinel TEST DATE(S): 2/25/2013 212612013 

LOCATION: 5 SAMPLER(S): "'R"'M'-__________ _ 

SAMPLELOCATlON: SIl< PROJECT MANAGER: BF 

TEST METHOD(S): SCAQMD 5.1 DATE DUE: 3/6/2013 

OUTSIDE LAB REQUIRED?: No COMPLIANCE TEST? Yes 

DATE TIME TEST# ~---.~-- .. _- -.- -- - --.-

line 1m 1 RM Water 

5.1 Filter 1 RM 55 mm 

Probe, line, 1m 1 RM Water 

5.1 Filter 1 RM 55 mm 

Probe, Line Imp. 1 RM Water 

5.1 Filter 1 RM 55 mm I 

Probe, Line Imp. 1 RM Water I 

!5/20 5.1 Filter 

R~agentJot #'~l 

Water ,.L i 

~y =1--- -F --- --OATElTIME- - r fj,RECE~ I DATEITIME 

7tUO Uz.,,/J:S Ii.: 'f.{) ~ . _ U2Jdli.... ItJl(O 

I ' 

z ----- -T '''' C( 

A 
(;1Z8'> 

re l'1-li ~ 

CA.I -Z-f! 7 

~ lt-l1d 

Q l7-ffM 

A ,"-'10 

/!//c::/l /307/<7 

CHAIN OF CUSTODY 

CUENT: Sentinel TEST OATE(S): 212512013 2/2612013 

LOCATION: 5 SAMPLER(S): ~RM~ ___________ _ 

SAMPLELOCAnON: Stk PROJECT MANAGER: BF 

TEST METHOO{S): SCAQMO 25.3 DATE DUE: 3ISI2013 

OUTSIDE lAB REQUIRED?: Yes COMPLIANCE 

_ .. . .. - TEST? Ves .-

212512013 S5/ -VQC-100-1A QM025.3 CanLSter# ()OD 1 RM 

212512013 S51Stk-VOC-1 (l().1 B SCAQMD25.3 Canister' I[) <0 1 RM 

212512013 S5lStkNOC-75--1A SCAQMD25..3 Canister" Oe>o 0 ~ .; 1 RM 

212512013 SSlStk-VQC..75-1B SCAOMD25.3 Canister' =1 1 RM 

2126J2013 S5/Stk-VOC-5Q..1A SCAQMD25.3 Canister # 2- 1 RM 

2126/2013 S5JStk·VOC-5()..1 B SCAQM025.3 Canister" 1 RM 

()1a es 

t 

01\1 . : 

~ .. - . 

- .... :z. " /"/ 

- - :L 'f':::' ,,,,. , 

' -

.MLl 

-..----- ---- - --------_._-_._--------- _.-
APPENDIX F INSTRUMENT STRIP CHARTS 

R521 0729 F-1 















APPENDIXG FACILITY PERMIT TO OPERATE CONDITION 029.1 

R5210729 G-1 
SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 91765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H Page: 35 

Facility 10: 152707 

R~i5ion#: 0 

Date: April 15.20tI 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

The operator shall comply with the terms and conditions set forth helow: 

The operator shall also install and maintain a device to continuously record the 

parameter being measured 

The measuring device or gauge shall he accurate to within plus or minus 5 

percent. It shall be calibrated once every twelve months 

It shall be calibrated once every twelve months 

The pressure drop across the catalyst shall not exceed 12 inches water column 

[RULE 1303(a)(1)-BACT, 5-10-1996; RULE 1303(aXI)-BACT, 12-6-2002; RULE 

1703(aX2) - PSD-BACT, 10-7-1988; RULE 2005, 5-6-2005] 

[Devices subject to this condition: C4, CIO, C16, C22, C28, C34, C40, C46] 

012.5 The operator shall install and maintain a(n) non-resettable elapsed time meter to 

accurately indicate the elapsed operating time from the engine. 

[RULE I I 10.2, 2-1-2008; RULE 1303(b)(2)-OlTset, 5-10-1996; RULE 1303(bX2) 

-Offset, 12-6-2002; RULE 1470,6-1-2007; RULE 2012, 5-6-2005] 

[Devices subject to this condition: 049] 

029.1 The operator shall conduct source testes) for the pollutant(s) identified below. 

Pollutant(s) to Required Test Methodes) Averaging Time I Test Location 

he tested 

NOX emissions District method 100.1 I hour Outlet of the SCR 

serving this equipment 

CO emissions I District method 100.1 I hour I Outlet of the SCR 

serving this equipment 

SOX emissions I AQMD Laboratory 

Method 307-9\ 

Not Applicable I Fuel sample 

VOC emissions I District Method 25.3 I hour I Outlet of the SCR 

serving this equipment 
SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 91765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H Page: 36 

Facilitv 10: 152707 

Revision #: 0 

Date: April IS, 2011 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

The operator shall comply with the terms and conditions set forth below: 

PMIO 

emissions 

NH3 em issions 

I District Method 5 

I District method 207.1 

and 5.3 or EPA method 

17 

4 hours 

1 hour 

I Outlet of the SCR 

serving this equipment 

1 Outlet of the SCR 

serving this equipment 
SOLITH COAST AIR QUALITY MANAGEMENT DISTRlcr 

21865 Copley Drive, Diamond Bar, CA 91 765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H Page: 37 

Facility 10: 152707 

Revision N: 0 

Date: April IS. 2011 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

The operator shall comply with the terms and conditions set forth below: 

The test shall be conducted after AQMD approval of the source test protocol, but 

no later the later of 180 days after initial start-up or three hundred hours of 

operations after start-up. The AQMD shall be notified of the date and time of the 

test at least 10 days prior to the test 

The test shall be conducted to determine the oxygen levels in the exhaust. In 

addition, the tests shall measure the fuel flow rate (CFH), the flue gas flow rate, 

and the turbine generating output in MW. 

The test shall be conducted in accordance with AQMD approved test protocol. 

The protocol shall be submitted to the AQMD engineer no later than 45 days 

before the proposed test date and shall be approved by the AQMD before the test 

commences. 

The test protocol shall include the proposed operating conditions of the turbine 

during the tests, the identity of the testing lab, a statement from the testing lab 

certifYing that it meets the criteria of Rule 304, and a description of all sampling 

and analytical procedures 

The test shall be conducted when this equipment is operating at maximum, 

average, and minimum loads. 

For natural gas fired turbines only, VOC compliance shall be demonstrated as 

follows: a) Stack gas samples are extracted into 

final canister pressure between 400-500 mm Hg 

canisters are done with zero gas analyzed/certified 

total hydrocarbon as carbon, and c) Analysis of 

TO-12 (with pre concentration) and temperature 

samples for analysis is not below 70 deg F. 

Summa canisters maintaining a 

absolute, b) Pressurization of 

to contain less than 0.05 ppmv 

canisters are per EPA Method 

of canisters when extracting 

The test shall be conducted for compliance verification of the BACT VOC 2.0 

ppmv limit. 

The test results shall be reported with two significant digits. 
SOUlli COAST AIR QUALIlY MANAGEMENT DISTRICT 

21865 Copley DrIve. DIamond Bar. CA 91765 

FACll..ITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

SectionH 

Facility ID: 

Revision Ii; 

Date: 

Page: 38 

152707 

o 

AprillS,201l 

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)(1)-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 subject to this condition: DI, D7, DI3, D19, D25, D31, 037, D43] 

D29.2 The operator shall conduct source testes) for the pollutant(s) identified below. 

Pollutant(s) to 

be tested 

Required Test Method(s) Averaging Time I Test Location 

NH3 emissions District method 207.1 1 hour Outlet of the SCR 

and 5.3 or EPA method serving this equipment 

17 

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 8 60 minute averaging time 

period. 

If the turbine is not in operation during one quarter, then no testing is required 

during that quarter 

The test shall be conducted to demonstrate compliance with the Rule 1303 BACT 

concentration limit 

[RULE 1303(a)(1)-BACT, 5-10-1996; RULE 1303(a)(I)-BACT, 12-6-2002] 

[Devices subject to this condition: DI, D7, Dl3, D19, D25, D31, D37, D43] 
APPENDIX H CORRESPONDENCE AND TEST PLAN 

R521 0729 H-1 
Bob: 

Here is an answer to one of the issues for the CPY 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 YOC is 

acceptable to the SCAQMD. 

Sincerely, 

Carey Wifw'U{3/Wy 

Jtir Quaaty 'Enaineer II 

SCJtQ,:MV 

21865 Coyfey Vrive 

Viamona1Iar, CJt 91765 

'ref: (909) 396-3006 

:J'ax: (909) 396-2099 

cwiffirueIi6y@aqmtf.lJov 

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 YOC 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/ Street 

Sacramento, CA 95811 

(916) 273-5139 (direct/voice) 

(916) 444-8373 (fax) 
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 

8611811 

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 BY SCAQMD METHOD 207.1 ................................. .................. ..... ........... 9 

3.3 SOx BY SCAQMD METHOD 307.91 ................................................ ......... ........ 9 

3.4 ROG BY MODIFIED SCAQMD METHOD 25.3 ............ ...................................... 9 

3.5 PM BY SCAQMD METHOD 5.1 ....................................................................... 13 

4.0 REPORTING .......................................................................................................... 15 

APPENDICES 

A QUALITY ASSURANCE .......................................................... .............................. A-1 

B TEST METHODS ................. ......... ...... ..... ................. ... ... ............. .. ................ .... .. .. B-1 

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

D FORMS ................................................................................................................. D-1 

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

R021 0458-R 1 iii De/fit:.. "'-......... -
1.0 INTRODUCTION 

Delta Air Quality Services, Inc. has been contracted by Gemma Power Systems 

Califomia, Inc. (GEMMA) to perform the initial Permit to Operate Compliance Testing at 

the CPV Sentinel Energy Project Units 1, 2, 3, 4, 5, 6, 7, and 8. Condition D29.1 of the 

Permit to Operate requires source tests within 180 days of initial startup. This document 

will serve as the test plan for the aforementioned tests. 

Tests will be performed at three load conditions to determine oxides of nitrogen 

(NO,J, 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 Delfa/). 

.. _--
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) LMS1 DOPA 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 LMS1 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 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. 

R021 0458-R 1 2 Oellll1 

.. _..-.-
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 

R021045B-R1 //eltab.. 3 .. -.--
FIGURE 2-2 

GENERAL ARRANGEMENT OF MAJOR COMPONENTS 

;.l'.t ... T .... ·.TO· ... · ,. .... .r.""'t>' 

--.. ............... .... -.. -.. .. - ..... --]==I4i==~.- ............ ' ..... .. .... -

,.:_ ..... ........... , : ' 

.. \\, ".i'-, \ ' • \ ' 11''' I I~ \ "Z \ , -+--~ . '-=.:.i- I . " 

C~ ."'t. " ... ~:-. J : , //'~ '1 I 

I~ / , 

v 

J \ IN'/ ' ' 

,:: • ' . : . J,I 

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 111111811 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 

l Sample ports 

T 

323 Distance 8, inches, 2.0 Diameters 

",----,E::;xh;.:;aust Flow 4 

Elevation View 

5 

90 It. 

66 ft. 

o ft. 

0611811 "'---
Sample 

Point 

2 

3 

4 

5 

6 

7 

8 

9 

10 

11 

12 

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 pt. Short Line CEMS 

% of in. %of in. % of in. %01 in. %of 

Diameter from Wall Diameter from Wall Diameter from Wall Diameter from Wall Diameter 

2.1 3.4 3.2 5.2 4.4 7.1 16.7 27.1 N/A 

6.7 10.9 10.5 17.0 14.6 23.7 50 81 .0 N/A 

11 .8 19.1 19.4 31.4 29.6 48.0 

17.7 28.7 32.3 52.3 70.4 114.0 

25 40.5 67.7 109.7 

35.6 57.7 80.6 130.6 

64.4 104.3 

75 121.5 

82.3 133.3 

86.4 140.0 

93.3 151.1 

97. 158.6 

Prior to performing the tests, gaseous stratification will be investigated with a 12 

point traverse as described in 40 CFR 75, and the presence of cyclonic flow will be 

checked using the techniques described in SCAQMD Method 2.1. 

If stratification is less than 10% or less than 1 ppm, all future gaseous 

concentration measurements will be made from a single point. If stratification is greater 

than 10% and greater than 1 ppm, all future concentration measurements will be 

performed using a multi-point traverse (3-point short line, 3-point long line, or 12-points 

(using 40 CFR Part 75 criteria)). 

A 16-point cyclonic flow traverse will be performed with an S-type pitot tube. If 

the average yaw angle is less than 10 degrees, the location will be deemed acceptable 

for Method 2.1 velocity measurements. 

R0210458-R1 6 De/tat:.. ----

in. 

from Wall 

15.7 

47.2 
3.0 TEST DESCRIPTION 

Table 3-1 summarizes the test methods and techniques which will be used as the 

reference methods. The test matrix has been developed to meet the requirements of 

Section 29.1 of the facility Permit (Application Number 472137) dated April 15, 2011 . 

The permitted emission limits are summarized in Table 3-2. The following 

sections describe each method in further detail. Flue gas Oxygen and Carbon Dioxide 

concentration will be measured in conjunction with all tests using SCAQMD Method 

100.1. The flue gas flow rate will be measured in conjunction with each particulate test. 

This measured flue gas flow rate in each duct will be used for all emission rate 

calculations of NOx, CO, NH3, ROG's and SOx' 

TABLE 3-1 

TEST MATRIX 

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

NOx SCAQMD 100.1 1 run 1 run 1 run 60 minutes 

02/C02 SCAQMD 100.1 With each ru n 

CO SCAQMD 100.1 1 run 1 run 1 run 60 minutes 

NH3 SCAQMD 207.1 2 runs 2 runs 2 runs 60 minutes 

S02 SCAQMD 307.91 2 samples N/A 

PM EPA 201NSCAQMD 5.1 1 run 1 run 1 run 240 minutes 

RaG Modified SCAQMD 25.3 3 runs 3 runs 3 runs - 60 minutest') 

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 o458-R 1 7 lie/lab. ....... ~--.. 
TABLE 3-2 

CPV SENTINEL ENERGY PROJECT 

PERMITIED EMISSION LIMITS 

Parameter Units 

ppm@ 15%0, 

ppm @ 15% 0, 

Ibs/MMscf 

co ppm @ 15% 0 , 

NH3 ppm @ 15% 0, 

gr/dscf @ 3% 0, 

Particulate gr/dscf @ 12% CO, 

Ib/hr 

Ibs/MMscf 

(Ib/hr equivalent) PM1O"PM2.5 

Ib/MMBtu 

Ibs/MMscf SOx 

ROG's ppm @ 15% 0, 

(1) The 12.261bs1MMscf is a RECLAIM emission factor, not a limit. 

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

3,1 0,. CO,. NOx AND CO 

Limit 

2.5 

15 

12.26(1) 

4 

5 

0.01 

0.1 

11 

5.71(') 

(5.0) 

0.06 

0.69 

2.0 

Rule 

1703(a)(2) 

40 CFR 60 

2012 

1703(a)(2) 

1303(a)(1 ) 

475 

409 

475 

40 CFR 60 

Rule 2011 

1303(a)(1 ) 

0" CO" 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 perfonmed using a 12-point traverse at each test condition 

(or a single point if previous testing demonstrates the absence of significant stratification 

(less than 10% or less than 1 ppm). At the full load condition, the compliance test may 

be performed concurrently with the Relative Accuracy Test Audit (RATA). In this case, 

data from the RATA may be used to demonstrate compliance with the NOx and CO 

emission limits. NOx concentrations will be measured on a 0-5 ppm range. CO 

concentrations will be measured on a 0-10 ppm range. CO, concentrations will be 

measured on a 0-10% range. 0 , concentrations will be measured on a 0-20% range. 

The measured concentrations are averaged over each sampling period, then corrected 

R0210458-R1 8 lie/tab.. 

.. _--
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. 

R021 0458-R 1 9 
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 SCAQMO 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 ppmcarlxm. 

R021 0458-R 1 10 
Modifications suggested by SCAQMD to the Method 25.3 analytical procedures 

approved for MC under the LAP are: 

• Pressurization of the canisters to 900 mm Hg with Ultra High Purity (UHP) 

helium analyzed/certified to contain less than 0.05 ppmv of total hydrocarbons 

as carbon 

• Analyzing only the Summa canister fraction of the normal 25.3 sample. No 

water vial used in sampling, no water vial analysis. 

• Utilization of a larger (-2 ml) sampling loop 

• Development of a custom low level (0.1 - 5.0 ppmV propane) calibration 

curve 

• Performance of a Minimum Detection Limit (MOL) study 

• Determination of a Practical Quantitation Limit (PQl) from the MOL study 

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

digits, corrected to 15% 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 samples are 

extracted into Swnma 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 Dellal'1 

.. -.--
AQMD Method 25 . 3 without prior approval except for the 

determination of compliance with the VOC BACT level of 2.0 

ppmv calculated as carbon for natural gas fired turbines. 

Mike Garibay from source testing has proposed the following VOC 

testing 

For natural gas fired turbines only, VOC compliance shall be 

demonstrated as follows an alternative to AQMD Method 25.3 for the 

purpose of demonstrating compliance with BACT as determined by 

CARB and AQMD, may be the following: a} Triplicate S stack gas 

samples are extracted directly into Summa canisters, maintaining a 

final canister pressure between 400-500 mm Hg absolute, b} 

Pressurization of the Summa canisters are is done 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 with 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 wi th 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 

21855 Copley Drive 

Diamond Bar, CA 91755 

909-395-2208 

R021 0458-R 1 12 
3.5 PM BY SCAQMD METHOD 5.1 

Particulate matter will be measured using EPA Method 201A in conjunction with 

SCAQMD Method 5.1. SCAQMD Method 5.1 is cited as the Table in Condition D29.1 

lists District Method 5. District Method 5.1 measures total particulate. This total 

particulate measurement could include material >10 microns. Use of the cyclone as in 

201A will prevent overstating of 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 DellaJ1. ... -._--
Temperiture 

Sensor Probe 

~ PHot Tube 

S-Type Pitot Tube 

FIGURE 3-3 

SCAQMD METHOD 5.1 SAMPLE SYSTEM 

Manometer 

Orifice 

Connecting 

Tubing 

Dry Gas 

Meter 

Filter Temperature 

Line 

The sample is recovered in two fractions: 1) nozzle, probe, connecting line and 

impinger rinse (01 water) and 2) backup filter. Filter weight gain and water solution 

weight gain are each determined gravimetrically. 

R021 0458-R 1 14 lIellat3.. "'--"-' 
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, clienUsource 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 

R0210458-R1 15 Oe/1I11 .. ....,--
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 

R021 0458-R 1 16 llella/}. "'-----
APPENDIX A QUALITY ASSURANCE 

R0210458·R1 A·1 1Ie/1a1'1 "'-- -
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 ot 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-ot-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 0458-R 1 A-2 1Ie//l1J. --...-.--
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. 

R021 0458-R 1 A-3 M/le/talJ... _ ........ _ 
TABLE A-1 

EQUIPMENT MAINTENANCE SCHEDULE 

Equipment 

Pumps 

Flow Meters 

Sampling Instruments 

Acceptance Limits 

1. Absence of leaks 

2. Ability to draw 

manufacturers 

required vacuum 

and fiow 

1. Free mechanical 

movement 

1. Absence of 

malfunction 

2. Proper response to 

zero, span gas 

Integrated sampling 1. Absence of leaks 

tanks 

Mobile van sampling 1. Absence of leaks 

system 

Sampling lines 

R021 0458-R 1 

1. Sample 

degradation less 

than 2% 

A-4 

Frequency of Service 

Every 500 hours of 

operation or 6 months, 

whichever is less 

Every 500 hours of 

operation or 6 months, 

whichever is less 

As recommended by 

manufacturer 

Methods of Service 

1. Visual inspection 

2. Clean 

3. Replace parts 

4. Leak check 

1. Visual inspection 

2. Clean 

3. Calibrate 

As recommended by 

manufacturer 

Depends on nature of 1. Steam clean 

use 2. Leak check 

Depends on nature of 1. Change filters 

use 2. Change gas dryer 

3. Leak check 

4. Check for system 

contamination 

After each test series 1. Blow dry, inert gas 

through line until 

dry. 

lie/tal!!. 

... -.. ---
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 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 

llH@ 

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

NIST traceable standard 

R021 0458-R 1 A-5 

1le11al3. 

... -._-
APPENDIXB TEST METHODS 

R0210458-R1 8-1 llella/). 

.. -.-
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 NOx 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. 

8-2 llelfa/). 

.. _--
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 Calibratiori 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. 001 

10 10 

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 

R0210458-R1 8-3 Ileltal1 

.,.- --
where: 

Response to Analyzer Cal = The analyzer response to the last time the same 

calibration gas was introduced directly to the analyzer (this may be the pre-test 

calibration error value or a more recent analyzer calibration adjustment) 

Zero and Calibration Drift are calculated for each test run based on the analyzer 

response during the pre- and post-test sample system bias test. Zero and upscale drift 

must not exceed ±3% of the analyzer range. 

I D ·f Post- Test System Bias Resonse - Pre - Test System Bias Response Ana yzer n t = • 100% 

Analyzer Range 

The pre- and post-test analyzer response during the sample system bias test are 

used to correct the raw test average for any sample system bias and analyzer drift. The 

drifUbias corrected data are the actual reported concentrations and are used for 

subsequent calculations (mass emission rates, Ib/MMBtu, corrections to 3% or 15% Oz, 

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

c-c c = o. C c C _ C ma m 0 

where: 

Cc = Drift/bias corrected concentration 

C = Raw Test Average 

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, C02, 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 NOz to 

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

efficiency must be 90% or greater. 

R0210458-R1 8-4 Oe/1I11 

.... _--
Analyzer 

Cal 

Cal No 

Error < 2% 

No 

Yes IYes 

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 

I 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 

1 Bias < 5% t--

FIGURE 1: SCAQMD METHOD 100.1 CALIBRATION AND TEST SEQUENCE 

R021 0458-R 1 8-5 De/lat::,. 

---
Temperature 

~-Pti:olTube 

Nozzle 

S-Type Pitot Tube 

R0210458-R1 

Manometer 

Orifice 

Connecting 

Tubing 

Dry Gas 

Meter 

SCAQMD METHOD 5.1 SAMPLING TRAIN 

8-6 

Temperature 

Sensor 

Gel 

Vacuum 

Gauge 

Line 
Filter Probe 

Flow Controller 

MODIFIED SCAQMD METHOD 25.3 SAMPLING APPARATUS 

R0210458-R1 B-7 /Jella/). 

. ...,.--
APPENDIXC CALCULATIONS 

R0210458-R1 C-1 1l6//811 

... .....,.--
GENERAL EMISSION CALCULATIONS 

1) Stack Gas Velocity 

A. Stack gas molecular weight, Ibllb-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 

v, = 2.9 • Cp • .J AP • F. . 

2) Moisture 

A. Sample gas volume, dscf 

Vmstd = 0.03342 • Vm * (Pbar + 

B. Water vapor volume, scf 

v = 0.0472 • v.' Tref 

w,td Ie 528 oR 

29.92 • 28.95 

P, • MWwet 

c. Moisture content, dimensionless 

Bwo = 

3) Stack gas volumetric flow rate 

A. Actual stack gas volumetric flow rate, wacfm 

Q = V • A • 60 , , 

B. Standard stack gas flow rate, dscfm 

R021 0458-R 1 C-2 Ilellal1 

........ _-
Q = Q * (1- B ) * Tref * P, 

,d wo T, 29.92 

4) Gaseous Mass Emission Rates. Ib/hr 

M = ppm * MW; * Q Sd * 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 

1 = 17.32 x T, (Vm std) x 5280 R 

(1- Bwo)O x V, x Ps x Dn 2 T"i 

VII. Particulate emissions 

a) Grain loading, gr/dscf 

C = 0.01543 (MrlVm std) 

b) Grain loading at 12% CO2, gr/dscf 

Cm'. 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 = ex Qsd x (60 min/hr)/(7000 gr/lb) 

e) Particulate emission factor 

6 lIb 20 .. 9 

lb 110 Btu = ex 7000gr x F x 20.9 _ %02 

R021 0458-R 1 C-3 .. Della/).. _ .. _-
Nomenclature: 

As 

Bwo 

C' 2%C02 

C 3%02 

C 

Cp 

On 

F 

H 

HHV 

I 

Mn 

M 

MW 

MwJ 

o 

P 

Pbar 

Ps 

Psg 

a 

a ws 

aSd 

SV 

Tm 

Tref 

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, Ib/lb-mole 

= molecular weight of specie i: 

S02: 64 

NO. : 46 

CO: 28 

HC: 16 

= sample time, min. 

= average velocity head, iwg = (.J t,.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~ecif c 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 1Je/1811 

.. _--
APPENDIX D FORMS 

R0210458-R1 D-1 
South Coast 

Air Quality Management District 

21865 Copley Drtve. DIamond Bar. CA 91765-4178 

(909) 396-2000 • www.aqmd.gov 

Mr. Robert A. Finken 

Delta Air Quality Services, Inc. 

1845 N. Case Street 

Orange, CA 92865 

Subject: LAP Approval Notice 

Reference # 96LA 1220 

Dear Mr. Finken: 

January 11,2012 

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

Air Quality Management District's Laboratory Approval Program (AQMD LAP). We are pleased to 

inform you that your firm is approved for the period beginning January 31, 2012, and ending January 3 I, 

2013 for the following methods: 

SCAQMD Methods 1-4 

SCAQMD Method 100.1 

SCAQMD Methods 25.1 and 25.3 (Sampling) 

SCAQMD Methods 5.1, 5.2, 5.3, and 6.1 

SCAQMD Rule 1420 - (Lead) Ambient Sampling 

USEPA CTM-030 and ASTM D6522-00 

Thank you for participating in the SCAQMD LAP. Your cooperation helps us to achieve the goal of the 

LAP: to maintain high standards of quality in the sampling and anaJysis of source emissions. You may 

direct any questions or infonnation to LAP Coordinator. Glenn KasaL He may be reached by telephone 

at (909) 396-2271, by facsimilie at (909) 396-2099, or via e-mail at gkasai@aqmd.gov. 

RE:GK/gk 

cc: Mike Garibay 

Glenn Kasal 

120111 LapRenewaLdoc 

S:~& 

;/ ~n, Senior Manager 

Laboratory Services & 

Source Test Engineering 

Dellafl R021 0458-R 1 D-2 .....,--
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State of California 

Air Resources Board 

Approved Independent Contractor 

Delta Air Quality Servic.es, Incorporated 

This is to certifytl;i<!tthe company listeej above h~sbeen approved 

by the Air ResolircElS' Boaro ti:l'c(it:Kluct t:oinp~ance testing . . ".... . r ..... , .• ... 

pursuant to titie'-t7;,Califomia Code of Regulatlbns, section 91207 

until Ju~36;·. 2013, for those testmetliods:fisted below: .- -r 

ARB S.,...."" Test M.etli;,a,; F I, 2,.3,.4, ", 8, 17, 20,.501 

109 {CO; co;. NO" 0" SO,) 

Alberto Ayai!l, Ph.D., M.S.E. 

Chief, Monitoring and Laboratory Division 
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en 

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State of California 

Air Resources Board 

Approved Independent Contractor 

Delta Aii, Quality Se~iees>dncorporated 

This is to certifytl1at the coT)1pany liste<!:'above' has been approved 

by the Air Rfisoui:~S' Board to'con,ctilptcomll!iance testing 

pursuant to titIEi'11;:Cal[fonila Code'cpf RegUlations; section 91207 

until June 30; i013;:for thos&~~t.meihcidii listed below: 

" ,. ' .. ~ . . 

" visibIe·&nissioils Evaluanon 

U.S. EPA Test Methods)OIA:(19n nni.\~), 202 .(1991 •• "lion) 

p 

Alberto Ayala.Pfl.D .• M.S.E. 

Chief. Monitoring 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: 146536 Oate(s)Tes7te-d~:---------=Te~s~t~P~la-n------------------------------------

Facility Name: .,-____ ~C.!:P~V~S~e<!.n!ltl!!:·n~e:!,I.!::E~n~e!lrg:llyt....P!:.r!lo!1ie2!c!:.!t'--__________ _ 

Equipment Address: __ ---:9:;1-:'1 ... B<-:i;":xb:'-vl..;"0:!.ri;"v."e'"-=:-:-::;---:-===-_________ _ 

City of Industry, California 91748 

Equipment Tested: _____ ~U~nl!.!its~1..." 2~,,.,3!.L,-=4:a.,' 5~,....!6"".f:7~, &~8~:--=--:":,--______________ _ 

Device 10, AlN, PIN : _____ -=0"'1 .... , 0",7""...,0<...1",3,,-, -=0",1,,-9 ,,,,0~2,,,5<L' -=3 .... 1,...,3",7 ... , .,,&:.,:4"'2'__ ______________ _ 

I 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, I state that any contracts or agreements entered into by my source testing firm and 

the faciiity 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: (~ Ll {.,i J l,>. Bob Finken 

(Name) 

President 

<-

(Title) 

FORM ST -110 :stevforl.doc (Revised 11/18/98) 

R021 0458-R 1 0-5 

Date: ______ ~12~17!..!/,!:;20!!..1!..!!2'__ ______ _ 

714-279-6777 121712012 

(Phone) (Date) 

.. 

/Je/Ia~ _--
APPENDIX E FACILITY PERMIT TO OPERATE CONDITION 029.1 

R038842-R1 E-1 
SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT 

Z 1865 Copley Drive, DJamond Bar, CA 91 765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H 

FaciJitv 10: 

R~isionll : 

Date: 

Page: 35 

152701 

o 

April 15,2011 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

The operator shall comply with the terms and conditions set Corth 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 2005, 5-6-2005] 

[Devices subject to this condition: C4, CIO, C16, C22, C28, C34, C40, C46] 

D 12.5 The operator shall install and maintain a(n) non-resettable elapsed time meter to 

accurately indicate the elapsed operating time from the engine. 

[RULE 1110.2,2-1-2008; RULE 1303(b)(2)-OtTset, 5-10-1996; RULE I303(bX2) 

-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 I Required Test Methodes) I 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 I I hour I Outlet of the SCR 

serving this equipment 

SOX emissions I AQMD Laboratory 

Method 307-91 

I Not Applicable I Fuel sample 

VOC emissions I District Method 25.3 I 1 hour I Outlet of the SCR 

serving this equipment 
SOlIDi COAST AIR QUALITY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 9 J 765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H Page: 36 

FacilitY 10: 152707 

Revision I : 0 

Dele: 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: 

PM 1 0 I District Method 5 

emissions 

NH3 emissions I District method 207.1 

and 5.3 or EPA method 

17 

I 4 hours 

11 hour 

I Outlet of the SCR 

serving this equipment I Outlet of the SCR 

serving this equipment 
Im.i,< ".-. . _ -

SOUTH COAST AIR QUAUlY MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond Bar, CA 91 765 

FACILITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Seaion H 

Facility 10: 

Rcvisionll: 

Dale, 

Page: 37 

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: 

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 (CHI), 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 Jab, a statement from the testing Jab 

certifying that it meets the criteria of Rule 304, and a description of all sampling 

and analytical procedures 

The test shall be conducted when this equipment is operating at maximum, 

average, and minimum loads. 

For natural gas fired turbines only, VOC compliance shall be demonstrated as 

follows: a) Stack gas samples are extracted into Summa canisters maintaining a 

final canister pressure between 400-500 mm Hg absolute, b) Pressurization of 

canisters are done with zero gas analyzed/certified to contain less than 0.05 ppmv 

total hydrocarbon as carbon, and c) Analysis of canisters are per EPA Method 

TO-12 (with pre concentration) and temperature of canisters- when extracting 

samples for analysis is not below 70 deg F. 

The test shall be conducted for compliance verification of the BACT VOC 2.0 

ppmv limit. 

The test results shall be reported with two significant dip;its. 
SOtIll-f COAST AIR QUALI1Y MANAGEMENT DISTRICT 

21865 Copley Drive, Diamond 8ar, CA 91 765 

FACll..ITY PERMIT TO OPERATE 

CPV SENTINEL LLC 

Section H 

Facility ID; 

Revision II: 

Otle: 

Page: 31 

152701 

o 

AprillS,2011 

SECTION H: PERMIT TO CONSTRUCT AND TEMPORARY PERMIT TO OPERATE 

The operator shaD comply with the terms and conditions let forth below: 

[RULE 1303(a)(I)-BACT, 5-1(1..1996; RULE 1303(aXI)-BACT, 12-6-2002; RULE 

1303(b)(l)-Offset, 5-10-19%; RULE 1303(b)(2}-Offset, 12-6-2002; RULE 1703(8)(2) -

PSO-BACT, 10-7-1988; RULE 1005, 5-6-2005) 

[Devices subject to this condition: DI, D7, D13, Dl9, D25, 031, D37, D43] 

D29.2 The operator shall conduct source test(s) for the pollutant( s) identified below. 

Pollutant(s) to 

be tested 

NH3 em issions 

I Required Test Method(s) 

I District method 207.1 

and 5.3 or EPA method 

17 

I A vcraging Time 

II 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 shaH 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 ftrst twelve months of 

operation and at least annually thereafter. The NOx concentration, as determined 

by the CEMS, shall be simultaneously recorded during the ammonia slip test. If 

the CEMS is inoperable, a test shall be conducted to determine the NOx 

emissions using District Method 100.1 measured over a 60 minute averaging time 

period. 

If the turbine is not in operation during one quarter, then no testing is required 

during that quarter 

The test shall be conducted to demonstrate compliance with the Rule 1303 BACT 

concentration limit 

[RULE 1303(a)(1}-BACT, 5-10-1996; RULE 1303(aXI}-BACT, 12-6-2002] 

[Devices subject to this condition: DI, D7, 013, D19, D25, 031, D37, D43] 
END OF DOCUMENT