Name: John M. McManus

Title: Vice-President, Environmental Service

Company: American Electric Power

Sign Date: 7/29/2010

Name: Scott W. Banach

Title: Director, Project Engineering

Company: Platt Environmental Services, Inc.

Sign Date: 7/28/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Clinch River Unit 1

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
Clinch River Unit 1

7/29/2010

Facility Information:

Clinch River Unit 1

3464 Power Plant Road

Cleveland VA 24225

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:

SWRO10236

Permitted Source ID/Name:

Unit 1 Unit 1

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 0 456 1824 4 6

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
Clinch River Unit 1

7/29/2010

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 60 0

Stack O2 Method 3A O2 3 60 0

Tuesday, January 18, 2011 Page 3 of 18
Clinch River Unit 1

7/29/2010

Sampling / Stack Data Results Summary

Location Stack - Method 10

Average

Run Number 1 2 3

Test Date 5/14/2010 5/14/2010 5/14/2010

Run Start Time 8:25:00 AM 11:07:00 

AM

1:40:00 PM

Run Finish Time 10:24:00 AM 1:06:00 PM 3:39:00 PM

Carbon Dioxide, % 14.2 14.4 14.5 14.367

Oxygen, % 4.3 4.4 4.3 4.333

Dry Volumetric Flow Rate, dry scfm 492006 492065 492681 492,250.667

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

Moisture, % 9.7 8.8 8.7 9.067

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 5/14/2010 5/14/2010 5/14/2010

Run Start Time 8:25:00 AM 11:07:00 

AM

1:40:00 PM

Run Finish Time 10:24:00 AM 1:06:00 PM 3:39:00 PM

Carbon Dioxide, % 14.2 14.4 14.5 14.367

Oxygen, % 4.3 4.4 4.3 4.333

Dry Volumetric Flow Rate, dry scfm 492006 492065 492681 492,250.667

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

Moisture, % 9.7 8.8 8.7 9.067

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
Clinch River Unit 1

7/29/2010

Location Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 5/11/2010 5/12/2010 5/13/2010

Run Start Time 3:40:00 PM 11:45:00 

AM

11:50:00 AM

Run Finish Time 6:52:00 PM 3:00:00 PM 3:05:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 103.815 105.885 88.567 99.422

Moisture Content of Stack Gas, % 4.53 5.05 7.93 5.837

Moisture Saturation at Stack Gas Temperature, % 76.93 82.54 100.00 86.490

Carbon Dioxide, % 6.6 6.5 13.8 8.967

Oxygen, % 13.4 13.4 4.9 10.567

Average Stack Gas Temperature, °F 196.75 199.96 314.58 237.097

Dry Volumetric Flow Rate, dry scfm 1,038,174.5 1,026,831.9 477,055.9 847,354.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,420,990.6 1,425,073.5 803,634.6 1,216,566.23

3

Percent Isokinetic of Sampling Rate, % 99.9 103.0 97.1 100.000

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
Clinch River Unit 1

7/29/2010

Location Stack - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 5/11/2010 5/12/2010 5/13/2010

Run Start Time 10:00:00 AM 7:05:00 

AM

7:15:00 AM

Run Finish Time 3:05:00 PM 11:25:00 

AM

11:30:00 AM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 125.457 138.295 122.797 128.850

Moisture Content of Stack Gas, % 4.76 4.63 8.43 5.940

Moisture Saturation at Stack Gas Temperature, % 77.54 74.25 100.00 83.930

Carbon Dioxide, % 6.6 6.6 13.9 9.033

Oxygen, % 13.4 13.4 4.7 10.500

Average Stack Gas Temperature, °F 197.13 194.90 305.69 232.573

Dry Volumetric Flow Rate, dry scfm 1,025,409.1 1,037,605.7 493,252.3 852,089.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,407,721.5 1,422,691.8 797,680.5 1,209,364.60

0

Percent Isokinetic of Sampling Rate, % 91.7 99.9 97.6 96.400

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 3A CO2

Average

Run Number 1 2 3

Test Date 5/14/2010 5/14/2010 5/14/2010

Run Start Time 8:25:00 AM 11:07:00 

AM

1:40:00 PM

Run Finish Time 10:24:00 AM 1:06:00 PM 3:39:00 PM

Carbon Dioxide, % 14.2 14.4 14.5 14.367

Oxygen, % 4.3 4.4 4.3 4.333

Dry Volumetric Flow Rate, dry scfm 492006 492065 492681 492,250.667

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

Moisture, % 9.7 8.8 8.7 9.067

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
Clinch River Unit 1

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Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 5/14/2010 5/14/2010 5/14/2010

Run Start Time 1:40:00 PM 11:07:00 

AM

1:40:00 PM

Run Finish Time 3:39:00 PM 1:06:00 PM 3:39:00 PM

Carbon Dioxide, % 14.5 14.4 14.5 14.467

Oxygen, % 4.3 4.4 4.3 4.333

Dry Volumetric Flow Rate, dry scfm 492681 492065 492681 492,475.667

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

Moisture, % 8.7 8.8 8.7 8.733

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack - OTM - 27/28

Average

Run Number MOTM27/O

TM28-1

MOTM27/

OTM28-2

MOTM27/O

TM28-3

Test Date 5/11/2010 5/12/2010 5/13/2010

Run Start Time 9:40:00 AM 7:05:00 

AM

7:15:00 AM

Run Finish Time 4:53:00 PM 1:30:00 PM 1:33:00 PM

Net Run Time, minutes 360 360 360

Dry Gas Meter Volume Sampled, dscf 124.120 122.706 122.515 123.114

Moisture Content of Stack Gas, % 4.14 6.56 7.83 6.177

Moisture Saturation at Stack Gas Temperature, % 72.26 76.63 100.00 82.963

Carbon Dioxide, % 6.6 6.6 13.9 9.033

Oxygen, % 13.4 13.4 4.7 10.500

Average Stack Gas Temperature, °F 193.78 196.40 304.89 231.690

Dry Volumetric Flow Rate, dry scfm 1,071,095.2 1,033,932.3 504,072.7 869,700.067

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,453,483.1 1,450,250.8 837,317.8 1,247,017.23

3

Percent Isokinetic of Sampling Rate, % 91.8 94.0 101.4 95.733

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
Clinch River Unit 1

7/29/2010

Emissions Summary

Location: Stack - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.30E+00 1.07E+00 1.20E+00 1.190

ppm 1.45E+03 1.19E+03 1.34E+03 1,326.667

ppm@7%O2 1.21E+03 1.00E+03 1.12E+03 1,110.000

Location: Stack - Method 25A

Compound: Total organic compounds (TOC)

Average

Run 1 2 3

lb/mmBtuO2 2.06E-04 3.79E-04 2.63E-04 0.000

ppm 5.36E-01 9.82E-01 6.85E-01 0.734

ppm@7%O2 4.49E-01 8.27E-01 5.74E-01 0.617

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 48.0556 46.69329 103.67102 66.140

lb/mmBtuO2 2.78E-02 2.65E-02 3.30E-02 0.029

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 3.77582 3.33524 7.97469 5.029

lb/mmBtuO2 2.19E-03 1.89E-03 2.54E-03 0.002

Location: Stack - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.000793 0.000732 0.00159 0.001

lb/mmBtuO2 3.80E-07 3.18E-07 3.60E-07 0.000

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00173 0.001177 0.007075 0.003

lb/mmBtuO2 8.29E-07 5.11E-07 1.60E-06 0.000

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.000343 0.00022 0.001329 0.001

lb/mmBtuO2 1.64E-07 9.56E-08 3.01E-07 0.000

Tuesday, January 18, 2011 Page 8 of 18
Clinch River Unit 1

7/29/2010

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.000198 0.000179 0.000244 0.000

lb/mmBtuO2 9.48E-08 7.78E-08 5.53E-08 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.005184 0.004712 0.018639 0.010

lb/mmBtuO2 2.48E-06 2.05E-06 4.22E-06 0.000

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.000994 0.000553 0.004889 0.002

lb/mmBtuO2 4.76E-07 2.40E-07 1.11E-06 0.000

Compound: Filterable Particulate

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 51.3 25.2 273.2 116.567

lb/mmBtuO2 2.46E-02 1.09E-02 6.19E-02 0.032

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.002423 0.00139 0.010756 0.005

lb/mmBtuO2 1.16E-06 6.04E-07 2.44E-06 0.000

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.006993 0.004837 0.034654 0.015

lb/mmBtuO2 3.35E-06 2.10E-06 7.85E-06 0.000

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.006885 0.006352 0.013896 0.009

lb/mmBtuO2 3.30E-06 2.76E-06 3.15E-06 0.000

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.014892 0.008139 0.017399 0.013

lb/mmBtuO2 7.13E-06 3.54E-06 3.94E-06 0.000

Location: Stack - OTM - 27/28

Compound: Filterable Particulate

Average

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

Mass_mg 182.6 124.8 316.3 207.900

Tuesday, January 18, 2011 Page 9 of 18
Clinch River Unit 1

7/29/2010

Process Run Data

Compound: Filterable PM2.5

Average

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

Mass_mg 25.9 26.9 203.2 85.333

Compound: Total Particulate

Average

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

Mass_mg 213.3 158.2 366.7 246.067

Compound: Total PM2.5

Average

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

Mass_mg 56.6 60.3 253.6 123.500

Tuesday, January 18, 2011 Page 10 of 18
Clinch River Unit 1

7/29/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 2082 Million Btus/hr 2100.9

1 Steam Temperature 1008 F 1000

1 Steam Pressure 1987 psig 2000

1 Gross Load 181.1 MW 235

1 Opacity 4.8 % 20

2 Heat Input 2082 Million Btus/hr 2100.9

2 Steam Temperature 1016 F 1000

2 Steam Pressure 1854 psig 2000

2 Gross Load 181.3 MW 235

2 Opacity 5 % 20

3 Heat Input 2082 Million Btus/hr 2100.9

3 Steam Temperature 996 F 1000

3 Steam Pressure 1989.5 psig 2000

3 Gross Load 178.4 MW 235

3 Opacity 8.6 % 20

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

4.8 opacity 20

2 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

5 opacity 20

3 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

8.6 opacity 20

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0.24 lb/mmBTU 1

2 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0.26 lb/mmBTU 1

3 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0.28 lb/mmBTU 1

Tuesday, January 18, 2011 Page 11 of 18
Clinch River Unit 1

7/29/2010

Sampling / Stack Data Results Detail

Location Stack - Method 10

Average

Run Number 1 2 3

Test Date 5/14/2010 5/14/2010 5/14/2010

Run Start Time 8:25:00 AM 11:07:00 AM 1:40:00 PM

Run Finish Time 10:24:00 AM 1:06:00 PM 3:39:00 PM

Carbon Dioxide, % 14.2 14.4 14.5 14.367

Oxygen, % 4.3 4.4 4.3 4.333

Fuel Factor 1.17 1.15 1.14

Dry Volumetric Flow Rate, dry scfm 492006 492065 492681 492,250.667

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

Moisture, % 9.7 8.8 8.7 9.067

Analyzer Make

Analyzer Model

Analyzer Serial Number 0618817339 0618817339 0618817339 618,817,339

.000

Operating Range 5000 5000 5000 5,000.000

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 CC114878-CO CC114878-

CO

CC114878-

CO

Calibration Pre Zero Cylinder Instrument Response 0 2.3 2 1.433

Calibration Pre Zero Cylinder Bias 0 0.05 0.04 0.030

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC552665-CO CC552665-

CO

CC552665-

CO

Calibration Pre High Cylinder Instrument Response 2548 2549.4 2549.6 2,549.000

Calibration Pre High Cylinder Bias 0.02 0.05 0.06 0.043

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC114878-CO CC114878-

CO

CC114878-

CO

Calibration Post Zero Cylinder Instrument Response 2.3 2 2.8 2.367

Calibration Post Zero Cylinder Bias 0.05 0.04 0.06 0.050

Calibration Post Zero Cylinder Drift 0.05 0.01 0.02 0.027

Calibration Post High Cylinder ID CC552665-CO CC552665-

CO

CC552665-

CO

Calibration Post High Cylinder Instrument Response 2549.4 2549.6 2549 2,549.333

Calibration Post High Cylinder Bias 0.05 0.06 0.04 0.050

Calibration Post High Cylinder Drift 0.03 0.01 0.02 0.020

Cavg 1447.5 1187.2 1340.7 1,325.133

Cavg Units ppmvd ppmvd ppmvd

Cgas 1447.1732 1185.8176 1339.4035 1,324.131

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 12 of 18
Clinch River Unit 1

7/29/2010

Location Stack - Method 25A

Average

Run Number 1 2 3

Test Date 5/14/2010 5/14/2010 5/14/2010

Run Start Time 8:25:00 AM 11:07:00 AM 1:40:00 PM

Run Finish Time 10:24:00 AM 1:06:00 PM 3:39:00 PM

Carbon Dioxide, % 14.2 14.4 14.5 14.367

Oxygen, % 4.3 4.4 4.3 4.333

Fuel Factor 1.17 1.15 1.14

Dry Volumetric Flow Rate, dry scfm 492006 492065 492681 492,250.667

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

Moisture, % 9.7 8.8 8.7 9.067

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 10 10 10 10.000

Operating Units ppm ppm ppm

No. Readings/Avg. 120 120 120 120.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID ZERO AIRTHCZERO AIRTHCZERO AIRTHC

Calibration Pre Zero Cylinder Instrument Response 0.11 0.02 0.01 0.047

Calibration Pre Zero Cylinder Bias 0 -0.9 -1 -0.633

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC175572-

THC

CC175572-

THC

CC175572-

THC

Calibration Pre High Cylinder Instrument Response 6.03 6.03 6 6.020

Calibration Pre High Cylinder Bias 0 0 -0.3 -0.100

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID ZERO AIRTHCZERO AIRTHCZERO AIRTHC

Calibration Post Zero Cylinder Instrument Response 0.02 0.01 0.03 0.020

Calibration Post Zero Cylinder Bias -0.9 -1 -0.8 -0.900

Calibration Post Zero Cylinder Drift 0.9 0.1 0.2 0.400

Calibration Post High Cylinder ID CC175572-

THC

CC175572-

THC

CC175572-

THC

Calibration Post High Cylinder Instrument Response 6.03 6 5.92 5.983

Calibration Post High Cylinder Bias 0 -0.3 -1.1 -0.467

Calibration Post High Cylinder Drift 0 0.3 0.8 0.367

Cavg 0.6 1 0.7 0.767

Cavg Units ppmvd ppmvd ppmvd

Cgas 0.5363 0.9817 0.6846 0.734

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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7/29/2010

Location Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 5/11/2010 5/12/2010 5/13/2010

Run Start Time 3:40:00 PM 11:45:00 AM 11:50:00 AM

Run Finish Time 6:52:00 PM 3:00:00 PM 3:05:00 PM

Net Traversing Points 28 28 28

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.17 0.17 0.235 0.192

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.004 1.004 1.004 1.004

Barometric Pressure, inches of Mercury 28.26 28.2 28.19 28.217

Average Orifice Meter Differential, inches H2O 0.96 1.00 0.73 0.897

Dry Gas Meter Volume Sampled, cubic feet 110.936 114.162 96.983 107.360

Average Dry Gas Meter Temperature, °F 76.38 80.10 87.96 81.480

Dry Gas Meter Volume Sampled, dscf 103.815 105.885 88.567 99.422

Total Moisture Liquid collected, g 104.7 119.6 162.2 128.833

Volume of Water Vapor, standard cubic feet 4.93 5.63 7.63 6.063

Moisture Content of Stack Gas, % 4.53 5.05 7.93 5.837

Moisture Saturation at Stack Gas Temperature, % 76.93 82.54 100.00 86.490

Dry Mole Fraction 0.9547 0.9495 0.9207 0.942

Carbon Dioxide, % 6.6 6.5 13.8 8.967

Oxygen, % 13.4 13.4 4.9 10.567

Carbon Monoxide & Nitrogen, % 80 80.1 81.3 80.467

Fuel Factor 1.14 1.15 1.16

Dry Molecular Weight, lb/lb-Mole 29.59 29.58 30.40 29.857

Wet Molecular weight, lb/lb-Mole 29.06 29.00 29.42 29.160

Flue Gas Static Pressure, inches of H2O 3 2.5 1.5 2.333

Absolute Flue Gas Pressure, inches of Mercury 28.48 28.38 28.30 28.387

Average Stack Gas Temperature, °F 196.75 199.96 314.58 237.097

Average Velocity Head, inches of H2O 1.7052049946

1139

1.696857420

16438

0.465163190

055236

1.289

Average Stack Gas Velocity, feet/second 83.53 83.77 47.24 71.513

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

Dry Volumetric Flow Rate, dry scfm 1,038,174.5 1,026,831.9 477,055.9 847,354.100

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,420,990.6 1,425,073.5 803,634.6 1,216,566.2

33

Percent Isokinetic of Sampling Rate, % 99.9 103.0 97.1 100.000

Percent Excess Air, % 173.6 173.0 29.6 125.400

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
Clinch River Unit 1

7/29/2010

Location Stack - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 5/11/2010 5/12/2010 5/13/2010

Run Start Time 10:00:00 AM 7:05:00 AM 7:15:00 AM

Run Finish Time 3:05:00 PM 11:25:00 AM 11:30:00 AM

Net Traversing Points 53 52 52

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.17 0.17 0.235 0.192

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.004 1.004 1.004 1.004

Barometric Pressure, inches of Mercury 28.26 28.2 29.19 28.550

Average Orifice Meter Differential, inches H2O 0.80 0.96 0.74 0.833

Dry Gas Meter Volume Sampled, cubic feet 132.627 148.348 127.214 136.063

Average Dry Gas Meter Temperature, °F 70.42 77.30 76.78 74.833

Dry Gas Meter Volume Sampled, dscf 125.457 138.295 122.797 128.850

Total Moisture Liquid collected, g 133.2 142.6 240.1 171.967

Volume of Water Vapor, standard cubic feet 6.27 6.71 11.30 8.093

Moisture Content of Stack Gas, % 4.76 4.63 8.43 5.940

Moisture Saturation at Stack Gas Temperature, % 77.54 74.25 100.00 83.930

Dry Mole Fraction 0.9524 0.9537 0.9157 0.941

Carbon Dioxide, % 6.6 6.6 13.9 9.033

Oxygen, % 13.4 13.4 4.7 10.500

Carbon Monoxide & Nitrogen, % 80 80 81.4 80.467

Fuel Factor 1.14 1.14 1.17

Dry Molecular Weight, lb/lb-Mole 29.59 29.59 30.41 29.863

Wet Molecular weight, lb/lb-Mole 29.04 29.05 29.36 29.150

Flue Gas Static Pressure, inches of H2O 3 2.5 1.5 2.333

Absolute Flue Gas Pressure, inches of Mercury 28.48 28.38 29.30 28.720

Average Stack Gas Temperature, °F 197.13 194.90 305.69 232.573

Average Velocity Head, inches of H2O 1.6710602206

9204

1.707404843

2242

0.478914198

069737

1.286

Average Stack Gas Velocity, feet/second 82.75 83.63 46.89 71.090

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

Dry Volumetric Flow Rate, dry scfm 1,025,409.1 1,037,605.7 493,252.3 852,089.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,407,721.5 1,422,691.8 797,680.5 1,209,364.6

00

Percent Isokinetic of Sampling Rate, % 91.7 99.9 97.6 96.400

Percent Excess Air, % 173.6 173.6 28.0 125.067

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
Clinch River Unit 1

7/29/2010

Location Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 5/14/2010 5/14/2010 5/14/2010

Run Start Time 8:25:00 AM 11:07:00 AM 1:40:00 PM

Run Finish Time 10:24:00 AM 1:06:00 PM 3:39:00 PM

Carbon Dioxide, % 14.2 14.4 14.5 14.367

Oxygen, % 4.3 4.4 4.3 4.333

Fuel Factor 1.17 1.15 1.14

Dry Volumetric Flow Rate, dry scfm 492006 492065 492681 492,250.667

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

Moisture, % 9.7 8.8 8.7 9.067

Analyzer Make ServoMex ServoMex ServoMex

Analyzer Model 01440D1 01440D1 01440D1 14,400.000

Analyzer Serial Number 3791 3791 3791 3,791.000

Operating Range 20 20 20 20.000

Operating Units % % %

No. Readings/Avg. 120 120 120 120.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID XC027884BCO2XC027884BCO2XC027884BCO2

Calibration Pre Zero Cylinder Instrument Response 0 0.03 0.03 0.020

Calibration Pre Zero Cylinder Bias 0.15 0.3 0.3 0.250

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC114878-

CO2

CC114878-

CO2

CC114878-

CO2

Calibration Pre High Cylinder Instrument Response 9.83 9.82 9.84 9.830

Calibration Pre High Cylinder Bias -0.1 -0.15 -0.05 -0.100

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID XC027884BCO2XC027884BCO2XC027884BCO2

Calibration Post Zero Cylinder Instrument Response 0.03 0.03 0.04 0.033

Calibration Post Zero Cylinder Bias 0.3 0.3 0.35 0.317

Calibration Post Zero Cylinder Drift 0.15 0 0.05 0.067

Calibration Post High Cylinder ID CC114878-

CO2

CC114878-

CO2

CC114878-

CO2

Calibration Post High Cylinder Instrument Response 9.82 9.84 9.75 9.803

Calibration Post High Cylinder Bias -0.15 -0.05 -0.5 -0.233

Calibration Post High Cylinder Drift 0.05 0.1 0.45 0.200

Cavg 14.2 14.4 14.5 14.367

Cavg Units %vd %vd %vd

Cgas 14.1705 14.37 14.5243 14.355

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
Clinch River Unit 1

7/29/2010

Location Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 5/14/2010 5/14/2010 5/14/2010

Run Start Time 1:40:00 PM 11:07:00 AM 1:40:00 PM

Run Finish Time 3:39:00 PM 1:06:00 PM 3:39:00 PM

Carbon Dioxide, % 14.5 14.4 14.5 14.467

Oxygen, % 4.3 4.4 4.3 4.333

Fuel Factor 1.14 1.15 1.14

Dry Volumetric Flow Rate, dry scfm 492681 492065 492681 492,475.667

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

Moisture, % 8.7 8.8 8.7 8.733

Analyzer Make ServoMex ServoMex ServoMex

Analyzer Model 01440D1 01440D1 01440D1 14,400.000

Analyzer Serial Number 3791 3791 3791 3,791.000

Operating Range 25 25 25 25.000

Operating Units % % %

No. Readings/Avg. 120 120 120 120.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID CC40376-O2 CC40376-O2 CC40376-O2

Calibration Pre Zero Cylinder Instrument Response 0.05 0.02 0.02 0.030

Calibration Pre Zero Cylinder Bias -0.2 -0.32 -0.32 -0.280

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC114878-O2 CC114878-

O2

CC114878-

O2

Calibration Pre High Cylinder Instrument Response 11.94 11.89 11.81 11.880

Calibration Pre High Cylinder Bias -0.28 -0.48 -0.8 -0.520

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC40376-O2 CC40376-O2 CC40376-O2

Calibration Post Zero Cylinder Instrument Response 0.02 0.02 0.02 0.020

Calibration Post Zero Cylinder Bias -0.32 -0.32 -0.32 -0.320

Calibration Post Zero Cylinder Drift 0.12 0 0 0.040

Calibration Post High Cylinder ID CC114878-O2 CC114878-

O2

CC114878-

O2

Calibration Post High Cylinder Instrument Response 11.89 11.81 11.82 11.840

Calibration Post High Cylinder Bias -0.48 -0.8 -0.76 -0.680

Calibration Post High Cylinder Drift 0.2 0.32 0.04 0.187

Cavg 4.3 4.4 4.3 4.333

Cavg Units %vd %vd %vd

Cgas 4.3081 4.4429 4.3544 4.368

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
Clinch River Unit 1

7/29/2010

Location Stack - OTM - 27/28

Average

Run Number MOTM27/OT

M28-1

MOTM27/O

TM28-2

MOTM27/OT

M28-3

Test Date 5/11/2010 5/12/2010 5/13/2010

Run Start Time 9:40:00 AM 7:05:00 AM 7:15:00 AM

Run Finish Time 4:53:00 PM 1:30:00 PM 1:33:00 PM

Net Traversing Points 77 76 76

Net Run Time, minutes 360 360 360

Nozzle Diameter, inches 0.135 0.135 0.186 0.152

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.993 0.993 0.993 0.993

Barometric Pressure, inches of Mercury 28.26 28.2 28.2 28.220

Average Orifice Meter Differential, inches H2O 0.36 0.36 0.39 0.370

Dry Gas Meter Volume Sampled, cubic feet 132.268 131.764 132.450 132.161

Average Dry Gas Meter Temperature, °F 68.22 71.14 74.78 71.380

Dry Gas Meter Volume Sampled, dscf 124.120 122.706 122.515 123.114

Total Moisture Liquid collected, g 113.8 183.2 221.1 172.700

Volume of Water Vapor, standard cubic feet 5.36 8.62 10.41 8.130

Moisture Content of Stack Gas, % 4.14 6.56 7.83 6.177

Moisture Saturation at Stack Gas Temperature, % 72.26 76.63 100.00 82.963

Dry Mole Fraction 0.9586 0.9344 0.9217 0.938

Carbon Dioxide, % 6.6 6.6 13.9 9.033

Oxygen, % 13.4 13.4 4.7 10.500

Carbon Monoxide & Nitrogen, % 80 80 81.4 80.467

Fuel Factor 1.14 1.14 1.17

Dry Molecular Weight, lb/lb-Mole 29.59 29.59 30.41 29.863

Wet Molecular weight, lb/lb-Mole 29.11 28.83 29.44 29.127

Flue Gas Static Pressure, inches of H2O 3 2.5 1.5 2.333

Absolute Flue Gas Pressure, inches of Mercury 28.48 28.38 28.31 28.390

Average Stack Gas Temperature, °F 193.78 196.40 304.89 231.690

Average Velocity Head, inches of H2O 1.7952329570

5758

1.756737093

43926

0.511929534

064029

1.355

Average Stack Gas Velocity, feet/second 85.44 85.25 49.22 73.303

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

Dry Volumetric Flow Rate, dry scfm 1,071,095.2 1,033,932.3 504,072.7 869,700.067

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,453,483.1 1,450,250.8 837,317.8 1,247,017.2

33

Percent Isokinetic of Sampling Rate, % 91.8 94.0 101.4 95.733

Percent Excess Air, % 173.6 173.6 28.0 125.067

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