Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Wednesday, February 16, 2011 Page 1 of 14
Facility Information:

AES Petersburg

6925 N. State Road 57

Petersburg IN 47567

Contact: Angelique Oliger

Phone: (317) 261-5852 ext ____

Fax:

Email: angelique.oliger@aes.com

Testing Company:

URS Corporation

1600 Perimeter Park Dr.

Morrisville NC 27560

Contact:Brad Justus

Phone: 919-461-1100

Fax: 919-461-1415

Email: Brad_Justus@URScorp.com

Air Permit Number:

994

Permitted Source ID/Name:

4 4

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

530 MW, Low NOx Burner, Overfire Air, ESP, FGD

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 1812500002 FRS #: 330015653241

SCC / Description 10100211 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Wet Bottom (Tangential) (Bituminous Coal) 

The following state and federal regulations that apply to the proposed testing:

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Stack Exit 354 0 0 0 708 2832 4 3

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 180 0

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit Formaldehyde Method 0011 3 120 0

Stack Exit 2,3,7,8-TCDD Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDD Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0

Wednesday, February 16, 2011 Page 2 of 14
Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Stack Exit OCDD Method 23 3 480 0

Stack Exit 2,3,7,8-TCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDF Method 23 3 480 0

Stack Exit 2,3,4,7,8-PeCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8,9-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

Stack Exit OCDF Method 23 3 480 0

Stack Exit Other TCDD Method 23 0

Stack Exit Other PeCDD Method 23 0

Stack Exit Other HxCDD Method 23 0

Stack Exit Other HpCDD Method 23 0

Stack Exit Other TCDF Method 23 0

Stack Exit Other PeCDF Method 23 0

Stack Exit Other HxCDF Method 23 0

Stack Exit Other HpCDF Method 23 0

Stack Exit Total Dioxins Method 23 3 480 0

Stack Exit Total Furans Method 23 3 480 0

Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0

Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Stack Exit Method 23 3 480 0

Stack Exit 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Stack Exit Method 23 3 480 0

Stack Exit Total PCBs Method 23 3 480 0

Stack Exit Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Wednesday, February 16, 2011 Page 3 of 14
The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

Organic Condensible 

Particulate

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Magnesium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Mercury Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit O2 Method 3A O2 3 480 0

Stack Exit O2 Method 3A O2 3 240 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit Co2 Method 3A CO2 3 480 0

Total Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Organic Condensible 

Particulate

Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Filterable Particulate Method 5 3 240 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0

Wednesday, February 16, 2011 Page 4 of 14
Sampling / Stack Data Results Summary

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 4/1/2010 4/1/2010 4/1/2010

Run Start Time 11:23:00 AM 12:50:00 

PM

3:55:00 PM

Run Finish Time 12:22:00 PM 3:22:00 PM 6:23:00 PM

Carbon Dioxide, % 13.27 12.7 12.75 12.907

Oxygen, % 5.91 6.13 6.37 6.137

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 4/1/2010 4/1/2010 4/1/2010

Run Start Time 11:23:00 AM 12:50:00 

PM

3:55:00 PM

Run Finish Time 12:22:00 PM 3:22:00 PM 6:23:00 PM

Carbon Dioxide, % 13.27 12.7 12.75 12.907

Oxygen, % 5.91 6.13 6.37 6.137

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 32.3 35.6 32.7 33.533

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, February 16, 2011 Page 5 of 14
Location Stack Exit - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/1/2010 4/1/2010 4/1/2010

Run Start Time 11:23:00 AM 12:50:00 

PM

3:55:00 PM

Run Finish Time 12:22:00 PM 3:22:00 PM 6:23:00 PM

Carbon Dioxide, % 13.27 12.7 12.75 12.907

Oxygen, % 5.91 6.13 6.37 6.137

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/1/2010 4/1/2010 4/1/2010

Run Start Time 11:23:00 AM 12:50:00 

PM

3:55:00 PM

Run Finish Time 12:22:00 PM 3:22:00 PM 6:23:00 PM

Carbon Dioxide, % 13.27 12.7 12.75 12.907

Oxygen, % 5.91 6.13 6.37 6.137

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, February 16, 2011 Page 6 of 14
Emissions Summary

Process Run Data

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.33E-01 4.57E-02 4.66E-02 0.075

ppm 1.34E+02 4.54E+01 4.56E+01 75.000

ppm@7%O2 1.24E+02 4.27E+01 4.36E+01 70.100

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ppm 0.00E+00 0.00E+00 0.00E+00 0.000

ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Wednesday, February 16, 2011 Page 7 of 14
Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 221 Tons/hr 0

2 Bituminous Coal Burned 229 Tons/hr 0

3 Bituminous Coal Burned 230 Tons/hr 0

1 Average Heat Input 4980 MMBtu/hr 0

2 Average Heat Input 5142 MMBtu/hr 0

3 Average Heat Input 5163 MMBtu/hr 0

1 Steam Output 3588 1000 lb steam/hr 0

2 Steam Output 3974 1000 lb steam/hr 0

3 Steam Output 3897 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

1 Fuel Oil Firing Rate 0 0

2 Fuel Oil Firing Rate 0 0

3 Fuel Oil Firing Rate 0 0

1 Flue Gas Flow Rate 0 dscfm 0

1 Pressure Drop Across FGD (if applicable) 0 in H20 0

1 FGD Scrubber Liquor pH 0 pH 0

1 FGD Scrubber Liquor Flow Rate 0 gal/min 0

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0

1 Flue Gas Carbon Dioxide Content 0 % 0

1 Flue Gas Moisture Content 0 % 0

1 Flue Gas Sampling Point Temperature 0 Deg F 0

1 Flue Gas Pressure 0 atm 0

1 Standard Pressure 0 atm 0

1 Standard Temperature 0 Deg F 0

Wednesday, February 16, 2011 Page 8 of 14
APCD Run Data

Process Lab Run Data

1 Unit Gross Electrical Output 549.4 MW 0

1 Unit Net Electric Generation 516.8 MWh 0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 OVERFIRE AIR 0 0

1 ELECTROSTATIC PRECIPITATOR 0 kvolts 0

1 CAUSTIC SCRUBBER 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 12859 Btu/lb

1 Fuel Moisture 14 %

1 Fuel Mercury Content 0 ppm

1 Fuel Cadmium Content 0 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 0 ppm

1 Fuel Arsenic Content 0 ppm

1 Fuel Chromium Content 0 ppm

1 Fuel Beryllium Content 0 ppm

1 Fuel Lead Content 0 ppm

1 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 0 ppm

2 Fuel Higher Heating Value 12780 Btu/lb

2 Fuel Moisture 14 %

2 Fuel Mercury Content 0 ppm

2 Fuel Cadmium Content 0 ppm

2 Ultimate/Proximate Analysis 0

2 Fuel Nickel Content 0 ppm

2 Fuel Arsenic Content 0 ppm

2 Fuel Chromium Content 0 ppm

2 Fuel Beryllium Content 0 ppm

2 Fuel Lead Content 0 ppm

2 Fuel Manganese Content 0 ppm

2 Fuel Chlorine Content 0 ppm

2 Fuel Fluorine Content 0 ppm

3 Fuel Higher Heating Value 12952 Btu/lb

3 Fuel Moisture 14 %

Wednesday, February 16, 2011 Page 9 of 14
3 Fuel Mercury Content 0 ppm

3 Fuel Cadmium Content 0 ppm

3 Ultimate/Proximate Analysis 0

3 Fuel Nickel Content 0 ppm

3 Fuel Arsenic Content 0 ppm

3 Fuel Chromium Content 0 ppm

3 Fuel Beryllium Content 0 ppm

3 Fuel Lead Content 0 ppm

3 Fuel Manganese Content 0 ppm

3 Fuel Chlorine Content 0 ppm

3 Fuel Fluorine Content 0 ppm

Wednesday, February 16, 2011 Page 10 of 14
Sampling / Stack Data Results Detail

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 4/1/2010 4/1/2010 4/1/2010

Run Start Time 11:23:00 AM 12:50:00 PM 3:55:00 PM

Run Finish Time 12:22:00 PM 3:22:00 PM 6:23:00 PM

Carbon Dioxide, % 13.27 12.7 12.75 12.907

Oxygen, % 5.91 6.13 6.37 6.137

Fuel Factor 1.13 1.16 1.14

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 0 0 0 0.000

Analyzer Make CAI CAI CAI

Analyzer Model 602P 602P 602P

Analyzer Serial Number V12029-M V12029-M V12029-M

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 31 31 31 31.000

Calibration Pre Zero Cylinder ID MG08030973-

Zero

MG0803097

3-Zero

MG08030973

-Zero

Calibration Pre Zero Cylinder Instrument Response 0.1 -0.4 0.4 0.033

Calibration Pre Zero Cylinder Bias -0.04 -0.14 0.02 -0.053

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID COPlaceHolde

r

COPlaceHol

der

COPlaceHold

er

Calibration Pre High Cylinder Instrument Response 269.7 267.1 266.3 267.700

Calibration Pre High Cylinder Bias 0.31 -0.19 -0.35 -0.077

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID MG08030973-

Zero

MG0803097

3-Zero

MG08030973

-Zero

Calibration Post Zero Cylinder Instrument Response -0.4 0.4 0.4 0.133

Calibration Post Zero Cylinder Bias -0.14 0.02 0.02 -0.033

Calibration Post Zero Cylinder Drift 0.1 0.16 0 0.087

Calibration Post High Cylinder ID COPlaceHolde

r

COPlaceHol

der

COPlaceHold

er

Calibration Post High Cylinder Instrument Response 267.1 266.3 266.8 266.733

Calibration Post High Cylinder Bias -0.19 -0.35 -0.25 -0.263

Calibration Post High Cylinder Drift 0.5 0.16 0.1 0.253

Cavg 137.2 46.1 46.6 76.633

Cavg Units ppmvd ppmvd ppmvd

Cgas 134.3069 45.3913 45.5838 75.094

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 16, 2011 Page 11 of 14
Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 4/1/2010 4/1/2010 4/1/2010

Run Start Time 11:23:00 AM 12:50:00 PM 3:55:00 PM

Run Finish Time 12:22:00 PM 3:22:00 PM 6:23:00 PM

Carbon Dioxide, % 13.27 12.7 12.75 12.907

Oxygen, % 5.91 6.13 6.37 6.137

Fuel Factor 1.13 1.16 1.14

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 32.3 35.6 32.7 33.533

Analyzer Make CAI CAI CAI

Analyzer Model 300-HFID 300-HFID 300-HFID

Analyzer Serial Number 27JO2004 27JO2004 27JO2004

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 41 41 41 41.000

Calibration Pre Zero Cylinder ID MG08030973-

Zero

MG0803097

3-Zero

MG08030973

-Zero

Calibration Pre Zero Cylinder Instrument Response 0.1 0.09 0.1 0.097

Calibration Pre Zero Cylinder Bias 0 -0.01 0 -0.003

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID THCPlaceHol

der

THCPlaceHo

lder

THCPlaceHol

der

Calibration Pre High Cylinder Instrument Response 20.6 20.14 20.65 20.463

Calibration Pre High Cylinder Bias 0 -0.38 0.04 -0.113

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID MG08030973-

Zero

MG0803097

3-Zero

MG08030973

-Zero

Calibration Post Zero Cylinder Instrument Response 0.1 0.1 -0.2 0.000

Calibration Post Zero Cylinder Bias 0 0 -0.25 -0.083

Calibration Post Zero Cylinder Drift 0 0.01 0.25 0.087

Calibration Post High Cylinder ID THCPlaceHol

der

THCPlaceHo

lder

THCPlaceHol

der

Calibration Post High Cylinder Instrument Response 20.1 20.65 20.2 20.317

Calibration Post High Cylinder Bias -0.41 0.04 -0.33 -0.233

Calibration Post High Cylinder Drift 0.41 0.42 0.37 0.400

Cavg -0.2 -0.72 -0.4 -0.440

Cavg Units ppmvw ppmvw ppmvw

Cgas 0 0 0 0.000

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units ppmvw ppmvw ppmvw

Wednesday, February 16, 2011 Page 12 of 14
Location Stack Exit - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/1/2010 4/1/2010 4/1/2010

Run Start Time 11:23:00 AM 12:50:00 PM 3:55:00 PM

Run Finish Time 12:22:00 PM 3:22:00 PM 6:23:00 PM

Carbon Dioxide, % 13.27 12.7 12.75 12.907

Oxygen, % 5.91 6.13 6.37 6.137

Fuel Factor 1.13 1.16 1.14

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 0 0 0 0.000

Analyzer Make CAI CAI CAI

Analyzer Model 602P 602P 602P

Analyzer Serial Number V12029-M V12029-M V12029-M

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID MG08030973-

Zero

MG0803097

3-Zero

MG08030973

-Zero

Calibration Pre Zero Cylinder Instrument Response 0.03 0.09 0.38 0.167

Calibration Pre Zero Cylinder Bias 0.2 0.49 1.93 0.873

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC308547-

CO2

CC308547-

CO2

CC308547-

CO2

Calibration Pre High Cylinder Instrument Response 9.93 10.29 10.03 10.083

Calibration Pre High Cylinder Bias -0.99 0.79 -0.49 -0.230

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID MG08030973-

Zero

MG0803097

3-Zero

MG08030973

-Zero

Calibration Post Zero Cylinder Instrument Response 0.09 0.38 0.35 0.273

Calibration Post Zero Cylinder Bias 0.49 1.93 1.78 1.400

Calibration Post Zero Cylinder Drift 0.29 1.44 0.15 0.627

Calibration Post High Cylinder ID CC308547-

CO2

CC308547-

CO2

CC308547-

CO2

Calibration Post High Cylinder Instrument Response 10.29 10.03 10.23 10.183

Calibration Post High Cylinder Bias 0.79 -0.49 0.49 0.263

Calibration Post High Cylinder Drift 1.78 1.28 0.98 1.347

Cavg 13.27 12.7 12.75 12.907

Cavg Units %vd %vd %vd

Cgas 13.5649 12.9611 13.0889 13.205

Cgas Units %vd %vd %vd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 16, 2011 Page 13 of 14
Location Stack Exit - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/1/2010 4/1/2010 4/1/2010

Run Start Time 11:23:00 AM 12:50:00 PM 3:55:00 PM

Run Finish Time 12:22:00 PM 3:22:00 PM 6:23:00 PM

Carbon Dioxide, % 13.27 12.7 12.75 12.907

Oxygen, % 5.91 6.13 6.37 6.137

Fuel Factor 1.13 1.16 1.14

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 0 0 0 0.000

Analyzer Make CAI CAI CAI

Analyzer Model 602P 602P 602P

Analyzer Serial Number V12029-M V12029-M V12029-M

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 21 21 21 21.000

Calibration Pre Zero Cylinder ID MG08030973-

Zero

MG0803097

3-Zero

MG08030973

-Zero

Calibration Pre Zero Cylinder Instrument Response 0.13 0.14 0.38 0.217

Calibration Pre Zero Cylinder Bias 0.72 0.77 2.01 1.167

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC308547-O2 CC308547-

O2

CC308547-

O2

Calibration Pre High Cylinder Instrument Response 10.15 10.1 10.03 10.093

Calibration Pre High Cylinder Bias 0.77 0.52 0.15 0.480

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID MG08030973-

Zero

MG0803097

3-Zero

MG08030973

-Zero

Calibration Post Zero Cylinder Instrument Response 0.14 0.38 0.35 0.290

Calibration Post Zero Cylinder Bias 0.77 2.01 1.85 1.543

Calibration Post Zero Cylinder Drift 0.05 1.24 0.16 0.483

Calibration Post High Cylinder ID CC308547-O2 CC308547-

O2

CC308547-

O2

Calibration Post High Cylinder Instrument Response 10.1 10.03 10.23 10.120

Calibration Post High Cylinder Bias 0.52 0.15 1.18 0.617

Calibration Post High Cylinder Drift 0.25 0.37 1.03 0.550

Cavg 5.91 6.13 6.37 6.137

Cavg Units %vd %vd %vd

Cgas 5.8039 6.0107 6.1741 5.996

Cgas Units %vd %vd %vd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, February 16, 2011 Page 14 of 14