### Name:

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

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

Tuesday, February 15, 2011 Page 1 of 48

### Facility Information:

Harding Street 3700 S. Harding Street

Indianapolis IN 46217 Contact: Angelique Oliger Phone: (317) 261-5852 Fax: Email: angelique.oliger@aes.com Testing Company: URS Corporation
1600 Perimeter Park Dr.

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

Air Permit Number: 990 Permitted Source ID/Name: 09 09 Permitted Maximum Process Rate: N/A Max. Normal Operation Process Rate: N/A Target Process Test Rate N/A

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: Concentric firing, Dry Bottom, 527 MMBtu/hr Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 1809700033 FRS #: 110000396991

SCC / Description 10100501 External Combustion Boilers - Electric Generation - Distillate Oil - Grades 1 and 2 Oil

The following state and federal regulations that apply to the proposed testing:

Location Round

Duct Diam. Distance from upstream dist. Distance from

downstream dist. Number of

Traverse Ports Equiv. Diam Min.Travers Points Rect. Duct Length /Width Stack Exit 90.5 181 724 2 0 6 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location % H2O Method 1 - 4 3 180 0 Stack Exit Carbon Monoxide Method 10 3 120 0 Stack Exit Formaldehyde Method 0011 3 120 0 Stack Exit 2,3,7,8-TCDD Method 23 3 480 0 Stack Exit 1,2,3,7,8-PeCDD Method 23 3 480 0 Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0 Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0 Stack Exit



### Tuesday, February 15, 2011 Page 2 of 481,2,3,7,8,9-HxCDD Method 23 3 480 0

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

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

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

(PCB189) Method 23 3 480 0 Stack Exit

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

(TOC) as Propane Method 25A 3 120 0 Stack Exit
Hydrogen Chloride Method 26 3 180 0 Stack Exit Hydrogen Fluoride Method 26 3 180 0 Stack Exit Hydrogen Chloride Method 26A 3 180 0 Stack Exit Hydrogen Fluoride Method 26A 3 180 0 Stack Exit Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Organic Condensible

Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit



### Tuesday, February 15, 2011 Page 3 of 48

### 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.

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Total Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Beryllium Method 29 3 240 0 Stack Exit Manganese Method 29 3 240 0 Stack Exit Mercury Method 29 3 240 0 Stack Exit Nickel Method 29 3 240 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit Lead Method 29 3 240 0 Stack Exit Chromium Method 29 3 240 0 Stack Exit Magnesium Method 29 3 240 0 Stack Exit Cadmium Method 29 3 240 0 Stack Exit Filterable Particulate Method 29 3 240 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit Cobalt Method 29 3 360 0 Stack Exit Antimony Method 29 3 240 0 Stack Exit Co2 Method 3A CO2 3 120 0 Stack Exit O2 Method 3A O2 3 240 0 Stack Exit O2 Method 3A O2 3 120 0 Stack Exit O2 Method 3A O2 3 480 0 Stack Exit Co2 Method 3A CO2 3 480 0 Stack Exit Co2 Method 3A CO2 3 240 0 Stack Exit Inorganic (Aqueous)

Condensible Part. Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Organic Condensible

Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Total Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Filterable Particulate Method 5 3 240 0 Stack Exit Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

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



### Tuesday, February 15, 2011 Page 4 of 48

### Sampling / Stack Data Results Summary



### Location Stack Exit - Method 10 Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Location Stack Exit - Method 23 Average Run Number 1 2 3
Test Date 3/9/2010 3/9/2010 3/10/2010 Run Start Time 4:05:00 AM 3:10:00 PM 12:00:00 AM
Run Finish Time 1:10:00 PM 11:30:00 PM 3:15:00 AM

Net Run Time, minutes 485 480 195 Dry Gas Meter Volume Sampled, dscf 341.173 345.685 139.022 275.293 Moisture Content of Stack Gas, % 6.87 7.29 7.68 7.280 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 7.3 7.3 6.8 7.133 Oxygen, % 11.2 11.1 11.6 11.300 Average Stack Gas Temperature, °F 283.08 287.28 288.95 286.437 Dry Volumetric Flow Rate, dry scfm 95,190.6 95,338.9 94,463.4 94,997.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 148,004.0 148,674.0 149,076.1 148,584.700 Percent Isokinetic of Sampling Rate, % 94.6 96.7 98.9 96.733 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 15, 2011 Page 5 of 48

### Location Stack Exit - Method 25A Average

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



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



### Tuesday, February 15, 2011 Page 6 of 48

### Location Stack Exit - Method 29 Average

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



### Location Stack Exit - Method 3A CO2 Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Tuesday, February 15, 2011 Page 7 of 48

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

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



### Location Stack Exit - Method 3A CO2 3 6 Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Tuesday, February 15, 2011 Page 8 of 48

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

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



### Location Stack Exit - Method 3A O2 Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Tuesday, February 15, 2011 Page 9 of 48

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

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



### Location Stack Exit - Method 3A O2 3 6 Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Tuesday, February 15, 2011 Page 10 of 48

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

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



### Location Stack Exit - Method 6C Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Tuesday, February 15, 2011 Page 11 of 48

### Location Stack Exit - Method 7E Average

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



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



### Tuesday, February 15, 2011 Page 12 of 48

### Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run 1 2 3 lb/mmBtuO2 0.00E+00 -5.92E-04 5.26E-03 0.002 ppm 0.00E+00 -4.21E-01 3.56E+00 1.046 ppm@7%O2 0.00E+00 -5.89E-01 5.24E+00 1.550



### Location: Stack Exit - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.0000000111 0.00000000999 0.00000000504 0.000 lb/mmBtuO2 1.42E-12 1.25E-12 1.65E-12 0.000 ng/dscm 1.15E-03 1.02E-03 1.28E-03 0.001 ng/dscm@7%O2 1.65E-03 1.45E-03 1.91E-03 0.002 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.00000000397 0.00000000789 0.00000000209 0.000 lb/mmBtuO2 5.08E-13 9.86E-13 6.85E-13 0.000 ng/dscm 4.11E-04 8.06E-04 5.31E-04 0.001 ng/dscm@7%O2 5.89E-04 1.14E-03 7.94E-04 0.001 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000024 0.00000000228 0.00000000291 0.000 lb/mmBtuO2 3.07E-13 2.85E-13 9.53E-13 0.000 ng/dscm 2.48E-04 2.33E-04 7.39E-04 0.000 ng/dscm@7%O2 3.55E-04 3.30E-04 1.10E-03 0.001 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000022 0.00000000219 0.00000000191 0.000 lb/mmBtuO2 2.81E-13 2.74E-13 6.26E-13 0.000 ng/dscm 2.28E-04 2.24E-04 4.85E-04 0.000 ng/dscm@7%O2 3.27E-04 3.18E-04 7.25E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000152 0.00000000706 0.00000000171 0.000 lb/mmBtuO2 1.94E-13 8.82E-13 5.60E-13 0.000 ng/dscm 1.57E-04 7.21E-04 4.34E-04 0.000 ng/dscm@7%O2 2.25E-04 1.02E-03 6.49E-04 0.001 

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


### Tuesday, February 15, 2011 Page 13 of 48RunNumber 1 2 3 Mass_mg 0.00000000224 0.00000000232 0.00000000203 0.000 lb/mmBtuO2 2.87E-13 2.90E-13 6.65E-13 0.000 ng/dscm 2.32E-04 2.37E-04 5.16E-04 0.000 ng/dscm@7%O2 3.32E-04 3.36E-04 7.71E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000136 0.0000000112 0.00000000171 0.000 lb/mmBtuO2 1.74E-13 1.40E-12 5.60E-13 0.000 ng/dscm 1.41E-04 1.14E-03 4.34E-04 0.001 ng/dscm@7%O2 2.02E-04 1.62E-03 6.49E-04 0.001 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.00000000263 0.00000000267 0.00000000226 0.000 lb/mmBtuO2 3.37E-13 3.34E-13 7.40E-13 0.000 ng/dscm 2.72E-04 2.73E-04 5.74E-04 0.000 ng/dscm@7%O2 3.90E-04 3.87E-04 8.58E-04 0.001 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000202 0.00000000225 0.00000000255 0.000 lb/mmBtuO2 2.58E-13 2.81E-13 8.35E-13 0.000 ng/dscm 2.09E-04 2.30E-04 6.48E-04 0.000 ng/dscm@7%O2 2.99E-04 3.26E-04 9.69E-04 0.001 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.00000000241 0.00000000274 0.00000000275 0.000 lb/mmBtuO2 3.08E-13 3.42E-13 9.01E-13 0.000 ng/dscm 2.49E-04 2.80E-04 6.99E-04 0.000 ng/dscm@7%O2 3.57E-04 3.97E-04 1.04E-03 0.001 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.00000000165 0.0000000111 0.00000000144 0.000 lb/mmBtuO2 2.11E-13 1.39E-12 4.72E-13 0.000 ng/dscm 1.71E-04 1.13E-03 3.66E-04 0.001 ng/dscm@7%O2 2.45E-04 1.60E-03 5.47E-04 0.001 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 2 3 Mass_mg 0.00000000815 0.0000000121 0.00000000827 0.000 lb/mmBtuO2 1.04E-12 1.51E-12 2.71E-12 0.000 ng/dscm 8.44E-04 1.24E-03 2.10E-03 0.001 ng/dscm@7%O2 1.21E-03 1.76E-03 3.14E-03 0.002



### Tuesday, February 15, 2011 Page 14 of 48

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 2 3 Mass_mg 0.000000151 0.000000182 0.0000000702 0.000 lb/mmBtuO2 1.93E-11 2.27E-11 2.30E-11 0.000 ng/dscm 1.56E-02 1.86E-02 1.78E-02 0.017 ng/dscm@7%O2 2.24E-02 2.64E-02 2.66E-02 0.025 

### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 2 3 Mass_mg 0.000000582 0.000000688 0.000000254 0.000 lb/mmBtuO2 7.45E-11 8.60E-11 8.32E-11 0.000 ng/dscm 6.03E-02 7.03E-02 6.45E-02 0.065 ng/dscm@7%O2 8.64E-02 9.97E-02 9.64E-02 0.094 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 2 3 Mass_mg 0.0000000663 0.0000000898 0.0000000326 0.000 lb/mmBtuO2 8.48E-12 1.12E-11 1.07E-11 0.000 ng/dscm 6.86E-03 9.18E-03 8.28E-03 0.008 ng/dscm@7%O2 9.83E-03 1.30E-02 1.24E-02 0.012 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 2 3 Mass_mg 0.0000000413 0.0000000468 0.00000000999 0.000 lb/mmBtuO2 5.28E-12 5.85E-12 3.27E-12 0.000 ng/dscm 4.28E-03 4.78E-03 2.54E-03 0.004 ng/dscm@7%O2 6.13E-03 6.78E-03 3.80E-03 0.006 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 2 3 Mass_mg 0.00000188 0.00000215 0.000000786 0.000 lb/mmBtuO2 2.41E-10 2.69E-10 2.57E-10 0.000 ng/dscm 1.95E-01 2.20E-01 2.00E-01 0.205 ng/dscm@7%O2 2.79E-01 3.12E-01 2.99E-01 0.297 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 2 3 Mass_mg 0.0000000476 0.0000000635 0.000000019 0.000 lb/mmBtuO2 6.09E-12 7.94E-12 6.22E-12 0.000 ng/dscm 4.93E-03 6.49E-03 4.83E-03 0.005 ng/dscm@7%O2 7.06E-03 9.21E-03 7.22E-03 0.008 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000139 0.0000000104 0.00000000175 0.000 lb/mmBtuO2 1.78E-13 1.30E-12 5.73E-13 0.000



### Tuesday, February 15, 2011 Page 15 of 48ng/dscm 1.44E-04 1.06E-03 4.45E-04 0.001 ng/dscm@7%O2 2.06E-04 1.50E-03 6.65E-04 0.001 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.00000000153 0.0000000161 0.00000000132 0.000 lb/mmBtuO2 1.96E-13 2.01E-12 4.32E-13 0.000 ng/dscm 1.58E-04 1.65E-03 3.35E-04 0.001 ng/dscm@7%O2 2.26E-04 2.34E-03 5.01E-04 0.001 

### Compound: 2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.00000000231 0.00000000231 0.00000000225 0.000 lb/mmBtuO2 2.96E-13 2.89E-13 7.37E-13 0.000 ng/dscm 2.39E-04 2.36E-04 5.72E-04 0.000 ng/dscm@7%O2 3.42E-04 3.35E-04 8.55E-04 0.001 

### Compound: 2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.00000000248 0.00000000913 0.00000000135 0.000 lb/mmBtuO2 3.17E-13 1.14E-12 4.42E-13 0.000 ng/dscm 2.57E-04 9.33E-04 3.43E-04 0.001 ng/dscm@7%O2 3.68E-04 1.32E-03 5.13E-04 0.001 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 2 3 Mass_mg 0.00000000956 0.0000000133 0.00000000933 0.000 lb/mmBtuO2 1.22E-12 1.66E-12 3.06E-12 0.000 ng/dscm 9.90E-04 1.36E-03 2.37E-03 0.002 ng/dscm@7%O2 1.42E-03 1.93E-03 3.54E-03 0.002 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 2 3 Mass_mg 0.000000013 0.0000000174 0.00000000881 0.000 lb/mmBtuO2 1.66E-12 2.17E-12 2.89E-12 0.000 ng/dscm 1.35E-03 1.78E-03 2.24E-03 0.002 ng/dscm@7%O2 1.93E-03 2.52E-03 3.35E-03 0.003 

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 1 2 3 Mass_mg 0.000000222 0.000000252 0.0000000852 0.000 lb/mmBtuO2 2.84E-11 3.15E-11 2.79E-11 0.000 ng/dscm 2.30E-02 2.57E-02 2.16E-02 0.023 ng/dscm@7%O2 3.30E-02 3.65E-02 3.23E-02 0.034 

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


### Tuesday, February 15, 2011 Page 16 of 48Mass_mg 0.0000000124 0.000000011 0.0000000078 0.000 lb/mmBtuO2 1.59E-12 1.37E-12 2.55E-12 0.000 ng/dscm 1.28E-03 1.12E-03 1.98E-03 0.001 ng/dscm@7%O2 1.83E-03 1.59E-03 2.96E-03 0.002 

### Compound: OCDD Average RunNumber 1 2 3 Mass_mg 0.0000000457 0.000000041 0.0000000231 0.000 lb/mmBtuO2 5.85E-12 5.12E-12 7.57E-12 0.000 ng/dscm 4.73E-03 4.19E-03 5.87E-03 0.005 ng/dscm@7%O2 6.78E-03 5.94E-03 8.77E-03 0.007 

### Compound: OCDF Average RunNumber 1 2 3 Mass_mg 0.00000000376 0.00000000376 0.0000000045 0.000 lb/mmBtuO2 4.81E-13 4.70E-13 1.47E-12 0.000 ng/dscm 3.89E-04 3.84E-04 1.14E-03 0.001 ng/dscm@7%O2 5.57E-04 5.45E-04 1.70E-03 0.001 

### Compound: Other HpCDD Average RunNumber 1 2 3 Mass_mg 0 0.0000000154 0 0.000 lb/mmBtuO2 0.00E+00 1.92E-12 0.00E+00 0.000 ng/dscm 0.00E+00 1.57E-03 0.00E+00 0.001 ng/dscm@7%O2 0.00E+00 2.23E-03 0.00E+00 0.001 

### Compound: Other HpCDF Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Other HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000111 0.00000000929 0 0.000 lb/mmBtuO2 1.42E-12 1.16E-12 0.00E+00 0.000 ng/dscm 1.15E-03 9.49E-04 0.00E+00 0.001 ng/dscm@7%O2 1.65E-03 1.35E-03 0.00E+00 0.001 

### Compound: Other HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000422 0.0000000221 0.00000000212 0.000 lb/mmBtuO2 5.40E-13 2.76E-12 6.94E-13 0.000 ng/dscm 4.37E-04 2.26E-03 5.39E-04 0.001 ng/dscm@7%O2 6.26E-04 3.21E-03 8.06E-04 0.002



### Tuesday, February 15, 2011 Page 17 of 48

### Compound: Other PeCDD Average RunNumber 1 2 3 Mass_mg 0 0.0000000091 0 0.000 lb/mmBtuO2 0.00E+00 1.14E-12 0.00E+00 0.000 ng/dscm 0.00E+00 9.30E-04 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 1.32E-03 0.00E+00 0.000 

### Compound: Other PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000053 0.000000114 0 0.000 lb/mmBtuO2 6.78E-13 1.42E-11 0.00E+00 0.000 ng/dscm 5.49E-04 1.16E-02 0.00E+00 0.004 ng/dscm@7%O2 7.87E-04 1.65E-02 0.00E+00 0.006 

### Compound: Other TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000131 0.0000000505 0.00000000267 0.000 lb/mmBtuO2 1.68E-12 6.31E-12 8.74E-13 0.000 ng/dscm 1.36E-03 5.16E-03 6.78E-04 0.002 ng/dscm@7%O2 1.95E-03 7.32E-03 1.01E-03 0.003 

### Compound: Other TCDF Average RunNumber 1 2 3 Mass_mg 0.0000000202 0.000000314 0 0.000 lb/mmBtuO2 2.58E-12 3.92E-11 0.00E+00 0.000 ng/dscm 2.09E-03 3.21E-02 0.00E+00 0.011 ng/dscm@7%O2 2.99E-03 4.55E-02 0.00E+00 0.016 

### Compound: Total Dioxins Average RunNumber 1 2 3 Mass_mg 0.00000009279 0.00000014695 0.00000004201 0.000 lb/mmBtuO2 1.19E-11 1.84E-11 1.38E-11 0.000 ng/dscm 9.61E-03 1.50E-02 1.07E-02 0.012 ng/dscm@7%O2 1.38E-02 2.13E-02 1.60E-02 0.017 

### Compound: Total Furans Average RunNumber 1 2 3 Mass_mg 0.0000000518 0.00000053127 0.00000002345 0.000 lb/mmBtuO2 6.63E-12 6.64E-11 7.68E-12 0.000 ng/dscm 5.36E-03 5.43E-02 5.96E-03 0.022 ng/dscm@7%O2 7.68E-03 7.70E-02 8.91E-03 0.031 

### Compound: Total Mono-CBs Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000



### Tuesday, February 15, 2011 Page 18 of 48ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total Nona-CBs Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total Octa-CBs Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total PCBs Average RunNumber 1 2 3 Mass_mg 0.000003033 0.000003526 0.000001291 0.000 lb/mmBtuO2 3.88E-10 4.41E-10 4.23E-10 0.000 ng/dscm 3.14E-01 3.60E-01 3.28E-01 0.334 ng/dscm@7%O2 4.50E-01 5.11E-01 4.90E-01 0.484 

### Compound: Total PeCDD Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total PeCDF Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total Penta-CBs Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total TCDD Average RunNumber 1 2 3


### Tuesday, February 15, 2011 Page 19 of 48Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total TCDF Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total TEQ Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total Tetra-CBs Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Total Tri-CBs Average RunNumber 1 2 3 Mass_mg 0 0 0 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average Run 1 2 3 lb/mmBtuO2 0.00E+00 3.15E-03 1.85E-03 0.002 ppm 0.00E+00 1.42E+00 7.93E-01 0.738 ppm@7%O2 0.00E+00 1.99E+00 1.17E+00 1.053



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 0.287 0.309 0.319 0.305 Elb/hr 2.72E-02 2.99E-02 3.08E-02 0.029 lb/mmBtuO2 8.74E-05 1.00E-04 9.99E-05 0.000 mg/dscm 7.14E-02 7.87E-02 7.83E-02 0.076


### Tuesday, February 15, 2011 Page 20 of 48mg/dscm@7%O2 1.01E-01 1.16E-01 1.16E-01 0.111



### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 0.294 0.317 0.327 0.313 Elb/hr 2.79E-02 3.06E-02 3.15E-02 0.030 lb/mmBtuO2 8.95E-05 1.03E-04 1.02E-04 0.000 mg/dscm 7.32E-02 8.08E-02 8.03E-02 0.078 mg/dscm@7%O2 1.04E-01 1.19E-01 1.19E-01 0.114



### Location: Stack Exit - Method 29 Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.0001 0.0002 0.0001 0.000 Elb/hr 4.81E-06 9.46E-06 4.78E-06 0.000 lb/mmBtuO2 1.62E-08 3.18E-08 1.57E-08 0.000 mg/dscm 1.27E-05 2.54E-05 1.27E-05 0.000 mg/dscm@7%O2 1.88E-05 3.68E-05 1.82E-05 0.000 

### Compound: Arsenic Average RunNumber 2 3 1 Mass_mg 0.0021 0.0007 0.0013 0.001 Elb/hr 9.94E-05 3.35E-05 6.25E-05 0.000 lb/mmBtuO2 3.34E-07 1.10E-07 2.10E-07 0.000 mg/dscm 2.67E-04 8.91E-05 1.65E-04 0.000 mg/dscm@7%O2 3.87E-04 1.28E-04 2.44E-04 0.000 

### Compound: Beryllium Average RunNumber 2 3 1 Mass_mg 0.0001 0 0.0001 0.000 Elb/hr 4.73E-06 0.00E+00 4.81E-06 0.000 lb/mmBtuO2 1.59E-08 0.00E+00 1.62E-08 0.000 mg/dscm 1.27E-05 0.00E+00 1.27E-05 0.000 mg/dscm@7%O2 1.84E-05 0.00E+00 1.88E-05 0.000 

### Compound: Cadmium Average RunNumber 2 3 1 Mass_mg 0.0005 0.0003 0.0007 0.001 Elb/hr 2.37E-05 1.43E-05 3.36E-05 0.000 lb/mmBtuO2 7.94E-08 4.72E-08 1.13E-07 0.000 mg/dscm 6.36E-05 3.82E-05 8.88E-05 0.000 mg/dscm@7%O2 9.21E-05 5.47E-05 1.31E-04 0.000 

### Compound: Chromium Average RunNumber 2 3 1 Mass_mg 0.0057 0.0014 0.002 0.003 Elb/hr 2.70E-04 6.69E-05 9.61E-05 0.000



### Tuesday, February 15, 2011 Page 21 of 48lb/mmBtuO2 9.06E-07 2.20E-07 3.24E-07 0.000 mg/dscm 7.25E-04 1.78E-04 2.54E-04 0.000 mg/dscm@7%O2 1.05E-03 2.55E-04 3.76E-04 0.001 

### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.0009 0.0003 0.0003 0.001 Elb/hr 4.33E-05 1.42E-05 1.43E-05 0.000 lb/mmBtuO2 1.46E-07 4.77E-08 4.72E-08 0.000 mg/dscm 1.14E-04 3.82E-05 3.82E-05 0.000 mg/dscm@7%O2 1.69E-04 5.53E-05 5.47E-05 0.000 

### Compound: Filterable Particulate Average RunNumber 2 3 1 Mass_mg 7.4 4.4 7.8 6.533 Elb/hr 3.50E-01 2.10E-01 3.75E-01 0.312 lb/mmBtuO2 1.18E-03 6.92E-04 1.26E-03 0.001 mg/dscm 9.41E-01 5.60E-01 9.90E-01 0.830 mg/dscm@7%O2 1.36E+00 8.02E-01 1.46E+00 1.207 

### Compound: Lead Average RunNumber 2 3 1 Mass_mg 0.0307 0.0203 0.0293 0.027 Elb/hr 1.45E-03 9.71E-04 1.41E-03 0.001 lb/mmBtuO2 4.88E-06 3.19E-06 4.74E-06 0.000 mg/dscm 3.91E-03 2.58E-03 3.72E-03 0.003 mg/dscm@7%O2 5.66E-03 3.70E-03 5.50E-03 0.005 

### Compound: Magnesium Average RunNumber 2 3 1 Mass_mg 0 0 0 0.000 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 mg/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 mg/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Manganese Average RunNumber 2 3 1 Mass_mg 0.0081 0.0029 0.0048 0.005 Elb/hr 3.83E-04 1.39E-04 2.31E-04 0.000 lb/mmBtuO2 1.29E-06 4.56E-07 7.77E-07 0.000 mg/dscm 1.03E-03 3.69E-04 6.09E-04 0.001 mg/dscm@7%O2 1.49E-03 5.29E-04 9.01E-04 0.001 

### Compound: Mercury Average RunNumber 2 3 1 Mass_mg 0 0 0 0.000 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000



### Tuesday, February 15, 2011 Page 22 of 48lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 mg/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 mg/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 

### Compound: Nickel Average RunNumber 2 3 1 Mass_mg 0.0069 0.003 0.0048 0.005 Elb/hr 3.26E-04 1.43E-04 2.31E-04 0.000 lb/mmBtuO2 1.10E-06 4.72E-07 7.77E-07 0.000 mg/dscm 8.78E-04 3.82E-04 6.09E-04 0.001 mg/dscm@7%O2 1.27E-03 5.47E-04 9.01E-04 0.001 

### Compound: Selenium Average RunNumber 2 3 1 Mass_mg 0.0012 0.0012 0.001 0.001 Elb/hr 5.68E-05 5.74E-05 4.81E-05 0.000 lb/mmBtuO2 1.91E-07 1.89E-07 1.62E-07 0.000 mg/dscm 1.53E-04 1.53E-04 1.27E-04 0.000 mg/dscm@7%O2 2.22E-04 2.19E-04 1.88E-04 0.000



### Location: Stack Exit - Method 6C 

### Compound: Sulfur Dioxide Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 1.85E-02 2.35E-02 2.21E-02 0.021 mg/dscm 1.54E+01 1.88E+01 1.77E+01 17.300 mg/dscm@7%O2 2.14E+01 2.73E+01 2.56E+01 24.767 ppm 5.78E+00 7.06E+00 6.64E+00 6.493 ppm@7%O2 8.03E+00 1.03E+01 9.60E+00 9.310



### Location: Stack Exit - Method 7E Compound: Nitrogen oxides (NOx) Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 1.84E-01 1.87E-01 1.88E-01 0.186 mg/dscm 1.53E+02 1.50E+02 1.51E+02 151.333 mg/dscm@7%O2 2.13E+02 2.18E+02 2.18E+02 216.333 ppm 8.02E+01 7.82E+01 7.88E+01 79.067 ppm@7%O2 1.11E+02 1.14E+02 1.14E+02 113.000



### Location: Stack Exit - OTM - 27/28 Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 8.8 7.2 12.3 9.433 lb/mmBtuO2 2.81E-03 2.67E-03 3.98E-03 0.003



### Tuesday, February 15, 2011 Page 23 of 48

### Process Run Data

Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 4.6 4.9 1 3.500 lb/mmBtuO2 1.47E-03 1.82E-03 3.24E-04 0.001 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 7.2 3.9 5.2 5.433 lb/mmBtuO2 2.30E-03 1.44E-03 1.68E-03 0.002 

### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 4.1 3.3 3.6 3.667 lb/mmBtuO2 1.31E-03 1.22E-03 1.17E-03 0.001 

### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 20.1 14.4 21.1 18.533 lb/mmBtuO2 6.43E-03 5.34E-03 6.83E-03 0.006 

### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 15.9 12.1 9.8 12.600 lb/mmBtuO2 5.09E-03 4.48E-03 3.17E-03 0.004



### Tuesday, February 15, 2011 Page 24 of 48

### Process Run Data



### Run Name Value UOM Comments Target Value 1 Distillate Oil (No. 1 & 2) Burned 1.614 1000 Gallons/hr 0


### 10 Distillate Oil (No. 1 & 2) Burned 1.674 1000 Gallons/hr 0
11 Distillate Oil (No. 1 & 2) Burned 1.668 1000 Gallons/hr 0
12 Distillate Oil (No. 1 & 2) Burned 1.668 1000 Gallons/hr 0


### 2 Distillate Oil (No. 1 & 2) Burned 1.656 1000 Gallons/hr 0
3 Distillate Oil (No. 1 & 2) Burned 1.656 1000 Gallons/hr 0
4 Distillate Oil (No. 1 & 2) Burned 1.6548 1000 Gallons/hr 0


### 5 Distillate Oil (No. 1 & 2) Burned 1.6507 1000 Gallons/hr 0
6 Distillate Oil (No. 1 & 2) Burned 1.368 1000 Gallons/hr 0
7 Distillate Oil (No. 1 & 2) Burned 1.7385 1000 Gallons/hr 0


### 8 Distillate Oil (No. 1 & 2) Burned 1.674 1000 Gallons/hr 0
9 Distillate Oil (No. 1 & 2) Burned 1.674 1000 Gallons/hr 0
1 Average Heat Input 222.97 MMBtu/hr 0


### 10 Average Heat Input 231.26 MMBtu/hr 0
11 Average Heat Input 230.43 MMBtu/hr 0
12 Average Heat Input 230.43 MMBtu/hr 0


### 2 Average Heat Input 228.78 MMBtu/hr 0
3 Average Heat Input 228.78 MMBtu/hr 0
4 Average Heat Input 228.61 MMBtu/hr 0


### 5 Average Heat Input 228.04 MMBtu/hr 0
6 Average Heat Input 188.99 MMBtu/hr 0
7 Average Heat Input 240.17 MMBtu/hr 0


### 8 Average Heat Input 231.26 MMBtu/hr 0
9 Average Heat Input 231.26 MMBtu/hr 0


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


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


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



### Tuesday, February 15, 2011 Page 25 of 48

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



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


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


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


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


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


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


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


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


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


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


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


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



### Tuesday, February 15, 2011 Page 26 of 48

### 7 Coal Gas Firing Rate 0 0



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


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


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


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


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


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


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


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


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


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


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


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



### Tuesday, February 15, 2011 Page 27 of 48

### 10 FGD Scrubber Liquor pH 0 pH 0



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


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


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


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


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


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


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

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



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

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

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



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

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



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

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



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

1 Flue Gas Oxygen Content 0 % 0



### Tuesday, February 15, 2011 Page 28 of 48

### 10 Flue Gas Oxygen Content 0 % 0



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


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


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


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


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


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


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


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


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


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


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


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



### Tuesday, February 15, 2011 Page 29 of 48

### 7 Flue Gas Sampling Point Temperature 0 Deg F 0



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


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


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


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


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


### 12 Standard Pressure 0 atm 0
4 Standard Pressure 1 atm 0
5 Standard Pressure 1 atm 0


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


### 8 Standard Pressure 0 atm 0
9 Standard Pressure 0 atm 0
1 Standard Temperature 68 Deg F 0


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


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


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


### 1 Unit Gross Electrical Output 15.51 MW 0
10 Unit Gross Electrical Output 15.56 MW 0
11 Unit Gross Electrical Output 15.49 MW 0



### Tuesday, February 15, 2011 Page 30 of 48

### APCD Run Data

Process Lab Run Data 12 Unit Gross Electrical Output 15.35 MW 0


### 4 Unit Gross Electrical Output 16.11 MW 0
5 Unit Gross Electrical Output 16.11 MW 0
6 Unit Gross Electrical Output 15.79 MW 0


### 7 Unit Gross Electrical Output 14.64 MW 0
8 Unit Gross Electrical Output 14.43 MW 0
9 Unit Gross Electrical Output 15.51 MW 0


### 1 Unit Net Electric Generation 14.51 MWh 0
10 Unit Net Electric Generation 14.25 MWh 0
11 Unit Net Electric Generation 14.26 MWh 0


### 12 Unit Net Electric Generation 14.23 MWh 0
4 Unit Net Electric Generation 15.18 MWh 0
5 Unit Net Electric Generation 15.03 MWh 0


### 6 Unit Net Electric Generation 14.31 MWh 0
7 Unit Net Electric Generation 13.8 MWh 0
8 Unit Net Electric Generation 15.42 MWh 0


### 9 Unit Net Electric Generation 14.01 MWh 0

Run Name Value UOM Comments Target Value 1 List all emissions control devices in order of process flow. Choose from 0 0



### 1 drop down lists. If not on list add description and provide detailed 0 0

1 desription in section 5a. 0 0

Run Name Value UOM Comments 

### 1 Fuel Higher Heating Value 0 Btu/lb 1 Fuel Moisture 0 % 1 Fuel Mercury Content 0 ppm 

### 1 Fuel Cadmium Content 0 ppm 1 Ultimate/Proximate Analysis 0 1 Fuel Nickel Content 0 ppm 

### 1 Fuel Arsenic Content 0 ppm 1 Fuel Chromium Content 0 ppm 1 Fuel Beryllium Content 0 ppm 1 Fuel Lead Content 0 ppm



### Tuesday, February 15, 2011 Page 31 of 48

### 1 Fuel Manganese Content 0 ppm



### 1 Fuel Chlorine Content 0 ppm 1 Fuel Fluorine Content 0 ppm

Tuesday, February 15, 2011 Page 32 of 48

### Sampling / Stack Data Results Detail



### Location Stack Exit - Method 10 Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



### Tuesday, February 15, 2011 Page 33 of 48

### Location Stack Exit - Method 23 Average

Run Number 1 2 3 Test Date 3/9/2010 3/9/2010 3/10/2010 Run Start Time 4:05:00 AM 3:10:00 PM 12:00:00 AM Run Finish Time 1:10:00 PM 11:30:00 PM 3:15:00 AM Net Traversing Points 12 12 5 Net Run Time, minutes 485 480 195 Nozzle Diameter, inches 0.253 0.253 0.25 0.252 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.014 1.014 1.014 1.014 Barometric Pressure, inches of Mercury 29.12 29.32 29.16 29.200 Average Orifice Meter Differential, inches H2O 1.58 1.58 1.56 1.573 Dry Gas Meter Volume Sampled, cubic feet 345.050 351.470 142.505 279.675 Average Dry Gas Meter Temperature, °F 69.10 75.55 76.97 73.873 Dry Gas Meter Volume Sampled, dscf 341.173 345.685 139.022 275.293 Total Moisture Liquid collected, g 534.6 577.5 245.9 452.667 Volume of Water Vapor, standard cubic feet 25.16 27.18 11.57 21.303 Moisture Content of Stack Gas, % 6.87 7.29 7.68 7.280 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9313 0.9271 0.9232 0.927 Carbon Dioxide, % 7.3 7.3 6.8 7.133 Oxygen, % 11.2 11.1 11.6 11.300 Carbon Monoxide & Nitrogen, % 81.5 81.6 81.6 81.567 Fuel Factor 1.33 1.34 1.37 Dry Molecular Weight, lb/lb-Mole 29.62 29.61 29.55 29.593 Wet Molecular weight, lb/lb-Mole 28.82 28.76 28.66 28.747 Flue Gas Static Pressure, inches of H2O -0.53 -0.35 -0.35 -0.410 Absolute Flue Gas Pressure, inches of Mercury 29.08 29.29 29.13 29.167 Average Stack Gas Temperature, °F 283.08 287.28 288.95 286.437 Average Velocity Head, inches of H2O 0.6668082556 16071 0.672690250

318953 0.668595552

63099 0.669
Average Stack Gas Velocity, feet/second 55.22 55.47 55.62 55.437 Stack Cross-Sectional Area, square feet 44.671 44.671 44.671 44.671 Dry Volumetric Flow Rate, dry scfm 95,190.6 95,338.9 94,463.4 94,997.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 148,004.0 148,674.0 149,076.1 148,584.700 Percent Isokinetic of Sampling Rate, % 94.6 96.7 98.9 96.733 Percent Excess Air, % 108.6 106.3 116.7 110.533 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Round Duct Diameter, inches 90.5 90.5 90.5 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Tuesday, February 15, 2011 Page 34 of 48

### Location Stack Exit - Method 25A Average

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



### Tuesday, February 15, 2011 Page 35 of 48

### Location Stack Exit - Method 26A Average

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



### Tuesday, February 15, 2011 Page 36 of 48

### Location Stack Exit - Method 29 Average

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



### Tuesday, February 15, 2011 Page 37 of 48

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

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



### Tuesday, February 15, 2011 Page 38 of 48

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

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



### Tuesday, February 15, 2011 Page 39 of 48

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

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



### Tuesday, February 15, 2011 Page 40 of 48

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

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



### Tuesday, February 15, 2011 Page 41 of 48

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

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



### Tuesday, February 15, 2011 Page 42 of 48

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

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



### Tuesday, February 15, 2011 Page 43 of 48

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

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



### Tuesday, February 15, 2011 Page 44 of 48

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

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



### Tuesday, February 15, 2011 Page 45 of 48

### Location Stack Exit - Method 6C Average

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



### Tuesday, February 15, 2011 Page 46 of 48

### Location Stack Exit - Method 7E Average

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



### Tuesday, February 15, 2011 Page 47 of 48

### Location Stack Exit - OTM - 27/28 Average

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



### Tuesday, February 15, 2011 Page 48 of 48