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 1

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 S1 360 0 0 0 300 300 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 S1 - Method 26

Average

Run Number 1 2 3

Test Date 4/20/2010 4/20/2010 4/20/2010

Run Start Time 7:35:00 AM 11:35:00 

AM

3:15:00 PM

Run Finish Time 10:45:00 AM 2:42:00 PM 6:27:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 90.849 93.319 93.070 92.413

Moisture Content of Stack Gas, % 12.32 11.12 11.58 11.673

Moisture Saturation at Stack Gas Temperature, % 12.46 12.47 12.55 12.493

Carbon Dioxide, % 11.77 12.11 11.76 11.880

Oxygen, % 7.59 7.14 7.64 7.457

Average Stack Gas Temperature, °F 121.17 121.17 121.28 121.207

Dry Volumetric Flow Rate, dry scfm 2,467,107.6 2,528,478.2 2,509,150.8 2,501,578.86

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 3,249,143.5 3,287,313.8 3,289,010.3 3,275,155.86

7

Percent Isokinetic of Sampling Rate, % 108.9 109.2 109.7 109.267

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 S1 - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Saturday, January 15, 2011 Page 4 of 10
Location Stack S1 - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

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

Process Run Data

Location: Stack S1 - Method 26

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 3.09 1.06 0.77 1.640

Elb/hr 1.11E+01 3.80E+00 2.75E+00 5.883

lb/mmBtuO2 1.15E-03 3.72E-04 2.81E-04 0.001

mg/dscm 1.20E+00 4.01E-01 2.92E-01 0.631

ppm 7.92E-01 2.65E-01 1.93E-01 0.417

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.03 0.51 0.02 0.187

Elb/hr 1.08E-01 1.83E+00 7.13E-02 0.670

lb/mmBtuO2 1.12E-05 1.79E-04 7.30E-06 0.000

mg/dscm 1.17E-02 1.93E-01 7.59E-03 0.071

ppm 1.40E-02 2.32E-01 9.12E-03 0.085

Location: Stack S1 - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 1.42E+03 1.39E+03 1.40E+03 1,403.333

lb/mmBtuO2 1.83E-01 1.77E-01 1.75E-01 0.178

ppm 7.25E+01 7.08E+01 7.07E+01 71.333

Location: Stack S1 - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 5.10E+02 5.13E+02 5.26E+02 516.333

lb/mmBtuO2 6.60E-02 6.54E-02 6.58E-02 0.066

ppm 3.64E+01 3.65E+01 3.71E+01 36.667

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 S1 - Method 26

Average

Run Number 1 2 3

Test Date 4/20/2010 4/20/2010 4/20/2010

Run Start Time 7:35:00 AM 11:35:00 AM 3:15:00 PM

Run Finish Time 10:45:00 AM 2:42:00 PM 6:27:00 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 28.53 28.51 28.43 28.490

Average Orifice Meter Differential, inches H2O 0.72 0.77 0.76 0.750

Dry Gas Meter Volume Sampled, cubic feet 98.924 101.878 102.055 100.952

Average Dry Gas Meter Temperature, °F 102.97 104.11 105.00 104.027

Dry Gas Meter Volume Sampled, dscf 90.849 93.319 93.070 92.413

Total Moisture Liquid collected, g 271 248 259 259.333

Volume of Water Vapor, standard cubic feet 12.76 11.67 12.19 12.207

Moisture Content of Stack Gas, % 12.32 11.12 11.58 11.673

Moisture Saturation at Stack Gas Temperature, % 12.46 12.47 12.55 12.493

Dry Mole Fraction 0.8768 0.8888 0.8842 0.883

Carbon Dioxide, % 11.77 12.11 11.76 11.880

Oxygen, % 7.59 7.14 7.64 7.457

Carbon Monoxide & Nitrogen, % 80.64 80.75 80.6 80.663

Fuel Factor 1.13 1.14 1.13

Dry Molecular Weight, lb/lb-Mole 30.19 30.22 30.19 30.200

Wet Molecular weight, lb/lb-Mole 28.69 28.86 28.78 28.777

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 28.52 28.50 28.42 28.480

Average Stack Gas Temperature, °F 121.17 121.17 121.28 121.207

Average Velocity Head, inches of H2O 1.6024886941

1727

1.648608384

5337

1.640793186

12933

1.631

Average Stack Gas Velocity, feet/second 76.61 77.51 77.55 77.223

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

Dry Volumetric Flow Rate, dry scfm 2,467,107.6 2,528,478.2 2,509,150.8 2,501,578.8

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 3,249,143.5 3,287,313.8 3,289,010.3 3,275,155.8

67

Percent Isokinetic of Sampling Rate, % 108.9 109.2 109.7 109.267

Percent Excess Air, % 55.4 50.4 56.0 53.933

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 S1 - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, January 15, 2011 Page 9 of 10
Location Stack S1 - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Saturday, January 15, 2011 Page 10 of 10