### Name: Edward J. Bielarski

Title: General Manager Company: Panther Creek Energy Facility Sign Date: 9/23/2010 Name: Stephen S. Schell Title: President Company: Air Analysis, LLC Sign Date: 9/23/2010 Permitted Facility Representative / Date Testing Company Representative / Date 

## Panther Creek Energy Facility 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.

Tuesday, February 01, 2011 Page 1 of 30

### Panther Creek Energy Facility 9/23/2010 Facility Information: Panther Creek Energy Facility 4 Dennison Road

Nesquehoning PA18240 Contact:Jim Carroll Phone: 570-645-8721 Fax: 570-645-9763 Email: Jcarroll@PantherCreekEnergy.com Testing Company: Air Analysis, LLC 189 Hausman Road

Lenhartsville PA19534 Contact:Stephen Schell Phone:610-756-3490 Fax: 610-756-3491 Email: sschell@hughes.net

Air Permit Number: TV-13-00003 Permitted Source ID/Name: Panther Creek Energy Facility BLR1 & BLR Permitted Maximum Process Rate: 800,000 lbs./hr steam Max. Normal Operation Process Rate: Target Process Test Rate 90% of full load

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: The facility utilizes two circulating fluidized bed boilers which burn waste anthracite coal (culm) to generate 800,000 lbs./hr steam and generate electricity. Boiler flue gases exit each boiler via cyclone separators, superheaters, economizers and air heaters. The flue gas is then ducted thfough baghouses for removal of particulate. The pollution control equipment also consists of limestone feed for control of SO2 emissions and maintaining combustor outlet temperatures of 1500F for control of NOx emissions. A manually controlled ammonia injection system can also be activated for NOx emission control. Industry/SCC/NAIS221112

Sampling Location Information:

Test Parameter Information: AFS #:4202500101 FRS #:110001204599

SCC / Description10102018 External Combustion Boilers - Electric Generation - Waste Coal - Circulating Fluidized Bed Combustion

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 Exhaust Stack 115 10.64 13.77 4 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location Custom CH4 3 120 0 Method 18 Exhaust StackFlowrate Method 1 - 4 0 Determined during each test conducted Exhaust Stack

% H2O Method 1 - 4 0 Determined during each test conducted Exhaust Stack



### Tuesday, February 01, 2011 Page 2 of 30

### Panther Creek Energy Facility 9/23/2010 Carbon Monoxide Method 10 3 120 0 Exhaust StackFormaldehyde Method 0011 3 120 0 Exhaust Stack2,3,7,8-TCDD Method 23 0 Exhaust Stack1,2,3,7,8-PeCDD Method 23 0 Exhaust Stack1,2,3,4,7,8-HxCDD Method 23 0 Exhaust Stack1,2,3,6,7,8-HxCDD Method 23 0 Exhaust Stack1,2,3,7,8,9-HxCDD Method 23 0 Exhaust Stack1,2,3,4,6,7,8-HpCDD Method 23 0 Exhaust Stack2,3,7,8-TCDF Method 23 0 Exhaust Stack1,2,3,7,8-PeCDF Method 23 0 Exhaust Stack2,3,4,7,8-PeCDF Method 23 0 Exhaust Stack1,2,3,4,7,8-HxCDF Method 23 0 Exhaust Stack1,2,3,6,7,8-HxCDF Method 23 0 Exhaust Stack2,3,4,6,7,8-HxCDF Method 23 0 Exhaust Stack1,2,3,7,8,9-HxCDF Method 23 0 Exhaust Stack1,2,3,4,6,7,8-HpCDF Method 23 0 Exhaust Stack1,2,3,4,7,8,9-HpCDF Method 23 0 Exhaust Stack3,3',4,4'-TCB (PCB77) Method 23 3 480 0 Exhaust Stack3,4,4',5-TCB (PCB81) Method 23 3 480 0 Exhaust Stack2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0 Exhaust Stack2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0 Exhaust Stack2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0 Exhaust Stack2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0 Exhaust Stack3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0 Exhaust Stack2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 480 0 Exhaust Stack2,3',4,4',5,5'-HxCB (PCB167)Method 23 3 480 0 Exhaust Stack3,3',4,4',5,5'-HxCB (PCB169)Method 23 3 480 0 Exhaust Stack2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 0 Exhaust StackTotal TEQ Method 23 3 480 0 Exhaust StackTotal organic compounds

(TOC) as Propane Method 25A 3 120 0 Exhaust StackHydrogen Chloride Method 26A 3 90 0 Exhaust StackHydrogen Fluoride Method 26A 3 90 0 Exhaust StackTotal Particulate OTM - 27/28 3 330 0 Exhaust StackFilterable Particulate OTM - 27/28 3 330 0 Exhaust StackOrganic Condensible

Particulate OTM - 27/28 3 330 0 Exhaust Stack

Total PM2.5 OTM - 27/28 3 330 0 Exhaust StackInorganic (Aqueous)

Condensible Part. OTM - 27/28 3 330 0 Exhaust Stack

Filterable PM2.5 OTM - 27/28 3 330 0 Exhaust StackCobalt Method 29 3 330 0 Exhaust StackSelenium Method 29 3 330 0 Exhaust StackNickel Method 29 3 330 0 Exhaust StackAntimony Method 29 3 330 0 Exhaust StackLead Method 29 3 330 0 Exhaust StackChromium Method 29 3 330 0 Exhaust StackCadmium Method 29 3 330 0 Exhaust StackBeryllium Method 29 3 330 0 Exhaust StackArsenic Method 29 3 330 0 Exhaust StackFilterable Particulate Method 29 3 330 0 Exhaust Stack 

### Tuesday, February 01, 2011 Page 3 of 30

### Panther Creek Energy Facility 9/23/2010

The following describes any modifications and/or deviations to the applicable test methods. If alternative methods were requested, see the attachments for documentation of request AND approval, including dates. N/A Manganese Method 29 3 330 0 Exhaust StackCustom CTM 033 3 60 0 Hydrogen Cyanide Exhaust StackO2 Method 3A O2 0 Exhaust StackCo2 Method 3A CO2 0 Exhaust StackCustom Method 30B 3 150 0 Mercury Exhaust StackSulfur Dioxide Method 6C 3 60 0 Exhaust StackNitrogen oxides (NOx) Method 7E 3 60 0 Exhaust Stack



### Tuesday, February 01, 2011 Page 4 of 30

### Panther Creek Energy Facility 9/23/2010 Sampling / Stack Data Results Summary 

### Location Exhaust Stack - Method 10 Average Run Number 1 2 3 Test Date 7/21/2010 7/21/2010 7/21/2010 Run Start Time 7:05:00 AM 9:45:00 AM12:20:00 PM

Run Finish Time 9:07:00 AM 11:46:00 AM 2:21:00 PM

Carbon Dioxide, % 14 13.96 14.04 14.000 Oxygen, % 6.39 6.4 6.33 6.373 Dry Volumetric Flow Rate, dry scfm 284470 282340 284321 283,710.333 F-Factor, dscfm/MMBtu @ %O2 10600 10553 10540 10,564.333 Moisture, % 6.72 6.53 6.84 6.697 Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000



### Location Exhaust Stack - Method 23 Average Run Number 1 2 3 Test Date 7/6/2010 7/7/2010 7/8/2010 Run Start Time 7:16:00 AM 6:18:00 AM 6:13:00 AM

Run Finish Time 3:35:00 PM2:39:00 PM 2:32:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 351.070 354.378 358.085 354.511 Moisture Content of Stack Gas, % 5.52 5.50 5.89 5.637 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 14.11 14.03 14.12 14.087 Oxygen, % 6.22 6.28 6.31 6.270 Average Stack Gas Temperature, °F 341.25 338.33 336.33 338.637 Dry Volumetric Flow Rate, dry scfm 253,083.7 253,973.9 255,438.6 254,165.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 417,378.8 416,946.0 420,321.8 418,215.533 Percent Isokinetic of Sampling Rate, % 100.5 101.1 101.6 101.067 F-Factor, dscfm/MMBtu @ %O2 10215 10338 10203 10,252.000 Fw 0 0 0 0.000 Fc 0 0 0 0.000



### Tuesday, February 01, 2011 Page 5 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - Method 25A Average Run Number 1 2 3 Test Date 7/21/2010 7/21/2010 7/21/2010 Run Start Time 7:05:00 AM 9:45:00 AM12:20:00 PM

Run Finish Time 9:07:00 AM 11:46:00 AM 2:21:00 PM

Carbon Dioxide, % 14 13.96 14.04 14.000 Oxygen, % 6.39 6.4 6.33 6.373 Dry Volumetric Flow Rate, dry scfm 289096 282340 284321 285,252.333 F-Factor, dscfm/MMBtu @ %O2 10600 10553 10540 10,564.333 Moisture, % 6.72 6.53 6.84 6.697 Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000



### Location Exhaust Stack - Method 26A Average Run Number 1 2 3 Test Date 7/20/2010 7/20/2010 7/20/2010 Run Start Time 7:40:00 AM 10:30:00 AM 1:05:00 PM

Run Finish Time 9:26:00 AM 12:15:00 PM 2:50:00 PM

Net Run Time, minutes 90 90 90 Dry Gas Meter Volume Sampled, dscf 60.819 61.408 62.049 61.425 Moisture Content of Stack Gas, % 6.78 6.98 6.20 6.653 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 13.87 13.87 13.88 13.873 Oxygen, % 6.5 6.45 6.46 6.470 Average Stack Gas Temperature, °F 327.67 328.33 331.83 329.277 Dry Volumetric Flow Rate, dry scfm 261,646.0 264,471.0 268,506.9 264,874.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 415,517.8 420,841.1 425,169.0 420,509.300 Percent Isokinetic of Sampling Rate, % 103.1 103.0 102.5 102.867 F-Factor, dscfm/MMBtu @ %O2 10430 10558 10480 10,489.333 Fw 0 0 0 0.000 Fc 0 0 0 0.000



### Tuesday, February 01, 2011 Page 6 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - Method 29 Average Run Number 1 2 3 Test Date 7/15/2010 7/16/2010 7/19/2010 Run Start Time 8:09:00 AM 6:58:00 AM 7:00:00 AM

Run Finish Time 2:27:00 PM 12:54:00 PM12:55:00 PM

Net Run Time, minutes 330 330 330 Dry Gas Meter Volume Sampled, dscf 259.701 257.988 263.109 260.266 Moisture Content of Stack Gas, % 7.04 7.18 7.03 7.083 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 14.05 14.01 13.95 14.003 Oxygen, % 6.36 6.34 6.39 6.363 Average Stack Gas Temperature, °F 330.17 331.25 329.75 330.390 Dry Volumetric Flow Rate, dry scfm 263,193.0 264,902.3 266,426.0 264,840.433 Actual Wet Volumetric Flue Gas Flow Rate, acfm 418,807.0 424,000.4 426,640.4 423,149.267 Percent Isokinetic of Sampling Rate, % 104.0 102.6 104.1 103.567 F-Factor, dscfm/MMBtu @ %O2 10488 10597 10612 10,565.667 Fw 0 0 0 0.000 Fc 0 0 0 0.000



### Location Exhaust Stack - Method 6C Average Run Number 1 2 3 Test Date 7/20/2010 7/20/2010 7/20/2010 Run Start Time 7:40:00 AM 10:30:00 AM 1:05:00 PM

Run Finish Time 8:39:00 AM 11:29:00 AM 2:06:00 PM

Carbon Dioxide, % 13.87 13.87 13.88 13.873 Oxygen, % 6.5 6.45 6.46 6.470 Dry Volumetric Flow Rate, dry scfm 280685 284338 286258 283,760.333 F-Factor, dscfm/MMBtu @ %O2 10430 10558 10480 10,489.333 Moisture, % 6.79 6.99 6.2 6.660 Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000



### Tuesday, February 01, 2011 Page 7 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - Method 7E Average Run Number 1 2 3 Test Date 7/20/2010 7/20/2010 7/20/2010 Run Start Time 7:40:00 AM 10:30:00 AM 1:05:00 PM

Run Finish Time 8:39:00 AM 11:29:00 AM 2:06:00 PM

Carbon Dioxide, % 13.87 13.87 13.88 13.873 Oxygen, % 6.5 6.45 6.46 6.470 Dry Volumetric Flow Rate, dry scfm 280685 284338 286258 283,760.333 F-Factor, dscfm/MMBtu @ %O2 10430 10558 10480 10,489.333 Moisture, % 6.79 6.99 6.2 6.660 Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000



### Location Exhaust Stack - OTM - 27/28 Average Run Number 1 2 3 Test Date 7/15/2010 7/16/2010 7/19/2010 Run Start Time 8:09:00 AM 6:58:00 AM 7:00:00 AM

Run Finish Time 2:27:00 PM 12:54:00 PM 1:00:00 PM

Net Run Time, minutes 329.75 330.5 330.25 Dry Gas Meter Volume Sampled, dscf 119.359 120.800 119.548 119.902 Moisture Content of Stack Gas, % 6.90 6.96 7.84 7.233 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 14 14.01 14 14.003 Oxygen, % 6.4 6.34 6.4 6.380 Average Stack Gas Temperature, °F 333.25 333.42 331.25 332.640 Dry Volumetric Flow Rate, dry scfm 257,931.0 271,634.2 272,570.6 267,378.600 Actual Wet Volumetric Flue Gas Flow Rate, acfm 410,194.6 432,786.0 438,671.9 427,217.500 Percent Isokinetic of Sampling Rate, % 97.5 93.4 92.2 94.367 F-Factor, dscfm/MMBtu @ %O2 10488 10597 10612 10,565.667 Fw 0 0 0 0.000 Fc 0 0 0 0.000



### Tuesday, February 01, 2011 Page 8 of 30

### Panther Creek Energy Facility 9/23/2010 Emissions Summary 

### Location: Exhaust Stack - Method 10 Compound: Carbon Monoxide Average Run 1 2 3 lb/mmBtuO2 6.61E-02 6.31E-02 6.15E-02 0.064 ppm 5.96E+01 5.71E+01 5.60E+01 57.567 ppm@7%O2 5.71E+01 5.47E+01 5.34E+01 55.067



### Location: Exhaust Stack - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.0000000046 0.0000000035 0.0000000029 0.000 lb/mmBtuO2 4.20E-13 3.22E-13 2.61E-13 0.000 ng/dscm 4.63E-04 3.49E-04 2.86E-04 0.000 ng/dscm@7%O2 4.38E-04 3.32E-04 2.72E-04 0.000 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000063 0.0000000021 0.000000002 0.000 lb/mmBtuO2 5.75E-13 1.93E-13 1.80E-13 0.000 ng/dscm 6.34E-04 2.09E-04 1.97E-04 0.000 ng/dscm@7%O2 6.00E-04 1.99E-04 1.88E-04 0.000 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000028 0.0000000027 0.0000000024 0.000 lb/mmBtuO2 2.56E-13 2.48E-13 2.16E-13 0.000 ng/dscm 2.82E-04 2.69E-04 2.37E-04 0.000 ng/dscm@7%O2 2.67E-04 2.56E-04 2.26E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.000000003 0.0000000025 0.0000000027 0.000 lb/mmBtuO2 2.74E-13 2.30E-13 2.43E-13 0.000 ng/dscm 3.02E-04 2.49E-04 2.66E-04 0.000 ng/dscm@7%O2 2.86E-04 2.37E-04 2.53E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.000000005 0.000000002 0.0000000024 0.000 lb/mmBtuO2 4.57E-13 1.84E-13 2.16E-13 0.000 ng/dscm 5.03E-04 1.99E-04 2.37E-04 0.000 ng/dscm@7%O2 4.76E-04 1.89E-04 2.26E-04 0.000 

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

### Tuesday, February 01, 2011 Page 9 of 30

### Panther Creek Energy Facility 9/23/2010 RunNumber 1 2 3 Mass_mg 0.0000000032 0.0000000027 0.0000000028 0.000 lb/mmBtuO2 2.92E-13 2.48E-13 2.52E-13 0.000 ng/dscm 3.22E-04 2.69E-04 2.76E-04 0.000 ng/dscm@7%O2 3.05E-04 2.56E-04 2.63E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000027 0.0000000019 0.0000000023 0.000 lb/mmBtuO2 2.47E-13 1.75E-13 2.07E-13 0.000 ng/dscm 2.72E-04 1.89E-04 2.27E-04 0.000 ng/dscm@7%O2 2.58E-04 1.80E-04 2.16E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000029 0.0000000025 0.0000000026 0.000 lb/mmBtuO2 2.65E-13 2.30E-13 2.34E-13 0.000 ng/dscm 2.92E-04 2.49E-04 2.56E-04 0.000 ng/dscm@7%O2 2.76E-04 2.37E-04 2.44E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000022 0.0000000024 0.0000000029 0.000 lb/mmBtuO2 2.01E-13 2.21E-13 2.61E-13 0.000 ng/dscm 2.21E-04 2.39E-04 2.86E-04 0.000 ng/dscm@7%O2 2.09E-04 2.27E-04 2.72E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.0000000028 0.000000003 0.0000000028 0.000 lb/mmBtuO2 2.56E-13 2.76E-13 2.52E-13 0.000 ng/dscm 2.82E-04 2.99E-04 2.76E-04 0.000 ng/dscm@7%O2 2.67E-04 2.84E-04 2.63E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000032 0.0000000029 0.0000000026 0.000 lb/mmBtuO2 2.92E-13 2.67E-13 2.34E-13 0.000 ng/dscm 3.22E-04 2.89E-04 2.56E-04 0.000 ng/dscm@7%O2 3.05E-04 2.75E-04 2.44E-04 0.000 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 2 3 Mass_mg 0.00000000000028 0.00000000000023 0.00000000000016 0.000 lb/mmBtuO2 2.56E-17 2.11E-17 1.44E-17 0.000 ng/dscm 2.82E-08 2.29E-08 1.58E-08 0.000 ng/dscm@7%O2 2.67E-08 2.18E-08 1.51E-08 0.000



### Tuesday, February 01, 2011 Page 10 of 30

### Panther Creek Energy Facility 9/23/2010 Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 2 3 Mass_mg 0.0000000000021 0.0000000000023 0.0000000000015 0.000 lb/mmBtuO2 1.92E-16 2.11E-16 1.35E-16 0.000 ng/dscm 2.11E-07 2.29E-07 1.48E-07 0.000 ng/dscm@7%O2 2.00E-07 2.18E-07 1.41E-07 0.000 

### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 2 3 Mass_mg 0.0000000000054 0.0000000000051 0.000000000003 0.000 lb/mmBtuO2 4.93E-16 4.69E-16 2.70E-16 0.000 ng/dscm 5.43E-07 5.08E-07 2.96E-07 0.000 ng/dscm@7%O2 5.14E-07 4.83E-07 2.82E-07 0.000 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 2 3 Mass_mg 0.00000000000087 0.0000000000009 0.00000000000048 0.000 lb/mmBtuO2 7.95E-17 8.27E-17 4.32E-17 0.000 ng/dscm 8.75E-08 8.97E-08 4.73E-08 0.000 ng/dscm@7%O2 8.29E-08 8.53E-08 4.51E-08 0.000 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 2 3 Mass_mg 0.00000000000045 0.00000000000045 0.00000000000029 0.000 lb/mmBtuO2 4.11E-17 4.14E-17 2.61E-17 0.000 ng/dscm 4.53E-08 4.49E-08 2.86E-08 0.000 ng/dscm@7%O2 4.29E-08 4.27E-08 2.72E-08 0.000 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 2 3 Mass_mg 0.000000000015 0.000000000015 0.0000000000093 0.000 lb/mmBtuO2 1.37E-15 1.38E-15 8.37E-16 0.000 ng/dscm 1.51E-06 1.50E-06 9.17E-07 0.000 ng/dscm@7%O2 1.43E-06 1.43E-06 8.74E-07 0.000 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 2 3 Mass_mg 0.00000000000017 0.00000000000024 0.0000000000003 0.000 lb/mmBtuO2 1.55E-17 2.21E-17 2.70E-17 0.000 ng/dscm 1.71E-08 2.39E-08 2.96E-08 0.000 ng/dscm@7%O2 1.62E-08 2.27E-08 2.82E-08 0.000 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000021 0.0000000023 0.0000000026 0.000 lb/mmBtuO2 1.92E-13 2.11E-13 2.34E-13 0.000



### Tuesday, February 01, 2011 Page 11 of 30

### Panther Creek Energy Facility 9/23/2010 ng/dscm 2.11E-04 2.29E-04 2.56E-04 0.000 ng/dscm@7%O2 2.00E-04 2.18E-04 2.44E-04 0.000 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000067 0.0000000028 0.0000000025 0.000 lb/mmBtuO2 6.12E-13 2.57E-13 2.25E-13 0.000 ng/dscm 6.74E-04 2.79E-04 2.47E-04 0.000 ng/dscm@7%O2 6.38E-04 2.65E-04 2.35E-04 0.000 

### Compound: 2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000028 0.0000000031 0.0000000033 0.000 lb/mmBtuO2 2.56E-13 2.85E-13 2.97E-13 0.000 ng/dscm 2.82E-04 3.09E-04 3.25E-04 0.000 ng/dscm@7%O2 2.67E-04 2.94E-04 3.10E-04 0.000 

### Compound: 2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.0000000215 0.000000003 0.0000000028 0.000 lb/mmBtuO2 1.96E-12 2.76E-13 2.52E-13 0.000 ng/dscm 2.16E-03 2.99E-04 2.76E-04 0.001 ng/dscm@7%O2 2.05E-03 2.84E-04 2.63E-04 0.001 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 2 3 Mass_mg 0.00000000012 0.00000000014 0.00000000026 0.000 lb/mmBtuO2 1.10E-14 1.29E-14 2.34E-14 0.000 ng/dscm 1.21E-05 1.40E-05 2.56E-05 0.000 ng/dscm@7%O2 1.15E-05 1.33E-05 2.44E-05 0.000 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 2 3 Mass_mg 0.00000000044 0.00000000059 0.00000000099 0.000 lb/mmBtuO2 4.02E-14 5.42E-14 8.91E-14 0.000 ng/dscm 4.43E-05 5.88E-05 9.76E-05 0.000 ng/dscm@7%O2 4.19E-05 5.59E-05 9.30E-05 0.000 

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 1 2 3 Mass_mg 0.0000000000069 0.0000000000057 0.0000000000035 0.000 lb/mmBtuO2 6.30E-16 5.24E-16 3.15E-16 0.000 ng/dscm 6.94E-07 5.68E-07 3.45E-07 0.000 ng/dscm@7%O2 6.57E-07 5.40E-07 3.29E-07 0.000 

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

### Tuesday, February 01, 2011 Page 12 of 30

### Panther Creek Energy Facility 9/23/2010 Mass_mg 0.0000000000018 0.0000000000025 0.0000000000039 0.000 lb/mmBtuO2 1.64E-16 2.30E-16 3.51E-16 0.000 ng/dscm 1.81E-07 2.49E-07 3.85E-07 0.000 ng/dscm@7%O2 1.71E-07 2.37E-07 3.67E-07 0.000 

### Compound: Total TEQ Average RunNumber 1 2 3 Mass_mg 0.0000000121 0.00000000905 0.00000000912 0.000 lb/mmBtuO2 1.11E-12 8.32E-13 8.21E-13 0.000 ng/dscm 1.22E-03 9.02E-04 9.00E-04 0.001 ng/dscm@7%O2 1.16E-03 8.58E-04 8.57E-04 0.001



### Location: Exhaust Stack - Method 25A 

### Compound: Total organic compounds (TOC) as Average Run 1 2 3 lb/mmBtuO2 9.68E-04 6.63E-04 6.35E-04 0.001 ppm 5.54E-01 3.81E-01 3.67E-01 0.434 ppm@7%O2 5.31E-01 3.65E-01 3.50E-01 0.415



### Location: Exhaust Stack - Method 26A 

### Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 21.25 21.25 22.49 21.663 lb/mmBtuO2 1.17E-02 1.17E-02 1.21E-02 0.012 

### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 3.45 3.5 3.4 3.450 lb/mmBtuO2 1.89E-03 1.92E-03 1.83E-03 0.002



### Location: Exhaust Stack - Method 29 

### Compound: Antimony Average RunNumber 2 3 1 Mass_mg 0.0018 0.0018 0.0019 0.002 lb/mmBtuO2 2.34E-07 2.31E-07 2.43E-07 0.000 

### Compound: Arsenic Average RunNumber 2 3 1 Mass_mg 0.00269 0.00302 0.00337 0.003 lb/mmBtuO2 3.50E-07 3.87E-07 4.31E-07 0.000 

### Compound: Beryllium Average RunNumber 2 3 1 Mass_mg 0.00045 0.00045 0.00045 0.000 lb/mmBtuO2 5.85E-08 5.76E-08 5.76E-08 0.000



### Tuesday, February 01, 2011 Page 13 of 30

### Panther Creek Energy Facility 9/23/2010 Compound: Cadmium Average RunNumber 2 3 1 Mass_mg 0.00073 0.00085 0.00099 0.001 lb/mmBtuO2 9.49E-08 1.09E-07 1.27E-07 0.000 

### Compound: Chromium Average RunNumber 2 3 1 Mass_mg 0.01122 0.01356 0.01173 0.012 lb/mmBtuO2 1.46E-06 1.74E-06 1.50E-06 0.000 

### Compound: Cobalt Average RunNumber 2 3 1 Mass_mg 0.00162 0.00177 0.00176 0.002 lb/mmBtuO2 2.11E-07 2.27E-07 2.25E-07 0.000 

### Compound: Filterable Particulate Average RunNumber 2 3 1 Mass_mg 54.4 56.3 58.4 56.367 lb/mmBtuO2 7.07E-03 7.21E-03 7.47E-03 0.007 

### Compound: Lead Average RunNumber 2 3 1 Mass_mg 0.01689 0.01142 0.02535 0.018 lb/mmBtuO2 2.20E-06 1.46E-06 3.24E-06 0.000 

### Compound: Manganese Average RunNumber 2 1 3 Mass_mg 0.01766 0.01556 0.02016 0.018 lb/mmBtuO2 2.30E-06 1.99E-06 2.58E-06 0.000 

### Compound: Nickel Average RunNumber 2 1 3 Mass_mg 0.00684 0.00654 0.00814 0.007 lb/mmBtuO2 8.89E-07 8.37E-07 1.04E-06 0.000 

### Compound: Selenium Average RunNumber 2 1 3 Mass_mg 0.0045 0.005 0.0045 0.005 lb/mmBtuO2 5.85E-07 6.40E-07 5.76E-07 0.000



### Location: Exhaust Stack - Method 6C 

### Compound: Sulfur Dioxide Average Run 1 2 3 lb/mmBtuO2 1.43E-01 1.38E-01 1.35E-04 0.094 

### Tuesday, February 01, 2011 Page 14 of 30

### Panther Creek Energy Facility 9/23/2010

Process Run Data ppm 5.68E+01 5.43E+01 5.34E-02 37.051 ppm@7%O2 5.48E+01 5.22E+01 5.14E-02 35.684



### Location: Exhaust Stack - Method 7E Compound: Nitrogen oxides (NOx) Average Run 1 2 3 lb/mmBtuO2 1.37E-01 1.35E-01 1.33E-01 0.135 ppm 7.61E+01 7.42E+01 7.34E+01 74.567 ppm@7%O2 7.35E+01 7.14E+01 7.07E+01 71.867



### Location: Exhaust Stack - OTM - 27/28 Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 29.6 32.2 27.1 29.633 lb/mmBtuO2 8.26E-03 8.94E-03 7.64E-03 0.008 

### Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 12 10.6 11 11.200 lb/mmBtuO2 3.35E-03 2.94E-03 3.10E-03 0.003 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 4.3 2.6 3.8 3.567 lb/mmBtuO2 1.20E-03 7.22E-04 1.07E-03 0.001 

### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 2.4 1.4 1.9 1.900 lb/mmBtuO2 6.70E-04 3.89E-04 5.36E-04 0.001 

### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 36.3 36.2 32.8 35.100 lb/mmBtuO2 1.01E-02 1.00E-02 9.25E-03 0.010 

### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 18.7 14.6 16.7 16.667 lb/mmBtuO2 5.22E-03 4.05E-03 4.71E-03 0.005



### Tuesday, February 01, 2011 Page 15 of 30

### Panther Creek Energy Facility 9/23/2010 Process Run Data



### Run Name Value UOM Comments Target Value 1 MW Output 90 MW M23 Test Run 1 - 7/6/10 7:16-15:35 0



### 10MW Output 920 MW M7E, 6C, 26A and CTM033 Test Run 1 - 7/20/10 7:30- 8:30 0

11MW Output 91.5 MW M7E, 6C, 26A and CTM033 Test Run 2 - 7/20/10 10:30- 11:30 0

12MW Output 92 MW M7E, 6C, 26A and CTM033 Test Run 3 - 7/20/10 13:00- 14:00 0

13MW Output 91.5 MW M0011, 10, 25A Test Run1 - 7/21/10 7:00-9:00 0

14MW Output 91 MW M0011, 10, 25A Test Run 2 - 7/21/10 10:00- 12:00 0

15MW Output 91 MW M0011, 10, 25A Test Run 3 - 7/21/10 12:30- 14:30 0

2 MW Output 90.2 MW M23 Test Run 2 - 7/7/10 6:18-14:39 0

3 MW Output 90 MW M23 Test Run 3 - 7/8/10 6:13-14:32 0



### 4 MW Output 91 MW M29, OTM 27/28 Test Run 1 - 7/15/10 8:00-15:00 0

5 MW Output 91 MW M29, OTM 27/28 Test Run 2 - 7/16/10 7:00-13:00 0

6 MW Output 91 MW M29, OTM 27/28 Test Run 3 - 7/19/10 7:00-13:00 0



### 7 MW Output 92 MW Hg Test Run 1 - 7/19/10 7:00-9:30 0

8 MW Output 90 MW Hg Test Run 2 - 7/19/10 10:00- 12:30 0



### Tuesday, February 01, 2011 Page 16 of 30

### Panther Creek Energy Facility 9/23/2010 9 MW Output 91 MW HG Test Run 3 - 7/16/10 13:00- 15:30 0

1 Steam Flow - BLR 1 386 klbs/hr 0 10Steam Flow - BLR 1 393 klbs/hr 0 

### 11 Steam Flow - BLR 1 390 klbs/hr 0 12Steam Flow - BLR 1 394.5 klbs/hr 0 13Steam Flow - BLR 1 390 klbs/hr 0 

### 14Steam Flow - BLR 1 388.5 klbs/hr 0 15Steam Flow - BLR 1 390 klbs/hr 0 

### 2 Steam Flow - BLR 1 387 klbs/hr 0 3 Steam Flow - BLR 1 385 klbs/hr 0 4 Steam Flow - BLR 1 390 klbs/hr 0 

### 5 Steam Flow - BLR 1 391 klbs/hr 0 6 Steam Flow - BLR 1 389 klbs/hr 0 7 Steam Flow - BLR 1 392 klbs/hr 0 

### 8 Steam Flow - BLR 1 388 klbs/hr 0 9 Steam Flow - BLR 1 387 klbs/hr 0 1 Waste Anthracite Fuel Feed - BLR 1 87.3 klbs/hr 0 

### 10Waste Anthracite Fuel Feed - BLR 1 87.5 klbs/hr 0 11Waste Anthracite Fuel Feed - BLR 1 87.5 klbs/hr 0 12Waste Anthracite Fuel Feed - BLR 1 87.5 klbs/hr 0 

### 13Waste Anthracite Fuel Feed - BLR 1 87.5 klbs/hr 0 14Waste Anthracite Fuel Feed - BLR 1 87.05 klbs/hr 0 15Waste Anthracite Fuel Feed - BLR 1 86.8 klbs/hr 0 

### 2 Waste Anthracite Fuel Feed - BLR 1 86.5 klbs/hr 0 3 Waste Anthracite Fuel Feed - BLR 1 89.2 klbs/hr 0 4 Waste Anthracite Fuel Feed - BLR 1 87.1 klbs/hr 0 

### 5 Waste Anthracite Fuel Feed - BLR 1 85.7 klbs/hr 0 6 Waste Anthracite Fuel Feed - BLR 1 85 klbs/hr 0 7 Waste Anthracite Fuel Feed - BLR 1 85 klbs/hr 0 

### 8 Waste Anthracite Fuel Feed - BLR 1 84.5 klbs/hr 0 9 Waste Anthracite Fuel Feed - BLR 1 85.1 klbs/hr 0 1 Stack O2 6.22 % 0 

### 10Stack O2 6.5 % 0 11 Stack O2 6.45 % 0 12Stack O2 6.46 % 0



### Tuesday, February 01, 2011 Page 17 of 30

### Panther Creek Energy Facility 9/23/2010 13Stack O2 6.39 % 0 

### 14Stack O2 6.4 % 0 15Stack O2 6.33 % 0 2 Stack O2 6.28 % 0 

### 3 Stack O2 6.31 % 0 4 Stack O2 6.36 % 0 5 Stack O2 6.34 % 0 

### 6 Stack O2 6.39 % 0 7 Stack O2 6.37 % 0 8 Stack O2 6.4 % 0 

### 9 Stack O2 6.32 % 0 1 Stack CO2 14.11 % 0 10Stack CO2 13.87 % 0 

### 11 Stack CO2 13.87 % 0 12Stack CO2 13.88 % 0 13Stack CO2 14 % 0 

### 14Stack CO2 13.96 % 0 15Stack CO2 14.04 % 0 2 Stack CO2 14.03 % 0 

### 3 Stack CO2 14.12 % 0 4 Stack CO2 14.05 % 0 

### 5 Stack CO2 14.01 % 0 6 Stack CO2 13.95 % 0 7 Stack CO2 13.96 % 0 

### 8 Stack CO2 13.94 % 0 9 Stack CO2 14.01 % 0 1 Stack Moisture 5.53 % 0 

### 10Stack Moisture 6.79 % 0 11 Stack Moisture 6.99 % 0 12Stack Moisture 6.2 % 0 

### 13Stack Moisture 6.72 % 0 14Stack Moisture 6.53 % 0 15Stack Moisture 6.84 % 0 

### 2 Stack Moisture 5.5 % 0 3 Stack Moisture 5.89 % 0 4 Stack Moisture 7.03 % 0



### Tuesday, February 01, 2011 Page 18 of 30

### Panther Creek Energy Facility 9/23/2010 5 Stack Moisture 7.2 % 0 

### 6 Stack Moisture 7.04 % 0 7 Stack Moisture 7.04 % 0 8 Stack Moisture 7.04 % 0 

### 9 Stack Moisture 7.41 % 0 1 Stack Flow 267873 scfm 0 10Stack Flow 280685 scfm 0 

### 11 Stack Flow 284338 scfm 0 12Stack Flow 286258 scfm 0 13Stack Flow 284470 scfm 0 

### 14Stack Flow 282340 scfm 0 15Stack Flow 284321 scfm 0 2 Stack Flow 268764 scfm 0 

### 3 Stack Flow 271410 scfm 0 4 Stack Flow 283525 scfm 0 5 Stack Flow 285397 scfm 0 

### 6 Stack Flow 286584 scfm 0 7 Stack Flow 286584 scfm 0 8 Stack Flow 286584 scfm 0 

### 9 Stack Flow 286584 scfm 0 1 Stack Temp 341 F 0 

### 10Stack Temp 328 F 0 11 Stack Temp 328 F 0 12Stack Temp 332 F 0 

### 13Stack Temp 327 F 0 14Stack Temp 332 F 0 15Stack Temp 334 F 0 

### 2 Stack Temp 338 F 0 3 Stack Temp 336 F 0 4 Stack Temp 330 F 0 

### 5 Stack Temp 331 F 0 6 Stack Temp 330 F 0 7 Stack Temp 337 F 0 

### 8 Stack Temp 344 F 0 9 Stack Temp 339 F 0 1 Waste Anthracite Fuel Feed - BLR 2 77.5 klbs/hr 0



### Tuesday, February 01, 2011 Page 19 of 30

### Panther Creek Energy Facility 9/23/2010

APCD Run Data 10Waste Anthracite Fuel Feed - BLR 2 77 klbs/hr 0 

### 11Waste Anthracite Fuel Feed - BLR 2 76.5 klbs/hr 0 12Waste Anthracite Fuel Feed - BLR 2 77 klbs/hr 0 13Waste Anthracite Fuel Feed - BLR 2 76 klbs/hr 0 

### 14Waste Anthracite Fuel Feed - BLR 2 75.6 klbs/hr 0 15Waste Anthracite Fuel Feed - BLR 2 75.7 klbs/hr 0 2 Waste Anthracite Fuel Feed - BLR 2 76 klbs/hr 0 

### 3 Waste Anthracite Fuel Feed - BLR 2 79.3 klbs/hr 0 4 Waste Anthracite Fuel Feed - BLR 2 76.3 klbs/hr 0 5 Waste Anthracite Fuel Feed - BLR 2 75.7 klbs/hr 0 

### 6 Waste Anthracite Fuel Feed - BLR 2 75.3 klbs/hr 0 7 Waste Anthracite Fuel Feed - BLR 2 74.8 klbs/hr 0 8 Waste Anthracite Fuel Feed - BLR 2 75 klbs/hr 0 

### 9 Waste Anthracite Fuel Feed - BLR 2 76 klbs/hr 0 1 Steam Flow - BLR 2 380 klbs./hr 0 10Steam Flow - BLR 2 383 klbs./hr 0 

### 11 Steam Flow - BLR 2 384 klbs./hr 0 12Steam Flow - BLR 2 385 klbs./hr 0 13Steam Flow - BLR 2 380 klbs./hr 0 

### 14Steam Flow - BLR 2 380 klbs./hr 0 15Steam Flow - BLR 2 378 klbs./hr 0 

### 2 Steam Flow - BLR 2 378 klbs./hr 0 3 Steam Flow - BLR 2 380 klbs./hr 0 4 Steam Flow - BLR 2 380 klbs./hr 0 

### 5 Steam Flow - BLR 2 382 klbs./hr 0 6 Steam Flow - BLR 2 383 klbs./hr 0 7 Steam Flow - BLR 2 386 klbs./hr 0 

### 8 Steam Flow - BLR 2 380 klbs./hr 0 9 Steam Flow - BLR 2 382 klbs./hr 0

Run Name Value UOM Comments Target Value 1 BLR 1 Baghouse Pressure Drop 5.02 " H2O 0 

### 10BLR 1 Baghouse Pressure Drop 5.11 " H2O 0 11 BLR 1 Baghouse Pressure Drop 4.99 " H2O 0 12BLR 1 Baghouse Pressure Drop 5.03 " H2O 0



### Tuesday, February 01, 2011 Page 20 of 30

### Panther Creek Energy Facility 9/23/2010 13BLR 1 Baghouse Pressure Drop 5 " H2O 0 

### 14BLR 1 Baghouse Pressure Drop 5.03 " H2O 0 15BLR 1 Baghouse Pressure Drop 5.02 " H2O 0 16BLR 1 Baghouse Pressure Drop 5.02 " H2O 0 

### 2 BLR 1 Baghouse Pressure Drop 5.02 " H2O 0 3 BLR 1 Baghouse Pressure Drop 5.01 " H2O 0 4 BLR 1 Baghouse Pressure Drop 5.2 " H2O 0 

### 5 BLR 1 Baghouse Pressure Drop 5.17 " H2O 0 6 BLR 1 Baghouse Pressure Drop 5.11 " H2O 0 7 BLR 1 Baghouse Pressure Drop 5.11 " H2O 0 

### 8 BLR 1 Baghouse Pressure Drop 5.28 " H2O 0 9 BLR 1 Baghouse Pressure Drop 5.15 " H2O 0 1 BLR1 Dry Limestone Injection 6262 Lbs/hr 0 

### 10BLR1 Dry Limestone Injection 4427 Lbs/hr 0 11 BLR1 Dry Limestone Injection 4858 Lbs/hr 0 12BLR1 Dry Limestone Injection 4858 Lbs/hr 0 

### 13BLR1 Dry Limestone Injection 4858 Lbs/hr 0 14BLR1 Dry Limestone Injection 4885 Lbs/hr 0 15BLR1 Dry Limestone Injection 4855 Lbs/hr 0 

### 16BLR1 Dry Limestone Injection 4885 Lbs/hr 0 2 BLR1 Dry Limestone Injection 4804 Lbs/hr 0 

### 3 BLR1 Dry Limestone Injection 4870 Lbs/hr 0 4 BLR1 Dry Limestone Injection 5325 Lbs/hr 0 5 BLR1 Dry Limestone Injection 4850 Lbs/hr 0 

### 6 BLR1 Dry Limestone Injection 4427 Lbs/hr 0 7 BLR1 Dry Limestone Injection 4427 Lbs/hr 0 8 BLR1 Dry Limestone Injection 4427 Lbs/hr 0 

### 9 BLR1 Dry Limestone Injection 4427 Lbs/hr 0 1 BLR 2 Baghouse Pressure Drop 4.83 " H2O 0 10BLR 2 Baghouse Pressure Drop 4.85 " H2O 0 

### 11 BLR 2 Baghouse Pressure Drop 4.91 " H2O 0 12BLR 2 Baghouse Pressure Drop 4.8 " H2O 0 13BLR 2 Baghouse Pressure Drop 4.92 " H2O 0 

### 14BLR 2 Baghouse Pressure Drop 4.9 " H2O 0 15BLR 2 Baghouse Pressure Drop 4.9 " H2O 0 16BLR 2 Baghouse Pressure Drop 4.82 " H2O 0



### Tuesday, February 01, 2011 Page 21 of 30

### Panther Creek Energy Facility 9/23/2010

Process Lab Run Data 2 BLR 2 Baghouse Pressure Drop 4.86 " H2O 0 

### 3 BLR 2 Baghouse Pressure Drop 4.52 " H2O 0 4 BLR 2 Baghouse Pressure Drop 4.54 " H2O 0 5 BLR 2 Baghouse Pressure Drop 4.57 " H2O 0 

### 6 BLR 2 Baghouse Pressure Drop 4.77 " H2O 0 7 BLR 2 Baghouse Pressure Drop 4.77 " H2O 0 8 BLR 2 Baghouse Pressure Drop 4.8 " H2O 0 

### 9 BLR 2 Baghouse Pressure Drop 4.83 " H2O 0 1 BLR 2 Dry Limestone Injection 5128 Lbs/hr 0 10BLR 2 Dry Limestone Injection 3795 Lbs/hr 0 

### 11 BLR 2 Dry Limestone Injection 4137 Lbs/hr 0 12BLR 2 Dry Limestone Injection 4137 Lbs/hr 0 13BLR 2 Dry Limestone Injection 4137 Lbs/hr 0 

### 14BLR 2 Dry Limestone Injection 3955 Lbs/hr 0 15BLR 2 Dry Limestone Injection 3955 Lbs/hr 0 16BLR 2 Dry Limestone Injection 3955 Lbs/hr 0 

### 2 BLR 2 Dry Limestone Injection 4121 Lbs/hr 0 3 BLR 2 Dry Limestone Injection 4192 Lbs/hr 0 4 BLR 2 Dry Limestone Injection 4009 Lbs/hr 0 

### 5 BLR 2 Dry Limestone Injection 3920 Lbs/hr 0 6 BLR 2 Dry Limestone Injection 3795 Lbs/hr 0 

### 7 BLR 2 Dry Limestone Injection 3795 Lbs/hr 0 8 BLR 2 Dry Limestone Injection 3795 Lbs/hr 0 9 BLR 2 Dry Limestone Injection 3795 Lbs/hr 0



### Tuesday, February 01, 2011 Page 22 of 30

### Panther Creek Energy Facility 9/23/2010 Sampling / Stack Data Results Detail 

### Location Exhaust Stack - Method 10 Average Run Number 1 2 3 Test Date 7/21/2010 7/21/2010 7/21/2010 Run Start Time 7:05:00 AM9:45:00 AM12:20:00 PM Run Finish Time 9:07:00 AM11:46:00 AM 2:21:00 PM Carbon Dioxide, % 14 13.96 14.04 14.000 Oxygen, % 6.39 6.4 6.33 6.373 Fuel Factor 1.04 1.04 1.04 Dry Volumetric Flow Rate, dry scfm 284470 282340 284321283,710.333 F-Factor, dscfm/MMBtu @ %O2 10600 10553 1054010,564.333 Moisture, % 6.72 6.53 6.84 6.697 Analyzer Make Thermo Electron Thermo

Electron Thermo

Electron Analyzer Model 48C 48C 48C Analyzer Serial Number 48C-67476- 35648C-67476-

35648-67476-356 Operating Range 126 126 126 126.000 Operating Units ppm ppm ppm No. Readings/Avg. 120 120 120 120.000 Calibration Set 10 11 12 11.000 Calibration Pre Zero Cylinder ID CC-133012 CC-133012 CC-133012 Calibration Pre Zero Cylinder Instrument Response 0.28 0.15 0.94 0.457 Calibration Pre Zero Cylinder Bias 0 -0.1 0.52 0.140 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC-91200 CC-91200 CC-91200 Calibration Pre High Cylinder Instrument Response 49.78 49.25 49.25 49.427 Calibration Pre High Cylinder Bias 0.1 -0.32 -0.32 -0.180 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID CC-133012 CC-133012 CC-133012 Calibration Post Zero Cylinder Instrument Response 0.15 0.94 0.8 0.630 Calibration Post Zero Cylinder Bias -0.1 0.52 0.41 0.277 Calibration Post Zero Cylinder Drift 0.1 0.62 0.11 0.277 Calibration Post High Cylinder ID CC-91200 CC-91200 CC-91200 Calibration Post High Cylinder Instrument Response 49.25 49.25 49.38 49.293 Calibration Post High Cylinder Bias -0.32 -0.32 -0.21 -0.283 Calibration Post High Cylinder Drift 0.42 0 0.11 0.177 Cavg 59.32 56.48 55.42 57.073 Cavg Units ppmvd ppmvd ppmvd Cgas 59.5846 57.0777 55.9632 57.542 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 01, 2011 Page 23 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - Method 23 Average Run Number 1 2 3 Test Date 7/6/2010 7/7/2010 7/8/2010 Run Start Time 7:16:00 AM6:18:00 AM 6:13:00 AM Run Finish Time 3:35:00 PM 2:39:00 PM 2:32:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.195 0.195 0.195 0.195 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.992 0.992 0.992 0.992 Barometric Pressure, inches of Mercury 28.82 28.85 28.82 28.830 Average Orifice Meter Differential, inches H2O 2.07 2.09 2.10 2.087 Dry Gas Meter Volume Sampled, cubic feet 398.822 398.067 402.284 399.724 Average Dry Gas Meter Temperature, °F 116.17 110.33 109.83 112.110 Dry Gas Meter Volume Sampled, dscf 351.070 354.378 358.085 354.511 Total Moisture Liquid collected, g 436 438 476 450.000 Volume of Water Vapor, standard cubic feet 20.52 20.62 22.41 21.183 Moisture Content of Stack Gas, % 5.52 5.50 5.89 5.637 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9448 0.945 0.9411 0.944 Carbon Dioxide, % 14.11 14.03 14.12 14.087 Oxygen, % 6.22 6.28 6.31 6.270 Carbon Monoxide & Nitrogen, % 79.67 79.69 79.57 79.643 Fuel Factor 1.04 1.04 1.03 Dry Molecular Weight, lb/lb-Mole 30.51 30.50 30.51 30.507 Wet Molecular weight, lb/lb-Mole 29.82 29.81 29.77 29.800 Flue Gas Static Pressure, inches of H2O 4.31 4.23 4.33 4.290 Absolute Flue Gas Pressure, inches of Mercury 29.14 29.16 29.14 29.147 Average Stack Gas Temperature, °F 341.25 338.33 336.33 338.637 Average Velocity Head, inches of H2O 1.9558537813 26041.959616191

099131.992712440

615 1.969 Average Stack Gas Velocity, feet/second 96.44 96.34 97.12 96.633 Stack Cross-Sectional Area, square feet 72.131 72.131 72.131 72.131 Dry Volumetric Flow Rate, dry scfm 253,083.7 253,973.9 255,438.6254,165.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 417,378.8 416,946.0 420,321.8418,215.533 Percent Isokinetic of Sampling Rate, % 100.5 101.1 101.6 101.067 Percent Excess Air, % 42.0 42.6 42.9 42.500 F-Factor, dscfm/MMBtu @ %O2 10215 10338 1020310,252.000 Round Duct Diameter, inches 115 115 115 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



### Tuesday, February 01, 2011 Page 24 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - Method 25A Average Run Number 1 2 3 Test Date 7/21/2010 7/21/2010 7/21/2010 Run Start Time 7:05:00 AM9:45:00 AM12:20:00 PM Run Finish Time 9:07:00 AM11:46:00 AM 2:21:00 PM Carbon Dioxide, % 14 13.96 14.04 14.000 Oxygen, % 6.39 6.4 6.33 6.373 Fuel Factor 1.04 1.04 1.04 Dry Volumetric Flow Rate, dry scfm 289096 282340 284321285,252.333 F-Factor, dscfm/MMBtu @ %O2 10600 10553 1054010,564.333 Moisture, % 6.72 6.53 6.84 6.697 Analyzer Make JUM JUM JUM Analyzer Model VE-7 VE-7 VE-7 Analyzer Serial Number Operating Range 15 15 15 15.000 Operating Units ppm ppm ppm No. Readings/Avg. 120 120 120 120.000 Calibration Set 1 2 3 2.000 Calibration Pre Zero Cylinder ID CC-133012 CC-133012 CC-133012 Calibration Pre Zero Cylinder Instrument Response 0.01 0.1 0.11 0.073 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 CC-98752 CC-98752 CC-98752 Calibration Pre High Cylinder Instrument Response 6.35 6.3 6.3 6.317 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 CC-133012 CC-133012 CC-133012 Calibration Post Zero Cylinder Instrument Response -0.16 0.04 0.3 0.060 Calibration Post Zero Cylinder Bias -1.13 -0.4 1.27 -0.087 Calibration Post Zero Cylinder Drift 1.13 0.4 1.27 0.933 Calibration Post High Cylinder ID CC-98752 CC-98752 CC-98752 Calibration Post High Cylinder Instrument Response 5.98 6.03 5.93 5.980 Calibration Post High Cylinder Bias -2.47 -1.8 -2.47 -2.247 Calibration Post High Cylinder Drift 2.47 1.8 2.47 2.247 Cavg 0.46 0.43 0.54 0.477 Cavg Units ppmvw ppmvw ppmvw Cgas 0.5542 0.381 0.3669 0.434 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 0.5169951923 076920.356160787

5307630.341802030

456853 0.405 Cgasw Units ppmvw ppmvw ppmvw



### Tuesday, February 01, 2011 Page 25 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - Method 26A Average Run Number 1 2 3 Test Date 7/20/2010 7/20/2010 7/20/2010 Run Start Time 7:40:00 AM10:30:00 AM 1:05:00 PM Run Finish Time 9:26:00 AM12:15:00 PM 2:50:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 90 90 90 Nozzle Diameter, inches 0.182 0.182 0.182 0.182 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9998 0.9998 0.9998 1.000 Barometric Pressure, inches of Mercury 29.83 29.85 29.88 29.853 Average Orifice Meter Differential, inches H2O 1.51 1.54 1.56 1.537 Dry Gas Meter Volume Sampled, cubic feet 62.697 63.751 65.629 64.026 Average Dry Gas Meter Temperature, °F 84.58 88.83 99.75 91.053 Dry Gas Meter Volume Sampled, dscf 60.819 61.408 62.049 61.425 Total Moisture Liquid collected, g 94 98 87 93.000 Volume of Water Vapor, standard cubic feet 4.42 4.61 4.10 4.377 Moisture Content of Stack Gas, % 6.78 6.98 6.20 6.653 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9322 0.9302 0.938 0.933 Carbon Dioxide, % 13.87 13.87 13.88 13.873 Oxygen, % 6.5 6.45 6.46 6.470 Carbon Monoxide & Nitrogen, % 79.63 79.68 79.66 79.657 Fuel Factor 1.04 1.04 1.04 Dry Molecular Weight, lb/lb-Mole 30.48 30.48 30.48 30.480 Wet Molecular weight, lb/lb-Mole 29.63 29.61 29.71 29.650 Flue Gas Static Pressure, inches of H2O 4.4 4.48 4.43 4.437 Absolute Flue Gas Pressure, inches of Mercury 30.15 30.18 30.21 30.180 Average Stack Gas Temperature, °F 327.67 328.33 331.83 329.277 Average Velocity Head, inches of H2O 2.0273122617 06452.078492182

770972.121414155

42651 2.076 Average Stack Gas Velocity, feet/second 96.01 97.24 98.24 97.163 Stack Cross-Sectional Area, square feet 72.131 72.131 72.131 72.131 Dry Volumetric Flow Rate, dry scfm 261,646.0 264,471.0 268,506.9264,874.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 415,517.8 420,841.1 425,169.0420,509.300 Percent Isokinetic of Sampling Rate, % 103.1 103.0 102.5 102.867 Percent Excess Air, % 44.8 44.2 44.3 44.433 F-Factor, dscfm/MMBtu @ %O2 10430 10558 1048010,489.333 Round Duct Diameter, inches 115 115 115 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



### Tuesday, February 01, 2011 Page 26 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - Method 29 Average Run Number 1 2 3 Test Date 7/15/2010 7/16/2010 7/19/2010 Run Start Time 8:09:00 AM6:58:00 AM 7:00:00 AM Run Finish Time 2:27:00 PM12:54:00 PM12:55:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 330 330 330 Nozzle Diameter, inches 0.195 0.195 0.195 0.195 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9998 0.9998 0.9998 1.000 Barometric Pressure, inches of Mercury 29.94 29.85 29.74 29.843 Average Orifice Meter Differential, inches H2O 2.01 2.05 2.08 2.047 Dry Gas Meter Volume Sampled, cubic feet 273.064 274.321 280.446 275.944 Average Dry Gas Meter Temperature, °F 98.17 102.83 102.17 101.057 Dry Gas Meter Volume Sampled, dscf 259.701 257.988 263.109 260.266 Total Moisture Liquid collected, g 418 424 423 421.667 Volume of Water Vapor, standard cubic feet 19.68 19.96 19.91 19.850 Moisture Content of Stack Gas, % 7.04 7.18 7.03 7.083 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9296 0.9282 0.9297 0.929 Carbon Dioxide, % 14.05 14.01 13.95 14.003 Oxygen, % 6.36 6.34 6.39 6.363 Carbon Monoxide & Nitrogen, % 79.59 79.65 79.66 79.633 Fuel Factor 1.03 1.04 1.04 Dry Molecular Weight, lb/lb-Mole 30.50 30.50 30.49 30.497 Wet Molecular weight, lb/lb-Mole 29.62 29.60 29.61 29.610 Flue Gas Static Pressure, inches of H2O 4.43 4.45 4.4 4.427 Absolute Flue Gas Pressure, inches of Mercury 30.27 30.18 30.06 30.170 Average Stack Gas Temperature, °F 330.17 331.25 329.75 330.390 Average Velocity Head, inches of H2O 2.0606605765 04682.101300687

449862.123647845

67904 2.095 Average Stack Gas Velocity, feet/second 96.77 97.97 98.58 97.773 Stack Cross-Sectional Area, square feet 72.131 72.131 72.131 72.131 Dry Volumetric Flow Rate, dry scfm 263,193.0 264,902.3 266,426.0264,840.433 Actual Wet Volumetric Flue Gas Flow Rate, acfm 418,807.0 424,000.4 426,640.4423,149.267 Percent Isokinetic of Sampling Rate, % 104.0 102.6 104.1 103.567 Percent Excess Air, % 43.4 43.2 43.6 43.400 F-Factor, dscfm/MMBtu @ %O2 10488 10597 1061210,565.667 Round Duct Diameter, inches 115 115 115 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



### Tuesday, February 01, 2011 Page 27 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - Method 6C Average Run Number 1 2 3 Test Date 7/20/2010 7/20/2010 7/20/2010 Run Start Time 7:40:00 AM10:30:00 AM 1:05:00 PM Run Finish Time 8:39:00 AM11:29:00 AM 2:06:00 PM Carbon Dioxide, % 13.87 13.87 13.88 13.873 Oxygen, % 6.5 6.45 6.46 6.470 Fuel Factor 1.04 1.04 1.04 Dry Volumetric Flow Rate, dry scfm 280685 284338 286258283,760.333 F-Factor, dscfm/MMBtu @ %O2 10430 10558 1048010,489.333 Moisture, % 6.79 6.99 6.2 6.660 Analyzer Make Bovar Bovar Bovar Analyzer Model 721M 721M 721M Analyzer Serial Number VD-721M8519-1 VD-721M8519-1 VD-721M8519-1 Operating Range 130 130 130 130.000 Operating Units ppm ppm ppm No. Readings/Avg. 60 60 60 60.000 Calibration Set 4 5 6 5.000 Calibration Pre Zero Cylinder ID CC-133012 CC-133012 CC-133012 Calibration Pre Zero Cylinder Instrument Response 0.02 0.95 1.8 0.923 Calibration Pre Zero Cylinder Bias -0.12 0.59 1.25 0.573 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC-19869 CC-19869 CC-19869 Calibration Pre High Cylinder Instrument Response 50.77 48.72 47.9 49.130 Calibration Pre High Cylinder Bias -2.85 -4.42 -5.05 -4.107 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID CC-133012 CC-133012 CC-133012 Calibration Post Zero Cylinder Instrument Response 0.95 1.8 1.5 1.417 Calibration Post Zero Cylinder Bias 0.59 1.25 1.02 0.953 Calibration Post Zero Cylinder Drift 0.71 0.66 0.23 0.533 Calibration Post High Cylinder ID CC-19869 CC-19869 CC-19869 Calibration Post High Cylinder Instrument Response 49.72 50.9 50.09 50.237 Calibration Post High Cylinder Bias -3.65 -2.75 -3.37 -3.257 Calibration Post High Cylinder Drift 0.8 1.67 1.68 1.383 Cavg 52.38 49.65 48.05 50.027 Cavg Units ppmvd ppmvd ppbvd Cgas 56.8384 54.32 53.4122 54.857 Cgas Units ppmvd ppmvd ppbvd Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 01, 2011 Page 28 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - Method 7E Average Run Number 1 2 3 Test Date 7/20/2010 7/20/2010 7/20/2010 Run Start Time 7:40:00 AM10:30:00 AM 1:05:00 PM Run Finish Time 8:39:00 AM11:29:00 AM 2:06:00 PM Carbon Dioxide, % 13.87 13.87 13.88 13.873 Oxygen, % 6.5 6.45 6.46 6.470 Fuel Factor 1.04 1.04 1.04 Dry Volumetric Flow Rate, dry scfm 280685 284338 286258283,760.333 F-Factor, dscfm/MMBtu @ %O2 10430 10558 1048010,489.333 Moisture, % 6.79 6.99 6.2 6.660 Analyzer Make Thermo Electron Thermo

Electron Thermo

Electron Analyzer Model 42C 42C 42C Analyzer Serial Number 42CHL78421-389 42CHL78421-389 42CHL78421-389 Operating Range 260 260 260 260.000 Operating Units ppm ppm ppm No. Readings/Avg. 60 60 60 60.000 Calibration Set 7 8 9 8.000 Calibration Pre Zero Cylinder ID CC-133012 CC-133012 CC-133012 Calibration Pre Zero Cylinder Instrument Response 0.67 1.87 1.91 1.483 Calibration Pre Zero Cylinder Bias 0.12 0.58 0.6 0.433 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC-114119BCC-114119BCC-114119B Calibration Pre High Cylinder Instrument Response 122.54 123.6 125 123.713 Calibration Pre High Cylinder Bias -1.79 -1.38 -0.85 -1.340 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID CC-133012 CC-133012 CC-133012 Calibration Post Zero Cylinder Instrument Response 1.87 1.91 1.95 1.910 Calibration Post Zero Cylinder Bias 0.58 0.6 0.62 0.600 Calibration Post Zero Cylinder Drift 0.46 0.02 0.02 0.167 Calibration Post High Cylinder ID CC-114119BCC-114119BCC-114119B Calibration Post High Cylinder Instrument Response 123.6 125 125.2 124.600 Calibration Post High Cylinder Bias -1.38 -0.85 -0.77 -1.000 Calibration Post High Cylinder Drift 0.41 0.53 0.08 0.340 Cavg 74.17 73.35 73.02 73.513 Cavg Units ppmvd ppmvd ppmvd Cgas 76.0722 74.1979 73.3583 74.543 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw 0 0 0 0.000 Fc 0 0 0 0.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 01, 2011 Page 29 of 30

### Panther Creek Energy Facility 9/23/2010 Location Exhaust Stack - OTM - 27/28 Average Run Number 1 2 3 Test Date 7/15/2010 7/16/2010 7/19/2010 Run Start Time 8:09:00 AM6:58:00 AM 7:00:00 AM Run Finish Time 2:27:00 PM12:54:00 PM 1:00:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 329.75 330.5 330.25 Nozzle Diameter, inches 0.138 0.138 0.138 0.138 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9876 0.9876 0.9876 0.988 Barometric Pressure, inches of Mercury 30.03 30 29.9 29.977 Average Orifice Meter Differential, inches H2O 0.49 0.49 0.49 0.490 Dry Gas Meter Volume Sampled, cubic feet 128.396 131.382 130.626 130.135 Average Dry Gas Meter Temperature, °F 103.67 109.33 110.08 107.693 Dry Gas Meter Volume Sampled, dscf 119.359 120.800 119.548 119.902 Total Moisture Liquid collected, g 188 192 216 198.667 Volume of Water Vapor, standard cubic feet 8.85 9.04 10.17 9.353 Moisture Content of Stack Gas, % 6.90 6.96 7.84 7.233 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.931 0.9304 0.9216 0.928 Carbon Dioxide, % 14 14.01 14 14.003 Oxygen, % 6.4 6.34 6.4 6.380 Carbon Monoxide & Nitrogen, % 79.6 79.65 79.6 79.617 Fuel Factor 1.04 1.04 1.04 Dry Molecular Weight, lb/lb-Mole 30.50 30.50 30.50 30.500 Wet Molecular weight, lb/lb-Mole 29.64 29.63 29.52 29.597 Flue Gas Static Pressure, inches of H2O 4.45 4.45 4.5 4.467 Absolute Flue Gas Pressure, inches of Mercury 30.36 30.33 30.23 30.307 Average Stack Gas Temperature, °F 333.25 333.42 331.25 332.640 Average Velocity Head, inches of H2O 1.9760720864 91162.196617060

8992.246713540

89771 2.140 Average Stack Gas Velocity, feet/second 94.78 100.00 101.36 98.713 Stack Cross-Sectional Area, square feet 72.131 72.131 72.131 72.131 Dry Volumetric Flow Rate, dry scfm 257,931.0 271,634.2 272,570.6267,378.600 Actual Wet Volumetric Flue Gas Flow Rate, acfm 410,194.6 432,786.0 438,671.9427,217.500 Percent Isokinetic of Sampling Rate, % 97.5 93.4 92.2 94.367 Percent Excess Air, % 43.8 43.2 43.8 43.600 F-Factor, dscfm/MMBtu @ %O2 10488 10597 1061210,565.667 Round Duct Diameter, inches 115 115 115 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



### Tuesday, February 01, 2011 Page 30 of 30