### Name:

Title: Company: Sign Date: Name: Title: Company: Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date 

## Northport Unit 2 ICR Test Program

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.

Monday, February 28, 2011 Page 1 of 57

### Northport Unit 2 ICR Test Program

Facility Information: Northport
301 Eatons Neck Road

Northport NY 11768 Contact: Paul Lynch
Phone: 516-545-2564
Fax: 516-545-2582
Email: paul.lynch@us.ngrid.com Testing Company:
AirNova Inc. 5845 Clayton Avenue

Pennsauken NJ 08109 Contact: Lenny D. Katerynczuk
Phone: 856-486-1500
Fax: 856-486-9896
Email: lenny@airnova.com

Air Permit Number: 1-4726-00130/00041 Permitted Source ID/Name: Boiler 2 U-00002
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: This source is a tangential fired external combustion boiler used for electric generation. Rated at 385 MW and can fire either #6 residual oil or natural gas. Exhaust gases from the boiler are split between two air heaters then travel through individual dual pass Buell electrostatic precipitators. From the ESP exhaust gas is passed through dual induced draft fans then enters the stack through dual breechings. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: Enter ARS ID FRS #: Enter FRS ID

SCC / Description 10100404 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: Tangential Firing

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
Duct near stack breaching 0 12 12 4 65.29 24 124 108

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location % H2O Method 1 - 4 3 180 0 Duct near stack breaching Regulation Description Compound Limit Unit
0



### Monday, February 28, 2011 Page 2 of 57

### Northport Unit 2 ICR Test Program

Carbon Monoxide Method 10 3 120 0 Duct near stack breaching Formaldehyde Method 0011 3 120 0 Duct near stack breaching 2,3,7,8-TCDD Method 23 3 480 0 Duct near stack breaching 1,2,3,7,8-PeCDD Method 23 3 480 0 Duct near stack breaching OCDD Method 23 3 480 0 Duct near stack breaching 2,3,7,8-TCDF Method 23 3 480 0 Duct near stack breaching 1,2,3,7,8-PeCDF Method 23 3 480 0 Duct near stack breaching 2,3,4,7,8-PeCDF Method 23 3 480 0 Duct near stack breaching 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0 Duct near stack breaching OCDF Method 23 3 480 0 Duct near stack breaching Other TCDD Method 23 3 480 0 Duct near stack breaching Other PeCDD Method 23 3 480 0 Duct near stack breaching Other HxCDD Method 23 3 480 0 Duct near stack breaching Other HpCDD Method 23 3 480 0 Duct near stack breaching Other TCDF Method 23 3 480 0 Duct near stack breaching Other PeCDF Method 23 3 480 0 Duct near stack breaching Other HxCDF Method 23 3 480 0 Duct near stack breaching Other HpCDF Method 23 3 480 0 Duct near stack breaching 3,3',4,4'-TCB (PCB77) Method 23 3 480 0 Duct near stack breaching



### Monday, February 28, 2011 Page 3 of 57

### Northport Unit 2 ICR Test Program

3,4,4',5-TCB (PCB81) Method 23 3 480 0 Duct near stack breaching 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0 Duct near stack breaching 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0 Duct near stack breaching 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0 Duct near stack breaching 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0 Duct near stack breaching 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0 Duct near stack breaching 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 480 0 Duct near stack breaching 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0 Duct near stack breaching 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0 Duct near stack breaching 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 0 Duct near stack breaching Total organic compounds

(TOC) as Propane Method 25A 3 120 0 Duct near stack breaching Hydrogen Fluoride Method 26A 3 180 0 Duct near stack breaching Hydrogen Chloride Method 26A 3 180 0 Duct near stack breaching Hydrogen Chloride Method 26 3 180 0 Duct near stack breaching Hydrogen Fluoride Method 26 3 180 0 Duct near stack breaching Filterable PM2.5 OTM - 27/28 3 240 0 Duct near stack breaching Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 240 0 Duct near stack breaching Organic Condensible

Particulate OTM - 27/28 3 240 0 Duct near stack breaching Total PM2.5 OTM - 27/28 3 240 0 Duct near stack breaching



### Monday, February 28, 2011 Page 4 of 57

### Northport Unit 2 ICR Test Program

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.

Filterable Particulate Method 29 3 240 0 Duct near stack breaching Antimony Method 29 3 240 0 Duct near stack breaching Manganese Method 29 3 240 0 Duct near stack breaching Cadmium Method 29 3 240 0 Duct near stack breaching Selenium Method 29 3 240 0 Duct near stack breaching Lead Method 29 3 240 0 Duct near stack breaching Chromium Method 29 3 240 0 Duct near stack breaching Arsenic Method 29 3 240 0 Duct near stack breaching Beryllium Method 29 3 240 0 Duct near stack breaching Nickel Method 29 3 240 0 Duct near stack breaching O2 Method 3A O2 3 480 0 Duct near stack breaching Co2 Method 3A CO2 3 480 0 Duct near stack breaching O2 Method 3A O2 3 120 0 Duct near stack breaching Co2 Method 3A CO2 3 120 0 Duct near stack breaching O2 Method 3A O2 3 240 0 Duct near stack breaching Co2 Method 3A CO2 3 240 0 Duct near stack breaching Filterable Particulate Method 5 3 240 0 Duct near stack breaching Sulfur Dioxide Method 6C 3 180 0 Duct near stack breaching Nitrogen oxides (NOx) Method 7E 3 180 0 Duct near stack breaching



### Monday, February 28, 2011 Page 5 of 57

### Northport Unit 2 ICR Test Program

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. Selection of sampling location is not in accordance with applicable methods. 3D traverses were conducted in accordance with a plan previously approved by Bill Maxwell to verify cyclonic conditions were not present in the sampling location utilized during testing.



### Monday, February 28, 2011 Page 6 of 57

### Northport Unit 2 ICR Test Program

Sampling / Stack Data Results Summary



### Location Duct near stack breaching - Method 0011 Average Run Number NPT2 R1N NPT2 R1S NPT2 R2N
Test Date 6/12/2010 6/12/2010 6/12/2010
Run Start Time 6/12/2010 7:10:00 AM 6/12/2010

7:10:00 AM 6/12/2010 10:45:00 AM

Run Finish Time 6/12/2010 9:22:00 AM 6/12/2010

9:22:00 AM 6/12/2010 1:00:00 PM

Net Run Time, minutes 120 120 120 Dry Gas Meter Volume Sampled, dscf 85.366 83.894 81.699 83.653 Moisture Content of Stack Gas, % 9.84 7.43 9.62 8.963 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 13 12.1 13 12.700 Oxygen, % 5.2 6.1 5.3 5.533 Average Stack Gas Temperature, °F 346.17 353.79 350.29 350.083 Dry Volumetric Flow Rate, dry scfm 331,648.4 336,275.6 328,593.9 332,172.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 538,079.4 536,405.4 535,401.0 536,628.600 Percent Isokinetic of Sampling Rate, % 98.2 109.4 3.3 70.300 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Monday, February 28, 2011 Page 7 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 0011 3 Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Location Duct near stack breaching - Method 10 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



### Monday, February 28, 2011 Page 8 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 10 3 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



### Location Duct near stack breaching - Method 23 Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Monday, February 28, 2011 Page 9 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 23 3 Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Location Duct near stack breaching - Method 25A 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



### Monday, February 28, 2011 Page 10 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 25A 3 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



### Location Duct near stack breaching - Method 26A Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Monday, February 28, 2011 Page 11 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 26A 3 Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Location Duct near stack breaching - Method 29 Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Monday, February 28, 2011 Page 12 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 29 3 Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Location Duct near stack breaching - 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



### Monday, February 28, 2011 Page 13 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 6C 3 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



### Location Duct near stack breaching - 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



### Monday, February 28, 2011 Page 14 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 7E 3 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



### Location Duct near stack breaching - OTM - 27/28 Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Monday, February 28, 2011 Page 15 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - OTM - 27/28 3 Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Monday, February 28, 2011 Page 16 of 57

### Northport Unit 2 ICR Test Program

Emissions Summary



### Location: Duct near stack breaching - Method 0011 Compound: Formaldehyde Average RunNumber NPT2 R2S NPT2 R1N NPT2 R1S Mass_mg 0.00638 0.0062 0.0064 0.006 lb/mmBtuO2 2.35E-06 1.96E-06 2.18E-06 0.000 ppm 2.34E-03 2.05E-03 2.16E-03 0.002 ppm@7%O2 2.18E-03 1.81E-03 2.03E-03 0.002



### Location: Duct near stack breaching - Method 0011 3 Compound: Formaldehyde Average RunNumber NPT2 R2N NPT2 R3N NPT2 R3S Mass_mg 0.00625 0.00613 0.00608 0.006 lb/mmBtuO2 2.08E-06 2.04E-06 2.15E-06 0.000 ppm 2.16E-03 2.11E-03 2.14E-03 0.002 ppm@7%O2 1.92E-03 1.89E-03 2.00E-03 0.002



### Location: Duct near stack breaching - Method 10 Compound: Carbon Monoxide Average Run NPT2 R1N NPT2 R1S NPT2 R2N Elb/hr 8.01E+00 1.39E+00 2.84E+01 12.600 lb/mmBtuO2 5.09E-03 9.61E-04 1.70E-02 0.008 mg/dscm 6.28E+00 1.16E+00 2.21E+01 9.847



### Location: Duct near stack breaching - Method 10 3 Compound: Carbon Monoxide Average Run NPT2 R2S NPT2 R3N NPT2 R3S Elb/hr 2.05E+00 1.78E+01 1.46E+00 7.103 lb/mmBtuO2 1.55E-03 1.07E-02 9.43E-04 0.004 mg/dscm 1.63E+00 1.41E+01 1.16E+00 5.630



### Location: Duct near stack breaching - Method 23 Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.000000002537 0.000000003305 0.000000003305 0.000 lb/mmBtuO2 2.21E-13 3.36E-13 2.80E-13 0.000 ng/dscm 2.73E-04 4.06E-04 3.64E-04 0.000 ng/dscm@7%O2 2.56E-04 3.89E-04 3.24E-04 0.000


### Compound: 1,2,3,7,8-PeCDD Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.00000000103 0.00000000135 0.00000000135 0.000 lb/mmBtuO2 8.97E-14 1.37E-13 1.14E-13 0.000 ng/dscm 1.11E-04 1.66E-04 1.49E-04 0.000



### Monday, February 28, 2011 Page 17 of 57

### Northport Unit 2 ICR Test Program

ng/dscm@7%O2 1.04E-04 1.59E-04 1.33E-04 0.000


### Compound: 1,2,3,7,8-PeCDF Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.000000000707 0.00000000107 0.00000000107 0.000 lb/mmBtuO2 6.16E-14 1.09E-13 9.06E-14 0.000 ng/dscm 7.60E-05 1.31E-04 1.18E-04 0.000 ng/dscm@7%O2 7.14E-05 1.26E-04 1.05E-04 0.000


### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000712 0.00000000712 0.0000000156 0.000 lb/mmBtuO2 7.23E-13 6.03E-13 1.49E-12 0.000 ng/dscm 8.74E-04 7.85E-04 1.81E-03 0.001 ng/dscm@7%O2 8.38E-04 6.99E-04 1.72E-03 0.001


### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.000000133 0.000000133 0.0000001645 0.000 lb/mmBtuO2 1.35E-11 1.13E-11 1.57E-11 0.000 ng/dscm 1.63E-02 1.47E-02 1.91E-02 0.017 ng/dscm@7%O2 1.56E-02 1.31E-02 1.82E-02 0.016


### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.000000511 0.000000511 0.000000522 0.000 lb/mmBtuO2 5.19E-11 4.33E-11 4.97E-11 0.000 ng/dscm 6.27E-02 5.63E-02 6.06E-02 0.060 ng/dscm@7%O2 6.01E-02 5.02E-02 5.77E-02 0.056


### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.0000000495 0.0000000495 0.0000000607 0.000 lb/mmBtuO2 5.03E-12 4.19E-12 5.78E-12 0.000 ng/dscm 6.08E-03 5.46E-03 7.04E-03 0.006 ng/dscm@7%O2 5.83E-03 4.87E-03 6.70E-03 0.006


### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.0000000375 0.0000000375 0.0000000359 0.000 lb/mmBtuO2 3.81E-12 3.18E-12 3.42E-12 0.000 ng/dscm 4.60E-03 4.13E-03 4.17E-03 0.004 ng/dscm@7%O2 4.41E-03 3.68E-03 3.97E-03 0.004


### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000161 0.00000161 0.00000149 0.000



### Monday, February 28, 2011 Page 18 of 57

### Northport Unit 2 ICR Test Program

lb/mmBtuO2 1.63E-10 1.36E-10 1.42E-10 0.000 ng/dscm 1.98E-01 1.77E-01 1.73E-01 0.183 ng/dscm@7%O2 1.90E-01 1.58E-01 1.65E-01 0.171


### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.0000000254 0.0000000254 0.0000000309 0.000 lb/mmBtuO2 2.58E-12 2.15E-12 2.94E-12 0.000 ng/dscm 3.12E-03 2.80E-03 3.59E-03 0.003 ng/dscm@7%O2 2.99E-03 2.49E-03 3.42E-03 0.003


### Compound: 2,3,4,7,8-PeCDF Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000103 0.00000000103 0.00000000283 0.000 lb/mmBtuO2 1.05E-13 8.72E-14 2.70E-13 0.000 ng/dscm 1.26E-04 1.14E-04 3.28E-04 0.000 ng/dscm@7%O2 1.21E-04 1.02E-04 3.12E-04 0.000


### Compound: 2,3,7,8-TCDD Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.000000000811 0.000000000811 0.00000000135 0.000 lb/mmBtuO2 8.23E-14 6.87E-14 1.29E-13 0.000 ng/dscm 9.96E-05 8.94E-05 1.57E-04 0.000 ng/dscm@7%O2 9.55E-05 7.97E-05 1.49E-04 0.000


### Compound: 2,3,7,8-TCDF Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.0000000015 0.0000000015 0.00000000281 0.000 lb/mmBtuO2 1.52E-13 1.27E-13 2.68E-13 0.000 ng/dscm 1.84E-04 1.65E-04 3.26E-04 0.000 ng/dscm@7%O2 1.76E-04 1.47E-04 3.10E-04 0.000


### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000188 0.00000000188 0.00000000552 0.000 lb/mmBtuO2 1.91E-13 1.59E-13 5.26E-13 0.000 ng/dscm 2.31E-04 2.07E-04 6.41E-04 0.000 ng/dscm@7%O2 2.21E-04 1.84E-04 6.10E-04 0.000


### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000296 0.00000000296 0.00000000848 0.000 lb/mmBtuO2 3.01E-13 2.51E-13 8.08E-13 0.000 ng/dscm 3.63E-04 3.26E-04 9.84E-04 0.001 ng/dscm@7%O2 3.48E-04 2.90E-04 9.37E-04 0.001


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



### Monday, February 28, 2011 Page 19 of 57

### Northport Unit 2 ICR Test Program

RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.0000000352 0.0000000352 0.0000000526 0.000 lb/mmBtuO2 3.57E-12 2.98E-12 5.01E-12 0.000 ng/dscm 4.32E-03 3.88E-03 6.10E-03 0.005 ng/dscm@7%O2 4.14E-03 3.46E-03 5.81E-03 0.004


### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.0000000034 0.0000000034 0.00000000379 0.000 lb/mmBtuO2 3.45E-13 2.88E-13 3.61E-13 0.000 ng/dscm 4.18E-04 3.75E-04 4.40E-04 0.000 ng/dscm@7%O2 4.01E-04 3.34E-04 4.19E-04 0.000


### Compound: OCDD Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.0000000727 0.0000000727 0.0000000511 0.000 lb/mmBtuO2 7.38E-12 6.16E-12 4.87E-12 0.000 ng/dscm 8.93E-03 8.01E-03 5.93E-03 0.008 ng/dscm@7%O2 8.56E-03 7.14E-03 5.65E-03 0.007


### Compound: OCDF Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.0000000136 0.0000000136 0.0000000115 0.000 lb/mmBtuO2 1.38E-12 1.15E-12 1.10E-12 0.000 ng/dscm 1.67E-03 1.50E-03 1.33E-03 0.002 ng/dscm@7%O2 1.60E-03 1.34E-03 1.27E-03 0.001


### Compound: Other HpCDD Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000642 0.00000000642 0.0000000058 0.000 lb/mmBtuO2 6.52E-13 5.44E-13 5.53E-13 0.000 ng/dscm 7.88E-04 7.08E-04 6.73E-04 0.001 ng/dscm@7%O2 7.55E-04 6.31E-04 6.41E-04 0.001


### Compound: Other HpCDF Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000567 0.00000000567 0.00000000438 0.000 lb/mmBtuO2 5.76E-13 4.80E-13 4.17E-13 0.000 ng/dscm 6.96E-04 6.25E-04 5.08E-04 0.001 ng/dscm@7%O2 6.67E-04 5.57E-04 4.84E-04 0.001


### Compound: Other HxCDD Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000



### Monday, February 28, 2011 Page 20 of 57

### Northport Unit 2 ICR Test Program

Compound: Other HxCDF Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000195 0.00000000195 0.00000000786 0.000 lb/mmBtuO2 1.98E-13 1.65E-13 7.49E-13 0.000 ng/dscm 2.39E-04 2.15E-04 9.12E-04 0.000 ng/dscm@7%O2 2.29E-04 1.92E-04 8.68E-04 0.000


### Compound: Other PeCDD Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000


### Compound: Other PeCDF Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000175 0.00000000175 0.0000000192 0.000 lb/mmBtuO2 1.78E-13 1.48E-13 1.83E-12 0.000 ng/dscm 2.15E-04 1.93E-04 2.23E-03 0.001 ng/dscm@7%O2 2.06E-04 1.72E-04 2.12E-03 0.001


### Compound: Other TCDD Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000809 0.00000000809 0.00000000935 0.000 lb/mmBtuO2 8.21E-13 6.85E-13 8.91E-13 0.000 ng/dscm 9.93E-04 8.92E-04 1.09E-03 0.001 ng/dscm@7%O2 9.52E-04 7.95E-04 1.04E-03 0.001


### Compound: Other TCDF Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 0.00000000381 0.00000000381 0.000000035 0.000 lb/mmBtuO2 3.87E-13 3.23E-13 3.34E-12 0.000 ng/dscm 4.68E-04 4.20E-04 4.06E-03 0.002 ng/dscm@7%O2 4.49E-04 3.74E-04 3.87E-03 0.002



### Location: Duct near stack breaching - Method 23 3 Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.00000000737 0.000000004103 0.0000000106 0.000 lb/mmBtuO2 7.02E-13 3.36E-13 1.03E-12 0.000 ng/dscm 8.55E-04 4.39E-04 1.27E-03 0.001 ng/dscm@7%O2 8.14E-04 3.89E-04 1.19E-03 0.001


### Compound: 1,2,3,7,8-PeCDD Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.00000000189 0.00000000171 0.00000000305 0.000


### Monday, February 28, 2011 Page 21 of 57

### Northport Unit 2 ICR Test Program

lb/mmBtuO2 1.80E-13 1.40E-13 2.97E-13 0.000 ng/dscm 2.19E-04 1.83E-04 3.67E-04 0.000 ng/dscm@7%O2 2.09E-04 1.62E-04 3.45E-04 0.000


### Compound: 1,2,3,7,8-PeCDF Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.00000000369 0.00000000136 0.0000000102 0.000 lb/mmBtuO2 3.52E-13 1.11E-13 9.93E-13 0.000 ng/dscm 4.28E-04 1.46E-04 1.23E-03 0.001 ng/dscm@7%O2 4.07E-04 1.29E-04 1.16E-03 0.001


### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000553 0.0000000163 0.00000000769 0.000 lb/mmBtuO2 4.52E-13 1.59E-12 6.70E-13 0.000 ng/dscm 5.92E-04 1.96E-03 8.27E-04 0.001 ng/dscm@7%O2 5.24E-04 1.84E-03 7.77E-04 0.001


### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.0000001338 0.000000214 0.0000001457 0.000 lb/mmBtuO2 1.09E-11 2.08E-11 1.27E-11 0.000 ng/dscm 1.43E-02 2.57E-02 1.57E-02 0.019 ng/dscm@7%O2 1.27E-02 2.41E-02 1.47E-02 0.017


### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000056 0.000000583 0.000000607 0.000 lb/mmBtuO2 4.58E-11 5.68E-11 5.29E-11 0.000 ng/dscm 6.00E-02 7.01E-02 6.53E-02 0.065 ng/dscm@7%O2 5.31E-02 6.58E-02 6.13E-02 0.060


### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.0000000508 0.0000000771 0.0000000554 0.000 lb/mmBtuO2 4.15E-12 7.51E-12 4.83E-12 0.000 ng/dscm 5.44E-03 9.27E-03 5.96E-03 0.007 ng/dscm@7%O2 4.82E-03 8.71E-03 5.60E-03 0.006


### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.0000000387 0.000000043 0.0000000439 0.000 lb/mmBtuO2 3.16E-12 4.19E-12 3.82E-12 0.000 ng/dscm 4.14E-03 5.17E-03 4.72E-03 0.005 ng/dscm@7%O2 3.67E-03 4.86E-03 4.43E-03 0.004


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



### Monday, February 28, 2011 Page 22 of 57

### Northport Unit 2 ICR Test Program

RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000172 0.00000165 0.00000186 0.000 lb/mmBtuO2 1.41E-10 1.61E-10 1.62E-10 0.000 ng/dscm 1.84E-01 1.98E-01 2.00E-01 0.194 ng/dscm@7%O2 1.63E-01 1.86E-01 1.88E-01 0.179


### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.0000000299 0.000000213 0.0000000418 0.000 lb/mmBtuO2 2.45E-12 2.07E-11 3.64E-12 0.000 ng/dscm 3.20E-03 2.56E-02 4.50E-03 0.011 ng/dscm@7%O2 2.83E-03 2.40E-02 4.23E-03 0.010


### Compound: 2,3,4,7,8-PeCDF Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000129 0.0000000533 0.000000000751 0.000 lb/mmBtuO2 1.05E-13 5.19E-12 6.54E-14 0.000 ng/dscm 1.38E-04 6.41E-03 8.08E-05 0.002 ng/dscm@7%O2 1.22E-04 6.02E-03 7.59E-05 0.002


### Compound: 2,3,7,8-TCDD Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000096 0.00000000143 0.000000000682 0.000 lb/mmBtuO2 7.85E-14 1.39E-13 5.94E-14 0.000 ng/dscm 1.03E-04 1.72E-04 7.33E-05 0.000 ng/dscm@7%O2 9.12E-05 1.62E-04 6.88E-05 0.000


### Compound: 2,3,7,8-TCDF Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000109 0.0000000126 0.000000000767 0.000 lb/mmBtuO2 8.91E-14 1.23E-12 6.68E-14 0.000 ng/dscm 1.17E-04 1.51E-03 8.25E-05 0.001 ng/dscm@7%O2 1.04E-04 1.42E-03 7.75E-05 0.001


### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000364 0.0000000255 0.00000000297 0.000 lb/mmBtuO2 2.98E-13 2.48E-12 2.59E-13 0.000 ng/dscm 3.90E-04 3.06E-03 3.19E-04 0.001 ng/dscm@7%O2 3.45E-04 2.87E-03 3.00E-04 0.001


### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000655 0.0000000581 0.00000000733 0.000 lb/mmBtuO2 5.36E-13 5.66E-12 6.39E-13 0.000 ng/dscm 7.01E-04 6.98E-03 7.88E-04 0.003 ng/dscm@7%O2 6.21E-04 6.56E-03 7.40E-04 0.003



### Monday, February 28, 2011 Page 23 of 57

### Northport Unit 2 ICR Test Program

Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.0000000683 0.0000000782 0.000000113 0.000 lb/mmBtuO2 5.59E-12 7.61E-12 9.84E-12 0.000 ng/dscm 7.31E-03 9.40E-03 1.22E-02 0.010 ng/dscm@7%O2 6.47E-03 8.83E-03 1.15E-02 0.009


### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000811 0.00000000628 0.00000000897 0.000 lb/mmBtuO2 6.63E-13 6.11E-13 7.81E-13 0.000 ng/dscm 8.69E-04 7.55E-04 9.65E-04 0.001 ng/dscm@7%O2 7.69E-04 7.09E-04 9.06E-04 0.001


### Compound: OCDD Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.0000000308 0.0000000284 0.0000000293 0.000 lb/mmBtuO2 2.52E-12 2.76E-12 2.55E-12 0.000 ng/dscm 3.30E-03 3.41E-03 3.15E-03 0.003 ng/dscm@7%O2 2.92E-03 3.20E-03 2.96E-03 0.003


### Compound: OCDF Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000697 0.00000000653 0.0000000067 0.000 lb/mmBtuO2 5.70E-13 6.36E-13 5.84E-13 0.000 ng/dscm 7.46E-04 7.85E-04 7.21E-04 0.001 ng/dscm@7%O2 6.60E-04 7.37E-04 6.77E-04 0.001


### Compound: Other HpCDD Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000335 0.00000000434 0.00000000327 0.000 lb/mmBtuO2 2.74E-13 4.23E-13 2.85E-13 0.000 ng/dscm 3.59E-04 5.22E-04 3.52E-04 0.000 ng/dscm@7%O2 3.18E-04 4.90E-04 3.31E-04 0.000


### Compound: Other HpCDF Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0 0.00000000215 0.00000000225 0.000 lb/mmBtuO2 0.00E+00 2.09E-13 1.96E-13 0.000 ng/dscm 0.00E+00 2.58E-04 2.42E-04 0.000 ng/dscm@7%O2 0.00E+00 2.42E-04 2.27E-04 0.000


### Compound: Other HxCDD Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0 0 0.00000000103 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 8.97E-14 0.000



### Monday, February 28, 2011 Page 24 of 57

### Northport Unit 2 ICR Test Program

ng/dscm 0.00E+00 0.00E+00 1.11E-04 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 1.04E-04 0.000


### Compound: Other HxCDF Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.0000000017 0.0000000112 0.00000000284 0.000 lb/mmBtuO2 1.39E-13 1.09E-12 2.47E-13 0.000 ng/dscm 1.82E-04 1.35E-03 3.05E-04 0.001 ng/dscm@7%O2 1.61E-04 1.27E-03 2.86E-04 0.001


### Compound: Other PeCDD Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000


### Compound: Other PeCDF Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0 0.0000000722 0.00000000546 0.000 lb/mmBtuO2 0.00E+00 7.03E-12 4.76E-13 0.000 ng/dscm 0.00E+00 8.68E-03 5.87E-04 0.003 ng/dscm@7%O2 0.00E+00 8.15E-03 5.51E-04 0.003


### Compound: Other TCDD Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000767 0.0000000136 0.00000000634 0.000 lb/mmBtuO2 6.27E-13 1.32E-12 5.52E-13 0.000 ng/dscm 8.21E-04 1.63E-03 6.82E-04 0.001 ng/dscm@7%O2 7.27E-04 1.53E-03 6.41E-04 0.001


### Compound: Other TCDF Average RunNumber NPT2 R3N NPT2 R3S NPT2 R1N Mass_mg 0.00000000116 0.000000266 0.0000000105 0.000 lb/mmBtuO2 9.49E-14 2.59E-11 9.15E-13 0.000 ng/dscm 1.24E-04 3.20E-02 1.13E-03 0.011 ng/dscm@7%O2 1.10E-04 3.01E-02 1.06E-03 0.010



### Location: Duct near stack breaching - Method 25A Compound: Total organic compounds (TOC) as Average Run NPT2 R1N NPT2 R1S NPT2 R2N Elb/hr 2.29E-01 2.31E-01 2.26E-01 0.229 gr/dscf 8.06E-05 8.06E-05 8.01E-05 0.000 lb/mmBtuO2 1.41E-04 1.49E-04 1.41E-04 0.000 mg/dscm 1.84E-01 1.84E-01 1.83E-01 0.184 ppm 1.01E-01 1.01E-01 1.00E-01 0.101 ppm@7%O2 8.94E-02 9.49E-02 8.91E-02 0.091



### Monday, February 28, 2011 Page 25 of 57

### Northport Unit 2 ICR Test Program

Location: Duct near stack breaching - Method 25A 3 

### Compound: Total organic compounds (TOC) as Average Run NPT2 R2S NPT2 R3N NPT2 R3S Elb/hr 2.24E-01 6.76E-01 1.30E+00 0.733 gr/dscf 8.01E-05 2.40E-04 4.81E-04 0.000 lb/mmBtuO2 1.48E-04 4.25E-04 8.85E-04 0.000 mg/dscm 1.83E-01 5.50E-01 1.10E+00 0.611 ppm 1.00E-01 3.00E-01 6.00E-01 0.333 ppm@7%O2 9.33E-02 2.69E-01 5.60E-01 0.307



### Location: Duct near stack breaching - Method 26A Compound: Hydrogen Chloride Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.59 0.73 0.7 0.673 Elb/hr 2.13E-01 2.85E-01 2.51E-01 0.250 lb/mmBtuO2 1.32E-04 1.84E-04 1.69E-04 0.000 mg/dscm 1.69E-01 2.25E-01 2.02E-01 0.199 mg/dscm@7%O2 1.54E-01 2.13E-01 1.96E-01 0.188


### Compound: Hydrogen Fluoride Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 1.24 2.73 0.82 1.597 Elb/hr 4.47E-01 1.07E+00 2.94E-01 0.604 lb/mmBtuO2 2.78E-04 6.88E-04 1.98E-04 0.000 mg/dscm 3.55E-01 8.43E-01 2.36E-01 0.478 mg/dscm@7%O2 3.23E-01 7.97E-01 2.29E-01 0.450



### Location: Duct near stack breaching - Method 26A 3 Compound: Hydrogen Chloride Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 1.03 0.7 0.97 0.900 Elb/hr 3.81E-01 2.55E-01 3.55E-01 0.330 lb/mmBtuO2 2.48E-04 1.66E-04 2.30E-04 0.000 mg/dscm 2.97E-01 2.04E-01 2.78E-01 0.260 mg/dscm@7%O2 2.87E-01 1.93E-01 2.66E-01 0.249


### Compound: Hydrogen Fluoride Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.69 0.87 0.6 0.720 Elb/hr 2.55E-01 3.17E-01 2.19E-01 0.264 lb/mmBtuO2 1.66E-04 2.07E-04 1.42E-04 0.000 mg/dscm 1.99E-01 2.53E-01 1.72E-01 0.208 mg/dscm@7%O2 1.92E-01 2.39E-01 1.65E-01 0.199



### Location: Duct near stack breaching - Method 29



### Monday, February 28, 2011 Page 26 of 57

### Northport Unit 2 ICR Test Program

Compound: Antimony Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.103755 0.112116 0.28819 0.168 Elb/hr 1.81E-02 2.19E-02 5.23E-02 0.031 lb/mmBtuO2 1.10E-05 1.42E-05 3.21E-05 0.000 mg/dscm 1.45E-02 1.75E-02 4.21E-02 0.025 mg/dscm@7%O2 1.28E-02 1.64E-02 3.73E-02 0.022


### Compound: Arsenic Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.00684 0.0053 0.0098 0.007 Elb/hr 1.19E-03 1.03E-03 1.78E-03 0.001 lb/mmBtuO2 7.28E-07 6.71E-07 1.09E-06 0.000 mg/dscm 9.53E-04 8.28E-04 1.43E-03 0.001 mg/dscm@7%O2 8.44E-04 7.78E-04 1.27E-03 0.001


### Compound: Beryllium Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.000459 0.000297 0.000714 0.000 Elb/hr 8.00E-05 5.80E-05 1.30E-04 0.000 lb/mmBtuO2 4.88E-08 3.76E-08 7.96E-08 0.000 mg/dscm 6.40E-05 4.64E-05 1.04E-04 0.000 mg/dscm@7%O2 5.67E-05 4.36E-05 9.21E-05 0.000


### Compound: Cadmium Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.000859 0.000414 0.000692 0.001 Elb/hr 1.50E-04 8.08E-05 1.26E-04 0.000 lb/mmBtuO2 9.14E-08 5.24E-08 7.71E-08 0.000 mg/dscm 1.20E-04 6.47E-05 1.01E-04 0.000 mg/dscm@7%O2 1.06E-04 6.08E-05 8.94E-05 0.000


### Compound: Chromium Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.01128 0.007096 0.011099 0.010 Elb/hr 1.97E-03 1.38E-03 2.02E-03 0.002 lb/mmBtuO2 1.20E-06 8.98E-07 1.24E-06 0.000 mg/dscm 1.57E-03 1.11E-03 1.62E-03 0.001 mg/dscm@7%O2 1.39E-03 1.04E-03 1.43E-03 0.001


### Compound: Filterable Particulate Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 253.2 156.6 276.2 228.667 Elb/hr 4.41E+01 3.06E+01 5.02E+01 41.633 lb/mmBtuO2 2.69E-02 1.98E-02 3.08E-02 0.026 mg/dscm 3.53E+01 2.45E+01 4.03E+01 33.367 mg/dscm@7%O2 3.13E+01 2.30E+01 3.57E+01 30.000



### Monday, February 28, 2011 Page 27 of 57

### Northport Unit 2 ICR Test Program

Compound: Lead Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.0116 0.007869 0.014992 0.011 Elb/hr 2.02E-03 1.54E-03 2.72E-03 0.002 lb/mmBtuO2 1.23E-06 9.96E-07 1.67E-06 0.000 mg/dscm 1.62E-03 1.23E-03 2.19E-03 0.002 mg/dscm@7%O2 1.43E-03 1.16E-03 1.94E-03 0.002


### Compound: Manganese Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 1.09183 0.87705 1.67833 1.216 Elb/hr 1.90E-01 1.71E-01 3.05E-01 0.222 lb/mmBtuO2 1.16E-04 1.11E-04 1.87E-04 0.000 mg/dscm 1.52E-01 1.37E-01 2.45E-01 0.178 mg/dscm@7%O2 1.35E-01 1.29E-01 2.17E-01 0.160


### Compound: Nickel Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 1.2047 0.83617 1.8112 1.284 Elb/hr 2.10E-01 1.63E-01 3.29E-01 0.234 lb/mmBtuO2 1.28E-04 1.06E-04 2.02E-04 0.000 mg/dscm 1.68E-01 1.31E-01 2.64E-01 0.188 mg/dscm@7%O2 1.49E-01 1.23E-01 2.34E-01 0.169


### Compound: Selenium Average RunNumber NPT2 R1N NPT2 R1S NPT2 R2N Mass_mg 0.00805 0.00742 0.00776 0.008 Elb/hr 1.40E-03 1.45E-03 1.41E-03 0.001 lb/mmBtuO2 8.57E-07 9.39E-07 8.65E-07 0.000 mg/dscm 1.12E-03 1.16E-03 1.13E-03 0.001 mg/dscm@7%O2 9.92E-04 1.09E-03 1.00E-03 0.001



### Location: Duct near stack breaching - Method 29 3 Compound: Antimony Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.137203 0.148469 0.128127 0.138 Elb/hr 2.64E-02 2.68E-02 2.48E-02 0.026 lb/mmBtuO2 1.77E-05 1.52E-05 1.53E-05 0.000 mg/dscm 2.19E-02 2.11E-02 2.02E-02 0.021 mg/dscm@7%O2 2.06E-02 1.76E-02 1.78E-02 0.019


### Compound: Arsenic Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.00551 0.00696 0.00451 0.006 Elb/hr 1.06E-03 1.25E-03 8.72E-04 0.001 lb/mmBtuO2 7.13E-07 7.11E-07 5.39E-07 0.000 mg/dscm 8.80E-04 9.90E-04 7.10E-04 0.001



### Monday, February 28, 2011 Page 28 of 57

### Northport Unit 2 ICR Test Program

mg/dscm@7%O2 8.26E-04 8.24E-04 6.25E-04 0.001


### Compound: Beryllium Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.000351 0.000524 0.000353 0.000 Elb/hr 6.76E-05 9.44E-05 6.83E-05 0.000 lb/mmBtuO2 4.54E-08 5.35E-08 4.22E-08 0.000 mg/dscm 5.60E-05 7.45E-05 5.56E-05 0.000 mg/dscm@7%O2 5.26E-05 6.20E-05 4.89E-05 0.000


### Compound: Cadmium Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.000371 0.000671 0.000329 0.000 Elb/hr 7.15E-05 1.21E-04 6.36E-05 0.000 lb/mmBtuO2 4.80E-08 6.85E-08 3.93E-08 0.000 mg/dscm 5.92E-05 9.54E-05 5.18E-05 0.000 mg/dscm@7%O2 5.56E-05 7.94E-05 4.56E-05 0.000


### Compound: Chromium Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.007807 0.001541 0.007174 0.006 Elb/hr 1.50E-03 2.78E-04 1.39E-03 0.001 lb/mmBtuO2 1.01E-06 1.57E-07 8.57E-07 0.000 mg/dscm 1.25E-03 2.19E-04 1.13E-03 0.001 mg/dscm@7%O2 1.17E-03 1.82E-04 9.94E-04 0.001


### Compound: Filterable Particulate Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 191.1 262.7 238.2 230.667 Elb/hr 3.68E+01 4.73E+01 4.61E+01 43.400 lb/mmBtuO2 2.47E-02 2.68E-02 2.84E-02 0.027 mg/dscm 3.05E+01 3.74E+01 3.75E+01 35.133 mg/dscm@7%O2 2.86E+01 3.11E+01 3.30E+01 30.900


### Compound: Lead Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.008949 0.01327 0.006609 0.010 Elb/hr 1.72E-03 2.39E-03 1.28E-03 0.002 lb/mmBtuO2 1.16E-06 1.36E-06 7.89E-07 0.000 mg/dscm 1.43E-03 1.89E-03 1.04E-03 0.001 mg/dscm@7%O2 1.34E-03 1.57E-03 9.15E-04 0.001


### Compound: Manganese Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 1.04843 1.387952 0.899883 1.112 Elb/hr 2.02E-01 2.50E-01 1.74E-01 0.209 lb/mmBtuO2 1.36E-04 1.42E-04 1.07E-04 0.000 mg/dscm 1.67E-01 1.97E-01 1.42E-01 0.169



### Monday, February 28, 2011 Page 29 of 57

### Northport Unit 2 ICR Test Program

mg/dscm@7%O2 1.57E-01 1.64E-01 1.25E-01 0.149


### Compound: Nickel Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 1.05608 1.53845 0.93699 1.177 Elb/hr 2.03E-01 2.77E-01 1.81E-01 0.220 lb/mmBtuO2 1.37E-04 1.57E-04 1.12E-04 0.000 mg/dscm 1.69E-01 2.19E-01 1.47E-01 0.178 mg/dscm@7%O2 1.59E-01 1.82E-01 1.29E-01 0.157


### Compound: Selenium Average RunNumber NPT2 R2S NPT2 R3N NPT2 R3S Mass_mg 0.00816 0.00725 0.00586 0.007 Elb/hr 1.57E-03 1.31E-03 1.13E-03 0.001 lb/mmBtuO2 1.06E-06 7.40E-07 7.00E-07 0.000 mg/dscm 1.30E-03 1.03E-03 9.22E-04 0.001 mg/dscm@7%O2 1.22E-03 8.57E-04 8.11E-04 0.001



### Location: Duct near stack breaching - Method 6C Compound: Sulfur Dioxide Average Run NPT2 R1N NPT2 R1S NPT2 R2N Elb/hr 1.02E+03 9.77E+02 1.01E+03 1,002.333 lb/mmBtuO2 6.35E-01 6.31E-01 6.78E-01 0.648 mg/dscm 8.10E+02 7.74E+02 8.09E+02 797.667 mg/dscm@7%O2 7.36E+02 7.32E+02 7.86E+02 751.333 ppm 3.04E+02 2.90E+02 3.04E+02 299.333 ppm@7%O2 2.76E+02 2.74E+02 2.95E+02 281.667



### Location: Duct near stack breaching - Method 6C 3 Compound: Sulfur Dioxide Average Run NPT2 R2S NPT2 R3N NPT2 R3S Elb/hr 9.84E+02 1.04E+03 9.84E+02 1,002.667 lb/mmBtuO2 6.40E-01 6.77E-01 6.39E-01 0.652 mg/dscm 7.69E+02 8.31E+02 7.73E+02 791.000 mg/dscm@7%O2 7.42E+02 7.86E+02 7.41E+02 756.333 ppm 2.89E+02 3.12E+02 2.90E+02 297.000 ppm@7%O2 2.79E+02 2.95E+02 2.78E+02 284.000



### Location: Duct near stack breaching - Method 7E Compound: Nitrogen oxides (NOx) Average Run NPT2 R1N NPT2 R1S NPT2 R2N Elb/hr 3.10E+02 3.02E+02 3.32E+02 314.667 lb/mmBtuO2 1.93E-01 1.95E-01 2.23E-01 0.204 mg/dscm 2.47E+02 2.39E+02 2.66E+02 250.667 mg/dscm@7%O2 2.24E+02 2.26E+02 2.59E+02 236.333 ppm 1.29E+02 1.25E+02 1.39E+02 131.000 ppm@7%O2 1.17E+02 1.18E+02 1.35E+02 123.333



### Monday, February 28, 2011 Page 30 of 57

### Northport Unit 2 ICR Test Program

Location: Duct near stack breaching - Method 7E 3 

### Compound: Nitrogen oxides (NOx) Average Run NPT2 R2S NPT2 R3N NPT2 R3S Elb/hr 3.15E+02 3.24E+02 3.10E+02 316.333 lb/mmBtuO2 2.05E-01 2.11E-01 1.95E-01 0.204 mg/dscm 2.46E+02 2.59E+02 2.36E+02 247.000 mg/dscm@7%O2 2.37E+02 2.45E+02 2.26E+02 236.000 ppm 1.29E+02 1.35E+02 1.24E+02 129.333 ppm@7%O2 1.25E+02 1.28E+02 1.19E+02 124.000



### Location: Duct near stack breaching - OTM - 27/28 Compound: Filterable PM2.5 Average RunNumber NPT2 R1N NPT2 R1S NPT2 R3S Mass_mg 11.6 5.9 6 7.833 lb/mmBtuO2 2.19E-03 1.27E-03 1.15E-03 0.002


### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber NPT2 R1N NPT2 R1S NPT2 R3S Mass_mg 39.4 361.3 29.7 143.467 lb/mmBtuO2 7.44E-03 7.79E-02 5.71E-03 0.030


### Compound: Organic Condensible Particulate Average RunNumber NPT2 R1N NPT2 R3S NPT2 R3N Mass_mg 11.6 2.2 56.7 23.500 lb/mmBtuO2 2.19E-03 4.23E-04 9.73E-03 0.004


### Compound: Total PM2.5 Average RunNumber NPT2 R1N NPT2 R3S NPT2 R3N Mass_mg 62.6 37.9 93.5 64.667 lb/mmBtuO2 1.18E-02 7.29E-03 1.60E-02 0.012



### Location: Duct near stack breaching - OTM - 27/28 3 Compound: Filterable PM2.5 Average RunNumber NPT2 R3N NPT2 R2N NPT2 R2S Mass_mg 10.9 18.2 6.4 11.833 lb/mmBtuO2 1.87E-03 3.33E-03 1.30E-03 0.002


### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber NPT2 R3N NPT2 R2N NPT2 R2S Mass_mg 25.9 7.6 4.2 12.567 lb/mmBtuO2 4.44E-03 1.39E-03 8.52E-04 0.002


### Compound: Organic Condensible Particulate Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S


### Monday, February 28, 2011 Page 31 of 57

### Northport Unit 2 ICR Test Program

Process Run Data Mass_mg 10.1 29.3 101.1 46.833 lb/mmBtuO2 2.18E-03 5.36E-03 2.05E-02 0.009


### Compound: Total PM2.5 Average RunNumber NPT2 R1S NPT2 R2N NPT2 R2S Mass_mg 377.3 55.1 111.7 181.367 lb/mmBtuO2 8.14E-02 1.01E-02 2.27E-02 0.038



### Monday, February 28, 2011 Page 32 of 57

### Northport Unit 2 ICR Test Program

Process Run Data



### Run Name Value UOM Comments Target Value 1 Heat Input 0 Million Btus 0


### 10 Heat Input 0 Million Btus 0
11 Heat Input 0 Million Btus 0
12 Heat Input 0 Million Btus 0


### 2 Heat Input 0 Million Btus 0
3 Heat Input 0 Million Btus 0
4 Heat Input 0 Million Btus 0


### 5 Heat Input 0 Million Btus 0
6 Heat Input 0 Million Btus 0
7 Heat Input 0 Million Btus 0


### 8 Heat Input 0 Million Btus 0
9 Heat Input 0 Million Btus 0
1 Average Heat Input 0 MMBtu/hr 0


### 10 Average Heat Input 0 MMBtu/hr 0
11 Average Heat Input 0 MMBtu/hr 0
12 Average Heat Input 0 MMBtu/hr 0


### 2 Average Heat Input 0 MMBtu/hr 0
3 Average Heat Input 0 MMBtu/hr 0
4 Average Heat Input 0 MMBtu/hr 0


### 5 Average Heat Input 0 MMBtu/hr 0
6 Average Heat Input 0 MMBtu/hr 0
7 Average Heat Input 0 MMBtu/hr 0


### 8 Average Heat Input 0 MMBtu/hr 0
9 Average Heat Input 0 MMBtu/hr 0


### 1 Steam Output 0 1000 lb steam/hr 0
10 Steam Output 0 1000 lb steam/hr 0
11 Steam Output 0 1000 lb steam/hr 0


### 12 Steam Output 0 1000 lb steam/hr 0
2 Steam Output 0 1000 lb steam/hr 0
3 Steam Output 0 1000 lb steam/hr 0


### 4 Steam Output 0 1000 lb steam/hr 0
5 Steam Output 0 1000 lb steam/hr 0
6 Steam Output 0 1000 lb steam/hr 0



### Monday, February 28, 2011 Page 33 of 57

### Northport Unit 2 ICR Test Program

7 Steam Output 0 1000 lb steam/hr 0


### 8 Steam Output 0 1000 lb steam/hr 0
9 Steam Output 0 1000 lb steam/hr 0
1 Synfuel Firing Rate 0 0


### 10 Synfuel Firing Rate 0 0
11 Synfuel Firing Rate 0 0
12 Synfuel Firing Rate 0 0


### 2 Synfuel Firing Rate 0 0
3 Synfuel Firing Rate 0 0
4 Synfuel Firing Rate 0 0


### 5 Synfuel Firing Rate 0 0
6 Synfuel Firing Rate 0 0
7 Synfuel Firing Rate 0 0


### 8 Synfuel Firing Rate 0 0
9 Synfuel Firing Rate 0 0
1 Petroleum Coke Firing Rate 0 0


### 10 Petroleum Coke Firing Rate 0 0
11 Petroleum Coke Firing Rate 0 0
12 Petroleum Coke Firing Rate 0 0


### 2 Petroleum Coke Firing Rate 0 0
3 Petroleum Coke Firing Rate 0 0


### 4 Petroleum Coke Firing Rate 0 0
5 Petroleum Coke Firing Rate 0 0
6 Petroleum Coke Firing Rate 0 0


### 7 Petroleum Coke Firing Rate 0 0
8 Petroleum Coke Firing Rate 0 0
9 Petroleum Coke Firing Rate 0 0


### 1 Coal Gas Firing Rate 0 0
10 Coal Gas Firing Rate 0 0
11 Coal Gas Firing Rate 0 0


### 12 Coal Gas Firing Rate 0 0
2 Coal Gas Firing Rate 0 0
3 Coal Gas Firing Rate 0 0


### 4 Coal Gas Firing Rate 0 0
5 Coal Gas Firing Rate 0 0
6 Coal Gas Firing Rate 0 0



### Monday, February 28, 2011 Page 34 of 57

### Northport Unit 2 ICR Test Program

7 Coal Gas Firing Rate 0 0


### 8 Coal Gas Firing Rate 0 0
9 Coal Gas Firing Rate 0 0
1 Fuel Oil Firing Rate 0 gpm 0


### 10 Fuel Oil Firing Rate 0 gpm 0
11 Fuel Oil Firing Rate 0 gpm 0
12 Fuel Oil Firing Rate 0 gpm 0


### 2 Fuel Oil Firing Rate 0 gpm 0
3 Fuel Oil Firing Rate 0 gpm 0
4 Fuel Oil Firing Rate 0 gpm 0


### 5 Fuel Oil Firing Rate 0 gpm 0
6 Fuel Oil Firing Rate 0 gpm 0
7 Fuel Oil Firing Rate 0 gpm 0


### 8 Fuel Oil Firing Rate 0 gpm 0
9 Fuel Oil Firing Rate 0 gpm 0
1 Flue Gas Flow Rate 0 dscfm 0


### 10 Flue Gas Flow Rate 0 dscfm 0
11 Flue Gas Flow Rate 0 dscfm 0
12 Flue Gas Flow Rate 0 dscfm 0


### 4 Flue Gas Flow Rate 0 dscfm 0
5 Flue Gas Flow Rate 0 dscfm 0


### 6 Flue Gas Flow Rate 0 dscfm 0
7 Flue Gas Flow Rate 0 dscfm 0
8 Flue Gas Flow Rate 0 dscfm 0


### 9 Flue Gas Flow Rate 0 dscfm 0
1 Pressure Drop Across FGD (if applicable) 0 in H20 0
10 Pressure Drop Across FGD (if applicable) 0 in H20 0


### 11 Pressure Drop Across FGD (if applicable) 0 in H20 0
12 Pressure Drop Across FGD (if applicable) 0 in H20 0
4 Pressure Drop Across FGD (if applicable) 0 in H20 0


### 5 Pressure Drop Across FGD (if applicable) 0 in H20 0
6 Pressure Drop Across FGD (if applicable) 0 in H20 0
7 Pressure Drop Across FGD (if applicable) 0 in H20 0


### 8 Pressure Drop Across FGD (if applicable) 0 in H20 0
9 Pressure Drop Across FGD (if applicable) 0 in H20 0
1 FGD Scrubber Liquor pH 0 pH 0



### Monday, February 28, 2011 Page 35 of 57

### Northport Unit 2 ICR Test Program

10 FGD Scrubber Liquor pH 0 pH 0


### 11 FGD Scrubber Liquor pH 0 pH 0
12 FGD Scrubber Liquor pH 0 pH 0
4 FGD Scrubber Liquor pH 0 pH 0


### 5 FGD Scrubber Liquor pH 0 pH 0
6 FGD Scrubber Liquor pH 0 pH 0
7 FGD Scrubber Liquor pH 0 pH 0


### 8 FGD Scrubber Liquor pH 0 pH 0
9 FGD Scrubber Liquor pH 0 pH 0
1 FGD Scrubber Liquor Flow Rate 0 gal/min 0


### 10 FGD Scrubber Liquor Flow Rate 0 gal/min 0
11 FGD Scrubber Liquor Flow Rate 0 gal/min 0
12 FGD Scrubber Liquor Flow Rate 0 gal/min 0


### 4 FGD Scrubber Liquor Flow Rate 0 gal/min 0
5 FGD Scrubber Liquor Flow Rate 0 gal/min 0
6 FGD Scrubber Liquor Flow Rate 0 gal/min 0


### 7 FGD Scrubber Liquor Flow Rate 0 gal/min 0
8 FGD Scrubber Liquor Flow Rate 0 gal/min 0
9 FGD Scrubber Liquor Flow Rate 0 gal/min 0


### 1 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

10 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 11 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

12 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

4 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 5 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

6 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 7 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

8 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 9 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

1 Flue Gas Oxygen Content 0 % 0



### Monday, February 28, 2011 Page 36 of 57

### Northport Unit 2 ICR Test Program

10 Flue Gas Oxygen Content 0 % 0


### 11 Flue Gas Oxygen Content 0 % 0
12 Flue Gas Oxygen Content 0 % 0
4 Flue Gas Oxygen Content 0 % 0


### 5 Flue Gas Oxygen Content 0 % 0
6 Flue Gas Oxygen Content 0 % 0
7 Flue Gas Oxygen Content 0 % 0


### 8 Flue Gas Oxygen Content 0 % 0
9 Flue Gas Oxygen Content 0 % 0
1 Flue Gas Carbon Dioxide Content 0 % 0


### 10 Flue Gas Carbon Dioxide Content 0 % 0
11 Flue Gas Carbon Dioxide Content 0 % 0
12 Flue Gas Carbon Dioxide Content 0 % 0


### 4 Flue Gas Carbon Dioxide Content 0 % 0
5 Flue Gas Carbon Dioxide Content 0 % 0
6 Flue Gas Carbon Dioxide Content 0 % 0


### 7 Flue Gas Carbon Dioxide Content 0 % 0
8 Flue Gas Carbon Dioxide Content 0 % 0
9 Flue Gas Carbon Dioxide Content 0 % 0


### 1 Flue Gas Moisture Content 0 % 0
10 Flue Gas Moisture Content 0 % 0


### 11 Flue Gas Moisture Content 0 % 0
12 Flue Gas Moisture Content 0 % 0
4 Flue Gas Moisture Content 0 % 0


### 5 Flue Gas Moisture Content 0 % 0
6 Flue Gas Moisture Content 0 % 0
7 Flue Gas Moisture Content 0 % 0


### 8 Flue Gas Moisture Content 0 % 0
9 Flue Gas Moisture Content 0 % 0
1 Flue Gas Sampling Point Temperature 0 Deg F 0


### 10 Flue Gas Sampling Point Temperature 0 Deg F 0
11 Flue Gas Sampling Point Temperature 0 Deg F 0
12 Flue Gas Sampling Point Temperature 0 Deg F 0


### 4 Flue Gas Sampling Point Temperature 0 Deg F 0
5 Flue Gas Sampling Point Temperature 0 Deg F 0
6 Flue Gas Sampling Point Temperature 0 Deg F 0



### Monday, February 28, 2011 Page 37 of 57

### Northport Unit 2 ICR Test Program

7 Flue Gas Sampling Point Temperature 0 Deg F 0


### 8 Flue Gas Sampling Point Temperature 0 Deg F 0
9 Flue Gas Sampling Point Temperature 0 Deg F 0
1 Flue Gas Pressure 0 atm 0


### 10 Flue Gas Pressure 0 atm 0
11 Flue Gas Pressure 0 atm 0
12 Flue Gas Pressure 0 atm 0


### 4 Flue Gas Pressure 0 atm 0
5 Flue Gas Pressure 0 atm 0
6 Flue Gas Pressure 0 atm 0


### 7 Flue Gas Pressure 0 atm 0
8 Flue Gas Pressure 0 atm 0
9 Flue Gas Pressure 0 atm 0


### 1 Standard Pressure 0 atm 0
10 Standard Pressure 0 atm 0
11 Standard Pressure 0 atm 0


### 12 Standard Pressure 0 atm 0
4 Standard Pressure 0 atm 0
5 Standard Pressure 0 atm 0


### 6 Standard Pressure 0 atm 0
7 Standard Pressure 0 atm 0


### 8 Standard Pressure 0 atm 0
9 Standard Pressure 0 atm 0
1 Standard Temperature 0 Deg F 0


### 10 Standard Temperature 0 Deg F 0
11 Standard Temperature 0 Deg F 0
12 Standard Temperature 0 Deg F 0


### 4 Standard Temperature 0 Deg F 0
5 Standard Temperature 0 Deg F 0
6 Standard Temperature 0 Deg F 0


### 7 Standard Temperature 0 Deg F 0
8 Standard Temperature 0 Deg F 0
9 Standard Temperature 0 Deg F 0


### 1 Unit Gross Electrical Output 0 MW 0
10 Unit Gross Electrical Output 0 MW 0
11 Unit Gross Electrical Output 0 MW 0



### Monday, February 28, 2011 Page 38 of 57

### Northport Unit 2 ICR Test Program

APCD Run Data

Process Lab Run Data 12 Unit Gross Electrical Output 0 MW 0


### 4 Unit Gross Electrical Output 0 MW 0
5 Unit Gross Electrical Output 0 MW 0
6 Unit Gross Electrical Output 0 MW 0


### 7 Unit Gross Electrical Output 0 MW 0
8 Unit Gross Electrical Output 0 MW 0
9 Unit Gross Electrical Output 0 MW 0


### 1 Unit Net Electric Generation 0 MWh 0
10 Unit Net Electric Generation 0 MWh 0
11 Unit Net Electric Generation 0 MWh 0


### 12 Unit Net Electric Generation 0 MWh 0
4 Unit Net Electric Generation 0 MWh 0
5 Unit Net Electric Generation 0 MWh 0


### 6 Unit Net Electric Generation 0 MWh 0
7 Unit Net Electric Generation 0 MWh 0
8 Unit Net Electric Generation 0 MWh 0


### 9 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments Target Value 1 ELECTROSTATIC PRECIPITATOR 0 0


### 1 0 0
1 0 0



### Run Name Value UOM Comments 1 See 4b Comments. 0



### Monday, February 28, 2011 Page 39 of 57

### Northport Unit 2 ICR Test Program

Sampling / Stack Data Results Detail



### Location Duct near stack breaching - Method 0011 Average Run Number NPT2 R1N NPT2 R1S NPT2 R2N Test Date 6/12/2010 6/12/2010 6/12/2010 Run Start Time 6/12/2010 7:10:00 AM 6/12/2010

7:10:00 AM 6/12/2010

10:45:00 AM Run Finish Time 6/12/2010 9:22:00 AM 6/12/2010

9:22:00 AM 6/12/2010

1:00:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 120 120 120 Nozzle Diameter, inches 0.193 0.18 1.03 0.468 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.03 1.01 1.03 1.023 Barometric Pressure, inches of Mercury 30.13 30.13 30.08 30.113 Average Orifice Meter Differential, inches H2O 1.54 1.32 1.52 1.460 Dry Gas Meter Volume Sampled, cubic feet 83.792 83.792 81.342 82.975 Average Dry Gas Meter Temperature, °F 79.58 78.10 86.38 81.353 Dry Gas Meter Volume Sampled, dscf 85.366 83.894 81.699 83.653 Total Moisture Liquid collected, g 198 143 184.8 175.267 Volume of Water Vapor, standard cubic feet 9.32 6.73 8.70 8.250 Moisture Content of Stack Gas, % 9.84 7.43 9.62 8.963 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9016 0.9257 0.9038 0.910 Carbon Dioxide, % 13 12.1 13 12.700 Oxygen, % 5.2 6.1 5.3 5.533 Carbon Monoxide & Nitrogen, % 81.8 81.8 81.7 81.767 Fuel Factor 1.21 1.22 1.20 Dry Molecular Weight, lb/lb-Mole 30.29 30.18 30.29 30.253 Wet Molecular weight, lb/lb-Mole 29.08 29.28 29.11 29.157 Flue Gas Static Pressure, inches of H2O 15 15 15 15.000 Absolute Flue Gas Pressure, inches of Mercury 31.23 31.23 31.18 31.213 Average Stack Gas Temperature, °F 346.17 353.79 350.29 350.083 Average Velocity Head, inches of H2O 2.0314059127 9512 2.013412070

48913 1.999598036

83317 2.015

Average Stack Gas Velocity, feet/second 96.43 96.13 95.95 96.170 Stack Cross-Sectional Area, square feet 93.000 93.000 93.000 93.000 Dry Volumetric Flow Rate, dry scfm 331,648.4 336,275.6 328,593.9 332,172.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 538,079.4 536,405.4 535,401.0 536,628.600 Percent Isokinetic of Sampling Rate, % 98.2 109.4 3.3 70.300 Percent Excess Air, % 31.7 39.4 32.6 34.567 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Round Duct Diameter, inches 0 0 0 Rectangular Duct Width, inches 124 124 124 Rectangular Duct Length, inches 108 108 108 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Monday, February 28, 2011 Page 40 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 0011 3 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 28, 2011 Page 41 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 10 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



### Monday, February 28, 2011 Page 42 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 10 3 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



### Monday, February 28, 2011 Page 43 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 23 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 28, 2011 Page 44 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 23 3 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 28, 2011 Page 45 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 25A 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



### Monday, February 28, 2011 Page 46 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 25A 3 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



### Monday, February 28, 2011 Page 47 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 26A Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 28, 2011 Page 48 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 26A 3 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 28, 2011 Page 49 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 29 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 28, 2011 Page 50 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 29 3 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 28, 2011 Page 51 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - 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



### Monday, February 28, 2011 Page 52 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 6C 3 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



### Monday, February 28, 2011 Page 53 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - 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



### Monday, February 28, 2011 Page 54 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - Method 7E 3 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



### Monday, February 28, 2011 Page 55 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - OTM - 27/28 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 28, 2011 Page 56 of 57

### Northport Unit 2 ICR Test Program

Location Duct near stack breaching - OTM - 27/28 3 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 28, 2011 Page 57 of 57