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

Amos 2

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 24
Amos 2

8/27/2010

Facility Information:

John E. Amos

P.O. Box 4000

Winfield W 25177

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:

R30-07900006-2005

Permitted Source ID/Name:

Unit 2 Unit 2

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:

Unit 2 is a bituminous coal fired unit rated at 7020 mmBTU/hr equipped with an SCR, FGD, and precipitator.

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.

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 402.99 0 0 0 806 3224 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Hydrogen Fluoride Method 26A 3 0

Stack Hydrogen Chloride Method 26A 3 0

Stack O2 Method 3A O2 3 0

Stack Co2 Method 3A CO2 3 0

Tuesday, January 18, 2011 Page 2 of 24
Amos 2

8/27/2010

Tuesday, January 18, 2011 Page 3 of 24
Amos 2

8/27/2010

Sampling / Stack Data Results Summary

Location Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 7/27/2010 7/27/2010 7/28/2010

Run Start Time 8:30:00 AM 12:00:00 

PM

6:55:00 AM

Run Finish Time 11:42:00 AM 3:12:00 PM 10:07:00 AM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 101.382 101.019 101.282 101.228

Moisture Content of Stack Gas, % 15.47 15.82 16.08 15.790

Moisture Saturation at Stack Gas Temperature, % 16.19 16.19 16.18 16.187

Carbon Dioxide, % 13.2 13.3 13 13.167

Oxygen, % 6 6 6.1 6.033

Average Stack Gas Temperature, °F 132.00 132.00 132.00 132.000

Dry Volumetric Flow Rate, dry scfm 1,885,035.2 1,879,977.4 1,874,661.5 1,879,891.36

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,541,954.0 2,545,674.2 2,544,611.3 2,544,079.83

3

Percent Isokinetic of Sampling Rate, % 100.3 100.2 100.7 100.400

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

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

Tuesday, January 18, 2011 Page 4 of 24
Amos 2

8/27/2010

Location Stack - Method 3A O2

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

Tuesday, January 18, 2011 Page 5 of 24
Amos 2

8/27/2010

Emissions Summary

Process Run Data

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0.5 0.62 0.71 0.610

lb/mmBtuO2 1.49E-04 1.86E-04 2.13E-04 0.000

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0.39 0.23 0.23 0.283

lb/mmBtuO2 1.16E-04 6.89E-05 6.91E-05 0.000

Tuesday, January 18, 2011 Page 6 of 24
Amos 2

8/27/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 302 Tons/hr The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

300

Tuesday, January 18, 2011 Page 7 of 24
Amos 2

8/27/2010

2 Bituminous Coal Burned 302 Tons/hr The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

300

Tuesday, January 18, 2011 Page 8 of 24
Amos 2

8/27/2010

3 Bituminous Coal Burned 302 Tons/hr The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

300

Tuesday, January 18, 2011 Page 9 of 24
Amos 2

8/27/2010

1 Gross Load 812 MW The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

800

Tuesday, January 18, 2011 Page 10 of 24
Amos 2

8/27/2010

2 Gross Load 812 MW The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

800

Tuesday, January 18, 2011 Page 11 of 24
Amos 2

8/27/2010

3 Gross Load 812 MW The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

800

Tuesday, January 18, 2011 Page 12 of 24
Amos 2

8/27/2010

1 Steam Temperature 994 F The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

1000

Tuesday, January 18, 2011 Page 13 of 24
Amos 2

8/27/2010

2 Steam Temperature 994 F The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

1000

Tuesday, January 18, 2011 Page 14 of 24
Amos 2

8/27/2010

3 Steam Temperature 994 F The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

1000

Tuesday, January 18, 2011 Page 15 of 24
Amos 2

8/27/2010

1 Steam Pressure 3489 psig The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

3500

Tuesday, January 18, 2011 Page 16 of 24
Amos 2

8/27/2010

2 Steam Pressure 3489 psig The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

3500

Tuesday, January 18, 2011 Page 17 of 24
Amos 2

8/27/2010

3 Steam Pressure 3489 psig The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

3500

Tuesday, January 18, 2011 Page 18 of 24
Amos 2

8/27/2010

1 Opacity 3.52 % The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

10

Tuesday, January 18, 2011 Page 19 of 24
Amos 2

8/27/2010

2 Opacity 3.52 % The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

10

Tuesday, January 18, 2011 Page 20 of 24
Amos 2

8/27/2010

APCD Run Data

Process Lab Run Data

3 Opacity 3.52 % The ERT requires 

that the process 

data collected 

during the stack 

test period be 

accompanied by a 

target value. For 

the AEP tests, we 

want to clarify that 

the target value 

provided does not 

represent any limit 

or maximum 

design set point for 

operation of the 

steam generators 

and associated 

control 

equipment. In 

some cases, the 

value is a permit or 

regulatory limit, 

such as the case of 

opacity. Operation 

outside of the 

target value does 

not represent 

abnormal 

operation.

10

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

3.52 % 10

2 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

3.52 % 10

3 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

3.52 % 10

1 SCRUBBER 481 ppm 490

2 SCRUBBER 489 ppm 490

3 SCRUBBER 489 ppm 490

1 SCR (SELECTIVE CATALYTIC REDUCTION) 0.05 lb/mmbtu 0.1

Tuesday, January 18, 2011 Page 21 of 24
Amos 2

8/27/2010

Sampling / Stack Data Results Detail

Location Stack - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 7/27/2010 7/27/2010 7/28/2010

Run Start Time 8:30:00 AM 12:00:00 PM 6:55:00 AM

Run Finish Time 11:42:00 AM 3:12:00 PM 10:07:00 AM

Net Traversing Points 28 28 28

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.22 0.22 0.22 0.220

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.008 1.008 1.008 1.008

Barometric Pressure, inches of Mercury 29.5 29.5 29.52 29.507

Average Orifice Meter Differential, inches H2O 1.07 1.09 1.08 1.080

Dry Gas Meter Volume Sampled, cubic feet 108.875 108.424 107.995 108.431

Average Dry Gas Meter Temperature, °F 105.04 104.75 101.42 103.737

Dry Gas Meter Volume Sampled, dscf 101.382 101.019 101.282 101.228

Total Moisture Liquid collected, g 394.4 403.5 412.4 403.433

Volume of Water Vapor, standard cubic feet 18.56 18.99 19.41 18.987

Moisture Content of Stack Gas, % 15.47 15.82 16.08 15.790

Moisture Saturation at Stack Gas Temperature, % 16.19 16.19 16.18 16.187

Dry Mole Fraction 0.8453 0.8418 0.8392 0.842

Carbon Dioxide, % 13.2 13.3 13 13.167

Oxygen, % 6 6 6.1 6.033

Carbon Monoxide & Nitrogen, % 80.8 80.7 80.9 80.800

Fuel Factor 1.13 1.12 1.14

Dry Molecular Weight, lb/lb-Mole 30.35 30.37 30.32 30.347

Wet Molecular weight, lb/lb-Mole 28.44 28.41 28.34 28.397

Flue Gas Static Pressure, inches of H2O -1 -1 -1 -1.000

Absolute Flue Gas Pressure, inches of Mercury 29.43 29.43 29.45 29.437

Average Stack Gas Temperature, °F 132.00 132.00 132.00 132.000

Average Velocity Head, inches of H2O 0.6271031716

71862

0.628434623

35292

0.626630122

411014

0.627

Average Stack Gas Velocity, feet/second 47.83 47.90 47.88 47.870

Stack Cross-Sectional Area, square feet 885.760 885.760 885.760 885.760

Dry Volumetric Flow Rate, dry scfm 1,885,035.2 1,879,977.4 1,874,661.5 1,879,891.3

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,541,954.0 2,545,674.2 2,544,611.3 2,544,079.8

33

Percent Isokinetic of Sampling Rate, % 100.3 100.2 100.7 100.400

Percent Excess Air, % 39.1 39.2 40.0 39.433

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

Round Duct Diameter, inches 402.99 402.99 402.99

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

Tuesday, January 18, 2011 Page 22 of 24
Amos 2

8/27/2010

Location Stack - Method 3A CO2

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

Tuesday, January 18, 2011 Page 23 of 24
Amos 2

8/27/2010

Location Stack - Method 3A O2

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

Tuesday, January 18, 2011 Page 24 of 24