### 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 47

### Facility Information:

Harding Street 3700 S. Harding Street

Indianapolis IN 46217 Contact: Angelique Oliger Phone: (317) 261-5852 Fax: Of above personasdf 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: 10 10 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 471,2,3,7,8,9-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 47

### The following describes any modifications and/or deviations to the applicable test

methods. If alternative methods were requested, see the attachments for documentation of request AND approval, including dates.

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 47

### 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 2 3 4
Test Date 3/3/2010 3/4/2010 3/4/2010 Run Start Time 12:00:00 AM 9:30:00 AM 12:10:00 AM

Run Finish Time 11:55:00 PM 5:55:00 PM 11:50:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 353.535 335.130 328.935 339.200 Moisture Content of Stack Gas, % 6.10 6.23 6.30 6.210 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 6.7 6.51 6.52 6.577 Oxygen, % 11.9 11.91 11.94 11.917 Average Stack Gas Temperature, °F 287.65 287.47 285.65 286.923 Dry Volumetric Flow Rate, dry scfm 100,192.0 94,053.8 96,395.7 96,880.500 Actual Wet Volumetric Flue Gas Flow Rate, acfm 153,552.1 145,296.9 148,968.9 149,272.633 Percent Isokinetic of Sampling Rate, % 96.3 97.3 93.2 95.600 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 15, 2011 Page 5 of 47

### 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 47

### 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 0 -1.68 -1.68 -1.120 Moisture, % Fuel Type 0 8.64 8.64
Fw 0 0 0 0.000
Fc Zero Zero



### Tuesday, February 15, 2011 Page 7 of 47

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

Run Number Hg-1 Hg-2 M23/HCHO R2
Test Date 3/2/2010 3/2/2010 3/3/2010 Run Start Time 3:30:00 AM 6:15:00 AM 9:45:00 PM

Run Finish Time 5:30:00 AM 8:15:00 AM 6:42:00 AM

Carbon Dioxide, % 7.07 7.07 6.55 6.897 Oxygen, % 11.52 11.55 11.83 11.633 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Location Stack Exit - Method 3A CO2 3 6 Average Run Number M23/HCHO R3 M23/HCH

O R4 PM/Met-1

Test Date 3/4/2010 3/4/2010 3/1/2010 Run Start Time 9:30:00 AM 7:55:00 PM 1:40:00 AM Run Finish Time 6:04:00 PM 4:00:00 AM 7:52:00 AM

Carbon Dioxide, % 6.52 6.54 6.84 6.633 Oxygen, % 11.9 11.94 11.86 11.900 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 15, 2011 Page 8 of 47

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

Run Number PM/Met-2 PM/Met-3 VOST/SVO L R1
Test Date 3/1/2010 3/1/2010 3/5/2010 Run Start Time 10:11:00 AM 8:00:00 PM 11:31:00 PM Run Finish Time 5:18:00 PM 2:15:00 AM 2:09:00 AM

Carbon Dioxide, % 6.96 7.1 6.41 6.823 Oxygen, % 11.68 11.55 12.07 11.767 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Location Stack Exit - Method 3A CO2 3 6 9 12 Average Run Number VOST/SVO L- R2 VOST/SV

OL-R3
Test Date 3/6/2010 3/6/2010 Run Start Time 2:46:00 AM 5:15:00 AM Run Finish Time 4:57:00 AM 7:20:00 AM Carbon Dioxide, % 6.44 6.71 6.575 Oxygen, % 12.04 11.69 11.865 Dry Volumetric Flow Rate, dry scfm 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9,190.000 Moisture, % 0 0 0.000 Fuel Type Oil Oil
Fw 10320 10320 10,320.000
Fc 1420 1420 1,420.000



### Tuesday, February 15, 2011 Page 9 of 47

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

Run Number AG Run-1 AG Run-2 AG Run-3
Test Date 3/5/2010 3/6/2010 3/5/2010 Run Start Time 5:01:00 AM 10:22:00 AM 3:11:00 PM

Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM Carbon Dioxide, % 6.42 6.44 6.43 6.430 Oxygen, % 11.9 11.99 11.94 11.943 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Location Stack Exit - Method 3A O2 3 Average Run Number Hg-1 Hg-2 M23/HCHO R2
Test Date 3/2/2010 3/2/2010 3/3/2010 Run Start Time 3:30:00 AM 6:15:00 AM 9:45:00 PM

Run Finish Time 5:30:00 AM 8:15:00 AM 6:42:00 AM

Carbon Dioxide, % 7.07 7.07 6.55 6.897 Oxygen, % 11.52 11.55 11.83 11.633 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 15, 2011 Page 10 of 47

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

Run Number M23/HCHO R3 M23/HCH

O R4 PM/MET-1

Test Date 3/4/2010 3/4/2010 3/1/2010 Run Start Time 9:30:00 AM 7:55:00 PM 1:40:00 AM Run Finish Time 6:04:00 PM 4:00:00 AM 7:52:00 AM

Carbon Dioxide, % 6.52 6.54 6.84 6.633 Oxygen, % 11.9 11.94 11.86 11.900 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Location Stack Exit - Method 3A O2 3 6 9 Average Run Number PM/Met-2 PM/Met-3 VOST/SVO L-R1
Test Date 3/1/2010 3/1/2010 3/5/2010 Run Start Time 10:11:00 AM 8:00:00 PM 11:31:00 PM Run Finish Time 5:18:00 PM 2:15:00 AM 2:09:00 AM

Carbon Dioxide, % 6.96 7.1 6.41 6.823 Oxygen, % 11.68 11.55 12.07 11.767 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 15, 2011 Page 11 of 47

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

Run Number VOST/SVO L-R2 VOST/SV

OL-R3
Test Date 3/6/2010 3/6/2010 Run Start Time 2:46:00 AM 5:15:00 AM Run Finish Time 4:57:00 AM 7:20:00 AM Carbon Dioxide, % 6.44 6.71 6.575 Oxygen, % 12.04 11.69 11.865 Dry Volumetric Flow Rate, dry scfm 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9,190.000 Moisture, % 0 0 0.000 Fuel Type Oil Oil
Fw 10320 10320 10,320.000
Fc 1420 1420 1,420.000



### Location Stack Exit - Method 6C Average Run Number AG Run 1 AG Run 2 AG Run 3
Test Date 3/5/2010 3/5/2010 3/5/2010 Run Start Time 5:01:00 AM 10:22:00 AM 3:11:00 PM

Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM Carbon Dioxide, % 6.42 6.44 6.43 6.430 Oxygen, % 11.9 11.99 11.94 11.943 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 15, 2011 Page 12 of 47

### Location Stack Exit - Method 7E Average

Run Number AG Run 1 AG Run 2 AG Run 3
Test Date 3/5/2010 3/5/2010 3/5/2010 Run Start Time 5:01:00 AM 10:22:00 AM 3:11:00 PM

Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM Carbon Dioxide, % 6.42 6.44 6.43 6.430 Oxygen, % 11.9 11.99 11.94 11.943 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### 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 13 of 47

### Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run M23/HCHO R2 M23/HCHO R3 M23/HCHO R4 lb/mmBtuO2 -3.06E-05 5.71E-04 1.37E-03 0.001 ppm -1.99E-02 3.68E-01 8.77E-01 0.408 ppm@7%O2 -3.05E-02 5.68E-01 1.36E+00 0.633



### Location: Stack Exit - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 2 3 4 Mass_mg 0.0000000202 0.0000000127 0.0000000178 0.000 lb/mmBtuO2 2.69E-12 1.78E-12 2.56E-12 0.000 ng/dscm 2.02E-03 1.34E-03 1.91E-03 0.002 ng/dscm@7%O2 3.12E-03 2.07E-03 2.96E-03 0.003 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 2 3 4 Mass_mg 0.0000000161 0.00000000372 0.000000017 0.000 lb/mmBtuO2 2.14E-12 5.23E-13 2.44E-12 0.000 ng/dscm 1.61E-03 3.92E-04 1.83E-03 0.001 ng/dscm@7%O2 2.49E-03 6.06E-04 2.84E-03 0.002 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 2 3 4 Mass_mg 0.00000000307 0.00000000196 0.00000000351 0.000 lb/mmBtuO2 4.09E-13 2.75E-13 5.04E-13 0.000 ng/dscm 3.07E-04 2.07E-04 3.77E-04 0.000 ng/dscm@7%O2 4.74E-04 3.20E-04 5.85E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 2 3 4 Mass_mg 0.00000000593 0.00000000199 0.00000000441 0.000 lb/mmBtuO2 7.89E-13 2.80E-13 6.34E-13 0.000 ng/dscm 5.92E-04 2.10E-04 4.74E-04 0.000 ng/dscm@7%O2 9.14E-04 3.25E-04 7.35E-04 0.001 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 2 3 4 Mass_mg 0.0000000149 0.00000000224 0.0000000151 0.000 lb/mmBtuO2 1.98E-12 3.15E-13 2.17E-12 0.000 ng/dscm 1.49E-03 2.36E-04 1.62E-03 0.001 ng/dscm@7%O2 2.30E-03 3.65E-04 2.51E-03 0.002 

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


### Tuesday, February 15, 2011 Page 14 of 47RunNumber 2 3 4 Mass_mg 0.00000000861 0.00000000209 0.00000000675 0.000 lb/mmBtuO2 1.15E-12 2.94E-13 9.70E-13 0.000 ng/dscm 8.60E-04 2.20E-04 7.25E-04 0.001 ng/dscm@7%O2 1.33E-03 3.40E-04 1.12E-03 0.001 

### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 2 3 4 Mass_mg 0.0000000259 0.00000000247 0.0000000247 0.000 lb/mmBtuO2 3.45E-12 3.47E-13 3.55E-12 0.000 ng/dscm 2.59E-03 2.60E-04 2.65E-03 0.002 ng/dscm@7%O2 4.00E-03 4.02E-04 4.11E-03 0.003 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 2 3 4 Mass_mg 0.00000000918 0.00000000229 0.00000000754 0.000 lb/mmBtuO2 1.22E-12 3.22E-13 1.08E-12 0.000 ng/dscm 9.17E-04 2.41E-04 8.10E-04 0.001 ng/dscm@7%O2 1.42E-03 3.73E-04 1.26E-03 0.001 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 2 3 4 Mass_mg 0.00000000294 0.00000000203 0.00000000208 0.000 lb/mmBtuO2 3.91E-13 2.85E-13 2.99E-13 0.000 ng/dscm 2.94E-04 2.14E-04 2.23E-04 0.000 ng/dscm@7%O2 4.54E-04 3.31E-04 3.46E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber 2 3 4 Mass_mg 0.0000000147 0.00000000252 0.00000000917 0.000 lb/mmBtuO2 1.96E-12 3.54E-13 1.32E-12 0.000 ng/dscm 1.47E-03 2.66E-04 9.85E-04 0.001 ng/dscm@7%O2 2.27E-03 4.11E-04 1.53E-03 0.001 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber 2 3 4 Mass_mg 0.0000000264 0.00000000283 0.0000000219 0.000 lb/mmBtuO2 3.51E-12 3.98E-13 3.15E-12 0.000 ng/dscm 2.64E-03 2.98E-04 2.35E-03 0.002 ng/dscm@7%O2 4.08E-03 4.61E-04 3.65E-03 0.003 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 2 3 4 Mass_mg 0.00000000454 0.0000000112 0.00000000971 0.000 lb/mmBtuO2 6.04E-13 1.57E-12 1.40E-12 0.000 ng/dscm 4.54E-04 1.18E-03 1.04E-03 0.001 ng/dscm@7%O2 7.01E-04 1.82E-03 1.61E-03 0.001



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

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 2 3 4 Mass_mg 0.0000001 0.00000014 0.000000139 0.000 lb/mmBtuO2 1.33E-11 1.97E-11 2.00E-11 0.000 ng/dscm 9.99E-03 1.48E-02 1.49E-02 0.013 ng/dscm@7%O2 1.54E-02 2.29E-02 2.31E-02 0.020 

### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 2 3 4 Mass_mg 0.000000591 0.000000717 0.000000694 0.000 lb/mmBtuO2 7.87E-11 1.01E-10 9.97E-11 0.000 ng/dscm 5.90E-02 7.56E-02 7.45E-02 0.070 ng/dscm@7%O2 9.11E-02 1.17E-01 1.16E-01 0.108 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 2 3 4 Mass_mg 0.0000000422 0.0000000566 0.0000000591 0.000 lb/mmBtuO2 5.62E-12 7.95E-12 8.49E-12 0.000 ng/dscm 4.22E-03 5.97E-03 6.35E-03 0.006 ng/dscm@7%O2 6.52E-03 9.23E-03 9.85E-03 0.009 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 2 3 4 Mass_mg 0.0000000483 0.0000000588 0.0000000625 0.000 lb/mmBtuO2 6.43E-12 8.26E-12 8.98E-12 0.000 ng/dscm 4.83E-03 6.20E-03 6.71E-03 0.006 ng/dscm@7%O2 7.46E-03 9.59E-03 1.04E-02 0.009 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 2 3 4 Mass_mg 0.00000193 0.00000213 0.00000227 0.000 lb/mmBtuO2 2.57E-10 2.99E-10 3.26E-10 0.000 ng/dscm 1.93E-01 2.24E-01 2.44E-01 0.220 ng/dscm@7%O2 2.98E-01 3.46E-01 3.79E-01 0.341 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 2 3 4 Mass_mg 0.000000052 0.0000000525 0.000000178 0.000 lb/mmBtuO2 6.92E-12 7.38E-12 2.56E-11 0.000 ng/dscm 5.20E-03 5.53E-03 1.91E-02 0.010 ng/dscm@7%O2 8.03E-03 8.55E-03 2.96E-02 0.015 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 2 3 4 Mass_mg 0.0000000238 0.00000000266 0.0000000254 0.000 lb/mmBtuO2 3.17E-12 3.74E-13 3.65E-12 0.000



### Tuesday, February 15, 2011 Page 16 of 47ng/dscm 2.38E-03 2.80E-04 2.73E-03 0.002 ng/dscm@7%O2 3.68E-03 4.33E-04 4.24E-03 0.003 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber 2 3 4 Mass_mg 0.0000000452 0.00000000271 0.0000000366 0.000 lb/mmBtuO2 6.02E-12 3.81E-13 5.26E-12 0.000 ng/dscm 4.52E-03 2.86E-04 3.93E-03 0.003 ng/dscm@7%O2 6.98E-03 4.42E-04 6.10E-03 0.005 

### Compound: 2,3,7,8-TCDD Average RunNumber 2 3 4 Mass_mg 0.0000000151 0.00000000167 0.00000000975 0.000 lb/mmBtuO2 2.01E-12 2.35E-13 1.40E-12 0.000 ng/dscm 1.51E-03 1.76E-04 1.05E-03 0.001 ng/dscm@7%O2 2.33E-03 2.72E-04 1.63E-03 0.001 

### Compound: 2,3,7,8-TCDF Average RunNumber 2 3 4 Mass_mg 0.0000000186 0.00000000326 0.0000000126 0.000 lb/mmBtuO2 2.48E-12 4.58E-13 1.81E-12 0.000 ng/dscm 1.86E-03 3.44E-04 1.35E-03 0.001 ng/dscm@7%O2 2.87E-03 5.32E-04 2.09E-03 0.002 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 2 3 4 Mass_mg 0.00000000592 0.0000000104 0.00000000998 0.000 lb/mmBtuO2 7.88E-13 1.46E-12 1.43E-12 0.000 ng/dscm 5.91E-04 1.10E-03 1.07E-03 0.001 ng/dscm@7%O2 9.13E-04 1.70E-03 1.66E-03 0.001 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 2 3 4 Mass_mg 0.0000000144 0.0000000164 0.0000000152 0.000 lb/mmBtuO2 1.92E-12 2.30E-12 2.18E-12 0.000 ng/dscm 1.44E-03 1.73E-03 1.63E-03 0.002 ng/dscm@7%O2 2.22E-03 2.67E-03 2.53E-03 0.002 

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 2 3 4 Mass_mg 0.000000206 0.000000275 0.000000285 0.000 lb/mmBtuO2 2.74E-11 3.87E-11 4.09E-11 0.000 ng/dscm 2.06E-02 2.90E-02 3.06E-02 0.027 ng/dscm@7%O2 3.18E-02 4.48E-02 4.75E-02 0.041 

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


### Tuesday, February 15, 2011 Page 17 of 47Mass_mg 0.0000000171 0.0000000151 0.0000000198 0.000 lb/mmBtuO2 2.28E-12 2.12E-12 2.84E-12 0.000 ng/dscm 1.71E-03 1.59E-03 2.13E-03 0.002 ng/dscm@7%O2 2.64E-03 2.46E-03 3.30E-03 0.003 

### Compound: OCDD Average RunNumber 2 3 4 Mass_mg 0.0000000636 0.0000000534 0.0000000434 0.000 lb/mmBtuO2 8.46E-12 7.51E-12 6.24E-12 0.000 ng/dscm 6.35E-03 5.63E-03 4.66E-03 0.006 ng/dscm@7%O2 9.81E-03 8.70E-03 7.23E-03 0.009 

### Compound: OCDF Average RunNumber 2 3 4 Mass_mg 0.00000000356 0.00000000327 0.0000000034 0.000 lb/mmBtuO2 4.74E-13 4.60E-13 4.88E-13 0.000 ng/dscm 3.56E-04 3.45E-04 3.65E-04 0.000 ng/dscm@7%O2 5.50E-04 5.33E-04 5.66E-04 0.001 

### Compound: Other HpCDD Average RunNumber 2 3 4 Mass_mg 0.0000000257 0 0.0000000206 0.000 lb/mmBtuO2 3.42E-12 0.00E+00 2.96E-12 0.000 ng/dscm 2.57E-03 0.00E+00 2.21E-03 0.002 ng/dscm@7%O2 3.97E-03 0.00E+00 3.43E-03 0.002 

### Compound: Other HpCDF Average RunNumber 2 3 4 Mass_mg 0 0 0.00000000352 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 5.06E-13 0.000 ng/dscm 0.00E+00 0.00E+00 3.78E-04 0.000 ng/dscm@7%O2 0.00E+00 0.00E+00 5.86E-04 0.000 

### Compound: Other HxCDD Average RunNumber 2 3 4 Mass_mg 0.0000000839 0.00000000826 0.0000000487 0.000 lb/mmBtuO2 1.12E-11 1.16E-12 7.00E-12 0.000 ng/dscm 8.38E-03 8.71E-04 5.23E-03 0.005 ng/dscm@7%O2 1.29E-02 1.35E-03 8.11E-03 0.007 

### Compound: Other HxCDF Average RunNumber 2 3 4 Mass_mg 0.0000000684 0.00000000656 0.0000000565 0.000 lb/mmBtuO2 9.10E-12 9.22E-13 8.12E-12 0.000 ng/dscm 6.83E-03 6.91E-04 6.07E-03 0.005 ng/dscm@7%O2 1.05E-02 1.07E-03 9.42E-03 0.007



### Tuesday, February 15, 2011 Page 18 of 47

### Compound: Other PeCDD Average RunNumber 2 3 4 Mass_mg 0.000000156 0.00000000756 0.000000101 0.000 lb/mmBtuO2 2.08E-11 1.06E-12 1.45E-11 0.000 ng/dscm 1.56E-02 7.97E-04 1.08E-02 0.009 ng/dscm@7%O2 2.41E-02 1.23E-03 1.68E-02 0.014 

### Compound: Other PeCDF Average RunNumber 2 3 4 Mass_mg 0.000000301 0.00000000602 0.00000032 0.000 lb/mmBtuO2 4.01E-11 8.46E-13 4.60E-11 0.000 ng/dscm 3.01E-02 6.34E-04 3.44E-02 0.022 ng/dscm@7%O2 4.65E-02 9.80E-04 5.34E-02 0.034 

### Compound: Other TCDD Average RunNumber 2 3 4 Mass_mg 0.000000321 0.0000000221 0.000000222 0.000 lb/mmBtuO2 4.27E-11 3.11E-12 3.19E-11 0.000 ng/dscm 3.21E-02 2.33E-03 2.38E-02 0.019 ng/dscm@7%O2 4.96E-02 3.60E-03 3.69E-02 0.030 

### Compound: Other TCDF Average RunNumber 2 3 4 Mass_mg 0.000000811 0.000000032 0.000000823 0.000 lb/mmBtuO2 1.08E-10 4.50E-12 1.18E-10 0.000 ng/dscm 8.10E-02 3.37E-03 8.84E-02 0.058 ng/dscm@7%O2 1.25E-01 5.21E-03 1.37E-01 0.089 

### Compound: Total Dioxins Average RunNumber 2 3 4 Mass_mg 0.0000007236 0.00000011458 0.00000049112 0.000 lb/mmBtuO2 9.63E-11 1.61E-11 7.06E-11 0.000 ng/dscm 7.23E-02 1.21E-02 5.27E-02 0.046 ng/dscm@7%O2 1.12E-01 1.87E-02 8.18E-02 0.071 

### Compound: Total Furans Average RunNumber 2 3 4 Mass_mg 0.0000013609 0.00000007173 0.00000136531 0.000 lb/mmBtuO2 1.81E-10 1.01E-11 1.96E-10 0.000 ng/dscm 1.36E-01 7.56E-03 1.47E-01 0.097 ng/dscm@7%O2 2.10E-01 1.17E-02 2.28E-01 0.150 

### Compound: Total Mono-CBs Average RunNumber 2 3 4 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 19 of 47ng/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 2 3 4 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 2 3 4 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 2 3 4 Mass_mg 0.000003011 0.000003483 0.000003742 0.000 lb/mmBtuO2 4.01E-10 4.90E-10 5.38E-10 0.000 ng/dscm 3.01E-01 3.67E-01 4.02E-01 0.357 ng/dscm@7%O2 4.65E-01 5.67E-01 6.24E-01 0.552 

### Compound: Total PeCDD Average RunNumber 2 3 4 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 2 3 4 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 2 3 4 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 2 3 4


### Tuesday, February 15, 2011 Page 20 of 47

### Process Run Data 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 TCDF Average RunNumber 2 3 4 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 2 3 4 Mass_mg 0 0.000 lb/mmBtuO2 0.00E+00 0.000 ng/dscm #Num! ng/dscm@7%O2 0.00E+00 0.000



### Tuesday, February 15, 2011 Page 21 of 47

### Process Run Data



### Run Name Value UOM Comments Target Value 1 Distillate Oil (No. 1 & 2) Burned 1.5737 1000 Gallons 0


### 10 Distillate Oil (No. 1 & 2) Burned 1.6193 1000 Gallons 0
11 Distillate Oil (No. 1 & 2) Burned 1.6406 1000 Gallons 0
12 Distillate Oil (No. 1 & 2) Burned 1.5618 1000 Gallons 0


### 2 Distillate Oil (No. 1 & 2) Burned 1.5551 1000 Gallons 0
3 Distillate Oil (No. 1 & 2) Burned 1.5493 1000 Gallons 0
4 Distillate Oil (No. 1 & 2) Burned 1.5456 1000 Gallons 0


### 5 Distillate Oil (No. 1 & 2) Burned 1.5396 1000 Gallons 0
6 Distillate Oil (No. 1 & 2) Burned 1.5504 1000 Gallons 0
7 Distillate Oil (No. 1 & 2) Burned 1.552 1000 Gallons 0


### 8 Distillate Oil (No. 1 & 2) Burned 1.564 1000 Gallons 0
9 Distillate Oil (No. 1 & 2) Burned 1.604 1000 Gallons 0
1 Average Heat Input 217.41 MMBtu/hr 0


### 10 Average Heat Input 223.7 MMBtu/hr 0
11 Average Heat Input 226.65 MMBtu/hr 0
12 Average Heat Input 215.76 MMBtu/hr 0


### 2 Average Heat Input 214.84 MMBtu/hr 0
3 Average Heat Input 214.04 MMBtu/hr 0
4 Average Heat Input 213.52 MMBtu/hr 0


### 5 Average Heat Input 212.7 MMBtu/hr 0
6 Average Heat Input 214.19 MMBtu/hr 0
7 Average Heat Input 214.41 MMBtu/hr 0


### 8 Average Heat Input 216.07 MMBtu/hr 0
9 Average Heat Input 221.59 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 22 of 47

### 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 23 of 47

### 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 24 of 47

### 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 25 of 47

### 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 26 of 47

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


### 12 Standard Pressure 0 atm 0
4 Standard Pressure 0 atm 0
5 Standard Pressure 0 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 0 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 0 Deg F 0
5 Standard Temperature 0 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 13.59 MW 0
10 Unit Gross Electrical Output 14.41 MW 0
11 Unit Gross Electrical Output 15.08 MW 0



### Tuesday, February 15, 2011 Page 27 of 47

### APCD Run Data

Process Lab Run Data 12 Unit Gross Electrical Output 13.96 MW 0


### 4 Unit Gross Electrical Output 13.13 MW 0
5 Unit Gross Electrical Output 13.4 MW 0
6 Unit Gross Electrical Output 13.38 MW 0


### 7 Unit Gross Electrical Output 12.98 MW 0
8 Unit Gross Electrical Output 13.31 MW 0
9 Unit Gross Electrical Output 13.98 MW 0


### 1 Unit Net Electric Generation 12.78 MWh 0
10 Unit Net Electric Generation 13.33 MWh 0
11 Unit Net Electric Generation 14.14 MWh 0


### 12 Unit Net Electric Generation 13.16 MWh 0
4 Unit Net Electric Generation 12.25 MWh 0
5 Unit Net Electric Generation 12.21 MWh 0


### 6 Unit Net Electric Generation 12.45 MWh 0
7 Unit Net Electric Generation 12.46 MWh 0
8 Unit Net Electric Generation 12.61 MWh 0


### 9 Unit Net Electric Generation 12.95 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 28 of 47

### 1 Fuel Manganese Content 0 ppm



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

Tuesday, February 15, 2011 Page 29 of 47

### 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 30 of 47

### Location Stack Exit - Method 23 Average

Run Number 2 3 4 Test Date 3/3/2010 3/4/2010 3/4/2010 Run Start Time 12:00:00 AM 9:30:00 AM 12:10:00 AM Run Finish Time 11:55:00 PM 5:55:00 PM 11:50:00 PM Net Traversing Points 96 96 96 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.25 0.25 0.25 0.250 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 29.46 29.26 29.2 29.307 Average Orifice Meter Differential, inches H2O 1.59 1.48 1.45 1.507 Dry Gas Meter Volume Sampled, cubic feet 336.760 329.736 316.230 327.575 Average Dry Gas Meter Temperature, °F 44.14 57.07 44.16 48.457 Dry Gas Meter Volume Sampled, dscf 353.535 335.130 328.935 339.200 Total Moisture Liquid collected, g 488.1 473.4 469.8 477.100 Volume of Water Vapor, standard cubic feet 22.97 22.28 22.11 22.453 Moisture Content of Stack Gas, % 6.10 6.23 6.30 6.210 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.939 0.9377 0.937 0.938 Carbon Dioxide, % 6.7 6.51 6.52 6.577 Oxygen, % 11.9 11.91 11.94 11.917 Carbon Monoxide & Nitrogen, % 81.4 81.58 81.54 81.507 Fuel Factor 1.34 1.38 1.37 Dry Molecular Weight, lb/lb-Mole 29.55 29.52 29.52 29.530 Wet Molecular weight, lb/lb-Mole 28.85 28.80 28.79 28.813 Flue Gas Static Pressure, inches of H2O -0.22 -0.22 -0.22 -0.220 Absolute Flue Gas Pressure, inches of Mercury 29.44 29.24 29.18 29.287 Average Stack Gas Temperature, °F 287.65 287.47 285.65 286.923 Average Velocity Head, inches of H2O 0.7229526987 4778 0.642005349

640043 0.674988302

136405 0.680
Average Stack Gas Velocity, feet/second 57.29 54.21 55.58 55.693 Stack Cross-Sectional Area, square feet 44.671 44.671 44.671 44.671 Dry Volumetric Flow Rate, dry scfm 100,192.0 94,053.8 96,395.7 96,880.500 Actual Wet Volumetric Flue Gas Flow Rate, acfm 153,552.1 145,296.9 148,968.9 149,272.633 Percent Isokinetic of Sampling Rate, % 96.3 97.3 93.2 95.600 Percent Excess Air, % 124.1 123.7 124.5 124.100 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 31 of 47

### 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 32 of 47

### 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 33 of 47

### 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 34 of 47

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

Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor 0 -0.02 -0.06 Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 0 -1.68 -1.68 -1.120 Moisture, % Analyzer Make Analyzer Model Stack Exit Stack Exit Stack Exit Analyzer Serial Number Method 3A CO2 Method 3A

CO2 Method 3A

CO2 Operating Range AG Run 1 AG Run 2 AG Run 3 Operating Units 3/5/2010 3/5/2010 3/5/2010 No. Readings/Avg. 10:22:00 AM 3:11:00 PM Calibration Set 0 0 0 0.000 Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000 Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift 0 0 6.43 2.143 Calibration Pre High Cylinder ID 6.44 Calibration Pre High Cylinder Instrument Response 0 0 11.94 3.980 Calibration Pre High Cylinder Bias 11.99 11.990 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias 0 0 0 0.000 Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID 0 0 0 Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias 0 2 2 1.333 Calibration Post High Cylinder Drift Zero Zero Cavg 0 -0.04 -0.04 -0.027 Cavg Units 0 -0.2 -0.2 Cgas 0 0 0 0.000 Cgas Units CC179326 CC179326 Fuel Type 0 8.64 8.64 Fw 0 0 0 0.000 Fc Zero Zero Cgasw 0 -0.1 -0.3 -0.133 Cgasw Units 0 0.1 0.1



### Tuesday, February 15, 2011 Page 35 of 47

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

Run Number Hg-1 Hg-2 M23/HCHO R2 Test Date 3/2/2010 3/2/2010 3/3/2010 Run Start Time 3:30:00 AM 6:15:00 AM 9:45:00 PM Run Finish Time 5:30:00 AM 8:15:00 AM 6:42:00 AM Carbon Dioxide, % 7.07 7.07 6.55 6.897 Oxygen, % 11.52 11.55 11.83 11.633 Fuel Factor 1.33 1.32 1.38 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 2 2 21 8.333 Calibration Pre Zero Cylinder ID Zero Zero Zero Calibration Pre Zero Cylinder Instrument Response -0.02 -0.02 -0.01 -0.017 Calibration Pre Zero Cylinder Bias -0.1 -0.1 0.2 0.000 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC179326 CC179326 CC179326 Calibration Pre High Cylinder Instrument Response 8.88 8.88 8.67 8.810 Calibration Pre High Cylinder Bias -0.5 -0.5 -0.45 -0.483 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Zero Calibration Post Zero Cylinder Instrument Response 0.04 0.03 -0.03 0.013 Calibration Post Zero Cylinder Bias 0.2 0.15 0.1 0.150 Calibration Post Zero Cylinder Drift 0.3 0.25 0.1 0.217 Calibration Post High Cylinder ID CC179326 CC179326 CC179326 Calibration Post High Cylinder Instrument Response 8.86 8.85 8.74 8.817 Calibration Post High Cylinder Bias -0.59 -0.64 -0.1 -0.443 Calibration Post High Cylinder Drift 0.09 0.14 0.35 0.193 Cavg 7.07 7.07 6.55 6.897 Cavg Units %vd %vd %vd Cgas 7.1716 7.1766 6.7771 7.042 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 36 of 47

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

Run Number M23/HCHO R3 M23/HCHO

R4 PM/Met-1

Test Date 3/4/2010 3/4/2010 3/1/2010 Run Start Time 9:30:00 AM 7:55:00 PM 1:40:00 AM Run Finish Time 6:04:00 PM 4:00:00 AM 7:52:00 AM Carbon Dioxide, % 6.52 6.54 6.84 6.633 Oxygen, % 11.9 11.94 11.86 11.900 Fuel Factor 1.38 1.37 1.32 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Servomex Analyzer Model 1440 1,440.000 Analyzer Serial Number 3893 3,893.000 Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 21 21 2 14.667 Calibration Pre Zero Cylinder ID Zero Zero Zero Calibration Pre Zero Cylinder Instrument Response -0.01 -0.01 -0.02 -0.013 Calibration Pre Zero Cylinder Bias 0.2 0.2 -0.1 0.100 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC179326 CC179326 CC179326 Calibration Pre High Cylinder Instrument Response 8.67 8.67 8.88 8.740 Calibration Pre High Cylinder Bias -0.45 -0.45 -0.5 -0.467 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Zero Calibration Post Zero Cylinder Instrument Response -0.08 -0.06 -0.05 -0.063 Calibration Post Zero Cylinder Bias -0.15 -0.05 -0.25 -0.150 Calibration Post Zero Cylinder Drift 0.35 0.25 0.15 0.250 Calibration Post High Cylinder ID CC179326 CC179326 CC179326 Calibration Post High Cylinder Instrument Response 8.72 8.74 8.86 8.773 Calibration Post High Cylinder Bias -0.2 -0.1 -0.59 -0.297 Calibration Post High Cylinder Drift 0.25 0.35 0.09 0.230 Cavg 6.52 6.54 6.84 6.633 Cavg Units %vd %vd %vd Cgas 6.7603 6.7706 6.9483 6.826 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 37 of 47

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

Run Number PM/Met-2 PM/Met-3 VOST/SVOL R1 Test Date 3/1/2010 3/1/2010 3/5/2010 Run Start Time 10:11:00 AM 8:00:00 PM 11:31:00 PM Run Finish Time 5:18:00 PM 2:15:00 AM 2:09:00 AM Carbon Dioxide, % 6.96 7.1 6.41 6.823 Oxygen, % 11.68 11.55 12.07 11.767 Fuel Factor 1.32 1.32 1.38 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 2 2 2 2.000 Calibration Pre Zero Cylinder ID Zero Zero Zero Calibration Pre Zero Cylinder Instrument Response -0.02 -0.02 -0.04 -0.027 Calibration Pre Zero Cylinder Bias -0.1 -0.1 -0.2 -0.133 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC179326 CC179326 CC179326 Calibration Pre High Cylinder Instrument Response 8.88 8.88 8.64 8.800 Calibration Pre High Cylinder Bias -0.5 -0.5 -1.68 -0.893 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Zero Calibration Post Zero Cylinder Instrument Response -0.01 0.02 -0.03 -0.007 Calibration Post Zero Cylinder Bias -0.05 0.1 -0.15 -0.033 Calibration Post Zero Cylinder Drift 0.05 0.2 0.15 0.133 Calibration Post High Cylinder ID CC179326 CC179326 CC179326 Calibration Post High Cylinder Instrument Response 8.86 8.87 8.7 8.810 Calibration Post High Cylinder Bias -0.59 -0.54 -1.39 -0.840 Calibration Post High Cylinder Drift 0.09 0.04 1.39 0.507 Cavg 6.96 7.1 6.41 6.823 Cavg Units %vd %vd %vd Cgas 7.0653 7.2 6.6634 6.976 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 38 of 47

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

Run Number VOST/SVOLR2 VOST/SVO

L-R3 Test Date 3/6/2010 3/6/2010 Run Start Time 2:46:00 AM 5:15:00 AM Run Finish Time 4:57:00 AM 7:20:00 AM Carbon Dioxide, % 6.44 6.71 6.575 Oxygen, % 12.04 11.69 11.865 Fuel Factor 1.38 1.37 Dry Volumetric Flow Rate, dry scfm 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9,190.000 Moisture, % 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0.000 Calibration Set 2 2 2.000 Calibration Pre Zero Cylinder ID Zero Zero Calibration Pre Zero Cylinder Instrument Response -0.04 -0.04 -0.040 Calibration Pre Zero Cylinder Bias -0.21 -0.2 -0.205 Calibration Pre Zero Cylinder Drift 0 0 0.000 Calibration Pre High Cylinder ID CC179326 CC179326 Calibration Pre High Cylinder Instrument Response 8.64 8.64 8.640 Calibration Pre High Cylinder Bias -1.68 -1.68 -1.680 Calibration Pre High Cylinder Drift 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Calibration Post Zero Cylinder Instrument Response -0.03 -0.02 -0.025 Calibration Post Zero Cylinder Bias -0.15 -0.1 -0.125 Calibration Post Zero Cylinder Drift 0.15 0.1 0.125 Calibration Post High Cylinder ID CC179326 CC179326 Calibration Post High Cylinder Instrument Response 8.7 8.7 8.700 Calibration Post High Cylinder Bias 44.66 -1.39 21.635 Calibration Post High Cylinder Drift 44.66 1.39 23.025 Cavg 6.44 6.71 6.575 Cavg Units %vd %vd Cgas 6.6944 6.9724 6.833 Cgas Units %vd %vd Fuel Type Oil Oil Fw 10320 10320 10,320.000 Fc 1420 1420 1,420.000 Cgasw 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 39 of 47

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

Run Number AG Run-1 AG Run-2 AG Run-3 Test Date 3/5/2010 3/6/2010 3/5/2010 Run Start Time 5:01:00 AM 10:22:00 AM 3:11:00 PM Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM Carbon Dioxide, % 6.42 6.44 6.43 6.430 Oxygen, % 11.9 11.99 11.94 11.943 Fuel Factor 1.4 1.38 1.39 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Servomex Analyzer Model 1440 1,440.000 Analyzer Serial Number 3839 3,839.000 Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 1 1 1 1.000 Calibration Pre Zero Cylinder ID Zero Zero Zero Calibration Pre Zero Cylinder Instrument Response 0.03 0.03 0.03 0.030 Calibration Pre Zero Cylinder Bias 0.15 0.15 0.15 0.150 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC179326 CC179326 CC179326 Calibration Pre High Cylinder Instrument Response 8.93 8.93 8.93 8.930 Calibration Pre High Cylinder Bias 45.84 45.84 45.84 45.840 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Zero Calibration Post Zero Cylinder Instrument Response 0.05 0.07 0.05 0.057 Calibration Post Zero Cylinder Bias 0.26 0.36 0.26 0.293 Calibration Post Zero Cylinder Drift 0.11 0.21 0.11 0.143 Calibration Post High Cylinder ID CC179326 CC179326 CC179326 Calibration Post High Cylinder Instrument Response 8.99 9.03 8.97 8.997 Calibration Post High Cylinder Bias 46.15 46.36 46.05 46.187 Calibration Post High Cylinder Drift 0.3099999999 99995 0.519999999

999996 0.209999999

999994 0.347
Cavg 11.9 11.99 11.94 11.943 Cavg Units %vd %vd %vd Cgas 11.9664 12.0336 12.0202 12.007 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 40 of 47

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

Run Number Hg-1 Hg-2 M23/HCHO R2 Test Date 3/2/2010 3/2/2010 3/3/2010 Run Start Time 3:30:00 AM 6:15:00 AM 9:45:00 PM Run Finish Time 5:30:00 AM 8:15:00 AM 6:42:00 AM Carbon Dioxide, % 7.07 7.07 6.55 6.897 Oxygen, % 11.52 11.55 11.83 11.633 Fuel Factor 1.33 1.32 1.38 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 1 1 11 4.333 Calibration Pre Zero Cylinder ID Zero Zero Zero Calibration Pre Zero Cylinder Instrument Response -0.01 -0.01 0.04 0.007 Calibration Pre Zero Cylinder Bias -0.05 -0.05 0.36 0.087 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC179326 CC179326 CC179326 Calibration Pre High Cylinder Instrument Response 9.17 9.17 8.97 9.103 Calibration Pre High Cylinder Bias 47.07 47.07 -0.36 31.260 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Zero Calibration Post Zero Cylinder Instrument Response 0.06 0.05 0.04 0.050 Calibration Post Zero Cylinder Bias 0.31 0.26 0.36 0.310 Calibration Post Zero Cylinder Drift 0.36 0.31 0 0.223 Calibration Post High Cylinder ID CC179326 CC179326 CC179326 Calibration Post High Cylinder Instrument Response 9.15 9.15 9.01 9.103 Calibration Post High Cylinder Bias 46.97 46.97 -0.15 31.263 Calibration Post High Cylinder Drift 0.1000000000 00001 0.100000000

000001 0.21 0.137
Cavg 11.52 11.55 11.83 11.633 Cavg Units %vd %vd %vd Cgas 11.3251 11.3534 11.8559 11.511 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 41 of 47

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

Run Number M23/HCHO R3 M23/HCHO

R4 PM/MET-1

Test Date 3/4/2010 3/4/2010 3/1/2010 Run Start Time 9:30:00 AM 7:55:00 PM 1:40:00 AM Run Finish Time 6:04:00 PM 4:00:00 AM 7:52:00 AM Carbon Dioxide, % 6.52 6.54 6.84 6.633 Oxygen, % 11.9 11.94 11.86 11.900 Fuel Factor 1.38 1.37 1.32 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Servomex Analyzer Model 1440 1,440.000 Analyzer Serial Number 3893 3,893.000 Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 11 11 1 7.667 Calibration Pre Zero Cylinder ID Zero Zero Zero Calibration Pre Zero Cylinder Instrument Response 0.04 0.04 -0.01 0.023 Calibration Pre Zero Cylinder Bias 0.36 0.36 -0.05 0.223 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC179326 CC179326 CC179326 Calibration Pre High Cylinder Instrument Response 8.97 8.97 9.17 9.037 Calibration Pre High Cylinder Bias -0.36 -0.36 47.07 15.450 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Zero Calibration Post Zero Cylinder Instrument Response 0.01 0.04 0.08 0.043 Calibration Post Zero Cylinder Bias 0.21 0.36 0.41 0.327 Calibration Post Zero Cylinder Drift 0.21 0 0.46 0.223 Calibration Post High Cylinder ID CC179326 CC179326 CC179326 Calibration Post High Cylinder Instrument Response 8.99 9.02 9.2 9.070 Calibration Post High Cylinder Bias -0.26 -0.1 47.23 15.623 Calibration Post High Cylinder Drift 0.26 0.26 0.159999999 999997 0.227
Cavg 11.9 11.94 11.86 11.900 Cavg Units %vd %vd %vd Cgas 11.9347 11.9598 11.6311 11.842 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 42 of 47

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

Run Number PM/Met-2 PM/Met-3 VOST/SVOL -R1 Test Date 3/1/2010 3/1/2010 3/5/2010 Run Start Time 10:11:00 AM 8:00:00 PM 11:31:00 PM Run Finish Time 5:18:00 PM 2:15:00 AM 2:09:00 AM Carbon Dioxide, % 6.96 7.1 6.41 6.823 Oxygen, % 11.68 11.55 12.07 11.767 Fuel Factor 1.32 1.32 1.38 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 1 1 1 1.000 Calibration Pre Zero Cylinder ID Zero Zero Zero Calibration Pre Zero Cylinder Instrument Response -0.01 -0.01 0.03 0.003 Calibration Pre Zero Cylinder Bias -0.05 -0.05 0.15 0.017 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC179326 CC179326 CC179326 Calibration Pre High Cylinder Instrument Response 9.17 9.17 8.93 9.090 Calibration Pre High Cylinder Bias 47.07 47.07 45.84 46.660 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Zero Calibration Post Zero Cylinder Instrument Response 0.05 0.06 0.08 0.063 Calibration Post Zero Cylinder Bias 0.26 0.31 0.41 0.327 Calibration Post Zero Cylinder Drift 0.31 0.36 0.41 0.360 Calibration Post High Cylinder ID CC179326 CC179326 CC179326 Calibration Post High Cylinder Instrument Response 9.15 9.15 9.01 9.103 Calibration Post High Cylinder Bias 46.97 46.97 46.25 46.730 Calibration Post High Cylinder Drift 0.1000000000 00001 0.100000000

000001 46.25 15.483
Cavg 11.68 11.55 12.07 11.767 Cavg Units %vd %vd %vd Cgas 11.4814 11.3547 12.1296 11.655 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 43 of 47

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

Run Number VOST/SVOLR2 VOST/SVO

L-R3 Test Date 3/6/2010 3/6/2010 Run Start Time 2:46:00 AM 5:15:00 AM Run Finish Time 4:57:00 AM 7:20:00 AM Carbon Dioxide, % 6.44 6.71 6.575 Oxygen, % 12.04 11.69 11.865 Fuel Factor 1.38 1.37 Dry Volumetric Flow Rate, dry scfm 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9,190.000 Moisture, % 0 0 0.000 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0.000 Calibration Set 1 1 1.000 Calibration Pre Zero Cylinder ID Zero Zero Calibration Pre Zero Cylinder Instrument Response 0.03 0.03 0.030 Calibration Pre Zero Cylinder Bias 0.15 0.15 0.150 Calibration Pre Zero Cylinder Drift 0 0 0.000 Calibration Pre High Cylinder ID CC179326 CC179326 Calibration Pre High Cylinder Instrument Response 8.93 8.93 8.930 Calibration Pre High Cylinder Bias 45.84 45.84 45.840 Calibration Pre High Cylinder Drift 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Calibration Post Zero Cylinder Instrument Response 0.09 0.09 0.090 Calibration Post Zero Cylinder Bias 0.46 0.46 0.460 Calibration Post Zero Cylinder Drift 0.31 0.46 0.385 Calibration Post High Cylinder ID CC179326 CC179326 Calibration Post High Cylinder Instrument Response 9.01 9 9.005 Calibration Post High Cylinder Bias 46.25 46.2 46.225 Calibration Post High Cylinder Drift 0.4099999999 99997 46.2 23.305
Cavg 12.04 11.69 11.865 Cavg Units %vd %vd Cgas 12.101 11.7541 11.928 Cgas Units %vd %vd Fuel Type Oil Oil Fw 10320 10320 10,320.000 Fc 1420 1420 1,420.000 Cgasw 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 44 of 47

### Location Stack Exit - Method 6C Average

Run Number AG Run 1 AG Run 2 AG Run 3 Test Date 3/5/2010 3/5/2010 3/5/2010 Run Start Time 5:01:00 AM 10:22:00 AM 3:11:00 PM Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM Carbon Dioxide, % 6.42 6.44 6.43 6.430 Oxygen, % 11.9 11.99 11.94 11.943 Fuel Factor 1.4 1.38 1.39 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Bovar Bovar Bovar Analyzer Model 721-M 721-M 721-M Analyzer Serial Number 1W-721M8560-6 1W-721M8560-6 1W-721M8560-6 Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 41 41 41 41.000 Calibration Pre Zero Cylinder ID Zero Zero Zero Calibration Pre Zero Cylinder Instrument Response 0.55 1.97 -0.28 0.747 Calibration Pre Zero Cylinder Bias -0.16 1.38 -1.07 0.050 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID SA 7995 SA 7995 SA 7995 Calibration Pre High Cylinder Instrument Response 47.5 49.02 46.65 47.723 Calibration Pre High Cylinder Bias -1.96 -1.96 -2.88 -2.267 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Zero Calibration Post Zero Cylinder Instrument Response 1.97 -0.3 -1.4 0.090 Calibration Post Zero Cylinder Bias 1.38 -1.09 -2.28 -0.663 Calibration Post Zero Cylinder Drift 1.54 0.98 2.28 1.600 Calibration Post High Cylinder ID SA 7995 SA 7995 SA 7995 Calibration Post High Cylinder Instrument Response 49.02 46.7 45.1 46.940 Calibration Post High Cylinder Bias -0.3 -2.83 -4.57 -2.567 Calibration Post High Cylinder Drift 1.66 0.87 4.57 2.367 Cavg 8.05 8.19 5.78 7.340 Cavg Units ppmvd ppmvd ppmvd Cgas 6.9634 7.5388 6.8304 7.111 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 45 of 47

### Location Stack Exit - Method 7E Average

Run Number AG Run 1 AG Run 2 AG Run 3 Test Date 3/5/2010 3/5/2010 3/5/2010 Run Start Time 5:01:00 AM 10:22:00 AM 3:11:00 PM Run Finish Time 9:11:00 AM 3:00:00 PM 6:12:00 PM Carbon Dioxide, % 6.42 6.44 6.43 6.430 Oxygen, % 11.9 11.99 11.94 11.943 Fuel Factor 1.4 1.38 1.39 Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 0 0 0 0.000 Analyzer Make Teledyne Teledyne Teledyne Analyzer Model 200 EH 200 EH 200 EH Analyzer Serial Number 172 172 172 172.000 Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 31 31 31 31.000 Calibration Pre Zero Cylinder ID Zero Zero Zero Calibration Pre Zero Cylinder Instrument Response 0.87 0.83 0.07 0.590 Calibration Pre Zero Cylinder Bias 0.36 -0.03 -0.34 -0.003 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID CC116930 CC116930 CC116930 Calibration Pre High Cylinder Instrument Response 124.2 123.8 123.72 123.907 Calibration Pre High Cylinder Bias 0.49 -0.93 -0.96 -0.467 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Zero Zero Zero Calibration Post Zero Cylinder Instrument Response 0.83 0.07 0.05 0.317 Calibration Post Zero Cylinder Bias 0.34 0.14 -0.35 0.043 Calibration Post Zero Cylinder Drift 0.02 0.22 9.999999999 99995E-03 0.083
Calibration Post High Cylinder ID CC116930 CC116930 CC116930 Calibration Post High Cylinder Instrument Response 123.8 123.72 124.17 123.897 Calibration Post High Cylinder Bias 0.33 0.3 0.48 0.370 Calibration Post High Cylinder Drift 0.16 0.19 0.48 0.277 Cavg 73.3 72.7 73.3 73.100 Cavg Units ppmvd ppmvd ppmvd Cgas 72.3618 72.0684 72.7168 72.382 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 15, 2011 Page 46 of 47

### 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 47 of 47