### 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

### Northeastern 3313
7/29/2010 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: Northeastern Unit 3313 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 367 734 2935 4 0 24 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location 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 Stack



### Wednesday, January 19, 2011 Page 2 of 13

### Northeastern 3313
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.

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

HxCB (PCBs156/157) 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 Stack 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 8 0 Stack

Co2 Method 3A CO2 3 2 0 Stack O2 Method 3A O2 3 2 0 Stack



### Wednesday, January 19, 2011 Page 3 of 13

### Northeastern 3313
7/29/2010 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

### Northeastern 3313
7/29/2010
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



### Wednesday, January 19, 2011 Page 5 of 13

### Northeastern 3313
7/29/2010 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

### Northeastern 3313
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

### Northeastern 3313
7/29/2010
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

### Northeastern 3313
7/29/2010

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

### Northeastern 3313
7/29/2010 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

### Northeastern 3313
7/29/2010 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

### Northeastern 3313
7/29/2010
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



### Wednesday, January 19, 2011 Page 12 of 13

### Northeastern 3313
7/29/2010
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



### Wednesday, January 19, 2011 Page 13 of 13