Name: John M. McManus

Title: Vice President- Environmental Service

Company: American Electric Power

Sign Date: 8/27/2010

Name: Scott W. Banach

Title: Director, Project Engineering

Company: Platt Environmental

Sign Date: 8/26/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Conesville Unit 3

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.

Tuesday, January 18, 2011 Page 1 of 18
Conesville Unit 3

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Facility Information:

Conesville Plant

47201 CR 273

Conesville OH 43811

Contact: Paul Jackson

Phone: 614-716-3278

Fax: 614-716-1252

Email: pmjackson@aep.com

Testing Company:

Platt Environmental Services, Inc.

1520 Kensington Road

Suite 204

Oak Brook IL 60523

Contact: Scott Banach

Phone: 630-521-9400

Fax: 630-521-9494

Email: sbanach@plattenv.com

Air Permit Number:

06-16-00-0000

Permitted Source ID/Name:

Unit 3 Unit 3

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:

Electric generating dry bottom wall fired boiler utilizing bituminous coal as the primary fuel.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (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 228 0 556 1824 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Carbon Monoxide Method 10 3 0

Total organic compounds 

(TOC)

Stack Method 25A 3 0

Stack Hydrogen Fluoride Method 26A 3 0

Stack Hydrogen Chloride Method 26A 3 0

Stack Total PM2.5 OTM - 27/28 3 0

Stack Filterable PM2.5 OTM - 27/28 3 0

Stack Filterable Particulate OTM - 27/28 3 0

Tuesday, January 18, 2011 Page 2 of 18
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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.

Stack Total Particulate OTM - 27/28 3 0

Stack Selenium Method 29 3 0

Stack Antimony Method 29 3 0

Stack Arsenic Method 29 3 0

Stack Beryllium Method 29 3 0

Stack Cadmium Method 29 3 0

Stack Chromium Method 29 3 0

Stack Cobalt Method 29 3 0

Stack Lead Method 29 3 0

Stack Nickel Method 29 3 0

Stack Filterable Particulate Method 29 3 0

Stack Manganese Method 29 3 0

Stack Co2 Method 3A CO2 3 0

Stack O2 Method 3A O2 3 0

Tuesday, January 18, 2011 Page 3 of 18
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Sampling / Stack Data Results Summary

Location Stack - Method 10

Average

Run Number 1 2 3

Test Date 7/1/2010 7/1/2010 7/1/2010

Run Start Time 10:45:00 AM 1:10:00 PM 3:35:00 PM

Run Finish Time 12:44:00 PM 3:09:00 PM 5:34:00 PM

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 9 9 9 9.000

Dry Volumetric Flow Rate, dry scfm 388875 384853 384723 386,150.333

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

Moisture, % 7.5 6.7 6.5 6.900

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - Method 25A

Average

Run Number 1 2 3

Test Date 7/1/2010 7/1/2010 7/1/2010

Run Start Time 10:45:00 AM 1:10:00 PM 3:30:00 PM

Run Finish Time 12:44:00 PM 3:09:00 PM 5:29:00 PM

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 9 9 9 9.000

Dry Volumetric Flow Rate, dry scfm 388875 384853 384723 386,150.333

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

Moisture, % 7.5 6.7 6.5 6.900

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, January 18, 2011 Page 4 of 18
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Location Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 6/28/2010 6/28/2010 6/28/2010

Run Start Time 2:40:00 PM 2:45:00 PM 2:15:00 PM

Run Finish Time 5:55:00 PM 6:00:00 PM 5:30:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 123.643 107.793 104.714 112.050

Moisture Content of Stack Gas, % 6.71 7.13 6.25 6.697

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 10.7 10.4 10.3 10.467

Oxygen, % 8.9 9.1 9.2 9.067

Average Stack Gas Temperature, °F 286.21 279.50 279.92 281.877

Dry Volumetric Flow Rate, dry scfm 466,410.4 406,500.9 397,739.1 423,550.133

Actual Wet Volumetric Flue Gas Flow Rate, acfm 735,077.3 635,558.6 612,762.9 661,132.933

Percent Isokinetic of Sampling Rate, % 100.5 100.5 99.8 100.267

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 6/28/2010 6/29/2010 6/30/2010

Run Start Time 9:45:00 AM 10:00:00 

AM

9:50:00 AM

Run Finish Time 2:00:00 PM 2:15:00 PM 2:05:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 168.574 140.620 139.895 149.696

Moisture Content of Stack Gas, % 6.57 6.86 6.11 6.513

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 10.7 10.3 10.4 10.467

Oxygen, % 9 9.1 9.1 9.067

Average Stack Gas Temperature, °F 285.10 278.79 277.23 280.373

Dry Volumetric Flow Rate, dry scfm 474,085.5 391,581.2 398,659.1 421,441.933

Actual Wet Volumetric Flue Gas Flow Rate, acfm 744,944.1 609,870.9 614,634.2 656,483.067

Percent Isokinetic of Sampling Rate, % 101.1 102.1 99.8 101.000

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, January 18, 2011 Page 5 of 18
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Location Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 7/1/2010 7/1/2010 7/1/2010

Run Start Time 10:45:00 AM 1:10:00 PM 3:35:00 PM

Run Finish Time 12:44:00 PM 3:09:00 PM 5:34:00 PM

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 9 9 9 9.000

Dry Volumetric Flow Rate, dry scfm 388875 384853 384723 386,150.333

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

Moisture, % 7.5 6.7 6.5 6.900

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 7/1/2010 7/1/2010 7/1/2010

Run Start Time 10:45:00 AM 1:10:00 PM 3:35:00 PM

Run Finish Time 12:44:00 PM 3:09:00 PM 5:34:00 PM

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 9 9 9 9.000

Dry Volumetric Flow Rate, dry scfm 388875 384853 384723 386,150.333

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

Moisture, % 7.5 6.7 6.5 6.900

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, January 18, 2011 Page 6 of 18
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Location Stack - OTM - 27/28

Average

Run Number MOTM27/O

TM28-1

MOTM27/

OTM28-2

MOTM27/O

TM28-3

Test Date 6/28/2010 6/29/2010 6/30/2010

Run Start Time 9:45:00 AM 10:00:00 

AM

9:50:00 AM

Run Finish Time 3:31:15 PM 3:29:00 PM 3:24:30 PM

Net Run Time, minutes 330 330 330

Dry Gas Meter Volume Sampled, dscf 127.354 125.100 125.471 125.975

Moisture Content of Stack Gas, % 5.67 6.84 5.88 6.130

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 10.7 10.3 10.3 10.433

Oxygen, % 8.9 9.1 9.1 9.033

Average Stack Gas Temperature, °F 286.92 286.08 283.75 285.583

Dry Volumetric Flow Rate, dry scfm 499,948.2 437,819.1 421,184.8 452,984.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 779,988.3 688,465.1 649,678.4 706,043.933

Percent Isokinetic of Sampling Rate, % 100.3 102.1 106.4 102.933

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, January 18, 2011 Page 7 of 18
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Emissions Summary

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.69E-02 1.55E-02 1.44E-02 0.016

ppm 1.35E+01 1.24E+01 1.15E+01 12.467

ppm@7%O2 1.58E+01 1.45E+01 1.34E+01 14.567

Location: Stack - Method 25A

Compound: Total organic compounds (TOC)

Average

Run 1 2 3

lb/mmBtuO2 7.66E-04 4.70E-04 4.03E-04 0.001

ppm 1.43E+00 8.78E-01 7.53E-01 1.020

ppm@7%O2 1.67E+00 1.03E+00 8.80E-01 1.193

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 110 110 95 105.000

lb/mmBtuO2 3.34E-02 3.90E-02 3.49E-02 0.036

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 17 17 17 17.000

lb/mmBtuO2 5.16E-03 6.02E-03 6.25E-03 0.006

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0141 0.012 0.112 0.046

lb/mmBtuO2 3.17E-06 3.26E-06 3.06E-05 0.000

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0806 0.0468 0.0458 0.058

lb/mmBtuO2 1.81E-05 1.27E-05 1.25E-05 0.000

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.01155 0.0064 0.00603 0.008

lb/mmBtuO2 2.59E-06 1.74E-06 1.65E-06 0.000

Tuesday, January 18, 2011 Page 8 of 18
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Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00334 0.003 0.003 0.003

lb/mmBtuO2 7.50E-07 8.15E-07 8.19E-07 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 2.22232 4.50072 3.22872 3.317

lb/mmBtuO2 4.99E-04 1.22E-03 8.81E-04 0.001

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.041 0.04132 0.0257 0.036

lb/mmBtuO2 9.21E-06 1.12E-05 7.02E-06 0.000

Compound: Filterable Particulate

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 394.7 147.3 158.6 233.533

lb/mmBtuO2 8.87E-02 4.00E-02 4.33E-02 0.057

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.05158 0.0305 0.02528 0.036

lb/mmBtuO2 1.16E-05 8.28E-06 6.90E-06 0.000

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.25722 0.35642 0.21642 0.277

lb/mmBtuO2 5.78E-05 9.68E-05 5.91E-05 0.000

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 2.43427 2.24027 1.89427 2.190

lb/mmBtuO2 5.47E-04 6.08E-04 5.17E-04 0.001

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.603 0.3697 0.4184 0.464

lb/mmBtuO2 1.35E-04 1.00E-04 1.14E-04 0.000

Location: Stack - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 217.1 83.8 108 136.300

Tuesday, January 18, 2011 Page 9 of 18
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Process Run Data

Compound: Filterable PM2.5

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 40.4 20.8 20 27.067

Compound: Total Particulate

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 514.6 385.012 430.16 443.257

Compound: Total PM2.5

Average

RunNumber MOTM27/OTM28-1 MOTM27/OTM28-2 MOTM27/OTM28-3

Mass_mg 337.9 322 342.2 334.033

Tuesday, January 18, 2011 Page 10 of 18
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Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 43.9 Tons/hr 40

2 Bituminous Coal Burned 37.2 Tons/hr 40

3 Bituminous Coal Burned 38.3 Tons/hr 40

1 Steam Temperature 949 F 950

2 Steam Temperature 930.5 F 950

3 Steam Temperature 937 F 950

1 Steam Pressure 1491 psig 1500

2 Steam Pressure 1507.4 psig 1500

3 Steam Pressure 1516.5 psig 1500

1 Gross Load 101.2 MW 100

2 Gross Load 87 MW 100

3 Gross Load 88.1 MW 100

1 Opacity 9.9 % 20

2 Opacity 6.5 % 20

3 Opacity 6.6 % 20

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

9.9 % 20

2 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

6.5 % 20

3 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

6.6 % 20

Tuesday, January 18, 2011 Page 11 of 18
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Sampling / Stack Data Results Detail

Location Stack - Method 10

Average

Run Number 1 2 3

Test Date 7/1/2010 7/1/2010 7/1/2010

Run Start Time 10:45:00 AM 1:10:00 PM 3:35:00 PM

Run Finish Time 12:44:00 PM 3:09:00 PM 5:34:00 PM

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 9 9 9 9.000

Fuel Factor 1.14 1.14 1.14

Dry Volumetric Flow Rate, dry scfm 388875 384853 384723 386,150.333

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

Moisture, % 7.5 6.7 6.5 6.900

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 888.1 888.1 888.1 888.100

Operating Units ppm ppm ppm

No. Readings/Avg. 120 120 120 120.000

Calibration Set 0 0 0 0.000

Calibration Pre Zero Cylinder ID CC97654-CO CC97654-

CO

CC97654-CO

Calibration Pre Zero Cylinder Instrument Response 0 0.9 0.5 0.467

Calibration Pre Zero Cylinder Bias -0.03 0.07 0.02 0.020

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID SG9176680B

AL-CO

SG9176680B

AL-CO

SG9176680B

AL-CO

Calibration Pre High Cylinder Instrument Response 469.1 466 467 467.367

Calibration Pre High Cylinder Bias -0.34 -0.69 -0.57 -0.533

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC97654-CO CC97654-

CO

CC97654-CO

Calibration Post Zero Cylinder Instrument Response 0.9 0.5 0 0.467

Calibration Post Zero Cylinder Bias 0.07 0.02 -0.03 0.020

Calibration Post Zero Cylinder Drift 0.1 0.05 0.05 0.067

Calibration Post High Cylinder ID SG9176680B

AL-CO

SG9176680B

AL-CO

SG9176680B

AL-CO

Calibration Post High Cylinder Instrument Response 466 467 467.6 466.867

Calibration Post High Cylinder Bias -0.69 -0.57 -0.51 -0.590

Calibration Post High Cylinder Drift 0.35 0.12 5.999999999

99999E-02

0.177

Cavg 14 13.1 11.8 12.967

Cavg Units ppmvd ppmvd ppmvd

Cgas 13.5442 12.4293 11.5463 12.507

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

Tuesday, January 18, 2011 Page 12 of 18
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Location Stack - Method 25A

Average

Run Number 1 2 3

Test Date 7/1/2010 7/1/2010 7/1/2010

Run Start Time 10:45:00 AM 1:10:00 PM 3:30:00 PM

Run Finish Time 12:44:00 PM 3:09:00 PM 5:29:00 PM

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 9 9 9 9.000

Fuel Factor 1.14 1.14 1.14

Dry Volumetric Flow Rate, dry scfm 388875 384853 384723 386,150.333

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

Moisture, % 7.5 6.7 6.5 6.900

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 9.014 9.014 9.014 9.014

Operating Units ppm ppm ppm

No. Readings/Avg. 120 120 120 120.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID CC0000000-

THC

CC0000000-

THC

CC0000000-

THC

Calibration Pre Zero Cylinder Instrument Response 0.02 0 0.02 0.013

Calibration Pre Zero Cylinder Bias 0 -0.22 0 -0.073

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC183615-

THC

CC183615-

THC

CC183615-

THC

Calibration Pre High Cylinder Instrument Response 3.02 3.11 3.13 3.087

Calibration Pre High Cylinder Bias -32.62 1 1.22 -10.133

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC0000000-

THC

CC0000000-

THC

CC0000000-

THC

Calibration Post Zero Cylinder Instrument Response 0 0.02 0.01 0.010

Calibration Post Zero Cylinder Bias -0.22 0 -0.11 -0.110

Calibration Post Zero Cylinder Drift 0.22 0.22 0.11 0.183

Calibration Post High Cylinder ID CC183615-

THC

CC183615-

THC

CC183615-

THC

Calibration Post High Cylinder Instrument Response 3.11 3.13 3.15 3.130

Calibration Post High Cylinder Bias -31.62 1.22 1.44 -9.653

Calibration Post High Cylinder Drift 0.9999999999

99996

0.22 0.22 0.480

Cavg 1.45 0.91 0.79 1.050

Cavg Units ppmvd ppmvd ppmvd

Cgas 1.4306 0.8783 0.7527 1.021

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

Tuesday, January 18, 2011 Page 13 of 18
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Location Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 6/28/2010 6/28/2010 6/28/2010

Run Start Time 2:40:00 PM 2:45:00 PM 2:15:00 PM

Run Finish Time 5:55:00 PM 6:00:00 PM 5:30:00 PM

Net Traversing Points 28 28 28

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.276 0.276 0.276 0.276

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.01 1.01 1.01 1.010

Barometric Pressure, inches of Mercury 28.8 28.9 29.07 28.923

Average Orifice Meter Differential, inches H2O 1.34 1.02 0.96 1.107

Dry Gas Meter Volume Sampled, cubic feet 130.491 113.033 109.587 117.704

Average Dry Gas Meter Temperature, °F 83.60 81.54 83.56 82.900

Dry Gas Meter Volume Sampled, dscf 123.643 107.793 104.714 112.050

Total Moisture Liquid collected, g 189 175.8 148.2 171.000

Volume of Water Vapor, standard cubic feet 8.90 8.27 6.98 8.050

Moisture Content of Stack Gas, % 6.71 7.13 6.25 6.697

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9329 0.9287 0.9375 0.933

Carbon Dioxide, % 10.7 10.4 10.3 10.467

Oxygen, % 8.9 9.1 9.2 9.067

Carbon Monoxide & Nitrogen, % 80.4 80.5 80.5 80.467

Fuel Factor 1.12 1.13 1.14

Dry Molecular Weight, lb/lb-Mole 30.07 30.03 30.02 30.040

Wet Molecular weight, lb/lb-Mole 29.26 29.17 29.27 29.233

Flue Gas Static Pressure, inches of H2O -0.5 -0.5 -0.5 -0.500

Absolute Flue Gas Pressure, inches of Mercury 28.76 28.86 29.03 28.883

Average Stack Gas Temperature, °F 286.21 279.50 279.92 281.877

Average Velocity Head, inches of H2O 0.4082123869

01435

0.308056562

571094

0.288947777

833013

0.335

Average Stack Gas Velocity, feet/second 43.21 37.36 36.02 38.863

Stack Cross-Sectional Area, square feet 283.529 283.529 283.529 283.529

Dry Volumetric Flow Rate, dry scfm 466,410.4 406,500.9 397,739.1 423,550.133

Actual Wet Volumetric Flue Gas Flow Rate, acfm 735,077.3 635,558.6 612,762.9 661,132.933

Percent Isokinetic of Sampling Rate, % 100.5 100.5 99.8 100.267

Percent Excess Air, % 72.2 74.9 76.3 74.467

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

Round Duct Diameter, inches 228 228 228

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, January 18, 2011 Page 14 of 18
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Location Stack - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 6/28/2010 6/29/2010 6/30/2010

Run Start Time 9:45:00 AM 10:00:00 AM 9:50:00 AM

Run Finish Time 2:00:00 PM 2:15:00 PM 2:05:00 PM

Net Traversing Points 52 52 52

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.276 0.276 0.276 0.276

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.01 1.01 1.01 1.010

Barometric Pressure, inches of Mercury 28.8 28.9 28.9 28.867

Average Orifice Meter Differential, inches H2O 1.38 0.94 0.97 1.097

Dry Gas Meter Volume Sampled, cubic feet 176.393 144.857 146.294 155.848

Average Dry Gas Meter Temperature, °F 79.02 71.89 79.99 76.967

Dry Gas Meter Volume Sampled, dscf 168.574 140.620 139.895 149.696

Total Moisture Liquid collected, g 251.7 220 193.6 221.767

Volume of Water Vapor, standard cubic feet 11.85 10.36 9.11 10.440

Moisture Content of Stack Gas, % 6.57 6.86 6.11 6.513

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9343 0.9314 0.9389 0.935

Carbon Dioxide, % 10.7 10.3 10.4 10.467

Oxygen, % 9 9.1 9.1 9.067

Carbon Monoxide & Nitrogen, % 80.3 80.6 80.5 80.467

Fuel Factor 1.11 1.15 1.13

Dry Molecular Weight, lb/lb-Mole 30.07 30.01 30.03 30.037

Wet Molecular weight, lb/lb-Mole 29.28 29.19 29.29 29.253

Flue Gas Static Pressure, inches of H2O -0.5 -0.5 -0.5 -0.500

Absolute Flue Gas Pressure, inches of Mercury 28.76 28.86 28.86 28.827

Average Stack Gas Temperature, °F 285.10 278.79 277.23 280.373

Average Velocity Head, inches of H2O 0.4201611160

47249

0.284191720

012896

0.290253622

73016

0.332

Average Stack Gas Velocity, feet/second 43.79 35.85 36.13 38.590

Stack Cross-Sectional Area, square feet 283.529 283.529 283.529 283.529

Dry Volumetric Flow Rate, dry scfm 474,085.5 391,581.2 398,659.1 421,441.933

Actual Wet Volumetric Flue Gas Flow Rate, acfm 744,944.1 609,870.9 614,634.2 656,483.067

Percent Isokinetic of Sampling Rate, % 101.1 102.1 99.8 101.000

Percent Excess Air, % 73.8 74.7 74.9 74.467

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

Round Duct Diameter, inches 228 228 228

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, January 18, 2011 Page 15 of 18
Conesville Unit 3

8/27/2010

Location Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 7/1/2010 7/1/2010 7/1/2010

Run Start Time 10:45:00 AM 1:10:00 PM 3:35:00 PM

Run Finish Time 12:44:00 PM 3:09:00 PM 5:34:00 PM

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 9 9 9 9.000

Fuel Factor 1.14 1.14 1.14

Dry Volumetric Flow Rate, dry scfm 388875 384853 384723 386,150.333

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

Moisture, % 7.5 6.7 6.5 6.900

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 20 20 20 20.000

Operating Units % % %

No. Readings/Avg. 120 120 120 120.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID CC127111-

CO2

CC127111-

CO2

CC127111-

CO2

Calibration Pre Zero Cylinder Instrument Response 0.08 0.1 0.1 0.093

Calibration Pre Zero Cylinder Bias 0.15 0.25 0.25 0.217

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC89345-CO2 CC89345-

CO2

CC89345-

CO2

Calibration Pre High Cylinder Instrument Response 9.98 10 9.99 9.990

Calibration Pre High Cylinder Bias 0.1 0.2 0.15 0.150

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC127111-

CO2

CC127111-

CO2

CC127111-

CO2

Calibration Post Zero Cylinder Instrument Response 0.1 0.1 0.09 0.097

Calibration Post Zero Cylinder Bias 0.25 0.25 0.2 0.233

Calibration Post Zero Cylinder Drift 0.1 0 0.05 0.050

Calibration Post High Cylinder ID CC89345-CO2 CC89345-

CO2

CC89345-

CO2

Calibration Post High Cylinder Instrument Response 10 9.99 10.01 10.000

Calibration Post High Cylinder Bias 0.2 0.15 0.25 0.200

Calibration Post High Cylinder Drift 0.1 0.05 0.1 0.083

Cavg 10.4 10.4 10.4 10.400

Cavg Units %vd %vd %vd

Cgas 10.3725 10.3677 10.3622 10.367

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

Tuesday, January 18, 2011 Page 16 of 18
Conesville Unit 3

8/27/2010

Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 7/1/2010 7/1/2010 7/1/2010

Run Start Time 10:45:00 AM 1:10:00 PM 3:35:00 PM

Run Finish Time 12:44:00 PM 3:09:00 PM 5:34:00 PM

Carbon Dioxide, % 10.4 10.4 10.4 10.400

Oxygen, % 9 9 9 9.000

Fuel Factor 1.14 1.14 1.14

Dry Volumetric Flow Rate, dry scfm 388875 384853 384723 386,150.333

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

Moisture, % 7.5 6.7 6.5 6.900

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 120 120 120 120.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID CC127111-O2 CC127111-

O2

CC127111-

O2

Calibration Pre Zero Cylinder Instrument Response 0.05 0.04 0.04 0.043

Calibration Pre Zero Cylinder Bias 0 -0.04 -0.04 -0.027

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC89345-O2 CC89345-O2 CC89345-O2

Calibration Pre High Cylinder Instrument Response 11.97 11.95 11.93 11.950

Calibration Pre High Cylinder Bias 0.08 0 -0.08 0.000

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC127111-O2 CC127111-

O2

CC127111-

O2

Calibration Post Zero Cylinder Instrument Response 0.04 0.04 0.04 0.040

Calibration Post Zero Cylinder Bias -0.04 -0.04 -0.04 -0.040

Calibration Post Zero Cylinder Drift 0.04 0 0 0.013

Calibration Post High Cylinder ID CC89345-O2 CC89345-O2 CC89345-O2

Calibration Post High Cylinder Instrument Response 11.95 11.93 11.92 11.933

Calibration Post High Cylinder Bias 0 -0.08 -0.12 -0.067

Calibration Post High Cylinder Drift 0.08 0.08 0.04 0.067

Cavg 9 9 9 9.000

Cavg Units %vd %vd %vd

Cgas 9.0114 9.0278 9.0392 9.026

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

Tuesday, January 18, 2011 Page 17 of 18
Conesville Unit 3

8/27/2010

Location Stack - OTM - 27/28

Average

Run Number MOTM27/OT

M28-1

MOTM27/O

TM28-2

MOTM27/OT

M28-3

Test Date 6/28/2010 6/29/2010 6/30/2010

Run Start Time 9:45:00 AM 10:00:00 AM 9:50:00 AM

Run Finish Time 3:31:15 PM 3:29:00 PM 3:24:30 PM

Net Traversing Points 16 16 16

Net Run Time, minutes 330 330 330

Nozzle Diameter, inches 0.2 0.21 0.21 0.207

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.01 1.01 1.01 1.010

Barometric Pressure, inches of Mercury 28.8 28.9 29.07 28.923

Average Orifice Meter Differential, inches H2O 0.39 0.39 0.39 0.390

Dry Gas Meter Volume Sampled, cubic feet 132.467 129.229 129.158 130.285

Average Dry Gas Meter Temperature, °F 74.46 72.63 73.88 73.657

Dry Gas Meter Volume Sampled, dscf 127.354 125.100 125.471 125.975

Total Moisture Liquid collected, g 162.7 195.2 166.6 174.833

Volume of Water Vapor, standard cubic feet 7.66 9.19 7.84 8.230

Moisture Content of Stack Gas, % 5.67 6.84 5.88 6.130

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9433 0.9316 0.9412 0.939

Carbon Dioxide, % 10.7 10.3 10.3 10.433

Oxygen, % 8.9 9.1 9.1 9.033

Carbon Monoxide & Nitrogen, % 80.4 80.6 80.6 80.533

Fuel Factor 1.12 1.15 1.15

Dry Molecular Weight, lb/lb-Mole 30.07 30.01 30.01 30.030

Wet Molecular weight, lb/lb-Mole 29.39 29.19 29.30 29.293

Flue Gas Static Pressure, inches of H2O -0.5 -0.5 -0.5 -0.500

Absolute Flue Gas Pressure, inches of Mercury 28.76 28.86 29.03 28.883

Average Stack Gas Temperature, °F 286.92 286.08 283.75 285.583

Average Velocity Head, inches of H2O 0.4613311221

49786

0.358596216

816353

0.323513181

811478

0.381

Average Stack Gas Velocity, feet/second 45.85 40.47 38.19 41.503

Stack Cross-Sectional Area, square feet 283.529 283.529 283.529 283.529

Dry Volumetric Flow Rate, dry scfm 499,948.2 437,819.1 421,184.8 452,984.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 779,988.3 688,465.1 649,678.4 706,043.933

Percent Isokinetic of Sampling Rate, % 100.3 102.1 106.4 102.933

Percent Excess Air, % 72.2 74.7 74.7 73.867

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

Round Duct Diameter, inches 228 228 228

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, January 18, 2011 Page 18 of 18