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

Northeastern 3313

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.

Wednesday, January 19, 2011 Page 1 of 13
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Facility Information:

Northeastern

7300 E. Hwy 88

Oologah OK 74053

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:

2003-410-TVR

Permitted Source ID/Name:

3313 Northeastern Unit 3313

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 3313 has overfire air and burns sub-bituminous coal and has an electrostatic precipitator.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100222 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Subbituminous 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 367 0 0 0 734 2935 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack 2,3,7,8-TCDD Method 23 3 8 0

Stack 1,2,3,7,8-PeCDD Method 23 3 8 0

Stack 1,2,3,4,7,8-HxCDD Method 23 3 8 0

Stack 1,2,3,6,7,8-HxCDD Method 23 3 8 0

Stack 1,2,3,7,8,9-HxCDD Method 23 3 8 0

Stack 1,2,3,4,6,7,8-HpCDD Method 23 3 8 0

Stack OCDD Method 23 3 8 0

Wednesday, January 19, 2011 Page 2 of 13
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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 2,3,7,8-TCDF Method 23 3 8 0

Stack 1,2,3,7,8-PeCDF Method 23 3 8 0

Stack 2,3,4,7,8-PeCDF Method 23 3 8 0

Stack 1,2,3,4,7,8-HxCDF Method 23 3 8 0

Stack 1,2,3,6,7,8-HxCDF Method 23 3 8 0

Stack 2,3,4,6,7,8-HxCDF Method 23 3 8 0

Stack 1,2,3,7,8,9-HxCDF Method 23 3 8 0

Stack 1,2,3,4,6,7,8-HpCDF Method 23 3 8 0

Stack 1,2,3,4,7,8,9-HpCDF Method 23 3 8 0

Stack OCDF Method 23 3 8 0

Stack 3,3',4,4'-TCB (PCB77) Method 23 3 8 0

Stack 3,4,4',5-TCB (PCB81) Method 23 3 8 0

Stack 2,3,3',4,4'-PeCB (PCB105) Method 23 3 8 0

Stack 2,3,4,4',5-PeCB (PCB114) Method 23 3 8 0

Stack 2,3',4,4',5-PeCB (PCB118) Method 23 3 8 0

Stack 2',3,4,4',5-PeCB (PCB123) Method 23 3 8 0

Stack 3,3',4,4',5-PeCB (PCB126) Method 23 3 8 0

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Stack Method 23 3 8 0

Stack 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 8 0

Stack 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 8 0

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Stack Method 23 3 8 0

Stack Co2 Method 3A CO2 3 2 0

Stack O2 Method 3A O2 3 2 0

Wednesday, January 19, 2011 Page 3 of 13
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Sampling / Stack Data Results Summary

Location Stack - Method 23

Average

Run Number M23-1 M23-2 M23-3

Test Date 4/20/2010 4/21/2010 4/22/2010

Run Start Time 8:05:00 AM 6:55:00 

AM

6:25:00 AM

Run Finish Time 4:43:00 PM 3:20:00 PM 2:48:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 349.882 354.741 355.131 353.251

Moisture Content of Stack Gas, % 9.64 9.67 9.68 9.663

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

Carbon Dioxide, % 11.8 11.8 11.9 11.833

Oxygen, % 7.8 7.8 7.8 7.800

Average Stack Gas Temperature, °F 280.79 281.46 284.02 282.090

Dry Volumetric Flow Rate, dry scfm 1,251,278.0 1,275,812.8 1,279,184.2 1,268,758.33

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,990,072.0 2,045,608.9 2,065,443.5 2,033,708.13

3

Percent Isokinetic of Sampling Rate, % 102.3 101.7 101.5 101.833

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

Wednesday, January 19, 2011 Page 4 of 13
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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

Wednesday, January 19, 2011 Page 5 of 13
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Emissions Summary

Location: Stack - Method 23

Compound: 1,2,3,4,6,7,8-HpCDD

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000036 0.0000000045 0.0000000206 0.000

lb/mmBtuO2 3.54E-13 4.36E-13 2.00E-12 0.000

ng/dscm 3.63E-04 4.48E-04 2.05E-03 0.001

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000006 0.0000000071 0.000000035 0.000

lb/mmBtuO2 5.90E-13 6.88E-13 3.39E-12 0.000

ng/dscm 6.06E-04 7.07E-04 3.48E-03 0.002

Compound: 1,2,3,4,7,8,9-HpCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000002 0.0000000019 0.0000000037 0.000

lb/mmBtuO2 1.97E-13 1.84E-13 3.58E-13 0.000

ng/dscm 2.02E-04 1.89E-04 3.68E-04 0.000

Compound: 1,2,3,4,7,8-HxCDD

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000016 0.0000000016 0.0000000031 0.000

lb/mmBtuO2 1.57E-13 1.55E-13 3.00E-13 0.000

ng/dscm 1.62E-04 1.59E-04 3.08E-04 0.000

Compound: 1,2,3,4,7,8-HxCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000021 0.0000000027 0.0000000122 0.000

lb/mmBtuO2 2.06E-13 2.62E-13 1.18E-12 0.000

ng/dscm 2.12E-04 2.69E-04 1.21E-03 0.001

Compound: 1,2,3,6,7,8-HxCDD

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000016 0.0000000016 0.0000000056 0.000

lb/mmBtuO2 1.57E-13 1.55E-13 5.42E-13 0.000

ng/dscm 1.62E-04 1.59E-04 5.57E-04 0.000

Compound: 1,2,3,6,7,8-HxCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000024 0.0000000029 0.0000000147 0.000

lb/mmBtuO2 2.36E-13 2.81E-13 1.42E-12 0.000

ng/dscm 2.42E-04 2.89E-04 1.46E-03 0.001

Wednesday, January 19, 2011 Page 6 of 13
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7/29/2010

Compound: 1,2,3,7,8,9-HxCDD

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000015 0.0000000015 0.0000000039 0.000

lb/mmBtuO2 1.47E-13 1.45E-13 3.78E-13 0.000

ng/dscm 1.51E-04 1.49E-04 3.88E-04 0.000

Compound: 1,2,3,7,8,9-HxCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000019 0.0000000022 0.0000000018 0.000

lb/mmBtuO2 1.87E-13 2.13E-13 1.74E-13 0.000

ng/dscm 1.92E-04 2.19E-04 1.79E-04 0.000

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000016 0.0000000016 0.0000000024 0.000

lb/mmBtuO2 1.57E-13 1.55E-13 2.32E-13 0.000

ng/dscm 1.62E-04 1.59E-04 2.39E-04 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000016 0.0000000017 0.0000000097 0.000

lb/mmBtuO2 1.57E-13 1.65E-13 9.40E-13 0.000

ng/dscm 1.62E-04 1.69E-04 9.65E-04 0.000

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000062 0.0000000087 0.000000011 0.000

lb/mmBtuO2 6.10E-13 8.44E-13 1.07E-12 0.000

ng/dscm 6.26E-04 8.66E-04 1.09E-03 0.001

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000065 0.00000012 0.00000012 0.000

lb/mmBtuO2 6.39E-12 1.16E-11 1.16E-11 0.000

ng/dscm 6.56E-03 1.19E-02 1.19E-02 0.010

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000004 0.00000081 0.00000063 0.000

lb/mmBtuO2 3.93E-11 7.85E-11 6.10E-11 0.000

ng/dscm 4.04E-02 8.06E-02 6.27E-02 0.061

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.00000002 0.000000039 0.000000035 0.000

Wednesday, January 19, 2011 Page 7 of 13
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lb/mmBtuO2 1.97E-12 3.78E-12 3.39E-12 0.000

ng/dscm 2.02E-03 3.88E-03 3.48E-03 0.003

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000019 0.000000052 0.000000029 0.000

lb/mmBtuO2 1.87E-12 5.04E-12 2.81E-12 0.000

ng/dscm 1.92E-03 5.18E-03 2.88E-03 0.003

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000001 0.0000022 0.0000016 0.000

lb/mmBtuO2 9.83E-11 2.13E-10 1.55E-10 0.000

ng/dscm 1.01E-01 2.19E-01 1.59E-01 0.160

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000018 0.000000033 0.000000014 0.000

lb/mmBtuO2 1.77E-12 3.20E-12 1.36E-12 0.000

ng/dscm 1.82E-03 3.29E-03 1.39E-03 0.002

Compound: 2,3,4,6,7,8-HxCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000033 0.0000000031 0.0000000146 0.000

lb/mmBtuO2 3.24E-13 3.01E-13 1.41E-12 0.000

ng/dscm 3.33E-04 3.09E-04 1.45E-03 0.001

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000033 0.0000000034 0.0000000148 0.000

lb/mmBtuO2 3.24E-13 3.30E-13 1.43E-12 0.000

ng/dscm 3.33E-04 3.39E-04 1.47E-03 0.001

Compound: 2,3,7,8-TCDD

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000018 0.000000002 0.0000000016 0.000

lb/mmBtuO2 1.77E-13 1.94E-13 1.55E-13 0.000

ng/dscm 1.82E-04 1.99E-04 1.59E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000095 0.000000007 0.000000033 0.000

lb/mmBtuO2 9.34E-13 6.79E-13 3.20E-12 0.000

ng/dscm 9.59E-04 6.97E-04 3.28E-03 0.002

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

Wednesday, January 19, 2011 Page 8 of 13
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Process Run Data

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000047 0.0000000047 0.0000000045 0.000

lb/mmBtuO2 4.62E-13 4.56E-13 4.36E-13 0.000

ng/dscm 4.74E-04 4.68E-04 4.48E-04 0.000

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000067 0.000000016 0.000000016 0.000

lb/mmBtuO2 6.59E-13 1.55E-12 1.55E-12 0.000

ng/dscm 6.76E-04 1.59E-03 1.59E-03 0.001

Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.00000014 0.00000024 0.00000021 0.000

lb/mmBtuO2 1.38E-11 2.33E-11 2.03E-11 0.000

ng/dscm 1.41E-02 2.39E-02 2.09E-02 0.020

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.000000006 0.0000000095 0.0000000043 0.000

lb/mmBtuO2 5.90E-13 9.21E-13 4.17E-13 0.000

ng/dscm 6.06E-04 9.46E-04 4.28E-04 0.001

Compound: OCDD

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000164 0.0000000161 0.0000000306 0.000

lb/mmBtuO2 1.61E-12 1.56E-12 2.96E-12 0.000

ng/dscm 1.66E-03 1.60E-03 3.04E-03 0.002

Compound: OCDF

Average

RunNumber M23-1 M23-2 M23-3

Mass_mg 0.0000000042 0.0000000031 0.0000000073 0.000

lb/mmBtuO2 4.13E-13 3.01E-13 7.07E-13 0.000

ng/dscm 4.24E-04 3.09E-04 7.26E-04 0.000

Wednesday, January 19, 2011 Page 9 of 13
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Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Subbituminous Coal Burned 532.1 Tons/hr 500

2 Subbituminous Coal Burned 539.4 Tons/hr 500

3 Subbituminous Coal Burned 505.5 Tons/hr 500

1 Steam Temperature 575 Degrees F 575

2 Steam Temperature 575 Degrees F 575

3 Steam Temperature 575 Degrees F 575

1 Steam Pressure 3500.7 PSIG 3500

2 Steam Pressure 3501.7 PSIG 3500

3 Steam Pressure 3499.2 PSIG 3500

1 Excess Air 27.8 % 30

2 Excess Air 27.7 % 30

3 Excess Air 29.5 % 30

1 Gross Load 463.1 MW 465

2 Gross Load 463.9 MW 465

3 Gross Load 448.1 MW 465

1 Opacity 4.9 % 10

2 Opacity 5.1 % 10

3 Opacity 5.1 % 10

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

4.9 Opacity 10

2 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

5.1 Opacity 10

3 ELECTROSTATIC PRECIPITATOR - HIGH 

EFFICIENCY

5.1 Opacity 10

Wednesday, January 19, 2011 Page 10 of 13
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Sampling / Stack Data Results Detail

Location Stack - Method 23

Average

Run Number M23-1 M23-2 M23-3

Test Date 4/20/2010 4/21/2010 4/22/2010

Run Start Time 8:05:00 AM 6:55:00 AM 6:25:00 AM

Run Finish Time 4:43:00 PM 3:20:00 PM 2:48:00 PM

Net Traversing Points 52 52 52

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.277 0.277 0.277 0.277

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.994 0.994 0.994 0.994

Barometric Pressure, inches of Mercury 29.3 29.1 29 29.133

Average Orifice Meter Differential, inches H2O 1.51 1.53 1.55 1.530

Dry Gas Meter Volume Sampled, cubic feet 364.203 365.809 369.016 366.343

Average Dry Gas Meter Temperature, °F 77.02 68.41 70.66 72.030

Dry Gas Meter Volume Sampled, dscf 349.882 354.741 355.131 353.251

Total Moisture Liquid collected, g 792.9 806.8 808.5 802.733

Volume of Water Vapor, standard cubic feet 37.32 37.98 38.06 37.787

Moisture Content of Stack Gas, % 9.64 9.67 9.68 9.663

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

Dry Mole Fraction 0.9036 0.9033 0.9032 0.903

Carbon Dioxide, % 11.8 11.8 11.9 11.833

Oxygen, % 7.8 7.8 7.8 7.800

Carbon Monoxide & Nitrogen, % 80.4 80.4 80.3 80.367

Fuel Factor 1.11 1.11 1.10

Dry Molecular Weight, lb/lb-Mole 30.20 30.20 30.22 30.207

Wet Molecular weight, lb/lb-Mole 29.02 29.02 29.04 29.027

Flue Gas Static Pressure, inches of H2O -1.2 -1.2 -1.2 -1.200

Absolute Flue Gas Pressure, inches of Mercury 29.21 29.01 28.91 29.043

Average Stack Gas Temperature, °F 280.79 281.46 284.02 282.090

Average Velocity Head, inches of H2O 0.4523618055

73104

0.474175445

882762

0.480534192

005578

0.469

Average Stack Gas Velocity, feet/second 45.15 46.41 46.86 46.140

Stack Cross-Sectional Area, square feet 734.615 734.615 734.615 734.615

Dry Volumetric Flow Rate, dry scfm 1,251,278.0 1,275,812.8 1,279,184.2 1,268,758.3

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,990,072.0 2,045,608.9 2,065,443.5 2,033,708.1

33

Percent Isokinetic of Sampling Rate, % 102.3 101.7 101.5 101.833

Percent Excess Air, % 58.1 58.1 58.2 58.133

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

Round Duct Diameter, inches 367 367 367

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

Wednesday, January 19, 2011 Page 11 of 13
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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

Wednesday, January 19, 2011 Page 12 of 13
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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

Wednesday, January 19, 2011 Page 13 of 13