### Name:

Title: Company: Sign Date: Name: Title: Company: Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date Final Test Report for

/ / Based on information and belief formed after reasonable inquiry, I certify that the statements and information in this test report are true, accurate, and complete. I have reviewed all testing details and results in this test report and hereby certify that the test report is authentic and accurate.

Monday, February 07, 2011 Page 1 of 34

### Facility Information:

Georgia Power Plant McManus 1 Crispen Island

Brunswick Ga31525 Contact:Sarah Markham Phone:205-257-6780 Fax: Email: sasander@southernco.com Testing Company:
Weston Solutions 1625 Pumphrey Ave

Auburn Al36832 Contact:Jon Howard Phone:33-466-5600 Fax: Email:j.howard@westonsolutions.com

Air Permit Number: 715 Permitted Source ID/Name: McManus Unit 1 1 Permitted Maximum Process Rate:Max. Normal Operation Process Rate: Target Process Test Rat

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: See attached report Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information: AFS #: FRS #:

SCC / Description

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 160.5 1200 480 2 0 24 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location Carbon Monoxide Method 10 3 0 Stack Formaldehyde Method 0011 3 0 Stack 2,3,7,8-TCDD Method 23 3 0 Stack 1,2,3,7,8-PeCDD Method 23 3 0 Stack 1,2,3,4,7,8-HxCDD Method 23 3 0 Stack 1,2,3,6,7,8-HxCDD Method 23 3 0 Stack 1,2,3,7,8,9-HxCDD Method 23 3 0 Stack 1,2,3,4,6,7,8-HpCDD Method 23 3 0 Stack



### Monday, February 07, 2011 Page 2 of 34OCDD Method 23 3 0

Stack 2,3,7,8-TCDF Method 23 3 0 Stack 1,2,3,7,8-PeCDF Method 23 3 0 Stack 2,3,4,7,8-PeCDF Method 23 3 0 Stack 1,2,3,4,7,8-HxCDF Method 23 3 0 Stack 1,2,3,6,7,8-HxCDF Method 23 3 0 Stack 2,3,4,6,7,8-HxCDF Method 23 3 0 Stack 1,2,3,7,8,9-HxCDF Method 23 3 0 Stack 1,2,3,4,6,7,8-HpCDF Method 23 3 0 Stack 1,2,3,4,7,8,9-HpCDF Method 23 3 0 Stack OCDF Method 23 3 0 Stack Other TCDD Method 23 0 Stack Other PeCDD Method 23 0 Stack Other HxCDD Method 23 0 Stack Other HpCDD Method 23 0 Stack Other TCDF Method 23 0 Stack Other PeCDF Method 23 0 Stack Other HxCDF Method 23 0 Stack Other HpCDF Method 23 0 Stack 3,3',4,4'-TCB (PCB77) Method 23 3 0 Stack 3,4,4',5-TCB (PCB81) Method 23 3 0 Stack 2,3,3',4,4'-PeCB (PCB105) Method 23 3 0 Stack 2,3,4,4',5-PeCB (PCB114) Method 23 3 0 Stack 2,3',4,4',5-PeCB (PCB118) Method 23 3 0 Stack 2',3,4,4',5-PeCB (PCB123) Method 23 3 0 Stack 3,3',4,4',5-PeCB (PCB126) Method 23 3 0 Stack 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 0 Stack

2,3',4,4',5,5'-HxCB (PCB167)Method 23 3 0 Stack 3,3',4,4',5,5'-HxCB (PCB169)Method 23 3 0 Stack 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 0 Stack

Total organic compounds

(TOC) as Propane Method 25A 3 0 Stack

Hydrogen Fluoride Method 26A 3 0 Stack Hydrogen Chloride Method 26A 3 0 Stack Filterable PM2.5 OTM - 27 3 0 Stack Total Particulate OTM - 28 3 0 Stack Organic Condensible

Particulate OTM - 28 3 0 Stack

Inorganic (Aqueous)

Condensible Part. OTM - 28 3 0 Stack

Cobalt Method 29 3 0 Stack Filterable Particulate Method 29 3 0 Stack Phosphorus (yellow or white)Method 29 3 0 Stack Selenium Method 29 3 0 Stack Nickel Method 29 3 0 Stack Lead Method 29 3 0 Stack Chromium Method 29 3 0 Stack Cadmium Method 29 3 0 Stack Beryllium Method 29 3 0 Stack Antimony Method 29 3 0 Stack Arsenic Method 29 3 0 Stack



### Monday, February 07, 2011 Page 3 of 34

### 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. See attached report

Manganese Method 29 3 0 Stack O2 Method 3A O2 3 0 Stack Co2 Method 3A CO2 3 0 Stack Sulfur Dioxide Method 6C 3 0 Stack Nitrogen oxides (NOx) Method 7E 3 0 Stack



### Monday, February 07, 2011 Page 4 of 34

### Sampling / Stack Data Results Summary

LocationStack - Method 0011 Average Run Number 1 2 3
Test Date 4/7/2010 4/7/2010 4/7/2010 Run Start Time 9:27:00 AM1:16:00 PM 4:55:00 PM
Run Finish Time 11:40:00 AM3:27:00 PM 7:05:00 PM Net Run Time, minutes 120 120 120 Dry Gas Meter Volume Sampled, dscf 62.790 58.379 59.144 60.104 Moisture Content of Stack Gas, % 9.80 9.88 10.12 9.933 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 11 10.9 10.9 10.933 Oxygen, % 6.9 6.7 6.8 6.800 Average Stack Gas Temperature, °F 310.46 312.50 313.83 312.263 Dry Volumetric Flow Rate, dry scfm 161,970.0 154,945.1 158,619.7 158,511.600 Actual Wet Volumetric Flue Gas Flow Rate, acfm 261,414.3 250,961.1 258,042.3256,805.900 Percent Isokinetic of Sampling Rate, % 103.9 101.0 99.9 101.600 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



### LocationStack - Method 10 Average Run Number 1 2 3
Test Date 4/6/2010 4/6/2010 4/6/2010
Run Start Time 10:02:00 AM 12:07:00 PM 2:11:00 PM

Run Finish Time 11:56:00 AM1:59:00 PM 4:02:00 PM Carbon Dioxide, % 11 11.2 11.1 11.100 Oxygen, % 6.8 6.5 6.6 6.633 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Monday, February 07, 2011 Page 5 of 34

### LocationStack - Method 23 Average

Run Number 1 2 3
Test Date 4/8/2010 4/11/2010 4/12/2010
Run Start Time 8:29:00 AM 12:05:00 AM 6:20:00 AM

Run Finish Time 6:01:00 PM4:00:00 PM 8:57:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 273.001 304.634 293.342 290.326 Moisture Content of Stack Gas, % 10.76 8.45 8.64 9.283 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 10.8 10.1 10.2 10.367 Oxygen, % 6.7 7.8 7.6 7.367 Average Stack Gas Temperature, °F 317.85 317.52 317.75 317.707 Dry Volumetric Flow Rate, dry scfm 154,828.3 164,040.7 166,854.3 161,907.767 Actual Wet Volumetric Flue Gas Flow Rate, acfm 255,766.2 261,498.6 267,146.7261,470.500 Percent Isokinetic of Sampling Rate, % 98.5 100.4 95.1 98.000 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



### LocationStack - Method 25A Average Run Number 1 2 3
Test Date 4/6/2010 4/6/2010 4/6/2010
Run Start Time 10:02:00 AM 12:07:00 PM 2:11:00 PM

Run Finish Time 11:56:00 AM1:59:00 PM 4:02:00 PM Carbon Dioxide, % 11 11.2 11.1 11.100 Oxygen, % 6.8 6.5 6.6 6.633 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Monday, February 07, 2011 Page 6 of 34

### LocationStack - Method 26A Average

Run Number 1 2 3
Test Date 4/7/2010 4/7/2010 4/7/2010
Run Start Time 11:31:00 AM 2:57:00 AM 4:38:00 PM

Run Finish Time 1:40:00 PM4:10:00 PM 6:32:00 PM Net Run Time, minutes 60 60 60 Dry Gas Meter Volume Sampled, dscf 36.806 35.377 35.795 35.993 Moisture Content of Stack Gas, % 15.63 15.32 15.69 15.547 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 11.5 11.5 11.4 11.467 Oxygen, % 7 7.1 7.1 7.067 Average Stack Gas Temperature, °F 311.96 313.13 314.92 313.337 Dry Volumetric Flow Rate, dry scfm 145,550.6 142,443.7 141,785.0 143,259.767 Actual Wet Volumetric Flue Gas Flow Rate, acfm 251,635.5 245,734.5 246,240.3247,870.100 Percent Isokinetic of Sampling Rate, % 110.1 108.1 109.9 109.367 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 07, 2011 Page 7 of 34

### LocationStack - Method 29 Average

Run Number 1 2 3
Test Date 4/13/2010 4/14/2010 4/14/2010
Run Start Time 12:12:00 PM 6:25:00 AM11:50:00 AM

Run Finish Time 5:22:00 PM 9:20:00 AM 4:00:00 PM

Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 149.603 146.648 145.866 147.372 Moisture Content of Stack Gas, % 8.61 8.82 9.06 8.830 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 10.5 10.8 10.7 10.667 Oxygen, % 7.3 7.1 7 7.133 Average Stack Gas Temperature, °F 335.06 318.10 330.06 327.740 Dry Volumetric Flow Rate, dry scfm 159,008.6 158,360.7 156,122.2157,830.500 Actual Wet Volumetric Flue Gas Flow Rate, acfm 259,391.1 253,405.8 254,333.1255,710.000 Percent Isokinetic of Sampling Rate, % 101.8 100.2 101.1 101.033 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



### LocationStack - Method 3A CO2 Average Run Number 1 2 3
Test Date 4/6/2010 4/6/2010 4/6/2010
Run Start Time 10:02:00 AM 12:07:00 PM 2:11:00 PM

Run Finish Time 11:56:00 AM1:59:00 PM 4:02:00 PM Carbon Dioxide, % 0 0 0 0.000 Oxygen, % 0 0 0 0.000 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Moisture, % 0 0 0 0.000 Fuel Type
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Monday, February 07, 2011 Page 8 of 34

### LocationStack - Method 3A O2 Average

Run Number 1 2 3
Test Date 4/6/2010 4/6/2010 4/6/2010
Run Start Time 10:02:00 AM 2:11:00 PM Run Finish Time 11:56:00 AM 4:02:00 PM Carbon Dioxide, % 0 0 0 0.000 Oxygen, % 0 0 0 0.000 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Moisture, % 0 0 0 0.000 Fuel Type
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### LocationStack - Method 6C Average Run Number 1 2 3
Test Date 4/7/2010 4/7/2010 4/7/2010
Run Start Time 9:27:00 AM 11:31:00 AM 1:16:00 PM

Run Finish Time 11:23:00 AM 12:51:00 PM 4:10:00 PM

Carbon Dioxide, % 11 11.1 11 11.033 Oxygen, % 6.9 6.7 6.8 6.800 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Monday, February 07, 2011 Page 9 of 34

### LocationStack - Method 7E Average

Run Number 1 2 3
Test Date 4/6/2010 4/6/2010 4/6/2010
Run Start Time 10:02:00 AM 12:07:00 PM 2:11:00 PM

Run Finish Time 11:56:00 AM1:59:00 PM 4:02:00 PM Carbon Dioxide, % 11 11.2 11.1 11.100 Oxygen, % 6.8 6.5 6.6 6.633 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### LocationStack - OTM - 27 Average Run Number 1 2 3
Test Date 4/8/2010 4/8/2010 4/11/2010 Run Start Time 12:50:00 PM4:29:00 PM 6:15:00 AM
Run Finish Time 1:58:00 PM6:50:00 PM 7:30:00 AM Net Run Time, minutes 57.75 58.25 59.25 Dry Gas Meter Volume Sampled, dscf 20.896 21.283 21.534 21.238 Moisture Content of Stack Gas, % 11.10 11.77 9.42 10.763 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 10.9 10 10.1 10.333 Oxygen, % 6.7 7 7.6 7.100 Average Stack Gas Temperature, °F 317.69 319.46 304.21 313.787 Dry Volumetric Flow Rate, dry scfm 156,761.7 152,608.8 163,754.1 157,708.200 Actual Wet Volumetric Flue Gas Flow Rate, acfm 259,896.9 255,513.3 261,835.8259,082.000 Percent Isokinetic of Sampling Rate, % 100.7 104.4 96.8 100.633 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 07, 2011 Page 10 of 34

### LocationStack - OTM - 28 Average

Run Number 1 2 3
Test Date 4/13/2010 4/14/2010 4/14/2010
Run Start Time 12:15:00 PM 6:42:00 AM12:19:00 PM

Run Finish Time 5:19:00 PM 11:58:00 AM 3:01:00 PM

Net Run Time, minutes 240 240 125 Dry Gas Meter Volume Sampled, dscf 144.833 136.460 72.409 117.901 Moisture Content of Stack Gas, % 8.80 10.05 9.18 9.343 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 10.5 10.8 10.5 10.600 Oxygen, % 7.3 7.1 7.1 7.167 Average Stack Gas Temperature, °F 335.81 320.42 330.92 329.050 Dry Volumetric Flow Rate, dry scfm 159,199.4 153,427.3 158,070.3 156,899.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 260,402.7 249,528.0 258,042.3255,991.000 Percent Isokinetic of Sampling Rate, % 101.6 99.3 98.2 99.700 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 07, 2011 Page 11 of 34

### Emissions Summary

Location: Stack - Method 0011 Compound: Formaldehyde Average RunNumber 1 2 3 Mass_mg 0.447 0.402 0.106 0.318 lb/mmBtuO2 2.15E-04 2.05E-04 5.38E-05 0.000 ppm 2.01E-01 1.95E-01 5.07E-02 0.149 ppm@7%O2 2.00E-01 1.91E-01 5.00E-02 0.147



### Location: Stack - Method 10 

### Compound: Carbon Monoxide Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 1.04E-03 1.53E-03 1.03E-03 0.001 ppm 1.05E+00 1.58E+00 1.05E+00 1.227 ppm@7%O2 1.04E+00 1.53E+00 1.02E+00 1.197



### Location: Stack - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.0000000016 0.0000000016 0.0000000016 0.000 lb/mmBtuO2 1.75E-13 1.70E-13 1.74E-13 0.000 ng/dscm 2.07E-04 1.86E-04 1.93E-04 0.000 ng/dscm@7%O2 2.03E-04 1.97E-04 2.02E-04 0.000 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000039 0.0000000098 0.0000000063 0.000 lb/mmBtuO2 4.26E-13 1.04E-12 6.84E-13 0.000 ng/dscm 5.05E-04 1.14E-03 7.59E-04 0.001 ng/dscm@7%O2 4.94E-04 1.21E-03 7.93E-04 0.001 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.000000002 0.0000000021 0.0000000021 0.000 lb/mmBtuO2 2.18E-13 2.23E-13 2.28E-13 0.000 ng/dscm 2.59E-04 2.43E-04 2.53E-04 0.000 ng/dscm@7%O2 2.54E-04 2.58E-04 2.64E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000017 0.0000000016 0.0000000018 0.000 lb/mmBtuO2 1.86E-13 1.70E-13 1.95E-13 0.000 ng/dscm 2.20E-04 1.86E-04 2.17E-04 0.000 ng/dscm@7%O2 2.15E-04 1.97E-04 2.27E-04 0.000



### Monday, February 07, 2011 Page 12 of 34

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000018 0.0000000015 0.0000000015 0.000 lb/mmBtuO2 1.97E-13 1.59E-13 1.63E-13 0.000 ng/dscm 2.33E-04 1.74E-04 1.81E-04 0.000 ng/dscm@7%O2 2.28E-04 1.85E-04 1.89E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000017 0.0000000016 0.0000000017 0.000 lb/mmBtuO2 1.86E-13 1.70E-13 1.85E-13 0.000 ng/dscm 2.20E-04 1.86E-04 2.05E-04 0.000 ng/dscm@7%O2 2.15E-04 1.97E-04 2.14E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000016 0.0000000016 0.0000000014 0.000 lb/mmBtuO2 1.75E-13 1.70E-13 1.52E-13 0.000 ng/dscm 2.07E-04 1.86E-04 1.69E-04 0.000 ng/dscm@7%O2 2.03E-04 1.97E-04 1.77E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000016 0.0000000015 0.0000000017 0.000 lb/mmBtuO2 1.75E-13 1.59E-13 1.85E-13 0.000 ng/dscm 2.07E-04 1.74E-04 2.05E-04 0.000 ng/dscm@7%O2 2.03E-04 1.85E-04 2.14E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000022 0.0000000021 0.0000000018 0.000 lb/mmBtuO2 2.40E-13 2.23E-13 1.95E-13 0.000 ng/dscm 2.85E-04 2.43E-04 2.17E-04 0.000 ng/dscm@7%O2 2.79E-04 2.58E-04 2.27E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.0000000015 0.0000000021 0.0000000016 0.000 lb/mmBtuO2 1.64E-13 2.23E-13 1.74E-13 0.000 ng/dscm 1.94E-04 2.43E-04 1.93E-04 0.000 ng/dscm@7%O2 1.90E-04 2.58E-04 2.02E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000017 0.0000000017 0.0000000016 0.000 lb/mmBtuO2 1.86E-13 1.80E-13 1.74E-13 0.000



### Monday, February 07, 2011 Page 13 of 34ng/dscm 2.20E-04 1.97E-04 1.93E-04 0.000 ng/dscm@7%O2 2.15E-04 2.09E-04 2.02E-04 0.000 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 2 3 Mass_mg 0.000000014 0.000000013 0.000000024 0.000 lb/mmBtuO2 1.53E-12 1.38E-12 2.60E-12 0.000 ng/dscm 1.81E-03 1.51E-03 2.89E-03 0.002 ng/dscm@7%O2 1.77E-03 1.60E-03 3.02E-03 0.002 

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 2 3 Mass_mg 0.000000095 0.00000005 0.000000048 0.000 lb/mmBtuO2 1.04E-11 5.31E-12 5.21E-12 0.000 ng/dscm 1.23E-02 5.80E-03 5.78E-03 0.008 ng/dscm@7%O2 1.20E-02 6.15E-03 6.04E-03 0.008 

### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 2 3 Mass_mg 0.00000043 0.00000033 0.00000027 0.000 lb/mmBtuO2 4.70E-11 3.50E-11 2.93E-11 0.000 ng/dscm 5.56E-02 3.83E-02 3.25E-02 0.042 ng/dscm@7%O2 5.44E-02 4.06E-02 3.40E-02 0.043 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 2 3 Mass_mg 0.000000027 0.000000015 0.00000002 0.000 lb/mmBtuO2 2.95E-12 1.59E-12 2.17E-12 0.000 ng/dscm 3.49E-03 1.74E-03 2.41E-03 0.003 ng/dscm@7%O2 3.42E-03 1.85E-03 2.52E-03 0.003 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 2 3 Mass_mg 0.000000024 0.00000002 0.000000016 0.000 lb/mmBtuO2 2.62E-12 2.12E-12 1.74E-12 0.000 ng/dscm 3.11E-03 2.32E-03 1.93E-03 0.002 ng/dscm@7%O2 3.04E-03 2.46E-03 2.02E-03 0.003 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 2 3 Mass_mg 0.0000012 0.00000089 0.0000007 0.000 lb/mmBtuO2 1.31E-10 9.44E-11 7.60E-11 0.000 ng/dscm 1.55E-01 1.03E-01 8.43E-02 0.114 ng/dscm@7%O2 1.52E-01 1.09E-01 8.81E-02 0.116 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 2 3



### Monday, February 07, 2011 Page 14 of 34Mass_mg 0.0000000094 0.00000002 0.000000014 0.000 lb/mmBtuO2 1.03E-12 2.12E-12 1.52E-12 0.000 ng/dscm 1.22E-03 2.32E-03 1.69E-03 0.002 ng/dscm@7%O2 1.19E-03 2.46E-03 1.77E-03 0.002 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.000000002 0.0000000021 0.0000000017 0.000 lb/mmBtuO2 2.18E-13 2.23E-13 1.85E-13 0.000 ng/dscm 2.59E-04 2.43E-04 2.05E-04 0.000 ng/dscm@7%O2 2.54E-04 2.58E-04 2.14E-04 0.000 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000016 0.0000000016 0.0000000015 0.000 lb/mmBtuO2 1.75E-13 1.70E-13 1.63E-13 0.000 ng/dscm 2.07E-04 1.86E-04 1.81E-04 0.000 ng/dscm@7%O2 2.03E-04 1.97E-04 1.89E-04 0.000 

### Compound: 2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000016 0.0000000024 0.0000000021 0.000 lb/mmBtuO2 1.75E-13 2.55E-13 2.28E-13 0.000 ng/dscm 2.07E-04 2.78E-04 2.53E-04 0.000 ng/dscm@7%O2 2.03E-04 2.95E-04 2.64E-04 0.000 

### Compound: 2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.0000000015 0.0000000016 0.0000000075 0.000 lb/mmBtuO2 1.64E-13 1.70E-13 8.14E-13 0.000 ng/dscm 1.94E-04 1.86E-04 9.03E-04 0.000 ng/dscm@7%O2 1.90E-04 1.97E-04 9.44E-04 0.000 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 2 3 Mass_mg 0.0000000073 0.000000014 0.000000014 0.000 lb/mmBtuO2 7.97E-13 1.49E-12 1.52E-12 0.000 ng/dscm 9.44E-04 1.62E-03 1.69E-03 0.001 ng/dscm@7%O2 9.24E-04 1.72E-03 1.77E-03 0.001 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 2 3 Mass_mg 0.0000000092 0.00000002 0.000000014 0.000 lb/mmBtuO2 1.00E-12 2.12E-12 1.52E-12 0.000 ng/dscm 1.19E-03 2.32E-03 1.69E-03 0.002 ng/dscm@7%O2 1.16E-03 2.46E-03 1.77E-03 0.002



### Monday, February 07, 2011 Page 15 of 34

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 1 2 3 Mass_mg 0.000000083 0.00000014 0.000000063 0.000 lb/mmBtuO2 9.07E-12 1.49E-11 6.84E-12 0.000 ng/dscm 1.07E-02 1.62E-02 7.59E-03 0.011 ng/dscm@7%O2 1.05E-02 1.72E-02 7.93E-03 0.012 

### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber 1 2 3 Mass_mg 0.0000000053 0.000000013 0.0000000097 0.000 lb/mmBtuO2 5.79E-13 1.38E-12 1.05E-12 0.000 ng/dscm 6.86E-04 1.51E-03 1.17E-03 0.001 ng/dscm@7%O2 6.72E-04 1.60E-03 1.22E-03 0.001 

### Compound: OCDD Average RunNumber 1 2 3 Mass_mg 0.0000000031 0.000000016 0.0000000035 0.000 lb/mmBtuO2 3.39E-13 1.70E-12 3.80E-13 0.000 ng/dscm 4.01E-04 1.86E-03 4.21E-04 0.001 ng/dscm@7%O2 3.93E-04 1.97E-03 4.40E-04 0.001 

### Compound: OCDF Average RunNumber 1 2 3 Mass_mg 0.0000000033 0.0000000033 0.0000000036 0.000 lb/mmBtuO2 3.60E-13 3.50E-13 3.91E-13 0.000 ng/dscm 4.27E-04 3.83E-04 4.33E-04 0.000 ng/dscm@7%O2 4.18E-04 4.06E-04 4.53E-04 0.000 

### Compound: Other HpCDD Average RunNumber 1 2 3 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 HpCDF Average RunNumber 1 2 3 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 HxCDD Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000



### Monday, February 07, 2011 Page 16 of 34ng/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 HxCDF Average RunNumber 1 2 3 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 PeCDD Average RunNumber 1 2 3 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 1 2 3 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 TCDD Average RunNumber 1 2 3 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 TCDF Average RunNumber 1 2 3 Mass_mg 0.000000055 0.00000005 0.00000004 0.000 lb/mmBtuO2 6.01E-12 5.31E-12 4.34E-12 0.000 ng/dscm 7.12E-03 5.80E-03 4.82E-03 0.006 ng/dscm@7%O2 6.97E-03 6.15E-03 5.04E-03 0.006



### Location: Stack - Method 25A Compound: Total organic compounds (TOC) as Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 1.07E-03 1.05E-03 9.08E-04 0.001 ppm 6.89E-01 6.89E-01 5.90E-01 0.656 ppm@7%O2 6.79E-01 6.65E-01 5.73E-01 0.639



### Location: Stack - Method 26A

Monday, February 07, 2011 Page 17 of 34

### Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 1.53 1.2 1.07 1.267 lb/mmBtuO2 1.27E-03 1.04E-03 9.17E-04 0.001 ppm 9.68E-01 7.90E-01 6.96E-01 0.818 ppm@7%O2 9.68E-01 7.96E-01 7.01E-01 0.822 

### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 0.236 0.434 0.373 0.348 lb/mmBtuO2 1.95E-04 3.76E-04 3.20E-04 0.000 ppm 2.72E-01 5.21E-01 4.42E-01 0.412 ppm@7%O2 2.72E-01 5.25E-01 4.45E-01 0.414



### Location: Stack - Method 29 Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.0748 0.0756 0.0765 0.076 lb/mmBtuO2 1.56E-05 1.58E-05 1.60E-05 0.000 mg/dscm 1.77E-02 1.82E-02 1.85E-02 0.018 mg/dscm@7%O2 1.81E-02 1.83E-02 1.85E-02 0.018 

### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.01263 0.01293 0.01263 0.013 lb/mmBtuO2 2.63E-06 2.71E-06 2.64E-06 0.000 mg/dscm 2.98E-03 3.11E-03 3.06E-03 0.003 mg/dscm@7%O2 3.05E-03 3.13E-03 3.06E-03 0.003 

### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.0015 0.0015 0.0015 0.002 lb/mmBtuO2 3.12E-07 3.14E-07 3.13E-07 0.000 mg/dscm 3.54E-04 3.61E-04 3.63E-04 0.000 mg/dscm@7%O2 3.62E-04 3.64E-04 3.63E-04 0.000 

### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.0021 0.0015 0.00205 0.002 lb/mmBtuO2 4.37E-07 3.14E-07 4.28E-07 0.000 mg/dscm 4.96E-04 3.61E-04 4.96E-04 0.000 mg/dscm@7%O2 5.07E-04 3.64E-04 4.96E-04 0.000 

### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.02067 0.01647 0.01677 0.018



### Monday, February 07, 2011 Page 18 of 34lb/mmBtuO2 4.30E-06 3.45E-06 3.50E-06 0.000 mg/dscm 4.88E-03 3.97E-03 4.06E-03 0.004 mg/dscm@7%O2 4.99E-03 4.00E-03 4.06E-03 0.004 

### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.119 0.114 0.117 0.117 lb/mmBtuO2 2.48E-05 2.39E-05 2.44E-05 0.000 mg/dscm 2.81E-02 2.75E-02 2.83E-02 0.028 mg/dscm@7%O2 2.87E-02 2.77E-02 2.83E-02 0.028 

### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 273 231 228 244.000 lb/mmBtuO2 5.68E-02 4.83E-02 4.76E-02 0.051 mg/dscm 6.45E+01 5.56E+01 5.52E+01 58.433 mg/dscm@7%O2 6.59E+01 5.60E+01 5.52E+01 59.033 

### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.02229 0.02139 0.02179 0.022 lb/mmBtuO2 4.64E-06 4.48E-06 4.55E-06 0.000 mg/dscm 5.26E-03 5.15E-03 5.28E-03 0.005 mg/dscm@7%O2 5.38E-03 5.19E-03 5.28E-03 0.005 

### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.593 0.565 0.577 0.578 lb/mmBtuO2 1.23E-04 1.18E-04 1.21E-04 0.000 mg/dscm 1.40E-01 1.36E-01 1.40E-01 0.139 mg/dscm@7%O2 1.43E-01 1.37E-01 1.40E-01 0.140 

### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 4.76209 4.53209 4.63209 4.642 lb/mmBtuO2 9.91E-04 9.48E-04 9.67E-04 0.001 mg/dscm 1.12E+00 1.09E+00 1.12E+00 1.110 mg/dscm@7%O2 1.14E+00 1.10E+00 1.12E+00 1.120 

### Compound: Phosphorus (yellow or white) Average RunNumber 1 2 3 Mass_mg 0.9176 0.8936 0.91295 0.908 lb/mmBtuO2 1.91E-04 1.87E-04 1.91E-04 0.000 mg/dscm 2.17E-01 2.15E-01 2.21E-01 0.218 mg/dscm@7%O2 2.22E-01 2.17E-01 2.21E-01 0.220 

### Compound: Selenium Average

Monday, February 07, 2011 Page 19 of 34RunNumber 1 2 3 Mass_mg 0.0374 0.015 0.019 0.024 lb/mmBtuO2 7.78E-06 3.14E-06 3.97E-06 0.000 mg/dscm 8.83E-03 3.61E-03 4.60E-03 0.006 mg/dscm@7%O2 9.02E-03 3.64E-03 4.60E-03 0.006



### Location: Stack - Method 6C 

### Compound: Sulfur Dioxide Average Run 1 2 3 lb/mmBtuO2 2.04E+00 2.02E+00 2.02E+00 2.027 ppm 8.92E+02 8.96E+02 8.91E+02 893.000 ppm@7%O2 8.86E+02 8.77E+02 8.78E+02 880.333



### Location: Stack - Method 7E 

### Compound: Nitrogen oxides (NOx) Average Run 1 2 3 lb/mmBtuO2 4.65E-01 4.94E-01 4.64E-01 0.474 ppm 2.86E+02 3.10E+02 2.89E+02 295.000 ppm@7%O2 2.82E+02 2.99E+02 2.81E+02 287.333



### Location: Stack - OTM - 27 

### Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 26.8 27.1 10.1 21.333 Elb/hr 2.66E+01 2.57E+01 1.02E+01 20.833 lb/mmBtuO2 3.82E-02 3.88E-02 1.49E-02 0.031



### Location: Stack - OTM - 28 Compound: Inorganic (Aqueous) Condensible P Average RunNumber 1 2 3 Mass_mg 176 137 88 133.667 Elb/hr 2.56E+01 2.04E+01 2.54E+01 23.800 lb/mmBtuO2 3.78E-02 3.08E-02 3.73E-02 0.035 

### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 6 3 2 3.667 Elb/hr 8.72E-01 4.46E-01 5.78E-01 0.632 lb/mmBtuO2 1.29E-03 6.75E-04 8.48E-04 0.001 

### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 182 140 90 137.333 Elb/hr 2.65E+01 2.08E+01 2.60E+01 24.433 lb/mmBtuO2 3.91E-02 3.15E-02 3.81E-02 0.036



### Monday, February 07, 2011 Page 20 of 34

### Process Run Data

Monday, February 07, 2011 Page 21 of 34

### Process Run Data

APCD Run Data

Process Lab Run Data Run Name Value UOM Comments Target Value 1 Total power output 0 0

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

Monday, February 07, 2011 Page 22 of 34

### Sampling / Stack Data Results Detail

LocationStack - Method 0011 Average Run Number 1 2 3 Test Date 4/7/2010 4/7/2010 4/7/2010 Run Start Time 9:27:00 AM1:16:00 PM 4:55:00 PM Run Finish Time 11:40:00 AM3:27:00 PM 7:05:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 120 120 120 Nozzle Diameter, inches 0.283 0.283 0.283 0.283 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.005 1.005 1.005 1.005 Barometric Pressure, inches of Mercury 30 30 30 30.000 Average Orifice Meter Differential, inches H2O 0.97 0.86 0.89 0.907 Dry Gas Meter Volume Sampled, cubic feet 62.561 59.195 59.572 60.443 Average Dry Gas Meter Temperature, °F 71.38 80.63 77.08 76.363 Dry Gas Meter Volume Sampled, dscf 62.790 58.379 59.144 60.104 Total Moisture Liquid collected, g 144.9 135.9 141.5 140.767 Volume of Water Vapor, standard cubic feet 6.82 6.40 6.66 6.627 Moisture Content of Stack Gas, % 9.80 9.88 10.12 9.933 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.902 0.9012 0.8988 0.901 Carbon Dioxide, % 11 10.9 10.9 10.933 Oxygen, % 6.9 6.7 6.8 6.800 Carbon Monoxide & Nitrogen, % 82.1 82.4 82.3 82.267 Fuel Factor 1.27 1.30 1.29 Dry Molecular Weight, lb/lb-Mole 30.04 30.01 30.02 30.023 Wet Molecular weight, lb/lb-Mole 28.86 28.82 28.80 28.827 Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200 Absolute Flue Gas Pressure, inches of Mercury 29.99 29.99 29.99 29.990 Average Stack Gas Temperature, °F 310.46 312.50 313.83 312.263 Average Velocity Head, inches of H2O 0.2094136920 084810.192303839

9161990.202744974

270916 0.201

Average Stack Gas Velocity, feet/second 31.01 29.77 30.61 30.463 Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500 Dry Volumetric Flow Rate, dry scfm 161,970.0 154,945.1 158,619.7158,511.600 Actual Wet Volumetric Flue Gas Flow Rate, acfm 261,414.3 250,961.1 258,042.3256,805.900 Percent Isokinetic of Sampling Rate, % 103.9 101.0 99.9 101.600 Percent Excess Air, % 46.7 44.5 45.6 45.600 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 160.5 160.5 160.5 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000



### Monday, February 07, 2011 Page 23 of 34

### LocationStack - Method 10 Average

Run Number 1 2 3 Test Date 4/6/2010 4/6/2010 4/6/2010 Run Start Time 10:02:00 AM12:07:00 PM 2:11:00 PM Run Finish Time 11:56:00 AM1:59:00 PM 4:02:00 PM Carbon Dioxide, % 11 11.2 11.1 11.100 Oxygen, % 6.8 6.5 6.6 6.633 Fuel Factor 1.28 1.29 1.29 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 852 852 852 852.000 Operating Units ppm ppm ppm No. Readings/Avg. Calibration Set 3 3 3 3.000 Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Pre Zero Cylinder Instrument Response 9 5 8 7.333 Calibration Pre Zero Cylinder Bias 0.35 -0.12 0.23 0.153 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC119377 CC119377 CC119377 Calibration Pre High Cylinder Instrument Response 440 439 438 439.000 Calibration Pre High Cylinder Bias -0.12 -0.23 -0.35 -0.233 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Post Zero Cylinder Instrument Response 5 8 8 7.000 Calibration Post Zero Cylinder Bias -0.12 0.23 0.23 0.113 Calibration Post Zero Cylinder Drift 0.47 0.35 0 0.273 Calibration Post High Cylinder ID CC119377 CC119377 CC119377 Calibration Post High Cylinder Instrument Response 439 438 439 438.667 Calibration Post High Cylinder Bias -0.23 -0.35 -0.23 -0.270 Calibration Post High Cylinder Drift 0.11 0.12 0.12 0.117 Cavg 8 8 9 8.333 Cavg Units ppmvd ppmvd ppmvd Cgas 1.0497 1.5764 1.0546 1.227 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Monday, February 07, 2011 Page 24 of 34

### LocationStack - Method 23 Average

Run Number 1 2 3 Test Date 4/8/2010 4/11/2010 4/12/2010 Run Start Time 8:29:00 AM12:05:00 AM 6:20:00 AM Run Finish Time 6:01:00 PM4:00:00 PM 8:57:00 PM Net Traversing Points 97 96 96 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.31 0.315 0.315 0.313 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.981 0.981 0.981 0.981 Barometric Pressure, inches of Mercury 29.91 30.21 30.15 30.090 Average Orifice Meter Differential, inches H2O 1.26 1.60 1.48 1.447 Dry Gas Meter Volume Sampled, cubic feet 287.272 317.245 305.833 303.450 Average Dry Gas Meter Temperature, °F 86.55 86.76 86.14 86.483 Dry Gas Meter Volume Sampled, dscf 273.001 304.634 293.342 290.326 Total Moisture Liquid collected, g 698.9 597.5 589.6 628.667 Volume of Water Vapor, standard cubic feet 32.90 28.12 27.75 29.590 Moisture Content of Stack Gas, % 10.76 8.45 8.64 9.283 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8924 0.9155 0.9136 0.907 Carbon Dioxide, % 10.8 10.1 10.2 10.367 Oxygen, % 6.7 7.8 7.6 7.367 Carbon Monoxide & Nitrogen, % 82.5 82.1 82.2 82.267 Fuel Factor 1.31 1.30 1.30 Dry Molecular Weight, lb/lb-Mole 30.00 29.93 29.94 29.957 Wet Molecular weight, lb/lb-Mole 28.71 28.92 28.91 28.847 Flue Gas Static Pressure, inches of H2O -0.2 -0.21 -0.21 -0.207 Absolute Flue Gas Pressure, inches of Mercury 29.90 30.19 30.13 30.073 Average Stack Gas Temperature, °F 317.85 317.52 317.75 317.707 Average Velocity Head, inches of H2O 0.1970434433 23530.209480704

640250.218076660

192309 0.208

Average Stack Gas Velocity, feet/second 30.34 31.02 31.69 31.017 Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500 Dry Volumetric Flow Rate, dry scfm 154,828.3 164,040.7 166,854.3161,907.767 Actual Wet Volumetric Flue Gas Flow Rate, acfm 255,766.2 261,498.6 267,146.7261,470.500 Percent Isokinetic of Sampling Rate, % 98.5 100.4 95.1 98.000 Percent Excess Air, % 44.4 56.2 53.9 51.500 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 160.5 160.5 160.5 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000



### Monday, February 07, 2011 Page 25 of 34

### LocationStack - Method 25A Average

Run Number 1 2 3 Test Date 4/6/2010 4/6/2010 4/6/2010 Run Start Time 10:02:00 AM12:07:00 PM 2:11:00 PM Run Finish Time 11:56:00 AM1:59:00 PM 4:02:00 PM Carbon Dioxide, % 11 11.2 11.1 11.100 Oxygen, % 6.8 6.5 6.6 6.633 Fuel Factor 1.28 1.29 1.29 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 100 100 100 100.000 Operating Units ppm ppm ppm No. Readings/Avg. Calibration Set 4 4 4 4.000 Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000 Calibration Pre Zero Cylinder Bias 0 0 0 0.000 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC23540 CC23540 CC23540 Calibration Pre High Cylinder Instrument Response 12.6 12.6 12.6 12.600 Calibration Pre High Cylinder Bias 0 0 0 0.000 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000 Calibration Post Zero Cylinder Bias 0 0 0 0.000 Calibration Post Zero Cylinder Drift 0 0 0 0.000 Calibration Post High Cylinder ID CC23540 CC23540 CC23540 Calibration Post High Cylinder Instrument Response 12.6 12.6 12.6 12.600 Calibration Post High Cylinder Bias 0 0 0 0.000 Calibration Post High Cylinder Drift 0 0 0 0.000 Cavg 0.7 0.7 0.6 0.667 Cavg Units ppmvd ppmvd ppmvd Cgas 0.6889 0.6889 0.5905 0.656 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Monday, February 07, 2011 Page 26 of 34

### LocationStack - Method 26A Average

Run Number 1 2 3 Test Date 4/7/2010 4/7/2010 4/7/2010 Run Start Time 11:31:00 AM2:57:00 AM 4:38:00 PM Run Finish Time 1:40:00 PM4:10:00 PM 6:32:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 60 60 60 Nozzle Diameter, inches 0.314 0.314 0.314 0.314 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.972 0.972 0.972 0.972 Barometric Pressure, inches of Mercury 30 30 30 30.000 Average Orifice Meter Differential, inches H2O 1.22 1.17 1.17 1.187 Dry Gas Meter Volume Sampled, cubic feet 38.324 36.907 37.242 37.491 Average Dry Gas Meter Temperature, °F 77.42 78.38 76.92 77.573 Dry Gas Meter Volume Sampled, dscf 36.806 35.377 35.795 35.993 Total Moisture Liquid collected, g 144.9 135.9 141.5 140.767 Volume of Water Vapor, standard cubic feet 6.82 6.40 6.66 6.627 Moisture Content of Stack Gas, % 15.63 15.32 15.69 15.547 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8437 0.8468 0.8431 0.845 Carbon Dioxide, % 11.5 11.5 11.4 11.467 Oxygen, % 7 7.1 7.1 7.067 Carbon Monoxide & Nitrogen, % 81.5 81.4 81.5 81.467 Fuel Factor 1.21 1.20 1.21 Dry Molecular Weight, lb/lb-Mole 30.12 30.12 30.11 30.117 Wet Molecular weight, lb/lb-Mole 28.23 28.26 28.21 28.233 Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200 Absolute Flue Gas Pressure, inches of Mercury 29.99 29.99 29.99 29.990 Average Stack Gas Temperature, °F 311.96 313.13 314.92 313.337 Average Velocity Head, inches of H2O 0.1895385365 663230.180603066

1464830.180609454

802809 0.184

Average Stack Gas Velocity, feet/second 29.85 29.15 29.21 29.403 Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500 Dry Volumetric Flow Rate, dry scfm 145,550.6 142,443.7 141,785.0143,259.767 Actual Wet Volumetric Flue Gas Flow Rate, acfm 251,635.5 245,734.5 246,240.3247,870.100 Percent Isokinetic of Sampling Rate, % 110.1 108.1 109.9 109.367 Percent Excess Air, % 48.2 49.3 49.3 48.933 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 160.5 160.5 160.5 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000



### Monday, February 07, 2011 Page 27 of 34

### LocationStack - Method 29 Average

Run Number 1 2 3 Test Date 4/13/2010 4/14/2010 4/14/2010 Run Start Time 12:12:00 PM6:25:00 AM11:50:00 AM Run Finish Time 5:22:00 PM9:20:00 AM 4:00:00 PM Net Traversing Points 48 48 48 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.315 0.315 0.315 0.315 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.98 0.98 0.98 0.980 Barometric Pressure, inches of Mercury 30.24 30.24 30.24 30.240 Average Orifice Meter Differential, inches H2O 1.33 1.31 1.28 1.307 Dry Gas Meter Volume Sampled, cubic feet 152.122 149.077 148.287 149.829 Average Dry Gas Meter Temperature, °F 73.50 73.33 73.31 73.380 Dry Gas Meter Volume Sampled, dscf 149.603 146.648 145.866 147.372 Total Moisture Liquid collected, g 299.3 301.3 308.6 303.067 Volume of Water Vapor, standard cubic feet 14.09 14.18 14.53 14.267 Moisture Content of Stack Gas, % 8.61 8.82 9.06 8.830 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9139 0.9118 0.9094 0.912 Carbon Dioxide, % 10.5 10.8 10.7 10.667 Oxygen, % 7.3 7.1 7 7.133 Carbon Monoxide & Nitrogen, % 82.2 82.1 82.3 82.200 Fuel Factor 1.30 1.28 1.30 Dry Molecular Weight, lb/lb-Mole 29.97 30.01 29.99 29.990 Wet Molecular weight, lb/lb-Mole 28.94 28.95 28.90 28.930 Flue Gas Static Pressure, inches of H2O -0.26 -0.26 -0.26 -0.260 Absolute Flue Gas Pressure, inches of Mercury 30.22 30.22 30.22 30.220 Average Stack Gas Temperature, °F 335.06 318.10 330.06 327.740 Average Velocity Head, inches of H2O 0.2019992131 233870.197032018

3735230.195084372

688685 0.198

Average Stack Gas Velocity, feet/second 30.77 30.06 30.17 30.333 Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500 Dry Volumetric Flow Rate, dry scfm 159,008.6 158,360.7 156,122.2157,830.500 Actual Wet Volumetric Flue Gas Flow Rate, acfm 259,391.1 253,405.8 254,333.1255,710.000 Percent Isokinetic of Sampling Rate, % 101.8 100.2 101.1 101.033 Percent Excess Air, % 50.7 48.7 47.5 48.967 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 160.5 160.5 160.5 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000



### Monday, February 07, 2011 Page 28 of 34

### LocationStack - Method 3A CO2 Average

Run Number 1 2 3 Test Date 4/6/2010 4/6/2010 4/6/2010 Run Start Time 10:02:00 AM12:07:00 PM 2:11:00 PM Run Finish Time 11:56:00 AM1:59:00 PM 4:02:00 PM Carbon Dioxide, % 0 0 0 0.000 Oxygen, % 0 0 0 0.000 Fuel Factor 0 0 0 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 20.1 20.1 20.1 20.100 Operating Units % % % No. Readings/Avg. Calibration Set 2 2 2 2.000 Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Pre Zero Cylinder Instrument Response 0 0 0.1 0.033 Calibration Pre Zero Cylinder Bias 0 0 0.5 0.167 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC112251 CO2 CC112251

CO2 CC112251

CO2 Calibration Pre High Cylinder Instrument Response 10 10 10 10.000 Calibration Pre High Cylinder Bias 0 0 0 0.000 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Post Zero Cylinder Instrument Response 0 0.1 0.1 0.067 Calibration Post Zero Cylinder Bias 0 0.5 0.5 0.333 Calibration Post Zero Cylinder Drift 0 0.5 0 0.167 Calibration Post High Cylinder ID CC112251 CO2 CC112251

CO2 CC112251

CO2 Calibration Post High Cylinder Instrument Response 10 10 10 10.000 Calibration Post High Cylinder Bias 0 0 0 0.000 Calibration Post High Cylinder Drift 0 0 0 0.000 Cavg 10.9 11.1 11 11.000 Cavg Units %vd %vd %vd Cgas 11.009 11.2166 11.1202 11.115 Cgas Units %vd %vd %vd Fuel Type Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 0 0 0 0.000 Cgasw Units



### Monday, February 07, 2011 Page 29 of 34

### LocationStack - Method 3A O2 Average

Run Number 1 2 3 Test Date 4/6/2010 4/6/2010 4/6/2010 Run Start Time 10:02:00 AM 2:11:00 PM Run Finish Time 11:56:00 AM 4:02:00 PM Carbon Dioxide, % 0 0 0 0.000 Oxygen, % 0 0 0 0.000 Fuel Factor 0 0 0 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 20.1 20.1 20.1 20.100 Operating Units % % % No. Readings/Avg. Calibration Set 1 1 1 1.000 Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Pre Zero Cylinder Instrument Response 0 0 0.1 0.033 Calibration Pre Zero Cylinder Bias 0 0 0.5 0.167 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC112251 O2 CC112251 O2 CC112251

O2 Calibration Pre High Cylinder Instrument Response 10 10 10 10.000 Calibration Pre High Cylinder Bias 0 0 0 0.000 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Post Zero Cylinder Instrument Response 0 0.1 0 0.033 Calibration Post Zero Cylinder Bias 0 0.5 0 0.167 Calibration Post Zero Cylinder Drift 0 0.5 0.5 0.333 Calibration Post High Cylinder ID CC112251 O2 CC112251 O2 CC112251

O2 Calibration Post High Cylinder Instrument Response 10 10 10 10.000 Calibration Post High Cylinder Bias 0 0 0 0.000 Calibration Post High Cylinder Drift 0 0 0 0.000 Cavg 6.8 6.5 6.6 6.633 Cavg Units %vd %vd %vd Cgas 6.8 6.4824 6.5829 6.622 Cgas Units %vd %vd %vd Fuel Type Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 0 0 0 0.000 Cgasw Units



### Monday, February 07, 2011 Page 30 of 34

### LocationStack - Method 6C Average

Run Number 1 2 3 Test Date 4/7/2010 4/7/2010 4/7/2010 Run Start Time 9:27:00 AM11:31:00 AM 1:16:00 PM Run Finish Time 11:23:00 AM12:51:00 PM 4:10:00 PM Carbon Dioxide, % 11 11.1 11 11.033 Oxygen, % 6.9 6.7 6.8 6.800 Fuel Factor 1.27 1.28 1.28 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 2414 2414 24142,414.000 Operating Units ppm ppm ppm No. Readings/Avg. Calibration Set 6 6 6 6.000 Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Pre Zero Cylinder Instrument Response 3 6 9 6.000 Calibration Pre Zero Cylinder Bias 0.04 0.17 0.29 0.167 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID SG9121056B ALSG9121056B

ALSG9121056B

AL Calibration Pre High Cylinder Instrument Response 1219 1225 1225 1,223.000 Calibration Pre High Cylinder Bias -1.41 -1.16 -1.16 -1.243 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Post Zero Cylinder Instrument Response 6 9 12 9.000 Calibration Post Zero Cylinder Bias 0.17 0.29 0.41 0.290 Calibration Post Zero Cylinder Drift 0.13 0.12 0.12 0.123 Calibration Post High Cylinder ID SG9121056B ALSG9121056B

ALSG9121056B

AL Calibration Post High Cylinder Instrument Response 1225 1225 1221 1,223.667 Calibration Post High Cylinder Bias -1.16 -1.16 -1.33 -1.217 Calibration Post High Cylinder Drift 0.25 0 0.17 0.140 Cavg 868 875 869 870.667 Cavg Units ppmvd ppmvd ppmvd Cgas 892.2242 896.3573 890.7159 893.099 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Monday, February 07, 2011 Page 31 of 34

### LocationStack - Method 7E Average

Run Number 1 2 3 Test Date 4/6/2010 4/6/2010 4/6/2010 Run Start Time 10:02:00 AM12:07:00 PM 2:11:00 PM Run Finish Time 11:56:00 AM1:59:00 PM 4:02:00 PM Carbon Dioxide, % 11 11.2 11.1 11.100 Oxygen, % 6.8 6.5 6.6 6.633 Fuel Factor 1.28 1.29 1.29 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 441 441 441 441.000 Operating Units ppm ppm ppm No. Readings/Avg. Calibration Set 5 5 5 5.000 Calibration Pre Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Pre Zero Cylinder Instrument Response 2 2 2 2.000 Calibration Pre Zero Cylinder Bias 0.45 0.45 0.45 0.450 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC111553 CC111553 CC111553 Calibration Pre High Cylinder Instrument Response 248 245 241 244.667 Calibration Pre High Cylinder Bias 0.45 -0.23 -1.13 -0.303 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID XC01167B XC01167B XC01167B Calibration Post Zero Cylinder Instrument Response 2 2 2 2.000 Calibration Post Zero Cylinder Bias 0.45 0.45 0.45 0.450 Calibration Post Zero Cylinder Drift 0 0 0 0.000 Calibration Post High Cylinder ID CC111553 CC111553 CC111553 Calibration Post High Cylinder Instrument Response 245 241 241 242.333 Calibration Post High Cylinder Bias -0.23 -1.13 -1.13 -0.830 Calibration Post High Cylinder Drift 0.68 0.9 0 0.527 Cavg 286 306 283 291.667 Cavg Units ppmvd ppmvd ppmvd Cgas 285.7423 310.3071 289.2301 295.093 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Monday, February 07, 2011 Page 32 of 34

### LocationStack - OTM - 27 Average

Run Number 1 2 3 Test Date 4/8/2010 4/8/2010 4/11/2010 Run Start Time 12:50:00 PM4:29:00 PM 6:15:00 AM Run Finish Time 1:58:00 PM6:50:00 PM 7:30:00 AM Net Traversing Points 13 13 14 Net Run Time, minutes 57.75 58.25 59.25 Nozzle Diameter, inches 0.243 0.243 0.243 0.243 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.972 0.972 0.972 0.972 Barometric Pressure, inches of Mercury 29.91 29.91 29.91 29.910 Average Orifice Meter Differential, inches H2O 0.42 0.42 0.42 0.420 Dry Gas Meter Volume Sampled, cubic feet 21.768 22.062 22.519 22.116 Average Dry Gas Meter Temperature, °F 75.00 72.38 77.07 74.817 Dry Gas Meter Volume Sampled, dscf 20.896 21.283 21.534 21.238 Total Moisture Liquid collected, g 55.4 60.4 47.6 54.467 Volume of Water Vapor, standard cubic feet 2.61 2.84 2.24 2.563 Moisture Content of Stack Gas, % 11.10 11.77 9.42 10.763 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.889 0.8823 0.9058 0.892 Carbon Dioxide, % 10.9 10 10.1 10.333 Oxygen, % 6.7 7 7.6 7.100 Carbon Monoxide & Nitrogen, % 82.4 83 82.3 82.567 Fuel Factor 1.30 1.39 1.32 Dry Molecular Weight, lb/lb-Mole 30.01 29.88 29.92 29.937 Wet Molecular weight, lb/lb-Mole 28.68 28.48 28.80 28.653 Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200 Absolute Flue Gas Pressure, inches of Mercury 29.90 29.90 29.90 29.900 Average Stack Gas Temperature, °F 317.69 319.46 304.21 313.787 Average Velocity Head, inches of H2O 0.2032665672 139480.194654446

5474870.210829116

831624 0.203

Average Stack Gas Velocity, feet/second 30.83 30.31 31.06 30.733 Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500 Dry Volumetric Flow Rate, dry scfm 156,761.7 152,608.8 163,754.1157,708.200 Actual Wet Volumetric Flue Gas Flow Rate, acfm 259,896.9 255,513.3 261,835.8259,082.000 Percent Isokinetic of Sampling Rate, % 100.7 104.4 96.8 100.633 Percent Excess Air, % 44.5 46.9 53.8 48.400 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 160.5 160.5 160.5 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000



### Monday, February 07, 2011 Page 33 of 34

### LocationStack - OTM - 28 Average

Run Number 1 2 3 Test Date 4/13/2010 4/14/2010 4/14/2010 Run Start Time 12:15:00 PM6:42:00 AM12:19:00 PM Run Finish Time 5:19:00 PM11:58:00 AM 3:01:00 PM Net Traversing Points 48 48 25 Net Run Time, minutes 240 240 125 Nozzle Diameter, inches 0.31 0.31 0.31 0.310 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.972 0.972 0.972 0.972 Barometric Pressure, inches of Mercury 30.24 30.24 30.24 30.240 Average Orifice Meter Differential, inches H2O 1.26 1.18 1.24 1.227 Dry Gas Meter Volume Sampled, cubic feet 151.251 142.149 75.439 122.946 Average Dry Gas Meter Temperature, °F 83.35 81.88 82.04 82.423 Dry Gas Meter Volume Sampled, dscf 144.833 136.460 72.409 117.901 Total Moisture Liquid collected, g 296.8 323.7 155.6 258.700 Volume of Water Vapor, standard cubic feet 13.97 15.24 7.32 12.177 Moisture Content of Stack Gas, % 8.80 10.05 9.18 9.343 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.912 0.8995 0.9082 0.907 Carbon Dioxide, % 10.5 10.8 10.5 10.600 Oxygen, % 7.3 7.1 7.1 7.167 Carbon Monoxide & Nitrogen, % 82.2 82.1 82.4 82.233 Fuel Factor 1.30 1.28 1.31 Dry Molecular Weight, lb/lb-Mole 29.97 30.01 29.96 29.980 Wet Molecular weight, lb/lb-Mole 28.92 28.80 28.86 28.860 Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200 Absolute Flue Gas Pressure, inches of Mercury 30.23 30.23 30.23 30.230 Average Stack Gas Temperature, °F 335.81 320.42 330.92 329.050 Average Velocity Head, inches of H2O 0.2032818342 006270.189553260

1510690.200363552

027636 0.198

Average Stack Gas Velocity, feet/second 30.89 29.60 30.61 30.367 Stack Cross-Sectional Area, square feet 140.500 140.500 140.500 140.500 Dry Volumetric Flow Rate, dry scfm 159,199.4 153,427.3 158,070.3156,899.000 Actual Wet Volumetric Flue Gas Flow Rate, acfm 260,402.7 249,528.0 258,042.3255,991.000 Percent Isokinetic of Sampling Rate, % 101.6 99.3 98.2 99.700 Percent Excess Air, % 50.7 48.7 48.5 49.300 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 160.5 160.5 160.5 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 1032010,320.000 Fc 1420 1420 14201,420.000



### Monday, February 07, 2011 Page 34 of 34