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.

Saturday, January 15, 2011 Page 1 of 10
Facility Information:

Harrison Power Station

State Route 20

Haywood W 26366

Contact: Mark Sowa

Phone: 724-838-6133

Fax: 724-830-7711

Email: msowa@alleghenyenergy.com

Testing Company:

TEST, Inc.

Route 2 Box 33B

Poca W 25159

Contact: Paul Chinuntdet

Phone: 304 755 1077

Fax: 304 755 1099

Email: pchin@testincorp.com

Air Permit Number:

R30-03300015-2009

Permitted Source ID/Name:

3944 Harrison Power Station Unit 3

Permitted Maximum Process Rate: Max. Normal Operation Process Rate:

693 MW NSOC

Target Process Test Rate

> 623.7 MW (net)

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

 process flow diagram:

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 110000586125 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 S3 360 0 0 0 0 0 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack S1 Hydrogen Fluoride Method 26A 3 180 0

Stack S1 Hydrogen Chloride Method 26A 3 180 0

Hydrogen Chloride Method 26 3 180 0 Please change to 

Method 26A

Stack S1

Hydrogen Fluoride Method 26 3 180 0 Please change to 

Method 26A

Stack S1

Regulation Description Compound Limit Unit

Utilty MACT ICR 0

Saturday, January 15, 2011 Page 2 of 10
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 S1 Sulfur Dioxide Method 6C 3 60 0

Stack S1 Nitrogen oxides (NOx) Method 7E 3 60 0

Stack S2 Hydrogen Fluoride Method 26A 3 180 0

Stack S2 Hydrogen Chloride Method 26A 3 180 0

Stack S2 Sulfur Dioxide Method 6C 3 60 0

Stack S2 Nitrogen oxides (NOx) Method 7E 3 60 0

Stack S3 Hydrogen Fluoride Method 26A 3 180 0

Stack S3 Hydrogen Chloride Method 26A 3 180 0

Stack S3 Sulfur Dioxide Method 6C 3 60 0

Stack S3 Nitrogen oxides (NOx) Method 7E 3 60 0

Saturday, January 15, 2011 Page 3 of 10
Sampling / Stack Data Results Summary

Location Stack S3 - Method 26A

Average

Run Number 1 2 3

Test Date 3/18/2010 3/18/2010 3/18/2010

Run Start Time 8:15:00 AM 12:00:00 

PM

3:45:00 PM

Run Finish Time 11:30:00 AM 3:15:00 PM 7:00:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 91.833 90.083 89.703 90.540

Moisture Content of Stack Gas, % 12.32 12.13 12.29 12.247

Moisture Saturation at Stack Gas Temperature, % 12.68 12.82 12.86 12.787

Carbon Dioxide, % 11.65 11.58 11.76 11.663

Oxygen, % 7.45 7.42 7.34 7.403

Average Stack Gas Temperature, °F 123.58 124.00 124.00 123.860

Dry Volumetric Flow Rate, dry scfm 2,660,142.2 2,667,363.2 2,658,755.5 2,662,086.96

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 3,348,810.5 3,353,051.6 3,357,292.8 3,353,051.63

3

Percent Isokinetic of Sampling Rate, % 102.1 99.9 99.8 100.600

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 S3 - Method 6C

Average

Run Number 1 2 3

Test Date 3/18/2010 3/18/2010 3/18/2010

Run Start Time 8:07:00 AM 11:49:00 

AM

3:43:00 PM

Run Finish Time 9:07:00 AM 12:49:00 

PM

4:43:00 PM

Carbon Dioxide, % 11.65 11.58 11.76 11.663

Oxygen, % 7.45 7.42 7.34 7.403

Dry Volumetric Flow Rate, dry scfm 2004682 2015983 2013227 2,011,297.33

3

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

Moisture, % 12.37 12.06 12.05 12.160

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, January 15, 2011 Page 4 of 10
Location Stack S3 - Method 7E

Average

Run Number 1 2 3

Test Date 3/18/2010 3/18/2010 3/18/2010

Run Start Time 8:07:00 AM 11:49:00 

AM

3:43:00 PM

Run Finish Time 9:07:00 AM 12:49:00 

PM

4:43:00 PM

Carbon Dioxide, % 11.65 11.58 11.76 11.663

Oxygen, % 7.45 7.42 7.34 7.403

Dry Volumetric Flow Rate, dry scfm 2004682 2015983 2013227 2,011,297.33

3

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

Moisture, % 12.37 12.06 12.05 12.160

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, January 15, 2011 Page 5 of 10
Emissions Summary

Process Run Data

Location: Stack S3 - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 1.81 1.71 1.53 1.683

Elb/hr 6.94E+00 6.70E+00 6.00E+00 6.547

lb/mmBtuO2 6.60E-04 6.35E-04 5.67E-04 0.001

mg/dscm 6.96E-01 6.70E-01 6.02E-01 0.656

ppm 4.59E-01 4.42E-01 3.97E-01 0.433

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.37 0.33 0.33 0.343

Elb/hr 1.42E+00 1.29E+00 1.29E+00 1.333

lb/mmBtuO2 1.35E-04 1.22E-04 1.22E-04 0.000

mg/dscm 1.42E-01 1.29E-01 1.30E-01 0.134

ppm 1.71E-01 1.56E-01 1.56E-01 0.161

Location: Stack S3 - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 1.75E+03 1.60E+03 1.56E+03 1,636.667

lb/mmBtuO2 2.21E-01 2.01E-01 1.95E-01 0.206

ppm 8.73E+01 7.96E+01 7.77E+01 81.533

Location: Stack S3 - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 8.37E+02 7.96E+02 8.45E+02 826.000

lb/mmBtuO2 1.06E-01 9.98E-02 1.05E-01 0.104

ppm 5.83E+01 5.51E+01 5.86E+01 57.333

Saturday, January 15, 2011 Page 6 of 10
Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat input 0 lb/mmbtu 0

1 Bituminous Coal Burned 0 1000 Tons/hr 0

Run Name Value UOM Comments

Target

Value

1 WET SCRUBBER 0 0

Run Name Value UOM Comments

1 Cl 0.79 %

2 Cl 0 %

1 Fl 0 ppm

Saturday, January 15, 2011 Page 7 of 10
Sampling / Stack Data Results Detail

Location Stack S3 - Method 26A

Average

Run Number 1 2 3

Test Date 3/18/2010 3/18/2010 3/18/2010

Run Start Time 8:15:00 AM 12:00:00 PM 3:45:00 PM

Run Finish Time 11:30:00 AM 3:15:00 PM 7:00:00 PM

Net Traversing Points 37 37 37

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.156 0.156 0.156 0.156

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.025 1.025 1.025 1.025

Barometric Pressure, inches of Mercury 29.96 29.96 29.88 29.933

Average Orifice Meter Differential, inches H2O 0.69 0.66 0.65 0.667

Dry Gas Meter Volume Sampled, cubic feet 93.115 91.616 91.739 92.157

Average Dry Gas Meter Temperature, °F 90.42 92.04 93.63 92.030

Dry Gas Meter Volume Sampled, dscf 91.833 90.083 89.703 90.540

Total Moisture Liquid collected, g 274 264 267 268.333

Volume of Water Vapor, standard cubic feet 12.90 12.43 12.57 12.633

Moisture Content of Stack Gas, % 12.32 12.13 12.29 12.247

Moisture Saturation at Stack Gas Temperature, % 12.68 12.82 12.86 12.787

Dry Mole Fraction 0.8768 0.8787 0.8771 0.878

Carbon Dioxide, % 11.65 11.58 11.76 11.663

Oxygen, % 7.45 7.42 7.34 7.403

Carbon Monoxide & Nitrogen, % 80.9 81 80.9 80.933

Fuel Factor 1.15 1.16 1.15

Dry Molecular Weight, lb/lb-Mole 30.16 30.15 30.18 30.163

Wet Molecular weight, lb/lb-Mole 28.66 28.68 28.68 28.673

Flue Gas Static Pressure, inches of H2O 0 0 0 0.000

Absolute Flue Gas Pressure, inches of Mercury 29.96 29.96 29.88 29.933

Average Stack Gas Temperature, °F 123.58 124.00 124.00 123.860

Average Velocity Head, inches of H2O 1.7787807497

1373

1.783134880

126

1.783134880

126

1.782

Average Stack Gas Velocity, feet/second 78.96 79.06 79.16 79.060

Stack Cross-Sectional Area, square feet 706.858 706.858 706.858 706.858

Dry Volumetric Flow Rate, dry scfm 2,660,142.2 2,667,363.2 2,658,755.5 2,662,086.9

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 3,348,810.5 3,353,051.6 3,357,292.8 3,353,051.6

33

Percent Isokinetic of Sampling Rate, % 102.1 99.9 99.8 100.600

Percent Excess Air, % 53.6 53.1 52.4 53.033

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

Round Duct Diameter, inches 360 360 360

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Saturday, January 15, 2011 Page 8 of 10
Location Stack S3 - Method 6C

Average

Run Number 1 2 3

Test Date 3/18/2010 3/18/2010 3/18/2010

Run Start Time 8:07:00 AM 11:49:00 AM 3:43:00 PM

Run Finish Time 9:07:00 AM 12:49:00 PM 4:43:00 PM

Carbon Dioxide, % 11.65 11.58 11.76 11.663

Oxygen, % 7.45 7.42 7.34 7.403

Fuel Factor 1.15 1.16 1.15

Dry Volumetric Flow Rate, dry scfm 2004682 2015983 2013227 2,011,297.3

33

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

Moisture, % 12.37 12.06 12.05 12.160

Analyzer Make Western 

research

Western 

Research

Western 

research

Analyzer Model 721AT 721AT 721AT

Analyzer Serial Number

Operating Range 111.4 111.4 111.4 111.400

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 Nitrogen Nitrogen Nitrogen

Calibration Pre Zero Cylinder Instrument Response 0.2 0.9 1.2 0.767

Calibration Pre Zero Cylinder Bias 0.18 0.81 1.08 0.690

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID sg160260b sg160260b sg160260b

Calibration Pre High Cylinder Instrument Response 50.8 51.9 52.2 51.633

Calibration Pre High Cylinder Bias -0.27 0.72 0.99 0.480

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Nitrogen Nitrogen Nitrogen

Calibration Post Zero Cylinder Instrument Response 0.9 1.2 -2.7 -0.200

Calibration Post Zero Cylinder Bias 0.81 1.08 -2.42 -0.177

Calibration Post Zero Cylinder Drift 0.63 0.27 3.5 1.467

Calibration Post High Cylinder ID sg160260b sg160260b sg160260b

Calibration Post High Cylinder Instrument Response 51.9 52.2 47.1 50.400

Calibration Post High Cylinder Bias 0.72 0.99 -3.59 -0.627

Calibration Post High Cylinder Drift 0.99 0.27 4.58 1.947

Cavg 87.65 80.77 76.14 81.520

Cavg Units ppmvd ppmvd ppmvd

Cgas 87.2715 79.5637 77.6528 81.496

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

Saturday, January 15, 2011 Page 9 of 10
Location Stack S3 - Method 7E

Average

Run Number 1 2 3

Test Date 3/18/2010 3/18/2010 3/18/2010

Run Start Time 8:07:00 AM 11:49:00 AM 3:43:00 PM

Run Finish Time 9:07:00 AM 12:49:00 PM 4:43:00 PM

Carbon Dioxide, % 11.65 11.58 11.76 11.663

Oxygen, % 7.45 7.42 7.34 7.403

Fuel Factor 1.15 1.16 1.15

Dry Volumetric Flow Rate, dry scfm 2004682 2015983 2013227 2,011,297.3

33

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

Moisture, % 12.37 12.06 12.05 12.160

Analyzer Make Thermo Thermo Thermo

Analyzer Model 10 10 10 10.000

Analyzer Serial Number

Operating Range 108.7 108.7 108.7 108.700

Operating Units ppm ppm ppm

No. Readings/Avg. 120 120 120 120.000

Calibration Set 4 4 4 4.000

Calibration Pre Zero Cylinder ID Nitrogen Nitrogen Nitrogen

Calibration Pre Zero Cylinder Instrument Response 0.1 0.4 0.5 0.333

Calibration Pre Zero Cylinder Bias 0.09 0.37 0.46 0.307

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID cc165167 cc165167 cc165167

Calibration Pre High Cylinder Instrument Response 25 26.6 26.8 26.133

Calibration Pre High Cylinder Bias -0.18 1.29 1.47 0.860

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID Nitrogen Nitrogen Nitrogen

Calibration Post Zero Cylinder Instrument Response 0.4 0.5 0.1 0.333

Calibration Post Zero Cylinder Bias 0.37 0.46 0.09 0.307

Calibration Post Zero Cylinder Drift 0.28 0.09 0.37 0.247

Calibration Post High Cylinder ID cc165167 cc165167 cc165167

Calibration Post High Cylinder Instrument Response 26.6 26.8 22 25.133

Calibration Post High Cylinder Bias 1.29 1.47 -2.94 -0.060

Calibration Post High Cylinder Drift 1.47 0.18 4.41 2.020

Cavg 60.26 58.74 57.22 58.740

Cavg Units ppmvd ppmvd ppmvd

Cgas 58.2954 55.1146 58.6205 57.344

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

Saturday, January 15, 2011 Page 10 of 10