### 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.

Friday, January 14, 2011 Page 1 of 47

### Facility Information:

AES Deepwater 701 Light Company Rd

Pasadena TX 77506 Contact: Ken Niznik Phone: (713)472-8687 Fax: Email: Testing Company: URS Corporation 1600 Perimeter Park Drive, Suite 400

Morrisville NC 27560 Contact: Brad Justus Phone: 919-461-1326 Fax: 919-461-1415 Email: brad_justus@urscorp.com

Air Permit Number: 10670 Permitted Source ID/Name: Unit 1 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: Units 1 is rated at 160 MW (gross), combusts 100% pulverized petroleum coke, and consists of a wall-fired combustor equipped with LNB/OFA, a dry ESP, selective catalytic reduction (SCR), wet FGD, and a wet ESP to reduce air emissions. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 4820100405 FRS #: 110000462785

SCC / Description 10100801 External Combustion Boilers - Electric Generation - Petroleum Coke - All Boiler Sizes

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 Exit 204 1632 408 4 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location % H2O Method 1 - 4 3 180 0 Stack Exit Carbon Monoxide Method 10 3 120 0 Stack Exit 2,3,7,8-TCDD Method 23 3 480 0 Stack Exit 1,2,3,7,8-PeCDD Method 23 3 480 0 Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0 Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0 Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 480 0 Stack Exit



### Friday, January 14, 2011 Page 2 of 471,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Stack Exit OCDD Method 23 3 480 0 Stack Exit 2,3,7,8-TCDF Method 23 3 480 0 Stack Exit 1,2,3,7,8-PeCDF Method 23 3 480 0 Stack Exit 2,3,4,7,8-PeCDF Method 23 3 480 0 Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 480 0 Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 480 0 Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 480 0 Stack Exit 1,2,3,7,8,9-HxCDF Method 23 3 480 0 Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0 Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0 Stack Exit OCDF Method 23 3 480 0 Stack Exit Other TCDD Method 23 3 480 0 Stack Exit Other PeCDD Method 23 3 480 0 Stack Exit Other HxCDD Method 23 3 480 0 Stack Exit Other HpCDD Method 23 3 480 0 Stack Exit Other TCDF Method 23 3 480 0 Stack Exit Other PeCDF Method 23 3 480 0 Stack Exit Other HxCDF Method 23 3 480 0 Stack Exit Other HpCDF Method 23 3 480 0 Stack Exit Total Dioxins Method 23 3 480 0 Stack Exit Total Furans Method 23 3 480 0 Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0 Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0 Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0 Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0 Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0 Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0 Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0 Stack Exit 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 480 0 Stack Exit

2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0 Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0 Stack Exit 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 0 Stack Exit

Total PCBs Method 23 3 480 0 Stack Exit Total organic compounds

(TOC) as Propane Method 25A 3 120 0 Stack Exit
Hydrogen Chloride Method 26A 3 180 0 Stack Exit Hydrogen Fluoride Method 26A 3 180 0 Stack Exit Antimony Method 29 3 240 0 Stack Exit Beryllium Method 29 3 240 0 Stack Exit Cadmium Method 29 3 240 0 Stack Exit Chromium Method 29 3 240 0 Stack Exit Lead Method 29 3 240 0 Stack Exit Manganese Method 29 3 240 0 Stack Exit Nickel Method 29 3 240 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit Filterable Particulate Method 29 3 240 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit Cobalt Method 29 3 240 0 Stack Exit Co2 Method 3A CO2 3 480 0 Stack Exit O2 Method 3A O2 3 480 0 Stack Exit


### Friday, January 14, 2011 Page 3 of 47

### 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.
None O2 Method 3A O2 3 120 0 Stack Exit Co2 Method 3A CO2 3 120 0 Stack Exit Co2 Method 3A CO2 3 240 0 Stack Exit O2 Method 3A O2 3 240 0 Stack Exit Filterable Particulate Method 5/OTM-28 3 240 0 Stack Exit Total Particulate Method 5/OTM-28 3 240 0 Stack Exit Inorganic (Aqueous)

Condensible Part. Method 5/OTM-28 3 240 0 Stack Exit
Organic Condensible

Particulate Method 5/OTM-28 3 240 0 Stack Exit

Sulfur Dioxide Method 6C 3 180 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### Friday, January 14, 2011 Page 4 of 47

### Sampling / Stack Data Results Summary



### Location Stack Exit - Method 10 Average Run Number 1 Form 2 Form 3 Form
Test Date 7/24/2010 7/24/2010 7/24/2010 Run Start Time 7:53:00 AM 10:25:00 AM 1:24:00 PM

Run Finish Time 10:07:00 AM 12:47:00 PM 3:37:00 PM

Carbon Dioxide, % 12.81 13.15 13.18 13.047 Oxygen, % 6.72 6.32 6.24 6.427 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000 Moisture, % 0 0 0 0.000 Fuel Type Override Override Override
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Location Stack Exit - Method 23 Average Run Number 1 2 3
Test Date 7/24/2010 7/25/2010 7/26/2010 Run Start Time 8:53:00 AM 8:05:00 AM 7:03:00 AM

Run Finish Time 5:39:00 PM 5:17:00 PM 5:56:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 287.616 302.781 305.320 298.572 Moisture Content of Stack Gas, % 13.34 13.18 13.58 13.367 Moisture Saturation at Stack Gas Temperature, % 31.84 31.37 31.22 31.477 Carbon Dioxide, % 13 13 13 13.000 Oxygen, % 6.4 6.3 6.3 6.333 Average Stack Gas Temperature, °F 158.76 158.10 157.91 158.257 Dry Volumetric Flow Rate, dry scfm 451,824.6 446,296.5 440,530.8 446,217.300 Actual Wet Volumetric Flue Gas Flow Rate, acfm 622,651.5 613,663.1 608,351.8 614,888.800 Percent Isokinetic of Sampling Rate, % 95.8 96.4 98.5 96.900 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Friday, January 14, 2011 Page 5 of 47

### Location Stack Exit - Method 25A Average

Run Number 1 2 3
Test Date 7/24/2010 7/24/2010 7/24/2010 Run Start Time 7:53:00 AM 10:25:00 AM 1:24:00 PM

Run Finish Time 10:07:00 AM 12:47:00 PM 3:37:00 PM

Carbon Dioxide, % 12.81 13.15 13.18 13.047 Oxygen, % 6.72 6.32 6.24 6.427 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000 Moisture, % 0 0 0 0.000 Fuel Type Override Override Override
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Location Stack Exit - Method 26A Average Run Number 1 2 3
Test Date 8/18/2010 8/19/2010 8/19/2010 Run Start Time 2:36:00 PM 8:55:00 AM 12:23:00 PM

Run Finish Time 5:50:00 PM 12:08:00 PM 3:33:00 PM

Net Run Time, minutes 180 180 180 Dry Gas Meter Volume Sampled, dscf 104.282 106.823 108.390 106.498 Moisture Content of Stack Gas, % 13.02 13.23 13.56 13.270 Moisture Saturation at Stack Gas Temperature, % 30.95 30.29 30.35 30.530 Carbon Dioxide, % 12.3 11.9 11.9 12.033 Oxygen, % 6.9 6.9 6.7 6.833 Average Stack Gas Temperature, °F 158.08 157.17 157.28 157.510 Dry Volumetric Flow Rate, dry scfm 462,071.5 474,430.2 480,363.9 472,288.533 Actual Wet Volumetric Flue Gas Flow Rate, acfm 626,056.2 643,624.5 653,838.6 641,173.100 Percent Isokinetic of Sampling Rate, % 99.5 99.3 99.5 99.433 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Friday, January 14, 2011 Page 6 of 47

### Location Stack Exit - Method 29 Average

Run Number 1 2 3
Test Date 8/3/2010 8/3/2010 8/4/2010 Run Start Time 7:40:00 AM 1:23:00 PM 7:32:00 AM
Run Finish Time 12:05:00 PM 6:11:00 PM 12:00:00 PM Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 162.570 162.529 168.316 164.472 Moisture Content of Stack Gas, % 13.65 11.88 13.69 13.073 Moisture Saturation at Stack Gas Temperature, % 33.38 33.74 33.58 33.567 Carbon Dioxide, % 12.7 13 12.8 12.833 Oxygen, % 6.6 6.5 6.9 6.667 Average Stack Gas Temperature, °F 160.73 161.15 160.98 160.953 Dry Volumetric Flow Rate, dry scfm 472,730.2 478,564.5 481,343.7 477,546.133 Actual Wet Volumetric Flue Gas Flow Rate, acfm 655,881.4 651,523.4 668,410.7 658,605.167 Percent Isokinetic of Sampling Rate, % 97.7 96.5 99.4 97.867 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Location Stack Exit - Method 3A CO2 Average Run Number 1 DF 1 Form 1 Hg
Test Date 7/24/2010 7/24/2010 7/25/2010 Run Start Time 8:53:00 AM 7:53:00 AM 7:18:00 AM

Run Finish Time 5:39:00 PM 10:07:00 AM 9:40:00 AM

Carbon Dioxide, % 13.11 12.81 12.81 12.910 Oxygen, % 6.33 6.72 6.65 6.567 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Moisture, % 0 0 0 0.000 Fuel Type Coal - Bituminous Coal -

Bituminous Coal -

Bituminous
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Friday, January 14, 2011 Page 7 of 47

### Location Stack Exit - Method 3A CO2 3 Average

Run Number 1 ORG 1 PM 2 DF
Test Date 7/23/2010 8/3/2010 7/25/2010 Run Start Time 8:13:00 AM 7:40:00 AM 8:05:00 AM

Run Finish Time 10:54:00 AM 12:05:00 PM 5:17:00 PM

Carbon Dioxide, % 13.04 12.84 13.1 12.993 Oxygen, % 6.46 6.62 6.27 6.450 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Moisture, % 0 0 0 0.000 Fuel Type Coal - Bituminous Coal -

Bituminous Coal -

Bituminous
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Location Stack Exit - Method 3A CO2 3 6 Average Run Number 2 Form 2 Hg 2 ORG
Test Date 7/24/2010 7/25/2010 7/23/2010 Run Start Time 10:25:00 AM 10:53:00 AM 11:36:00 AM

Run Finish Time 12:47:00 PM 1:07:00 PM 1:52:00 PM Carbon Dioxide, % 13.15 13.16 13.14 13.150 Oxygen, % 6.32 6.23 6.29 6.280 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Moisture, % 0 0 0 0.000 Fuel Type Coal - Bituminous Coal -

Bituminous Coal -

Bituminous
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Friday, January 14, 2011 Page 8 of 47

### Location Stack Exit - Method 3A CO2 3 6 9 Average

Run Number 2 PM 3 DF 3 Form
Test Date 8/3/2010 7/26/2010 7/24/2010 Run Start Time 1:23:00 PM 6:21:00 AM 1:24:00 PM

Run Finish Time 6:11:00 PM 6:01:00 PM 3:37:00 PM Carbon Dioxide, % 12.97 13.07 13.18 13.073 Oxygen, % 6.4 6.31 6.24 6.317 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Moisture, % 0 0 0 0.000 Fuel Type Coal - Bituminous Coal -

Bituminous Coal -

Bituminous
Fw 10640 10640 10640 10,640.000
Fc 1800 1800 1800 1,800.000



### Location Stack Exit - Method 3A CO2 3 6 9 12 Average Run Number 3 Hg 3 ORG 3 PM
Test Date 7/25/2010 7/23/2010 8/4/2010 Run Start Time 1:46:00 PM 2:39:00 PM 7:32:00 AM
Run Finish Time 3:52:00 PM 5:37:00 PM 12:00:00 PM Carbon Dioxide, % 13.19 13.15 12.9 13.080 Oxygen, % 6.16 6.23 6.52 6.303 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 Moisture, % 0 0 0 0.000 Fuel Type
Fw
Fc



### Friday, January 14, 2011 Page 9 of 47

### Location Stack Exit - Method 3A O2 Average

Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Location Stack Exit - Method 3A O2 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



### Friday, January 14, 2011 Page 10 of 47

### Location Stack Exit - Method 3A O2 3 6 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 Stack Exit - Method 3A O2 3 6 9 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



### Friday, January 14, 2011 Page 11 of 47

### Location Stack Exit - Method 3A O2 3 6 9 12 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 Stack Exit - Method 5/OTM-28 Average Run Number 1 2 3
Test Date 8/3/2010 8/3/2010 8/4/2010 Run Start Time 7:40:00 AM 1:23:00 PM 7:32:00 AM
Run Finish Time 12:05:00 PM 6:11:00 PM 12:00:00 PM Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 154.524 147.779 151.689 151.331 Moisture Content of Stack Gas, % 13.63 13.52 13.65 13.600 Moisture Saturation at Stack Gas Temperature, % 33.64 34.32 33.64 33.867 Carbon Dioxide, % 13 13 12.8 12.933 Oxygen, % 6.4 6.3 6.6 6.433 Average Stack Gas Temperature, °F 161.06 161.90 161.06 161.340 Dry Volumetric Flow Rate, dry scfm 450,901.9 448,805.9 455,800.9 451,836.233 Actual Wet Volumetric Flue Gas Flow Rate, acfm 625,783.9 622,923.9 632,729.4 627,145.733 Percent Isokinetic of Sampling Rate, % 97.4 93.6 94.6 95.200 F-Factor, dscfm/MMBtu @ %O2 99360 9936 9936 39,744.000
Fw 0 0 0 0.000
Fc 0 0 0 0.000



### Friday, January 14, 2011 Page 12 of 47

### Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run 1 Form 2 Form 3 Form lb/mmBtuO2 5.92E-02 1.74E-01 1.81E-01 0.138 ppm 5.56E+01 1.68E+02 1.75E+02 132.867 ppm@7%O2 5.45E+01 1.60E+02 1.66E+02 126.833



### Location: Stack Exit - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.00000000277 0.00000000244 0.00000000401 0.000 lb/mmBtuO2 3.04E-13 2.53E-13 4.12E-13 0.000 ng/dscm 3.40E-04 2.85E-04 4.64E-04 0.000 ng/dscm@7%O2 3.26E-04 2.71E-04 4.42E-04 0.000 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000175 0.00000000672 0.0000000154 0.000 lb/mmBtuO2 1.92E-12 6.96E-13 1.58E-12 0.000 ng/dscm 2.15E-03 7.84E-04 1.78E-03 0.002 ng/dscm@7%O2 2.06E-03 7.46E-04 1.69E-03 0.001 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000112 0.00000000989 0.0000000209 0.000 lb/mmBtuO2 1.23E-12 1.02E-12 2.15E-12 0.000 ng/dscm 1.38E-03 1.15E-03 2.42E-03 0.002 ng/dscm@7%O2 1.32E-03 1.09E-03 2.30E-03 0.002 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.00000000215 0.00000000212 0.00000000287 0.000 lb/mmBtuO2 2.36E-13 2.20E-13 2.95E-13 0.000 ng/dscm 2.64E-04 2.47E-04 3.32E-04 0.000 ng/dscm@7%O2 2.53E-04 2.35E-04 3.16E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000297 0.00000000118 0.00000000195 0.000 lb/mmBtuO2 3.26E-13 1.22E-13 2.00E-13 0.000 ng/dscm 3.65E-04 1.38E-04 2.26E-04 0.000 ng/dscm@7%O2 3.50E-04 1.31E-04 2.15E-04 0.000 

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


### Friday, January 14, 2011 Page 13 of 47RunNumber 1 2 3 Mass_mg 0.00000000212 0.00000000207 0.00000000308 0.000 lb/mmBtuO2 2.33E-13 2.14E-13 3.16E-13 0.000 ng/dscm 2.60E-04 2.41E-04 3.56E-04 0.000 ng/dscm@7%O2 2.49E-04 2.29E-04 3.39E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000113 0.00000000111 0.00000000205 0.000 lb/mmBtuO2 1.24E-13 1.15E-13 2.11E-13 0.000 ng/dscm 1.39E-04 1.29E-04 2.37E-04 0.000 ng/dscm@7%O2 1.33E-04 1.23E-04 2.26E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.00000000215 0.00000000203 0.00000000286 0.000 lb/mmBtuO2 2.36E-13 2.10E-13 2.94E-13 0.000 ng/dscm 2.64E-04 2.37E-04 3.31E-04 0.000 ng/dscm@7%O2 2.53E-04 2.26E-04 3.15E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000144 0.00000000131 0.00000000223 0.000 lb/mmBtuO2 1.58E-13 1.36E-13 2.29E-13 0.000 ng/dscm 1.77E-04 1.53E-04 2.58E-04 0.000 ng/dscm@7%O2 1.70E-04 1.46E-04 2.46E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.00000000266 0.00000000217 0.00000000345 0.000 lb/mmBtuO2 2.92E-13 2.25E-13 3.54E-13 0.000 ng/dscm 3.27E-04 2.53E-04 3.99E-04 0.000 ng/dscm@7%O2 3.13E-04 2.41E-04 3.80E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.00000000228 0.000000002 0.00000000299 0.000 lb/mmBtuO2 2.50E-13 2.07E-13 3.07E-13 0.000 ng/dscm 2.80E-04 2.33E-04 3.46E-04 0.000 ng/dscm@7%O2 2.68E-04 2.22E-04 3.29E-04 0.000 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 2 3 Mass_mg 0.00000000728 0.00000000673 0.00000000751 0.000 lb/mmBtuO2 7.99E-13 6.97E-13 7.71E-13 0.000 ng/dscm 8.94E-04 7.85E-04 8.69E-04 0.001 ng/dscm@7%O2 8.57E-04 7.47E-04 8.27E-04 0.001



### Friday, January 14, 2011 Page 14 of 47

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 2 3 Mass_mg 0.0000000143 0.0000000148 0.0000000155 0.000 lb/mmBtuO2 1.57E-12 1.53E-12 1.59E-12 0.000 ng/dscm 1.76E-03 1.73E-03 1.79E-03 0.002 ng/dscm@7%O2 1.69E-03 1.65E-03 1.70E-03 0.002 

### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 2 3 Mass_mg 0.000000072 0.000000095 0.000000102 0.000 lb/mmBtuO2 7.90E-12 9.84E-12 1.05E-11 0.000 ng/dscm 8.84E-03 1.11E-02 1.18E-02 0.011 ng/dscm@7%O2 8.47E-03 1.06E-02 1.12E-02 0.010 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 2 3 Mass_mg 0.00000000396 0.0000000044 0.00000000592 0.000 lb/mmBtuO2 4.35E-13 4.56E-13 6.08E-13 0.000 ng/dscm 4.86E-04 5.13E-04 6.85E-04 0.001 ng/dscm@7%O2 4.66E-04 4.88E-04 6.52E-04 0.001 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 2 3 Mass_mg 0.00000000399 0.00000000903 0.00000000898 0.000 lb/mmBtuO2 4.38E-13 9.35E-13 9.22E-13 0.000 ng/dscm 4.90E-04 1.05E-03 1.04E-03 0.001 ng/dscm@7%O2 4.70E-04 1.00E-03 9.90E-04 0.001 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 2 3 Mass_mg 0.000000164 0.000000229 0.000000258 0.000 lb/mmBtuO2 1.80E-11 2.37E-11 2.65E-11 0.000 ng/dscm 2.01E-02 2.67E-02 2.98E-02 0.026 ng/dscm@7%O2 1.93E-02 2.54E-02 2.84E-02 0.024 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 2 3 Mass_mg 0.00000000393 0.00000000724 0.0000000085 0.000 lb/mmBtuO2 4.31E-13 7.50E-13 8.73E-13 0.000 ng/dscm 4.83E-04 8.45E-04 9.83E-04 0.001 ng/dscm@7%O2 4.63E-04 8.04E-04 9.36E-04 0.001 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000116 0.00000000116 0.00000000195 0.000 lb/mmBtuO2 1.27E-13 1.20E-13 2.00E-13 0.000



### Friday, January 14, 2011 Page 15 of 47ng/dscm 1.42E-04 1.35E-04 2.26E-04 0.000 ng/dscm@7%O2 1.36E-04 1.29E-04 2.15E-04 0.000 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.00000000215 0.00000000193 0.00000000296 0.000 lb/mmBtuO2 2.36E-13 2.00E-13 3.04E-13 0.000 ng/dscm 2.64E-04 2.25E-04 3.42E-04 0.000 ng/dscm@7%O2 2.53E-04 2.14E-04 3.26E-04 0.000 

### Compound: 2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.00000000192 0.00000000184 0.00000000308 0.000 lb/mmBtuO2 2.11E-13 1.91E-13 3.16E-13 0.000 ng/dscm 2.36E-04 2.15E-04 3.56E-04 0.000 ng/dscm@7%O2 2.26E-04 2.05E-04 3.39E-04 0.000 

### Compound: 2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.00000000151 0.00000000216 0.00000000279 0.000 lb/mmBtuO2 1.66E-13 2.24E-13 2.87E-13 0.000 ng/dscm 1.85E-04 2.52E-04 3.23E-04 0.000 ng/dscm@7%O2 1.77E-04 2.40E-04 3.08E-04 0.000 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 2 3 Mass_mg 0.00000000399 0.00000000409 0.00000000561 0.000 lb/mmBtuO2 4.38E-13 4.24E-13 5.76E-13 0.000 ng/dscm 4.90E-04 4.77E-04 6.49E-04 0.001 ng/dscm@7%O2 4.70E-04 4.54E-04 6.18E-04 0.001 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 2 3 Mass_mg 0.00000000315 0.00000000653 0.00000000953 0.000 lb/mmBtuO2 3.46E-13 6.76E-13 9.79E-13 0.000 ng/dscm 3.87E-04 7.62E-04 1.10E-03 0.001 ng/dscm@7%O2 3.71E-04 7.25E-04 1.05E-03 0.001 

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 1 2 3 Mass_mg 0.0000000298 0.0000000455 0.000000047 0.000 lb/mmBtuO2 3.27E-12 4.71E-12 4.83E-12 0.000 ng/dscm 3.66E-03 5.31E-03 5.44E-03 0.005 ng/dscm@7%O2 3.51E-03 5.06E-03 5.18E-03 0.005 

### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber 1 2 3


### Friday, January 14, 2011 Page 16 of 47Mass_mg 0.00000000188 0.0000000038 0.00000000493 0.000 lb/mmBtuO2 2.06E-13 3.94E-13 5.06E-13 0.000 ng/dscm 2.31E-04 4.43E-04 5.70E-04 0.000 ng/dscm@7%O2 2.21E-04 4.22E-04 5.43E-04 0.000 

### Compound: OCDD Average RunNumber 1 2 3 Mass_mg 0.0000000164 0.00000000945 0.00000000988 0.000 lb/mmBtuO2 1.80E-12 9.79E-13 1.01E-12 0.000 ng/dscm 2.01E-03 1.10E-03 1.14E-03 0.001 ng/dscm@7%O2 1.93E-03 1.05E-03 1.09E-03 0.001 

### Compound: OCDF Average RunNumber 1 2 3 Mass_mg 0.0000000346 0.0000000109 0.0000000187 0.000 lb/mmBtuO2 3.80E-12 1.13E-12 1.92E-12 0.000 ng/dscm 4.25E-03 1.27E-03 2.16E-03 0.003 ng/dscm@7%O2 4.07E-03 1.21E-03 2.06E-03 0.002 

### Compound: Other HpCDD Average RunNumber 1 2 3 Mass_mg 0 0.0000000029 0 0.000 lb/mmBtuO2 0.00E+00 3.00E-13 0.00E+00 0.000 ng/dscm 0.00E+00 3.38E-04 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 3.22E-04 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 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 HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000477 0.00000000183 0 0.000 lb/mmBtuO2 5.24E-13 1.90E-13 0.00E+00 0.000 ng/dscm 5.86E-04 2.13E-04 0.00E+00 0.000 ng/dscm@7%O2 5.62E-04 2.03E-04 0.00E+00 0.000



### Friday, January 14, 2011 Page 17 of 47

### 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 0.0000000051 0.00000000973 0.0000000174 0.000 lb/mmBtuO2 5.60E-13 1.01E-12 1.79E-12 0.000 ng/dscm 6.26E-04 1.14E-03 2.01E-03 0.001 ng/dscm@7%O2 6.00E-04 1.09E-03 1.91E-03 0.001 

### Compound: Other TCDF 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: Total Dioxins Average RunNumber 1 2 3 Mass_mg 0.00000003527 0.00000003475 0.00000004663 0.000 lb/mmBtuO2 3.87E-12 3.60E-12 4.79E-12 0.000 ng/dscm 4.33E-03 4.05E-03 5.39E-03 0.005 ng/dscm@7%O2 4.15E-03 3.86E-03 5.13E-03 0.004 

### Compound: Total Furans Average RunNumber 1 2 3 Mass_mg 0.00000008071 0.00000004019 0.00000007192 0.000 lb/mmBtuO2 8.86E-12 4.16E-12 7.39E-12 0.000 ng/dscm 9.91E-03 4.69E-03 8.32E-03 0.008 ng/dscm@7%O2 9.50E-03 4.47E-03 7.92E-03 0.007 

### Compound: Total PCBs Average RunNumber 1 2 3 Mass_mg 0.0000003083 0.0000004261 0.0000004735 0.000 lb/mmBtuO2 3.38E-11 4.41E-11 4.86E-11 0.000



### Friday, January 14, 2011 Page 18 of 47ng/dscm 3.79E-02 4.97E-02 5.48E-02 0.047 ng/dscm@7%O2 3.63E-02 4.73E-02 5.22E-02 0.045



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average Run 1 2 3 lb/mmBtuO2 2.79E-04 3.20E-04 3.21E-04 0.000 ppm 1.66E-01 1.96E-01 1.98E-01 0.187 ppm@7%O2 1.63E-01 1.87E-01 1.88E-01 0.179



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 0.0598 0.064 0.0601 0.061 Elb/hr 3.50E-02 3.76E-02 3.52E-02 0.036 lb/mmBtuO2 1.88E-05 1.96E-05 1.79E-05 0.000 mg/dscm 2.03E-02 2.12E-02 1.96E-02 0.020 mg/dscm@7%O2 2.02E-02 2.10E-02 1.92E-02 0.020 

### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 0.158 0.169 0.159 0.162 Elb/hr 9.26E-02 9.93E-02 9.32E-02 0.095 lb/mmBtuO2 4.95E-05 5.17E-05 4.73E-05 0.000 mg/dscm 5.35E-02 5.59E-02 5.18E-02 0.054 mg/dscm@7%O2 5.31E-02 5.55E-02 5.07E-02 0.053



### Location: Stack Exit - Method 29 

### Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.00007 0.00015 0.00006 0.000 Elb/hr 2.69E-05 5.84E-05 2.27E-05 0.000 lb/mmBtuO2 1.38E-08 2.93E-08 1.17E-08 0.000 mg/dscm 1.52E-05 3.26E-05 1.26E-05 0.000 mg/dscm@7%O2 1.48E-05 3.15E-05 1.25E-05 0.000 

### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.00028 0.00016 0.0002 0.000 Elb/hr 1.08E-04 6.23E-05 7.57E-05 0.000 lb/mmBtuO2 5.51E-08 3.13E-08 3.89E-08 0.000 mg/dscm 6.08E-05 3.48E-05 4.20E-05 0.000 mg/dscm@7%O2 5.91E-05 3.36E-05 4.17E-05 0.000 

### Compound: Beryllium Average RunNumber 1 2 3



### Friday, January 14, 2011 Page 19 of 47Mass_mg 0.00003 0.00003 0.00003 0.000 Elb/hr 1.15E-05 1.17E-05 1.13E-05 0.000 lb/mmBtuO2 5.91E-09 5.87E-09 5.83E-09 0.000 mg/dscm 6.52E-06 6.52E-06 6.30E-06 0.000 mg/dscm@7%O2 6.34E-06 6.29E-06 6.26E-06 0.000 

### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.00008 0.0001 0.00014 0.000 Elb/hr 3.08E-05 3.89E-05 5.30E-05 0.000 lb/mmBtuO2 1.58E-08 1.96E-08 2.72E-08 0.000 mg/dscm 1.74E-05 2.17E-05 2.94E-05 0.000 mg/dscm@7%O2 1.69E-05 2.09E-05 2.92E-05 0.000 

### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.00685 0.00799 0.00335 0.006 Elb/hr 2.63E-03 3.11E-03 1.27E-03 0.002 lb/mmBtuO2 1.35E-06 1.56E-06 6.51E-07 0.000 mg/dscm 1.49E-03 1.74E-03 7.03E-04 0.001 mg/dscm@7%O2 1.45E-03 1.68E-03 6.98E-04 0.001 

### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.00033 0.0002 0.00032 0.000 Elb/hr 1.27E-04 7.79E-05 1.21E-04 0.000 lb/mmBtuO2 6.50E-08 3.91E-08 6.22E-08 0.000 mg/dscm 7.17E-05 4.35E-05 6.71E-05 0.000 mg/dscm@7%O2 6.97E-05 4.20E-05 6.66E-05 0.000 

### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 47.5 33.3 40.2 40.333 Elb/hr 1.83E+01 1.30E+01 1.52E+01 15.500 lb/mmBtuO2 9.35E-03 6.51E-03 7.81E-03 0.008 mg/dscm 1.03E+01 7.24E+00 8.44E+00 8.660 mg/dscm@7%O2 1.00E+01 6.99E+00 8.38E+00 8.457 

### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.00266 0.00121 0.00174 0.002 Elb/hr 1.02E-03 4.71E-04 6.58E-04 0.001 lb/mmBtuO2 5.24E-07 2.37E-07 3.38E-07 0.000 mg/dscm 5.78E-04 2.63E-04 3.65E-04 0.000 mg/dscm@7%O2 5.62E-04 2.54E-04 3.62E-04 0.000 

### Compound: Manganese Average RunNumber 1 2 3



### Friday, January 14, 2011 Page 20 of 47Mass_mg 0.01074 0.00614 0.00714 0.008 Elb/hr 4.13E-03 2.39E-03 2.70E-03 0.003 lb/mmBtuO2 2.12E-06 1.20E-06 1.39E-06 0.000 mg/dscm 2.33E-03 1.33E-03 1.50E-03 0.002 mg/dscm@7%O2 2.26E-03 1.28E-03 1.49E-03 0.002 

### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 0.0155 0.0148 0.0089 0.013 Elb/hr 5.96E-03 5.76E-03 3.37E-03 0.005 lb/mmBtuO2 3.05E-06 2.90E-06 1.73E-06 0.000 mg/dscm 3.37E-03 3.22E-03 1.87E-03 0.003 mg/dscm@7%O2 3.28E-03 3.11E-03 1.86E-03 0.003 

### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 0.00616 0.00336 0.00576 0.005 Elb/hr 2.37E-03 1.31E-03 2.18E-03 0.002 lb/mmBtuO2 1.21E-06 6.57E-07 1.12E-06 0.000 mg/dscm 1.34E-03 7.30E-04 1.21E-03 0.001 mg/dscm@7%O2 1.30E-03 7.05E-04 1.20E-03 0.001



### Location: Stack Exit - Method 5/OTM-28 Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 13.2 8.5 10.2 10.633 Elb/hr 5.10E+00 3.41E+00 4.05E+00 4.187 gr/dscf 1.32E-03 8.88E-04 1.04E-03 0.001 lb/mmBtuO2 2.70E-02 1.80E-03 2.15E-03 0.010 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 124.4 113.4 38.5 92.100 Elb/hr 4.80E+01 4.56E+01 1.53E+01 36.300 gr/dscf 1.24E-02 1.18E-02 3.92E-03 0.009 lb/mmBtuO2 2.54E-01 2.41E-02 8.13E-03 0.095 

### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 2.3 3.1 1.5 2.300 Elb/hr 8.88E-01 1.25E+00 5.96E-01 0.911 gr/dscf 2.30E-04 3.24E-04 1.53E-04 0.000 lb/mmBtuO2 4.70E-03 6.58E-04 3.17E-04 0.002 

### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 139.9 125 50.2 105.033



### Friday, January 14, 2011 Page 21 of 47

### Process Run Data Elb/hr 5.40E+01 5.02E+01 2.00E+01 41.400 gr/dscf 1.40E-02 1.31E-02 5.11E-03 0.011 lb/mmBtuO2 2.86E-01 2.65E-02 1.06E-02 0.108



### Friday, January 14, 2011 Page 22 of 47

### Process Run Data



### Run Name Value UOM Comments Target Value 1 Heat Input 1875 Million Btus/hr 0


### 10 Heat Input 1727 Million Btus/hr 0
11 Heat Input 1899 Million Btus/hr 0
12 Heat Input 1899 Million Btus/hr 0


### 13 Heat Input 1899 Million Btus/hr 0
14 Heat Input 1888 Million Btus/hr 0
15 Heat Input 1898 Million Btus/hr 0


### 16 Heat Input 1892 Million Btus/hr 0
17 Heat Input 1899 Million Btus/hr 0
18 Heat Input 1899 Million Btus/hr 0


### 2 Heat Input 1899 Million Btus/hr 0
3 Heat Input 1899 Million Btus/hr 0
4 Heat Input 1869 Million Btus/hr 0


### 5 Heat Input 1849 Million Btus/hr 0
6 Heat Input 1829 Million Btus/hr 0
7 Heat Input 1727 Million Btus/hr 0


### 8 Heat Input 1899 Million Btus/hr 0
9 Heat Input 1899 Million Btus/hr 0
1 Steam Output 1366 1000 lb steam/hr 0


### 10 Steam Output 1346 1000 lb steam/hr 0
11 Steam Output 1411 1000 lb steam/hr 0
12 Steam Output 1413 1000 lb steam/hr 0


### 13 Steam Output 1418 1000 lb steam/hr 0
14 Steam Output 1296 1000 lb steam/hr 0


### 15 Steam Output 1417 1000 lb steam/hr 0
16 Steam Output 1346 1000 lb steam/hr 0
17 Steam Output 1411 1000 lb steam/hr 0


### 18 Steam Output 1413 1000 lb steam/hr 0
2 Steam Output 1412 1000 lb steam/hr 0
3 Steam Output 1361 1000 lb steam/hr 0


### 4 Steam Output 1360 1000 lb steam/hr 0
5 Steam Output 1342 1000 lb steam/hr 0
6 Steam Output 1395 1000 lb steam/hr 0



### Friday, January 14, 2011 Page 23 of 47

### 7 Steam Output 1346 1000 lb steam/hr 0



### 8 Steam Output 1411 1000 lb steam/hr 0
9 Steam Output 1413 1000 lb steam/hr 0
1 Standard Pressure 1 atm 0


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


### 13 Standard Pressure 1 atm 0
14 Standard Pressure 1 atm 0
15 Standard Pressure 1 atm 0


### 16 Standard Pressure 1 atm 0
17 Standard Pressure 1 atm 0
18 Standard Pressure 1 atm 0


### 2 Standard Pressure 1 atm 0
3 Standard Pressure 1 atm 0
4 Standard Pressure 1 atm 0


### 5 Standard Pressure 1 atm 0
6 Standard Pressure 1 atm 0
7 Standard Pressure 1 atm 0


### 8 Standard Pressure 1 atm 0
9 Standard Pressure 1 atm 0


### 1 Standard Temperature 68 Deg F 0
10 Standard Temperature 68 Deg F 0
11 Standard Temperature 68 Deg F 0


### 12 Standard Temperature 68 Deg F 0
13 Standard Temperature 68 Deg F 0
14 Standard Temperature 68 Deg F 0


### 15 Standard Temperature 68 Deg F 0
16 Standard Temperature 68 Deg F 0
17 Standard Temperature 68 Deg F 0


### 18 Standard Temperature 68 Deg F 0
2 Standard Temperature 68 Deg F 0
3 Standard Temperature 68 Deg F 0


### 4 Standard Temperature 68 Deg F 0
5 Standard Temperature 68 Deg F 0
6 Standard Temperature 68 Deg F 0



### Friday, January 14, 2011 Page 24 of 47

### APCD Run Data

Process Lab Run Data 7 Standard Temperature 68 Deg F 0


### 8 Standard Temperature 68 Deg F 0
9 Standard Temperature 68 Deg F 0
1 Unit Net Electric Generation 132 MWh 0


### 10 Unit Net Electric Generation 116 MWh 0
11 Unit Net Electric Generation 133 MWh 0
12 Unit Net Electric Generation 137 MWh 0


### 13 Unit Net Electric Generation 137 MWh 0
14 Unit Net Electric Generation 131 MWh 0
15 Unit Net Electric Generation 137 MWh 0


### 16 Unit Net Electric Generation 131 MWh 0
17 Unit Net Electric Generation 137 MWh 0
18 Unit Net Electric Generation 137 MWh 0


### 2 Unit Net Electric Generation 137 MWh 0
3 Unit Net Electric Generation 132 MWh 0
4 Unit Net Electric Generation 132 MWh 0


### 5 Unit Net Electric Generation 135 MWh 0
6 Unit Net Electric Generation 135 MWh 0
7 Unit Net Electric Generation 116 MWh 0


### 8 Unit Net Electric Generation 133 MWh 0
9 Unit Net Electric Generation 137 MWh 0

Run Name Value UOM Comments Target Value 

### 1 OVERFIRE AIR 0 0
1 ELECTROSTATIC PRECIPITATOR 0 0
1 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0


### 1 WET ELECTROSTATIC PRECIPITATOR 0 0

Run Name Value UOM Comments 1 Fuel Higher Heating Value 14811 Btu/lb 1 Fuel Moisture 4.2 % 

### 1 Fuel Mercury Content 0.0009 ppm 1 Fuel Cadmium Content 0.15 ppm 1 Ultimate/Proximate Analysis 0 

### 1 Fuel Nickel Content 314 ppm
Friday, January 14, 2011 Page 25 of 47

### 1 Fuel Arsenic Content 0.13 ppm



### 1 Fuel Chromium Content 0.2 ppm 1 Fuel Beryllium Content 0.11 ppm 1 Fuel Lead Content 0.09 ppm 1 Fuel Manganese Content 0.1 ppm 

### 1 Fuel Chlorine Content 7.5 ppm 1 Fuel Fluorine Content 0 ppm 2 Fuel Higher Heating Value 14527 Btu/lb 

### 2 Fuel Moisture 5.5 % 2 Fuel Mercury Content 0.019 ppm 2 Fuel Cadmium Content 0.15 ppm 2 Ultimate/Proximate Analysis 0 

### 2 Fuel Nickel Content 313 ppm 2 Fuel Arsenic Content 0.13 ppm 2 Fuel Chromium Content 0.2 ppm 

### 2 Fuel Beryllium Content 0.11 ppm 2 Fuel Lead Content 0.09 ppm 2 Fuel Manganese Content 0.1 ppm 2 Fuel Chlorine Content 7.5 ppm 

### 2 Fuel Fluorine Content 0 ppm 3 Fuel Higher Heating Value 14752 Btu/lb 3 Fuel Moisture 4.5 % 

### 3 Fuel Mercury Content 0.021 ppm 3 Fuel Cadmium Content 0.15 ppm 3 Ultimate/Proximate Analysis 0 3 Fuel Nickel Content 318 ppm 

### 3 Fuel Arsenic Content 0.13 ppm 3 Fuel Chromium Content 0.2 ppm 3 Fuel Beryllium Content 0.11 ppm 

### 3 Fuel Lead Content 1.4 ppm 3 Fuel Manganese Content 0.1 ppm 3 Fuel Chlorine Content 7.5 ppm 3 Fuel Fluorine Content 0 ppm 

### 4 Fuel Higher Heating Value 14704 Btu/lb 4 Fuel Moisture 4.7 % 4 Fuel Mercury Content 0 ppm 

### 4 Fuel Cadmium Content 0 ppm 4 Ultimate/Proximate Analysis 0 4 Fuel Nickel Content 0 ppm 4 Fuel Arsenic Content 0 ppm 

### 4 Fuel Chromium Content 0 ppm 4 Fuel Beryllium Content 0 ppm 4 Fuel Lead Content 0 ppm



### Friday, January 14, 2011 Page 26 of 47

### 4 Fuel Manganese Content 0 ppm



### 4 Fuel Chlorine Content 7.5 ppm 4 Fuel Fluorine Content 0 ppm 5 Fuel Higher Heating Value 14854 Btu/lb 5 Fuel Moisture 4 % 

### 5 Fuel Mercury Content 0 ppm 5 Fuel Cadmium Content 0 ppm 5 Ultimate/Proximate Analysis 0 

### 5 Fuel Nickel Content 0 ppm 5 Fuel Arsenic Content 0 ppm 5 Fuel Chromium Content 0 ppm 5 Fuel Beryllium Content 0 ppm 

### 5 Fuel Lead Content 0 ppm 5 Fuel Manganese Content 0 ppm 5 Fuel Chlorine Content 7.5 ppm 

### 5 Fuel Fluorine Content 0 ppm 6 Fuel Higher Heating Value 14593 Btu/lb 6 Fuel Moisture 5.4 % 6 Fuel Mercury Content 0 ppm 

### 6 Fuel Cadmium Content 0 ppm 6 Ultimate/Proximate Analysis 0 6 Fuel Nickel Content 0 ppm 

### 6 Fuel Arsenic Content 0 ppm 6 Fuel Chromium Content 0 ppm 6 Fuel Beryllium Content 0 ppm 6 Fuel Lead Content 0 ppm 

### 6 Fuel Manganese Content 0 ppm 6 Fuel Chlorine Content 7.5 ppm 6 Fuel Fluorine Content 0 ppm 

### 7 Fuel Higher Heating Value 14847 Btu/lb 7 Fuel Moisture 3 % 7 Fuel Mercury Content 0 ppm 7 Fuel Cadmium Content 0 ppm 

### 7 Ultimate/Proximate Analysis 0 7 Fuel Nickel Content 0 ppm 7 Fuel Arsenic Content 0 ppm 

### 7 Fuel Chromium Content 0 ppm 7 Fuel Beryllium Content 0 ppm 7 Fuel Lead Content 0 ppm 7 Fuel Manganese Content 0 ppm 

### 7 Fuel Chlorine Content 7.5 ppm 7 Fuel Fluorine Content 3 ppm 8 Fuel Higher Heating Value 14677 Btu/lb



### Friday, January 14, 2011 Page 27 of 47

### 8 Fuel Moisture 5 %



### 8 Fuel Mercury Content 0 ppm 8 Fuel Cadmium Content 0 ppm 8 Ultimate/Proximate Analysis 0 8 Fuel Nickel Content 0 ppm 

### 8 Fuel Arsenic Content 0 ppm 8 Fuel Chromium Content 0 ppm 8 Fuel Beryllium Content 0 ppm 

### 8 Fuel Lead Content 0 ppm 8 Fuel Manganese Content 0 ppm 8 Fuel Chlorine Content 7.5 ppm 8 Fuel Fluorine Content 3 ppm 

### 9 Fuel Higher Heating Value 14430 Btu/lb 9 Fuel Moisture 6 % 9 Fuel Mercury Content 0 ppm 

### 9 Fuel Cadmium Content 0 ppm 9 Ultimate/Proximate Analysis 0 9 Fuel Nickel Content 0 ppm 9 Fuel Arsenic Content 0 ppm 

### 9 Fuel Chromium Content 0 ppm 9 Fuel Beryllium Content 0 ppm 9 Fuel Lead Content 0 ppm 

### 9 Fuel Manganese Content 0 ppm 9 Fuel Chlorine Content 7.5 ppm 9 Fuel Fluorine Content 3 ppm 10 Fuel Higher Heating Value 14793 Btu/lb 

### 10 Fuel Moisture 3.8 % 10 Fuel Mercury Content 0 ppm 10 Fuel Cadmium Content 0 ppm 

### 10 Ultimate/Proximate Analysis 0 10 Fuel Nickel Content 0 ppm 10 Fuel Arsenic Content 0 ppm 10 Fuel Chromium Content 0 ppm 

### 10 Fuel Beryllium Content 0 ppm 10 Fuel Lead Content 0 ppm 10 Fuel Manganese Content 0 ppm 

### 10 Fuel Chlorine Content 7.5 ppm 10 Fuel Fluorine Content 0 ppm 11 Fuel Higher Heating Value 14840 Btu/lb 11 Fuel Moisture 3.9 % 

### 11 Fuel Mercury Content 0 ppm 11 Fuel Cadmium Content 0 ppm 11 Ultimate/Proximate Analysis 0



### Friday, January 14, 2011 Page 28 of 47

### 11 Fuel Nickel Content 0 ppm



### 11 Fuel Arsenic Content 0 ppm 11 Fuel Chromium Content 0 ppm 11 Fuel Beryllium Content 0 ppm 11 Fuel Lead Content 0 ppm 

### 11 Fuel Manganese Content 0 ppm 11 Fuel Chlorine Content 7.5 ppm 11 Fuel Fluorine Content 0 ppm 

### 12 Fuel Higher Heating Value 14744 Btu/lb 12 Fuel Moisture 4.3 % 12 Fuel Mercury Content 0 ppm 12 Fuel Cadmium Content 0 ppm 

### 12 Ultimate/Proximate Analysis 0 12 Fuel Nickel Content 0 ppm 12 Fuel Arsenic Content 0 ppm 

### 12 Fuel Chromium Content 0 ppm 12 Fuel Beryllium Content 0 ppm 12 Fuel Lead Content 0 ppm 12 Fuel Manganese Content 0 ppm 

### 12 Fuel Chlorine Content 7.5 ppm 12 Fuel Fluorine Content 0 ppm 13 Fuel Higher Heating Value 14854 Btu/lb 

### 13 Fuel Moisture 3.8 % 13 Fuel Mercury Content 0 ppm 13 Fuel Cadmium Content 0 ppm 13 Ultimate/Proximate Analysis 0 

### 13 Fuel Nickel Content 0 ppm 13 Fuel Arsenic Content 0 ppm 13 Fuel Chromium Content 0 ppm 

### 13 Fuel Beryllium Content 0 ppm 13 Fuel Lead Content 0 ppm 13 Fuel Manganese Content 0 ppm 13 Fuel Chlorine Content 52 ppm 

### 13 Fuel Fluorine Content 0 ppm 14 Fuel Higher Heating Value 14716 Btu/lb 14 Fuel Moisture 4.7 % 

### 14 Fuel Mercury Content 0 ppm 14 Fuel Cadmium Content 0 ppm 14 Ultimate/Proximate Analysis 0 14 Fuel Nickel Content 0 ppm 

### 14 Fuel Arsenic Content 0 ppm 14 Fuel Chromium Content 0 ppm 14 Fuel Beryllium Content 0 ppm



### Friday, January 14, 2011 Page 29 of 47

### 14 Fuel Lead Content 0 ppm



### 14 Fuel Manganese Content 0 ppm 14 Fuel Chlorine Content 7.5 ppm 14 Fuel Fluorine Content 0 ppm 15 Fuel Higher Heating Value 14734 Btu/lb 

### 15 Fuel Moisture 4.1 % 15 Fuel Mercury Content 0 ppm 15 Fuel Cadmium Content 0 ppm 

### 15 Ultimate/Proximate Analysis 0 15 Fuel Nickel Content 0 ppm 15 Fuel Arsenic Content 0 ppm 15 Fuel Chromium Content 0 ppm 

### 15 Fuel Beryllium Content 0 ppm 15 Fuel Lead Content 0 ppm 15 Fuel Manganese Content 0 ppm 

### 15 Fuel Chlorine Content 7.5 ppm 15 Fuel Fluorine Content 0 ppm 16 Fuel Higher Heating Value 14768 Btu/lb 16 Fuel Moisture 4.2 % 

### 16 Fuel Mercury Content 0 ppm 16 Fuel Cadmium Content 0 ppm 16 Ultimate/Proximate Analysis 0 

### 16 Fuel Nickel Content 0 ppm 16 Fuel Arsenic Content 0 ppm 16 Fuel Chromium Content 0 ppm 16 Fuel Beryllium Content 0 ppm 

### 16 Fuel Lead Content 0 ppm 16 Fuel Manganese Content 0 ppm 16 Fuel Chlorine Content 52 ppm 

### 16 Fuel Fluorine Content 0 ppm 17 Fuel Higher Heating Value 14717 Btu/lb 17 Fuel Moisture 4.7 % 17 Fuel Mercury Content 0 ppm 

### 17 Fuel Cadmium Content 0 ppm 17 Ultimate/Proximate Analysis 0 17 Fuel Nickel Content 0 ppm 

### 17 Fuel Arsenic Content 0 ppm 17 Fuel Chromium Content 0 ppm 17 Fuel Beryllium Content 0 ppm 17 Fuel Lead Content 0 ppm 

### 17 Fuel Manganese Content 0 ppm 17 Fuel Chlorine Content 7.5 ppm 17 Fuel Fluorine Content 0 ppm



### Friday, January 14, 2011 Page 30 of 47

### 18 Fuel Higher Heating Value 14876 Btu/lb



### 18 Fuel Moisture 3.8 % 18 Fuel Mercury Content 0 ppm 18 Fuel Cadmium Content 0 ppm 18 Ultimate/Proximate Analysis 0 

### 18 Fuel Nickel Content 0 ppm 18 Fuel Arsenic Content 0 ppm 18 Fuel Chromium Content 0 ppm 

### 18 Fuel Beryllium Content 0 ppm 18 Fuel Lead Content 0 ppm 18 Fuel Manganese Content 0 ppm 18 Fuel Chlorine Content 7.5 ppm 

### 18 Fuel Fluorine Content 0 ppm

Friday, January 14, 2011 Page 31 of 47

### Sampling / Stack Data Results Detail



### Location Stack Exit - Method 10 Average Run Number 1 Form 2 Form 3 Form Test Date 7/24/2010 7/24/2010 7/24/2010 Run Start Time 7:53:00 AM 10:25:00 AM 1:24:00 PM Run Finish Time 10:07:00 AM 12:47:00 PM 3:37:00 PM Carbon Dioxide, % 12.81 13.15 13.18 13.047 Oxygen, % 6.72 6.32 6.24 6.427 Fuel Factor 1.11 1.11 1.11 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000 Moisture, % 0 0 0 0.000 Analyzer Make TECO TECO TECO Analyzer Model 48i 48i 48i Analyzer Serial Number Mick Mick Mick Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 3 3 3 3.000 Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Pre Zero Cylinder Instrument Response 0.33 0.37 0.5 0.400 Calibration Pre Zero Cylinder Bias 0.03 0.04 0.07 0.047 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID ALM46599 ALM46599 ALM46599 Calibration Pre High Cylinder Instrument Response 244.93 245.35 244.99 245.090 Calibration Pre High Cylinder Bias -0.23 -0.15 -0.22 -0.200 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Post Zero Cylinder Instrument Response 0.37 0.5 0.47 0.447 Calibration Post Zero Cylinder Bias 0.04 0.07 0.06 0.057 Calibration Post Zero Cylinder Drift 0.01 0.03 0.01 0.017 Calibration Post High Cylinder ID ALM46599 ALM46599 ALM46599 Calibration Post High Cylinder Instrument Response 245.35 244.99 245.39 245.243 Calibration Post High Cylinder Bias -0.15 -0.22 -0.14 -0.170 Calibration Post High Cylinder Drift 0.08 0.07 0.08 0.077 Cavg 55.6 167.2 174.77 132.523 Cavg Units ppmvd ppmvd ppmvd Cgas 55.5908 167.8314 175.421 132.948 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000 Cgasw 0 0 0 0.000 Cgasw Units



### Friday, January 14, 2011 Page 32 of 47

### Location Stack Exit - Method 23 Average

Run Number 1 2 3 Test Date 7/24/2010 7/25/2010 7/26/2010 Run Start Time 8:53:00 AM 8:05:00 AM 7:03:00 AM Run Finish Time 5:39:00 PM 5:17:00 PM 5:56:00 PM Net Traversing Points 0 0 0 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.24 0.247 0.247 0.245 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.001 1.001 1.001 1.001 Barometric Pressure, inches of Mercury 29.39 29.37 29.37 29.377 Average Orifice Meter Differential, inches H2O 1.43 1.56 1.61 1.533 Dry Gas Meter Volume Sampled, cubic feet 312.152 327.279 327.867 322.433 Average Dry Gas Meter Temperature, °F 105.47 102.98 99.37 102.607 Dry Gas Meter Volume Sampled, dscf 287.616 302.781 305.320 298.572 Total Moisture Liquid collected, g 940.2 976.2 1019.2 978.533 Volume of Water Vapor, standard cubic feet 44.26 45.95 47.97 46.060 Moisture Content of Stack Gas, % 13.34 13.18 13.58 13.367 Moisture Saturation at Stack Gas Temperature, % 31.84 31.37 31.22 31.477 Dry Mole Fraction 0.8666 0.8682 0.8642 0.866 Carbon Dioxide, % 13 13 13 13.000 Oxygen, % 6.4 6.3 6.3 6.333 Carbon Monoxide & Nitrogen, % 80.6 80.7 80.7 80.667 Fuel Factor 1.12 1.12 1.12 Dry Molecular Weight, lb/lb-Mole 30.34 30.33 30.33 30.333 Wet Molecular weight, lb/lb-Mole 28.69 28.70 28.66 28.683 Flue Gas Static Pressure, inches of H2O -0.35 -0.35 -0.4 -0.367 Absolute Flue Gas Pressure, inches of Mercury 29.36 29.34 29.34 29.347 Average Stack Gas Temperature, °F 158.76 158.10 157.91 158.257 Average Velocity Head, inches of H2O 0.5517523451 48963 0.536280816

54093 0.526480138

804762 0.538
Average Stack Gas Velocity, feet/second 45.72 45.06 44.67 45.150 Stack Cross-Sectional Area, square feet 226.980 226.980 226.980 226.980 Dry Volumetric Flow Rate, dry scfm 451,824.6 446,296.5 440,530.8 446,217.300 Actual Wet Volumetric Flue Gas Flow Rate, acfm 622,651.5 613,663.1 608,351.8 614,888.800 Percent Isokinetic of Sampling Rate, % 95.8 96.4 98.5 96.900 Percent Excess Air, % 43.0 42.0 42.0 42.333 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000 Round Duct Diameter, inches 204 204 204 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000



### Friday, January 14, 2011 Page 33 of 47

### Location Stack Exit - Method 25A Average

Run Number 1 2 3 Test Date 7/24/2010 7/24/2010 7/24/2010 Run Start Time 7:53:00 AM 10:25:00 AM 1:24:00 PM Run Finish Time 10:07:00 AM 12:47:00 PM 3:37:00 PM Carbon Dioxide, % 12.81 13.15 13.18 13.047 Oxygen, % 6.72 6.32 6.24 6.427 Fuel Factor 1.11 1.11 1.11 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000 Moisture, % 0 0 0 0.000 Analyzer Make TECO TECO TECO Analyzer Model 51CHT 51CHT 51CHT Analyzer Serial Number Buddy Buddy Buddy Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 4 4 4 4.000 Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Pre Zero Cylinder Instrument Response 0 0 0.04 0.013 Calibration Pre Zero Cylinder Bias 0 0 0.19 0.063 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC155319 CC155319 CC155319 Calibration Pre High Cylinder Instrument Response 12.7 12.67 12.62 12.663 Calibration Pre High Cylinder Bias 0.38 0.24 0 0.207 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Post Zero Cylinder Instrument Response 0 0.04 0.02 0.020 Calibration Post Zero Cylinder Bias 0 0.19 0.09 0.093 Calibration Post Zero Cylinder Drift 0 0.14 0.1 0.080 Calibration Post High Cylinder ID CC155319 CC155319 CC155319 Calibration Post High Cylinder Instrument Response 12.67 12.62 12.53 12.607 Calibration Post High Cylinder Bias 0.24 0 -0.42 -0.060 Calibration Post High Cylinder Drift 0.14 0.14 0.66 0.313 Cavg 0.2 0.22 0.23 0.217 Cavg Units ppmvd ppmvd ppmvd Cgas 0.1662 0.1964 0.1977 0.187 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000 Cgasw 0 0 0 0.000 Cgasw Units



### Friday, January 14, 2011 Page 34 of 47

### Location Stack Exit - Method 26A Average

Run Number 1 2 3 Test Date 8/18/2010 8/19/2010 8/19/2010 Run Start Time 2:36:00 PM 8:55:00 AM 12:23:00 PM Run Finish Time 5:50:00 PM 12:08:00 PM 3:33:00 PM Net Traversing Points 0 22 0 Net Run Time, minutes 180 180 180 Nozzle Diameter, inches 0.229 0.229 0.229 0.229 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.999 0.999 0.999 0.999 Barometric Pressure, inches of Mercury 29.75 29.73 29.75 29.743 Average Orifice Meter Differential, inches H2O 1.28 1.35 1.39 1.340 Dry Gas Meter Volume Sampled, cubic feet 112.374 114.211 116.114 114.233 Average Dry Gas Meter Temperature, °F 106.96 102.24 103.78 104.327 Dry Gas Meter Volume Sampled, dscf 104.282 106.823 108.390 106.498 Total Moisture Liquid collected, g 331.6 346.1 361.4 346.367 Volume of Water Vapor, standard cubic feet 15.61 16.29 17.01 16.303 Moisture Content of Stack Gas, % 13.02 13.23 13.56 13.270 Moisture Saturation at Stack Gas Temperature, % 30.95 30.29 30.35 30.530 Dry Mole Fraction 0.8698 0.8677 0.8644 0.867 Carbon Dioxide, % 12.3 11.9 11.9 12.033 Oxygen, % 6.9 6.9 6.7 6.833 Carbon Monoxide & Nitrogen, % 80.8 81.2 81.4 81.133 Fuel Factor 1.14 1.18 1.19 Dry Molecular Weight, lb/lb-Mole 30.24 30.18 30.17 30.197 Wet Molecular weight, lb/lb-Mole 28.65 28.57 28.52 28.580 Flue Gas Static Pressure, inches of H2O -0.42 -0.33 -0.33 -0.360 Absolute Flue Gas Pressure, inches of Mercury 29.72 29.71 29.73 29.720 Average Stack Gas Temperature, °F 158.08 157.17 157.28 157.510 Average Velocity Head, inches of H2O 0.5645799915 06418 0.595699487

66388 0.613847494

842037 0.591
Average Stack Gas Velocity, feet/second 45.97 47.26 48.01 47.080 Stack Cross-Sectional Area, square feet 226.980 226.980 226.980 226.980 Dry Volumetric Flow Rate, dry scfm 462,071.5 474,430.2 480,363.9 472,288.533 Actual Wet Volumetric Flue Gas Flow Rate, acfm 626,056.2 643,624.5 653,838.6 641,173.100 Percent Isokinetic of Sampling Rate, % 99.5 99.3 99.5 99.433 Percent Excess Air, % 47.8 47.5 45.3 46.867 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000 Round Duct Diameter, inches 204 204 204 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000



### Friday, January 14, 2011 Page 35 of 47

### Location Stack Exit - Method 29 Average

Run Number 1 2 3 Test Date 8/3/2010 8/3/2010 8/4/2010 Run Start Time 7:40:00 AM 1:23:00 PM 7:32:00 AM Run Finish Time 12:05:00 PM 6:11:00 PM 12:00:00 PM Net Traversing Points 0 0 0 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.247 0.247 0.247 0.247 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.989 0.989 0.989 0.989 Barometric Pressure, inches of Mercury 29.39 29.37 29.39 29.383 Average Orifice Meter Differential, inches H2O 1.67 1.67 1.79 1.710 Dry Gas Meter Volume Sampled, cubic feet 178.043 179.038 184.209 180.430 Average Dry Gas Meter Temperature, °F 104.11 107.02 103.89 105.007 Dry Gas Meter Volume Sampled, dscf 162.570 162.529 168.316 164.472 Total Moisture Liquid collected, g 546.1 465.4 567.2 526.233 Volume of Water Vapor, standard cubic feet 25.70 21.91 26.70 24.770 Moisture Content of Stack Gas, % 13.65 11.88 13.69 13.073 Moisture Saturation at Stack Gas Temperature, % 33.38 33.74 33.58 33.567 Dry Mole Fraction 0.8635 0.8812 0.8631 0.869 Carbon Dioxide, % 12.7 13 12.8 12.833 Oxygen, % 6.6 6.5 6.9 6.667 Carbon Monoxide & Nitrogen, % 80.7 80.5 80.3 80.500 Fuel Factor 1.13 1.11 1.09 Dry Molecular Weight, lb/lb-Mole 30.30 30.34 30.32 30.320 Wet Molecular weight, lb/lb-Mole 28.62 28.87 28.63 28.707 Flue Gas Static Pressure, inches of H2O -0.42 -0.35 -0.4 -0.390 Absolute Flue Gas Pressure, inches of Mercury 29.36 29.34 29.36 29.353 Average Stack Gas Temperature, °F 160.73 161.15 160.98 160.953 Average Velocity Head, inches of H2O 0.6089638607 10644 0.605229324

309334 0.632231528

467615 0.615
Average Stack Gas Velocity, feet/second 48.16 47.84 49.08 48.360 Stack Cross-Sectional Area, square feet 226.980 226.980 226.980 226.980 Dry Volumetric Flow Rate, dry scfm 472,730.2 478,564.5 481,343.7 477,546.133 Actual Wet Volumetric Flue Gas Flow Rate, acfm 655,881.4 651,523.4 668,410.7 658,605.167 Percent Isokinetic of Sampling Rate, % 97.7 96.5 99.4 97.867 Percent Excess Air, % 44.9 44.1 48.3 45.767 F-Factor, dscfm/MMBtu @ %O2 9936 9936 9936 9,936.000 Round Duct Diameter, inches 204 204 204 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000



### Friday, January 14, 2011 Page 36 of 47

### Location Stack Exit - Method 3A CO2 Average

Run Number 1 DF 1 Form 1 Hg Test Date 7/24/2010 7/24/2010 7/25/2010 Run Start Time 8:53:00 AM 7:53:00 AM 7:18:00 AM Run Finish Time 5:39:00 PM 10:07:00 AM 9:40:00 AM Carbon Dioxide, % 13.11 12.81 12.81 12.910 Oxygen, % 6.33 6.72 6.65 6.567 Fuel Factor 1.11 1.11 1.11 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Moisture, % 0 0 0 0.000 Analyzer Make Servomex Servomex Servomex Analyzer Model 1440 1440 1440 1,440.000 Analyzer Serial Number Waits Waits Waits Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 11 11 111 44.333 Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Pre Zero Cylinder Instrument Response 0.08 0.08 0.15 0.103 Calibration Pre Zero Cylinder Bias 0 0 0.1 0.033 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID ALM015275 ALM015275 ALM015275 Calibration Pre High Cylinder Instrument Response 9.61 9.61 9.61 9.610 Calibration Pre High Cylinder Bias -0.51 -0.51 -0.56 -0.527 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Post Zero Cylinder Instrument Response 0.16 0.14 0.16 0.153 Calibration Post Zero Cylinder Bias 0.41 0.31 0.15 0.290 Calibration Post Zero Cylinder Drift 0.41 0.31 0.05 0.257 Calibration Post High Cylinder ID ALM015275 ALM015275 ALM015275 Calibration Post High Cylinder Instrument Response 9.61 9.63 9.62 9.620 Calibration Post High Cylinder Bias -0.51 -0.41 0 -0.307 Calibration Post High Cylinder Drift 0 0.1 0 0.033 Cavg 13.11 12.81 12.81 12.910 Cavg Units ppmvd ppmvd ppmvd Cgas 12.9763 12.6599 25.7999 17.145 Cgas Units ppmvd ppmvd ppmvd Fuel Type Coal - Bituminous Coal -

Bituminous Coal -

Bituminous Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000 Cgasw 0 0 0 0.000 Cgasw Units



### Friday, January 14, 2011 Page 37 of 47

### Location Stack Exit - Method 3A CO2 3 Average

Run Number 1 ORG 1 PM 2 DF Test Date 7/23/2010 8/3/2010 7/25/2010 Run Start Time 8:13:00 AM 7:40:00 AM 8:05:00 AM Run Finish Time 10:54:00 AM 12:05:00 PM 5:17:00 PM Carbon Dioxide, % 13.04 12.84 13.1 12.993 Oxygen, % 6.46 6.62 6.27 6.450 Fuel Factor 1.11 1.11 1.12 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Moisture, % 0 0 0 0.000 Analyzer Make Servomex Servomex Servomex Analyzer Model 1440 1440 1440 1,440.000 Analyzer Serial Number Waits Waits Waits Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 1 10 111 40.667 Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Pre Zero Cylinder Instrument Response 0.08 0.14 0.15 0.123 Calibration Pre Zero Cylinder Bias 0.1 0.15 0.1 0.117 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID ALM015275 ALM015275 ALM015275 Calibration Pre High Cylinder Instrument Response 9.59 9.59 9.61 9.597 Calibration Pre High Cylinder Bias -0.51 -0.51 -0.56 -0.527 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Post Zero Cylinder Instrument Response 0.14 0.18 0.21 0.177 Calibration Post Zero Cylinder Bias 0.41 0.36 0.41 0.393 Calibration Post Zero Cylinder Drift 0.31 0.21 0.31 0.277 Calibration Post High Cylinder ID ALM015275 ALM015275 ALM015275 Calibration Post High Cylinder Instrument Response 9.69 9.62 9.62 9.643 Calibration Post High Cylinder Bias 0 -0.36 -0.51 -0.290 Calibration Post High Cylinder Drift 0.51 0.15 0.05 0.237 Cavg 13.04 12.84 13.1 12.993 Cavg Units ppmvd ppmvd ppmvd Cgas 12.8622 12.727 12.9816 12.857 Cgas Units ppmvd ppmvd ppmvd Fuel Type Coal - Bituminous Coal -

Bituminous Coal -

Bituminous Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000 Cgasw 0 0 0 0.000 Cgasw Units



### Friday, January 14, 2011 Page 38 of 47

### Location Stack Exit - Method 3A CO2 3 6 Average

Run Number 2 Form 2 Hg 2 ORG Test Date 7/24/2010 7/25/2010 7/23/2010 Run Start Time 10:25:00 AM 10:53:00 AM 11:36:00 AM Run Finish Time 12:47:00 PM 1:07:00 PM 1:52:00 PM Carbon Dioxide, % 13.15 13.16 13.14 13.150 Oxygen, % 6.32 6.23 6.29 6.280 Fuel Factor 1.11 1.11 1.11 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Moisture, % 0 0 0 0.000 Analyzer Make Servomex Servomex Servomex Analyzer Model 1440 1440 1440 1,440.000 Analyzer Serial Number Waits Waits Waits Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 11 111 1 41.000 Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Pre Zero Cylinder Instrument Response 0.14 0.16 0.14 0.147 Calibration Pre Zero Cylinder Bias 0.31 0.15 0.41 0.290 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID ALM015275 ALM015275 ALM015275 Calibration Pre High Cylinder Instrument Response 9.63 9.62 9.69 9.647 Calibration Pre High Cylinder Bias -0.41 -0.51 0 -0.307 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Post Zero Cylinder Instrument Response 0.14 0.17 0.17 0.160 Calibration Post Zero Cylinder Bias 0.31 0.21 0.56 0.360 Calibration Post Zero Cylinder Drift 0 0.06 0.15 0.070 Calibration Post High Cylinder ID ALM015275 ALM015275 ALM015275 Calibration Post High Cylinder Instrument Response 9.61 9.66 9.64 9.637 Calibration Post High Cylinder Bias -0.51 -0.31 -0.26 -0.360 Calibration Post High Cylinder Drift 0.1 0.2 0.26 0.187 Cavg 13.15 13.16 13.14 13.150 Cavg Units ppmvd ppmvd ppmvd Cgas 13.01 13.0019 12.944 12.985 Cgas Units ppmvd ppmvd ppmvd Fuel Type Coal - Bituminous Coal -

Bituminous Coal -

Bituminous Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000 Cgasw 0 0 0 0.000 Cgasw Units



### Friday, January 14, 2011 Page 39 of 47

### Location Stack Exit - Method 3A CO2 3 6 9 Average

Run Number 2 PM 3 DF 3 Form Test Date 8/3/2010 7/26/2010 7/24/2010 Run Start Time 1:23:00 PM 6:21:00 AM 1:24:00 PM Run Finish Time 6:11:00 PM 6:01:00 PM 3:37:00 PM Carbon Dioxide, % 12.97 13.07 13.18 13.073 Oxygen, % 6.4 6.31 6.24 6.317 Fuel Factor 1.12 1.12 1.11 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Moisture, % 0 0 0 0.000 Analyzer Make Servomex Servomex Servomex Analyzer Model 1440 1440 1440 1,440.000 Analyzer Serial Number Waits Waits Waits Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 10 1111 11 377.333 Calibration Pre Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Pre Zero Cylinder Instrument Response 0.18 0.12 0.14 0.147 Calibration Pre Zero Cylinder Bias 0.36 0.15 0.31 0.273 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID ALM015275 ALM015275 ALM015275 Calibration Pre High Cylinder Instrument Response 9.62 9.58 9.61 9.603 Calibration Pre High Cylinder Bias -0.36 -0.41 -0.51 -0.427 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID CC9718 CC9718 CC9718 Calibration Post Zero Cylinder Instrument Response 0.19 0.17 0.15 0.170 Calibration Post Zero Cylinder Bias 0.41 0.41 0.36 0.393 Calibration Post Zero Cylinder Drift 0.05 0.26 0.05 0.120 Calibration Post High Cylinder ID ALM015275 ALM015275 ALM015275 Calibration Post High Cylinder Instrument Response 9.6 9.59 9.61 9.600 Calibration Post High Cylinder Bias -0.46 -0.36 -0.51 -0.443 Calibration Post High Cylinder Drift 0.1 0.05 0 0.050 Cavg 12.97 13.07 13.18 13.073 Cavg Units ppmvd ppmvd ppmvd Cgas 12.8596 12.9798 13.0557 12.965 Cgas Units ppmvd ppmvd ppmvd Fuel Type Coal - Bituminous Coal -

Bituminous Coal -

Bituminous Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000 Cgasw 0 0 0 0.000 Cgasw Units



### Friday, January 14, 2011 Page 40 of 47

### Location Stack Exit - Method 3A CO2 3 6 9 12 Average

Run Number 3 Hg 3 ORG 3 PM Test Date 7/25/2010 7/23/2010 8/4/2010 Run Start Time 1:46:00 PM 2:39:00 PM 7:32:00 AM Run Finish Time 3:52:00 PM 5:37:00 PM 12:00:00 PM Carbon Dioxide, % 13.19 13.15 12.9 13.080 Oxygen, % 6.16 6.23 6.52 6.303 Fuel Factor Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 Moisture, % 0 0 0 0.000 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



### Friday, January 14, 2011 Page 41 of 47

### Location Stack Exit - Method 3A O2 Average

Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



### Friday, January 14, 2011 Page 42 of 47

### Location Stack Exit - Method 3A O2 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



### Friday, January 14, 2011 Page 43 of 47

### Location Stack Exit - Method 3A O2 3 6 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



### Friday, January 14, 2011 Page 44 of 47

### Location Stack Exit - Method 3A O2 3 6 9 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



### Friday, January 14, 2011 Page 45 of 47

### Location Stack Exit - Method 3A O2 3 6 9 12 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



### Friday, January 14, 2011 Page 46 of 47

### Location Stack Exit - Method 5/OTM-28 Average

Run Number 1 2 3 Test Date 8/3/2010 8/3/2010 8/4/2010 Run Start Time 7:40:00 AM 1:23:00 PM 7:32:00 AM Run Finish Time 12:05:00 PM 6:11:00 PM 12:00:00 PM Net Traversing Points 0 0 0 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.247 0.247 0.247 0.247 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.001 1.001 1.001 1.001 Barometric Pressure, inches of Mercury 29.39 29.39 29.39 29.390 Average Orifice Meter Differential, inches H2O 1.64 1.56 1.63 1.610 Dry Gas Meter Volume Sampled, cubic feet 166.676 160.938 163.415 163.676 Average Dry Gas Meter Temperature, °F 102.29 107.60 101.58 103.823 Dry Gas Meter Volume Sampled, dscf 154.524 147.779 151.689 151.331 Total Moisture Liquid collected, g 517.9 490.9 509.4 506.067 Volume of Water Vapor, standard cubic feet 24.38 23.11 23.98 23.823 Moisture Content of Stack Gas, % 13.63 13.52 13.65 13.600 Moisture Saturation at Stack Gas Temperature, % 33.64 34.32 33.64 33.867 Dry Mole Fraction 0.8637 0.8648 0.8635 0.864 Carbon Dioxide, % 13 13 12.8 12.933 Oxygen, % 6.4 6.3 6.6 6.433 Carbon Monoxide & Nitrogen, % 80.6 80.7 80.6 80.633 Fuel Factor 1.12 1.12 1.12 Dry Molecular Weight, lb/lb-Mole 30.34 30.33 30.31 30.327 Wet Molecular weight, lb/lb-Mole 28.66 28.66 28.63 28.650 Flue Gas Static Pressure, inches of H2O -0.42 -0.45 -0.35 -0.407 Absolute Flue Gas Pressure, inches of Mercury 29.36 29.36 29.36 29.360 Average Stack Gas Temperature, °F 161.06 161.90 161.06 161.340 Average Velocity Head, inches of H2O 0.5546700024 2251 0.548849500

622287 0.566405009

682954 0.557
Average Stack Gas Velocity, feet/second 45.95 45.74 46.46 46.050 Stack Cross-Sectional Area, square feet 226.980 226.980 226.980 226.980 Dry Volumetric Flow Rate, dry scfm 450,901.9 448,805.9 455,800.9 451,836.233 Actual Wet Volumetric Flue Gas Flow Rate, acfm 625,783.9 622,923.9 632,729.4 627,145.733 Percent Isokinetic of Sampling Rate, % 97.4 93.6 94.6 95.200 Percent Excess Air, % 43.0 42.0 45.0 43.333 F-Factor, dscfm/MMBtu @ %O2 99360 9936 9936 39,744.000 Round Duct Diameter, inches 204 204 204 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 0 0 0 0.000 Fc 0 0 0 0.000



### Friday, January 14, 2011 Page 47 of 47