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 PA 18240

Contact: Jim Carroll

Phone: 570-645-8721

Fax: 570-645-9763

Email: Jcarroll@PantherCreekEnergy.com

Testing Company:

Air Analysis, LLC

189 Hausman Road

Lenhartsville PA 19534

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:

BLR1 & BLR Panther Creek Energy Facility

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/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 4202500101 FRS #: 110001204599

SCC / Description 10102018 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 0 0 0 10.64 13.77 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Exhaust Stack Custom CH4 3 120 0 Method 18

Flowrate 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

Exhaust Stack Carbon Monoxide Method 10 3 120 0

Exhaust Stack Formaldehyde Method 0011 3 120 0

Exhaust Stack 2,3,7,8-TCDD Method 23 0

Exhaust Stack 1,2,3,7,8-PeCDD Method 23 0

Exhaust Stack 1,2,3,4,7,8-HxCDD Method 23 0

Exhaust Stack 1,2,3,6,7,8-HxCDD Method 23 0

Exhaust Stack 1,2,3,7,8,9-HxCDD Method 23 0

Exhaust Stack 1,2,3,4,6,7,8-HpCDD Method 23 0

Exhaust Stack 2,3,7,8-TCDF Method 23 0

Exhaust Stack 1,2,3,7,8-PeCDF Method 23 0

Exhaust Stack 2,3,4,7,8-PeCDF Method 23 0

Exhaust Stack 1,2,3,4,7,8-HxCDF Method 23 0

Exhaust Stack 1,2,3,6,7,8-HxCDF Method 23 0

Exhaust Stack 2,3,4,6,7,8-HxCDF Method 23 0

Exhaust Stack 1,2,3,7,8,9-HxCDF Method 23 0

Exhaust Stack 1,2,3,4,6,7,8-HpCDF Method 23 0

Exhaust Stack 1,2,3,4,7,8,9-HpCDF Method 23 0

Exhaust Stack 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Exhaust Stack 3,4,4',5-TCB (PCB81) Method 23 3 480 0

Exhaust Stack 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

Exhaust Stack 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

Exhaust Stack 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

Exhaust Stack 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

Exhaust Stack 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

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

HxCB (PCBs156/157)

Exhaust Stack Method 23 3 480 0

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

Exhaust Stack 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Exhaust Stack Method 23 3 480 0

Exhaust Stack Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Exhaust Stack Method 25A 3 120 0

Exhaust Stack Hydrogen Chloride Method 26A 3 90 0

Exhaust Stack Hydrogen Fluoride Method 26A 3 90 0

Exhaust Stack Total Particulate OTM - 27/28 3 330 0

Exhaust Stack Filterable Particulate OTM - 27/28 3 330 0

Organic Condensible 

Particulate

Exhaust Stack OTM - 27/28 3 330 0

Exhaust Stack Total PM2.5 OTM - 27/28 3 330 0

Inorganic (Aqueous) 

Condensible Part.

Exhaust Stack OTM - 27/28 3 330 0

Exhaust Stack Filterable PM2.5 OTM - 27/28 3 330 0

Exhaust Stack Cobalt Method 29 3 330 0

Exhaust Stack Selenium Method 29 3 330 0

Exhaust Stack Nickel Method 29 3 330 0

Exhaust Stack Antimony Method 29 3 330 0

Exhaust Stack Lead Method 29 3 330 0

Exhaust Stack Chromium Method 29 3 330 0

Exhaust Stack Cadmium Method 29 3 330 0

Exhaust Stack Beryllium Method 29 3 330 0

Exhaust Stack Arsenic Method 29 3 330 0

Exhaust Stack Filterable Particulate Method 29 3 330 0

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

Exhaust Stack Manganese Method 29 3 330 0

Exhaust Stack Custom CTM 033 3 60 0 Hydrogen Cyanide

Exhaust Stack O2 Method 3A O2 0

Exhaust Stack Co2 Method 3A CO2 0

Exhaust Stack Custom Method 30B 3 150 0 Mercury

Exhaust Stack Sulfur Dioxide Method 6C 3 60 0

Exhaust Stack Nitrogen oxides (NOx) Method 7E 3 60 0

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 

AM

12:20:00 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 PM 2:39:00 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 

AM

12:20:00 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 

PM

12:55:00 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

10 MW Output 920 MW M7E, 6C, 26A and 

CTM033 Test Run 

1 - 7/20/10 7:30-

8:30

0

11 MW Output 91.5 MW M7E, 6C, 26A and 

CTM033 Test Run 

2 - 7/20/10 10:30-

11:30

0

12 MW Output 92 MW M7E, 6C, 26A and 

CTM033 Test Run 

3 - 7/20/10 13:00-

14:00

0

13 MW Output 91.5 MW M0011, 10, 25A 

Test Run1 - 

7/21/10 7:00-9:00

0

14 MW Output 91 MW M0011, 10, 25A 

Test Run 2 - 

7/21/10 10:00-

12:00

0

15 MW 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

10 Steam Flow - BLR 1 393 klbs/hr 0

11 Steam Flow - BLR 1 390 klbs/hr 0

12 Steam Flow - BLR 1 394.5 klbs/hr 0

13 Steam Flow - BLR 1 390 klbs/hr 0

14 Steam Flow - BLR 1 388.5 klbs/hr 0

15 Steam 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

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

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

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

13 Waste Anthracite Fuel Feed - BLR 1 87.5 klbs/hr 0

14 Waste Anthracite Fuel Feed - BLR 1 87.05 klbs/hr 0

15 Waste 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

10 Stack O2 6.5 % 0

11 Stack O2 6.45 % 0

12 Stack O2 6.46 % 0

Tuesday, February 01, 2011 Page 17 of 30
Panther Creek Energy Facility

9/23/2010

13 Stack O2 6.39 % 0

14 Stack O2 6.4 % 0

15 Stack 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

10 Stack CO2 13.87 % 0

11 Stack CO2 13.87 % 0

12 Stack CO2 13.88 % 0

13 Stack CO2 14 % 0

14 Stack CO2 13.96 % 0

15 Stack 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

10 Stack Moisture 6.79 % 0

11 Stack Moisture 6.99 % 0

12 Stack Moisture 6.2 % 0

13 Stack Moisture 6.72 % 0

14 Stack Moisture 6.53 % 0

15 Stack 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

10 Stack Flow 280685 scfm 0

11 Stack Flow 284338 scfm 0

12 Stack Flow 286258 scfm 0

13 Stack Flow 284470 scfm 0

14 Stack Flow 282340 scfm 0

15 Stack 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

10 Stack Temp 328 F 0

11 Stack Temp 328 F 0

12 Stack Temp 332 F 0

13 Stack Temp 327 F 0

14 Stack Temp 332 F 0

15 Stack 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

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

11 Waste Anthracite Fuel Feed - BLR 2 76.5 klbs/hr 0

12 Waste Anthracite Fuel Feed - BLR 2 77 klbs/hr 0

13 Waste Anthracite Fuel Feed - BLR 2 76 klbs/hr 0

14 Waste Anthracite Fuel Feed - BLR 2 75.6 klbs/hr 0

15 Waste 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

10 Steam Flow - BLR 2 383 klbs./hr 0

11 Steam Flow - BLR 2 384 klbs./hr 0

12 Steam Flow - BLR 2 385 klbs./hr 0

13 Steam Flow - BLR 2 380 klbs./hr 0

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

15 Steam 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

10 BLR 1 Baghouse Pressure Drop 5.11 " H2O 0

11 BLR 1 Baghouse Pressure Drop 4.99 " H2O 0

12 BLR 1 Baghouse Pressure Drop 5.03 " H2O 0

Tuesday, February 01, 2011 Page 20 of 30
Panther Creek Energy Facility

9/23/2010

13 BLR 1 Baghouse Pressure Drop 5 " H2O 0

14 BLR 1 Baghouse Pressure Drop 5.03 " H2O 0

15 BLR 1 Baghouse Pressure Drop 5.02 " H2O 0

16 BLR 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

10 BLR1 Dry Limestone Injection 4427 Lbs/hr 0

11 BLR1 Dry Limestone Injection 4858 Lbs/hr 0

12 BLR1 Dry Limestone Injection 4858 Lbs/hr 0

13 BLR1 Dry Limestone Injection 4858 Lbs/hr 0

14 BLR1 Dry Limestone Injection 4885 Lbs/hr 0

15 BLR1 Dry Limestone Injection 4855 Lbs/hr 0

16 BLR1 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

10 BLR 2 Baghouse Pressure Drop 4.85 " H2O 0

11 BLR 2 Baghouse Pressure Drop 4.91 " H2O 0

12 BLR 2 Baghouse Pressure Drop 4.8 " H2O 0

13 BLR 2 Baghouse Pressure Drop 4.92 " H2O 0

14 BLR 2 Baghouse Pressure Drop 4.9 " H2O 0

15 BLR 2 Baghouse Pressure Drop 4.9 " H2O 0

16 BLR 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

10 BLR 2 Dry Limestone Injection 3795 Lbs/hr 0

11 BLR 2 Dry Limestone Injection 4137 Lbs/hr 0

12 BLR 2 Dry Limestone Injection 4137 Lbs/hr 0

13 BLR 2 Dry Limestone Injection 4137 Lbs/hr 0

14 BLR 2 Dry Limestone Injection 3955 Lbs/hr 0

15 BLR 2 Dry Limestone Injection 3955 Lbs/hr 0

16 BLR 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 AM 9:45:00 AM 12:20:00 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

Fuel Factor 1.04 1.04 1.04

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

Analyzer Make Thermo 

Electron

Thermo 

Electron

Thermo 

Electron

Analyzer Model 48C 48C 48C

Analyzer Serial Number 48C-67476-

356

48C-67476-

356

48-67476-356

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 AM 6:18:00 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

2604

1.959616191

09913

1.992712440

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 253,083.7 253,973.9 255,438.6 254,165.400

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

Percent Excess Air, % 42.0 42.6 42.9 42.500

F-Factor, dscfm/MMBtu @ %O2 10215 10338 10203 10,252.000

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 AM 9:45:00 AM 12:20:00 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

Fuel Factor 1.04 1.04 1.04

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

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

07692

0.356160787

530763

0.341802030

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 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 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

0645

2.078492182

77097

2.121414155

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 261,646.0 264,471.0 268,506.9 264,874.633

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

Percent Excess Air, % 44.8 44.2 44.3 44.433

F-Factor, dscfm/MMBtu @ %O2 10430 10558 10480 10,489.333

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 AM 6:58:00 AM 7:00:00 AM

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

0468

2.101300687

44986

2.123647845

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 263,193.0 264,902.3 266,426.0 264,840.433

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

Percent Excess Air, % 43.4 43.2 43.6 43.400

F-Factor, dscfm/MMBtu @ %O2 10488 10597 10612 10,565.667

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 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

Fuel Factor 1.04 1.04 1.04

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

Analyzer Make Bovar Bovar Bovar

Analyzer Model 721M 721M 721M

Analyzer Serial Number VD-721M8519-1VD-721M8519-1VD-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 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

Fuel Factor 1.04 1.04 1.04

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

Analyzer Make Thermo 

Electron

Thermo 

Electron

Thermo 

Electron

Analyzer Model 42C 42C 42C

Analyzer Serial Number 42CHL78421-38942CHL78421-38942CHL78421-389

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-114119B CC-114119B CC-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-114119B CC-114119B CC-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 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 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

9116

2.196617060

899

2.246713540

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 257,931.0 271,634.2 272,570.6 267,378.600

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

Percent Excess Air, % 43.8 43.2 43.8 43.600

F-Factor, dscfm/MMBtu @ %O2 10488 10597 10612 10,565.667

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