### 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.

Wednesday, February 16, 2011 Page 1 of 45

### Facility Information:

IP&L Eagle Valley Generating Station

4040 Blue Bluff Road

Martinsville IN 46151
Contact: Kyle Noah

Phone: 317-439-1251

Fax: 765-342-2311
Email: kyle.noah@aes.com Testing Company: URS Corporation
1600 Perimeter Park Drive, Suite 400

Morrisville NC 27560
Contact: Brad Justus

Phone: 919-461-1326

Fax: 919-461-1415
Email: brad_justus@urscorp.com

Air Permit Number:
991 Permitted Source ID/Name:
Boilers 1 and 2 Combined Stack
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: Boilers 1 and 2 are rated at 45 MW each and fire No. 2 Distillate Fuel Oil. Both units exhaust through a common stack. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 110000396606 FRS #: 110000396606

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 15 180 50 4 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

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



### Wednesday, February 16, 2011 Page 2 of 451,2,3,4,6,7,8-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 Total Dioxins Method 23 3 480 0 Stack Exit Total Furans Method 23 3 480 0 Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0 Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0 Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0 Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0 Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0 Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0 Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0 Stack Exit 2,3,3',4,4',5/2,3,3',4,4',5'-

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

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

(PCB189) Method 23 3 480 0 Stack Exit

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

(TOC) as Propane Method 25A 3 120 0 Stack Exit

Hydrogen Fluoride Method 26A 3 180 0 Stack Exit Hydrogen Chloride Method 26A 3 180 0 Stack Exit Total Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Total 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

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

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

Filterable Particulate Method 29 3 240 0 Stack Exit Antimony Method 29 3 240 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit Beryllium Method 29 3 240 0 Stack Exit



### Wednesday, February 16, 2011 Page 3 of 45

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

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

None Cadmium Method 29 3 240 0 Stack Exit Chromium Method 29 3 240 0 Stack Exit Lead Method 29 3 240 0 Stack Exit Manganese Method 29 3 240 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit Nickel Method 29 3 240 0 Stack Exit Co2 Method 3A CO2 3 480 0 Stack Exit O2 Method 3A O2 3 480 0 Stack Exit Sulfur Dioxide Method 6C 3 180 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### Wednesday, February 16, 2011 Page 4 of 45

### 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 5/6/2010 5/6/2010 5/6/2010

Run Start Time 12:10:00 AM 9:00:00 AM 12:10:00 AM

Run Finish Time 8:27:00 AM 5:15:00 PM 11:35:00 PM
Net Run Time, minutes 485 480 480 Dry Gas Meter Volume Sampled, dscf 346.675 345.732 346.506 346.304
Moisture Content of Stack Gas, % 7.18 7.03 7.46 7.223 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000
Carbon Dioxide, % 7.4 7.4 7.5 7.433 Oxygen, % 11.5 11.5 11.2 11.400 Average Stack Gas Temperature, °F 269.79 269.19 271.78 270.253 Dry Volumetric Flow Rate, dry scfm 1,150.3 1,156.1 1,143.3 1,149.900
Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,749.2 1,753.6 1,748.5 1,750.433 Percent Isokinetic of Sampling Rate, % 96.8 97.1 98.4 97.433
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



### Wednesday, February 16, 2011 Page 5 of 45

### 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



### Wednesday, February 16, 2011 Page 6 of 45

### 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



### Wednesday, February 16, 2011 Page 7 of 45

### 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



### Wednesday, February 16, 2011 Page 8 of 45

### 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 CO2 3 6 9 12 Average
Run Number

Test Date

Run Start Time

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

Fw

Fc



### Wednesday, February 16, 2011 Page 9 of 45

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

Run Number

Test Date

Run Start Time

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

Fw

Fc



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

Test Date

Run Start Time

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

Fw

Fc



### Wednesday, February 16, 2011 Page 10 of 45

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

Run Number

Test Date

Run Start Time

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

Fw

Fc



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

Test Date

Run Start Time

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

Fw

Fc



### Wednesday, February 16, 2011 Page 11 of 45

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

Run Number

Test Date

Run Start Time

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

Fw

Fc



### Location Stack Exit - Method 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



### Wednesday, February 16, 2011 Page 12 of 45

### 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



### Wednesday, February 16, 2011 Page 13 of 45

### Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average
Run DF/30B Run 1 DF/30B Run 2 DF/30B Run 3 lb/mmBtuO2 1.01E-03 1.19E-03 3.33E-04 0.001
ppm 6.80E-01 8.04E-01 2.31E-01 0.572 ppm@7%O2 1.00E+00 1.18E+00 3.32E-01 0.837



### Location: Stack Exit - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.0000000976 0.0000000224 0.000000068 0.000 lb/mmBtuO2 1.27E-11 2.92E-12 8.57E-12 0.000 ng/dscm 9.94E-03 2.29E-03 6.93E-03 0.006 ng/dscm@7%O2 1.47E-02 3.39E-03 9.93E-03 0.009


### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.00000000931 0.00000000252 0.00000000517 0.000 lb/mmBtuO2 1.21E-12 3.28E-13 6.51E-13 0.000 ng/dscm 9.49E-04 2.57E-04 5.27E-04 0.001 ng/dscm@7%O2 1.40E-03 3.80E-04 7.55E-04 0.001


### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.00000000594 0.0000000031 0.00000000623 0.000 lb/mmBtuO2 7.72E-13 4.04E-13 7.85E-13 0.000 ng/dscm 6.05E-04 3.17E-04 6.35E-04 0.001 ng/dscm@7%O2 8.95E-04 4.69E-04 9.10E-04 0.001


### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000351 0.00000000319 0.0000000216 0.000 lb/mmBtuO2 4.56E-12 4.16E-13 2.72E-12 0.000 ng/dscm 3.58E-03 3.26E-04 2.20E-03 0.002 ng/dscm@7%O2 5.29E-03 4.82E-04 3.15E-03 0.003


### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000743 0.00000000173 0.00000000405 0.000 lb/mmBtuO2 9.65E-13 2.25E-13 5.10E-13 0.000 ng/dscm 7.57E-04 1.77E-04 4.13E-04 0.000 ng/dscm@7%O2 1.12E-03 2.62E-04 5.92E-04 0.001


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



### Wednesday, February 16, 2011 Page 14 of 45RunNumber 1 2 3 Mass_mg 0.0000000411 0.00000000433 0.000000024 0.000 lb/mmBtuO2 5.34E-12 5.64E-13 3.02E-12 0.000 ng/dscm 4.19E-03 4.42E-04 2.45E-03 0.002 ng/dscm@7%O2 6.20E-03 6.54E-04 3.51E-03 0.003


### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000445 0.00000000171 0.00000000297 0.000 lb/mmBtuO2 5.78E-13 2.23E-13 3.74E-13 0.000 ng/dscm 4.53E-04 1.75E-04 3.03E-04 0.000 ng/dscm@7%O2 6.70E-04 2.59E-04 4.34E-04 0.000


### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000525 0.00000000759 0.0000000294 0.000 lb/mmBtuO2 6.82E-12 9.89E-13 3.70E-12 0.000 ng/dscm 5.35E-03 7.75E-04 3.00E-03 0.003 ng/dscm@7%O2 7.91E-03 1.15E-03 4.30E-03 0.004


### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000333 0.00000000154 0.00000000411 0.000 lb/mmBtuO2 4.33E-13 2.01E-13 5.18E-13 0.000 ng/dscm 3.39E-04 1.57E-04 4.19E-04 0.000 ng/dscm@7%O2 5.01E-04 2.32E-04 6.00E-04 0.000


### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.0000000756 0.00000000424 0.0000000571 0.000 lb/mmBtuO2 9.82E-12 5.52E-13 7.19E-12 0.000 ng/dscm 7.70E-03 4.33E-04 5.82E-03 0.005 ng/dscm@7%O2 1.14E-02 6.40E-04 8.34E-03 0.007


### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000104 0.0000000024 0.00000000705 0.000 lb/mmBtuO2 1.35E-12 3.13E-13 8.88E-13 0.000 ng/dscm 1.06E-03 2.45E-04 7.19E-04 0.001 ng/dscm@7%O2 1.57E-03 3.62E-04 1.03E-03 0.001


### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 2 3 Mass_mg 0.0000000391 0.0000000623 0.0000000374 0.000 lb/mmBtuO2 5.08E-12 8.12E-12 4.71E-12 0.000 ng/dscm 3.98E-03 6.36E-03 3.81E-03 0.005 ng/dscm@7%O2 5.89E-03 9.40E-03 5.46E-03 0.007



### Wednesday, February 16, 2011 Page 15 of 45

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 2 3 Mass_mg 0.000000237 0.000000317 0.000000144 0.000 lb/mmBtuO2 3.08E-11 4.13E-11 1.81E-11 0.000 ng/dscm 2.41E-02 3.24E-02 1.47E-02 0.024 ng/dscm@7%O2 3.56E-02 4.79E-02 2.11E-02 0.035


### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 2 3 Mass_mg 0.00000152 0.00000186 0.000000794 0.000 lb/mmBtuO2 1.98E-10 2.42E-10 1.00E-10 0.000 ng/dscm 1.55E-01 1.90E-01 8.09E-02 0.142 ng/dscm@7%O2 2.29E-01 2.81E-01 1.16E-01 0.209


### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 2 3 Mass_mg 0.0000000753 0.000000133 0.0000000597 0.000 lb/mmBtuO2 9.78E-12 1.73E-11 7.52E-12 0.000 ng/dscm 7.67E-03 1.36E-02 6.09E-03 0.009 ng/dscm@7%O2 1.13E-02 2.01E-02 8.73E-03 0.013


### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 2 3 Mass_mg 0.0000000303 0.000000131 0.0000000703 0.000 lb/mmBtuO2 3.94E-12 1.71E-11 8.86E-12 0.000 ng/dscm 3.09E-03 1.34E-02 7.17E-03 0.008 ng/dscm@7%O2 4.57E-03 1.98E-02 1.03E-02 0.012


### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 2 3 Mass_mg 0.0000043 0.00000547 0.00000227 0.000 lb/mmBtuO2 5.59E-10 7.13E-10 2.86E-10 0.000 ng/dscm 4.38E-01 5.59E-01 2.31E-01 0.409 ng/dscm@7%O2 6.48E-01 8.27E-01 3.31E-01 0.602


### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 2 3 Mass_mg 0.0000000374 0.0000000564 0.0000000274 0.000 lb/mmBtuO2 4.86E-12 7.35E-12 3.45E-12 0.000 ng/dscm 3.81E-03 5.76E-03 2.79E-03 0.004 ng/dscm@7%O2 5.63E-03 8.52E-03 4.00E-03 0.006


### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000215 0.00000000109 0.00000000277 0.000 lb/mmBtuO2 2.79E-13 1.42E-13 3.49E-13 0.000



### Wednesday, February 16, 2011 Page 16 of 45ng/dscm 2.19E-04 1.11E-04 2.82E-04 0.000 ng/dscm@7%O2 3.24E-04 1.64E-04 4.04E-04 0.000


### Compound: 2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.00000000781 0.00000000156 0.00000000251 0.000 lb/mmBtuO2 1.01E-12 2.03E-13 3.16E-13 0.000 ng/dscm 7.96E-04 1.59E-04 2.56E-04 0.000 ng/dscm@7%O2 1.18E-03 2.35E-04 3.67E-04 0.001


### Compound: 2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000311 0.00000000259 0.0000000223 0.000 lb/mmBtuO2 4.04E-12 3.37E-13 2.81E-12 0.000 ng/dscm 3.17E-03 2.65E-04 2.27E-03 0.002 ng/dscm@7%O2 4.69E-03 3.92E-04 3.25E-03 0.003


### Compound: 2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.00000000759 0.0000000025 0.00000000305 0.000 lb/mmBtuO2 9.86E-13 3.26E-13 3.84E-13 0.000 ng/dscm 7.73E-04 2.55E-04 3.11E-04 0.000 ng/dscm@7%O2 1.14E-03 3.77E-04 4.46E-04 0.001


### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 2 3 Mass_mg 0.0000000399 0.0000000583 0.0000000404 0.000 lb/mmBtuO2 5.18E-12 7.60E-12 5.09E-12 0.000 ng/dscm 4.07E-03 5.96E-03 4.12E-03 0.005 ng/dscm@7%O2 6.02E-03 8.81E-03 5.90E-03 0.007


### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 2 3 Mass_mg 0.0000000472 0.0000000568 0.0000000399 0.000 lb/mmBtuO2 6.13E-12 7.40E-12 5.03E-12 0.000 ng/dscm 4.81E-03 5.80E-03 4.07E-03 0.005 ng/dscm@7%O2 7.11E-03 8.58E-03 5.83E-03 0.007


### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 1 2 3 Mass_mg 0.000000718 0.000000881 0.000000346 0.000 lb/mmBtuO2 9.33E-11 1.15E-10 4.36E-11 0.000 ng/dscm 7.32E-02 9.00E-02 3.53E-02 0.066 ng/dscm@7%O2 1.08E-01 1.33E-01 5.06E-02 0.097


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



### Wednesday, February 16, 2011 Page 17 of 45Mass_mg 0.0000000474 0.000000074 0.00000003 0.000 lb/mmBtuO2 6.16E-12 9.64E-12 3.78E-12 0.000 ng/dscm 4.83E-03 7.56E-03 3.06E-03 0.005 ng/dscm@7%O2 7.14E-03 1.12E-02 4.38E-03 0.008


### Compound: OCDD Average RunNumber 1 2 3 Mass_mg 0.0000000953 0.0000000401 0.0000000724 0.000 lb/mmBtuO2 1.24E-11 5.22E-12 9.12E-12 0.000 ng/dscm 9.71E-03 4.10E-03 7.38E-03 0.007 ng/dscm@7%O2 1.44E-02 6.06E-03 1.06E-02 0.010


### Compound: OCDF Average RunNumber 1 2 3 Mass_mg 0.0000000195 0.00000000893 0.0000000199 0.000 lb/mmBtuO2 2.53E-12 1.16E-12 2.51E-12 0.000 ng/dscm 1.99E-03 9.12E-04 2.03E-03 0.002 ng/dscm@7%O2 2.94E-03 1.35E-03 2.91E-03 0.002


### Compound: Other HpCDD Average RunNumber 1 2 3 Mass_mg 0.000000125 0.0000000249 0.0000000893 0.000 lb/mmBtuO2 1.62E-11 3.24E-12 1.13E-11 0.000 ng/dscm 1.27E-02 2.54E-03 9.10E-03 0.008 ng/dscm@7%O2 1.88E-02 3.76E-03 1.30E-02 0.012


### Compound: Other HpCDF Average RunNumber 1 2 3 Mass_mg 0.00000000928 0 0.00000000736 0.000 lb/mmBtuO2 1.21E-12 0.00E+00 9.27E-13 0.000 ng/dscm 9.45E-04 0.00E+00 7.50E-04 0.001 ng/dscm@7%O2 1.40E-03 0.00E+00 1.07E-03 0.001


### Compound: Other HxCDD Average RunNumber 1 2 3 Mass_mg 0.000000491 0.0000000459 0.000000302 0.000 lb/mmBtuO2 6.38E-11 5.98E-12 3.80E-11 0.000 ng/dscm 5.00E-02 4.69E-03 3.08E-02 0.028 ng/dscm@7%O2 7.39E-02 6.94E-03 4.41E-02 0.042


### Compound: Other HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000317 0.00000000382 0.0000000174 0.000 lb/mmBtuO2 4.12E-12 4.98E-13 2.19E-12 0.000 ng/dscm 3.23E-03 3.90E-04 1.77E-03 0.002 ng/dscm@7%O2 4.78E-03 5.77E-04 2.54E-03 0.003



### Wednesday, February 16, 2011 Page 18 of 45

### Compound: Other PeCDD Average RunNumber 1 2 3 Mass_mg 0.000000676 0.0000000424 0.000000479 0.000 lb/mmBtuO2 8.78E-11 5.52E-12 6.03E-11 0.000 ng/dscm 6.89E-02 4.33E-03 4.88E-02 0.041 ng/dscm@7%O2 1.02E-01 6.40E-03 6.99E-02 0.059


### Compound: Other PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000753 0.00000000724 0.0000000323 0.000 lb/mmBtuO2 9.78E-12 9.43E-13 4.07E-12 0.000 ng/dscm 7.67E-03 7.40E-04 3.29E-03 0.004 ng/dscm@7%O2 1.13E-02 1.09E-03 4.71E-03 0.006


### Compound: Other TCDD Average RunNumber 1 2 3 Mass_mg 0.000000573 0.0000000356 0.000000383 0.000 lb/mmBtuO2 7.45E-11 4.64E-12 4.83E-11 0.000 ng/dscm 5.84E-02 3.64E-03 3.90E-02 0.034 ng/dscm@7%O2 8.64E-02 5.38E-03 5.59E-02 0.049


### Compound: Other TCDF Average RunNumber 1 2 3 Mass_mg 0.000000103 0.0000000367 0.0000000742 0.000 lb/mmBtuO2 1.34E-11 4.78E-12 9.35E-12 0.000 ng/dscm 1.05E-02 3.75E-03 7.56E-03 0.007 ng/dscm@7%O2 1.55E-02 5.55E-03 1.08E-02 0.011


### Compound: Total Dioxins Average RunNumber 1 2 3 Mass_mg 0.000002293 0.000000233 0.0000015481 0.000 lb/mmBtuO2 2.98E-10 3.04E-11 1.95E-10 0.000 ng/dscm 2.34E-01 2.38E-02 1.58E-01 0.139 ng/dscm@7%O2 3.46E-01 3.52E-02 2.26E-01 0.202


### Compound: Total Furans Average RunNumber 1 2 3 Mass_mg 0.000000297 0.000000075 0.00000018907 0.000 lb/mmBtuO2 3.86E-11 9.77E-12 2.38E-11 0.000 ng/dscm 3.03E-02 7.66E-03 1.93E-02 0.019 ng/dscm@7%O2 4.48E-02 1.13E-02 2.77E-02 0.028


### Compound: Total PCBs Average RunNumber 1 2 3 Mass_mg 0.000007092 0.0000091 0.000003859 0.000 lb/mmBtuO2 9.22E-10 1.19E-09 4.86E-10 0.000



### Wednesday, February 16, 2011 Page 19 of 45ng/dscm 7.23E-01 9.30E-01 3.93E-01 0.682 ng/dscm@7%O2 1.07E+00 1.38E+00 5.63E-01 1.004



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average
Run DF/30B Run 1 DF/30B Run 2 DF/30B Run 3 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000
ppm 0.00E+00 0.00E+00 0.00E+00 0.000 ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 0.253 0.282 0.279 0.271 Elb/hr 2.85E-04 3.19E-04 3.21E-04 0.000 lb/mmBtuO2 8.76E-05 9.52E-05 9.76E-05 0.000


### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 0.26 0.289 0.286 0.278 Elb/hr 2.93E-04 3.27E-04 3.29E-04 0.000 lb/mmBtuO2 9.00E-05 9.76E-05 1.00E-04 0.000



### Location: Stack Exit - Method 29 Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.0003 0.0003 0.0015 0.001 Elb/hr 1.74E-07 1.65E-07 8.48E-07 0.000 lb/mmBtuO2 5.40E-08 4.78E-08 2.43E-07 0.000


### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.0017 0.0019 0.0167 0.007 Elb/hr 9.84E-07 1.05E-06 9.44E-06 0.000 lb/mmBtuO2 3.06E-07 3.03E-07 2.70E-06 0.000


### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.0001 0.0001 0.0006 0.000 Elb/hr 5.79E-08 5.51E-08 3.39E-07 0.000 lb/mmBtuO2 1.80E-08 1.59E-08 9.70E-08 0.000


### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.0003 0.0004 0.0003 0.000



### Wednesday, February 16, 2011 Page 20 of 45Elb/hr 1.74E-07 2.20E-07 1.70E-07 0.000 lb/mmBtuO2 5.40E-08 6.38E-08 4.85E-08 0.000


### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.0058 0.0055 0.0065 0.006 Elb/hr 3.36E-06 3.03E-06 3.67E-06 0.000 lb/mmBtuO2 1.04E-06 8.77E-07 1.05E-06 0.000


### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 13 16.8 11.7 13.833 Elb/hr 7.53E-03 9.26E-03 6.61E-03 0.008 lb/mmBtuO2 2.34E-03 2.68E-03 1.89E-03 0.002


### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.0395 0.0434 0.0468 0.043 Elb/hr 2.29E-05 2.39E-05 2.64E-05 0.000 lb/mmBtuO2 7.11E-06 6.92E-06 7.57E-06 0.000


### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.009 0.0098 0.0079 0.009 Elb/hr 5.21E-06 5.40E-06 4.46E-06 0.000 lb/mmBtuO2 1.62E-06 1.56E-06 1.28E-06 0.000


### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 0.0058 0.0067 0.009 0.007 Elb/hr 3.36E-06 3.69E-06 5.09E-06 0.000 lb/mmBtuO2 1.04E-06 1.07E-06 1.46E-06 0.000


### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 0.0012 0.0009 0.0093 0.004 Elb/hr 6.95E-07 4.96E-07 5.26E-06 0.000 lb/mmBtuO2 2.16E-07 1.43E-07 1.50E-06 0.000



### Location: Stack Exit - Method 6C Compound: Sulfur Dioxide Average
Run Acid Gas R1 Acid Gas R2 Acid Gas R3 lb/mmBtuO2 2.53E-02 2.10E-02 1.87E-02 0.022
ppm 7.68E+00 6.39E+00 5.72E+00 6.597 ppm@7%O2 1.10E+01 9.14E+00 8.14E+00 9.427



### Wednesday, February 16, 2011 Page 21 of 45

### Location: Stack Exit - Method 7E



### Compound: Nitrogen oxides (NOx) Average
Run Acid Gas R1 Acid Gas R2 Acid Gas R3 lb/mmBtuO2 1.17E-01 1.16E-01 1.14E-01 0.116
ppm 4.96E+01 4.94E+01 4.74E+01 48.800 ppm@7%O2 7.11E+01 7.06E+01 6.94E+01 70.367



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

### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 5.3 13.6 11.7 10.200 Elb/hr 5.50E-03 1.42E-02 1.19E-02 0.011 gr/dscf 5.92E-04 1.50E-03 1.18E-03 0.001 lb/mmBtuO2 1.71E-03 4.27E-03 2.43E-03 0.003


### Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 2.2 8.6 5.7 5.500 Elb/hr 2.28E-03 8.97E-03 5.79E-03 0.006 gr/dscf 2.46E-04 9.46E-04 5.74E-04 0.001 lb/mmBtuO2 7.10E-04 2.70E-03 1.18E-03 0.002


### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 1 7.6 5 4.533 Elb/hr 1.04E-03 7.93E-03 5.08E-03 0.005 gr/dscf 1.12E-04 8.36E-04 5.03E-04 0.000 lb/mmBtuO2 3.23E-04 2.39E-03 1.04E-03 0.001


### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 5.7 3.9 2.8 4.133 Elb/hr 5.92E-03 4.07E-03 2.85E-03 0.004 gr/dscf 6.37E-04 4.29E-04 2.82E-04 0.000 lb/mmBtuO2 1.84E-03 1.23E-03 5.81E-04 0.001


### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 12 25.1 19.5 18.867 Elb/hr 1.25E-02 2.62E-02 1.98E-02 0.020 gr/dscf 1.34E-03 2.76E-03 1.96E-03 0.002 lb/mmBtuO2 3.87E-03 7.89E-03 4.05E-03 0.005


### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 9.8 16.5 13.8 13.367



### Wednesday, February 16, 2011 Page 22 of 45

### Process Run Data Elb/hr 1.02E-02 1.72E-02 1.40E-02 0.014 gr/dscf 1.10E-03 1.81E-03 1.39E-03 0.001 lb/mmBtuO2 3.16E-03 5.19E-03 2.87E-03 0.004



### Wednesday, February 16, 2011 Page 23 of 45

### Process Run Data



### Run Name Value UOM Comments Target Value
1 Heat Input 418 Million Btus/hr 0



### 10 Heat Input 415.9 Million Btus/hr 0

11 Heat Input 419.4 Million Btus/hr 0

12 Heat Input 401.8 Million Btus/hr 0



### 13 Heat Input 400.3 Million Btus/hr 0

14 Heat Input 407.6 Million Btus/hr 0

15 Heat Input 399.6 Million Btus/hr 0



### 2 Heat Input 383.5 Million Btus/hr 0

3 Heat Input 391.3 Million Btus/hr 0

4 Heat Input 406.6 Million Btus/hr 0



### 5 Heat Input 395.5 Million Btus/hr 0

6 Heat Input 389.1 Million Btus/hr 0

7 Heat Input 415.3 Million Btus/hr 0



### 8 Heat Input 409.9 Million Btus/hr 0

9 Heat Input 412.8 Million Btus/hr 0

1 Average Heat Input 0 MMBtu/hr 0



### 10 Average Heat Input 0 MMBtu/hr 0

11 Average Heat Input 0 MMBtu/hr 0

12 Average Heat Input 0 MMBtu/hr 0



### 13 Average Heat Input 0 MMBtu/hr 0

14 Average Heat Input 0 MMBtu/hr 0

15 Average Heat Input 0 MMBtu/hr 0



### 2 Average Heat Input 0 MMBtu/hr 0

3 Average Heat Input 0 MMBtu/hr 0



### 4 Average Heat Input 0 MMBtu/hr 0

5 Average Heat Input 0 MMBtu/hr 0

6 Average Heat Input 0 MMBtu/hr 0



### 7 Average Heat Input 0 MMBtu/hr 0

8 Average Heat Input 0 MMBtu/hr 0

9 Average Heat Input 0 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



### Wednesday, February 16, 2011 Page 24 of 45

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



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

14 Steam Output 0 1000 lb steam/hr 0

15 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

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 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



### 13 Fuel Oil Firing Rate 0 0

14 Fuel Oil Firing Rate 0 0

15 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 Standard Pressure 1 atm 0

10 Standard Pressure 0 atm 0

11 Standard Pressure 0 atm 0



### 12 Standard Pressure 0 atm 0

13 Standard Pressure 0 atm 0

14 Standard Pressure 0 atm 0



### 15 Standard Pressure 0 atm 0

2 Standard Pressure 0 atm 0

3 Standard Pressure 0 atm 0



### Wednesday, February 16, 2011 Page 25 of 45

### 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 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



### 13 Standard Temperature 0 Deg F 0

14 Standard Temperature 0 Deg F 0

15 Standard Temperature 0 Deg F 0



### 2 Standard Temperature 0 Deg F 0

3 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 32 MW 0

10 Unit Gross Electrical Output 31.9 MW 0

11 Unit Gross Electrical Output 32.1 MW 0



### 12 Unit Gross Electrical Output 30.3 MW 0

13 Unit Gross Electrical Output 30.1 MW 0

14 Unit Gross Electrical Output 30.5 MW 0



### 15 Unit Gross Electrical Output 30 MW 0

2 Unit Gross Electrical Output 28.2 MW 0

3 Unit Gross Electrical Output 28.9 MW 0



### 4 Unit Gross Electrical Output 30.7 MW 0

5 Unit Gross Electrical Output 29.8 MW 0

6 Unit Gross Electrical Output 29 MW 0



### 7 Unit Gross Electrical Output 31.8 MW 0

8 Unit Gross Electrical Output 31 MW 0

9 Unit Gross Electrical Output 31.1 MW 0



### Wednesday, February 16, 2011 Page 26 of 45

### APCD Run Data

Process Lab Run Data 1 Unit Net Electric Generation 29.9 MWh 0



### 10 Unit Net Electric Generation 29.7 MWh 0

11 Unit Net Electric Generation 29.9 MWh 0

12 Unit Net Electric Generation 28.1 MWh 0



### 13 Unit Net Electric Generation 27.9 MWh 0

14 Unit Net Electric Generation 28.3 MWh 0

15 Unit Net Electric Generation 27.8 MWh 0



### 2 Unit Net Electric Generation 26 MWh 0

3 Unit Net Electric Generation 26.7 MWh 0

4 Unit Net Electric Generation 28.6 MWh 0



### 5 Unit Net Electric Generation 27.6 MWh 0

6 Unit Net Electric Generation 26.8 MWh 0

7 Unit Net Electric Generation 29.6 MWh 0



### 8 Unit Net Electric Generation 28.9 MWh 0

9 Unit Net Electric Generation 29 MWh 0

Run Name Value UOM Comments


### 1 Fuel Higher Heating Value 19509 Btu/lb
1 Fuel Moisture 0 %
1 Fuel Mercury Content 8E-06 ppm 1 Fuel Cadmium Content 0 ppm 

### 1 Ultimate/Proximate Analysis 0
1 Fuel Nickel Content 0.003 ppm 1 Fuel Arsenic Content 0.0006 ppm 

### 1 Fuel Chromium Content 0.0008 ppm 1 Fuel Beryllium Content 0.0002 ppm 1 Fuel Lead Content 0.001 ppm 1 Fuel Manganese Content 0.002 ppm 

### 1 Fuel Chlorine Content 0.008 ppm 1 Fuel Fluorine Content 0 ppm

Wednesday, February 16, 2011 Page 27 of 45

### 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



### Wednesday, February 16, 2011 Page 28 of 45

### Location Stack Exit - Method 23 Average

Run Number 1 2 3
Test Date 5/6/2010 5/6/2010 5/6/2010 Run Start Time 12:10:00 AM 9:00:00 AM 12:10:00 AM Run Finish Time 8:27:00 AM 5:15:00 PM 11:35:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 485 480 480 Nozzle Diameter, inches 0.38 0.38 0.38 0.380 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 29.3 29.3 29.3 29.300 Average Orifice Meter Differential, inches H2O 1.56 1.57 1.56 1.563 Dry Gas Meter Volume Sampled, cubic feet 345.588 353.310 350.034 349.644 Average Dry Gas Meter Temperature, °F 64.70 77.90 71.71 71.437 Dry Gas Meter Volume Sampled, dscf 346.675 345.732 346.506 346.304 Total Moisture Liquid collected, g 569.6 555.4 593.2 572.733 Volume of Water Vapor, standard cubic feet 26.81 26.14 27.92 26.957 Moisture Content of Stack Gas, % 7.18 7.03 7.46 7.223 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9282 0.9297 0.9254 0.928 Carbon Dioxide, % 7.4 7.4 7.5 7.433 Oxygen, % 11.5 11.5 11.2 11.400 Carbon Monoxide & Nitrogen, % 81.1 81.1 81.3 81.167 Fuel Factor 1.27 1.27 1.29 Dry Molecular Weight, lb/lb-Mole 29.64 29.64 29.65 29.643 Wet Molecular weight, lb/lb-Mole 28.80 28.82 28.78 28.800 Flue Gas Static Pressure, inches of H2O -0.05 -0.05 -0.05 -0.050 Absolute Flue Gas Pressure, inches of Mercury 29.30 29.30 29.30 29.300 Average Stack Gas Temperature, °F 269.79 269.19 271.78 270.253 Average Velocity Head, inches of H2O 0.1265522425 96508 0.127398901

322278 0.126048984

321641 0.127

Average Stack Gas Velocity, feet/second 23.76 23.82 23.75 23.777 Stack Cross-Sectional Area, square feet 1.227 1.227 1.227 1.227 Dry Volumetric Flow Rate, dry scfm 1,150.3 1,156.1 1,143.3 1,149.900 Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,749.2 1,753.6 1,748.5 1,750.433 Percent Isokinetic of Sampling Rate, % 96.8 97.1 98.4 97.433 Percent Excess Air, % 116.0 116.0 109.1 113.700 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Round Duct Diameter, inches 15 15 15 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



### Wednesday, February 16, 2011 Page 29 of 45

### 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



### Wednesday, February 16, 2011 Page 30 of 45

### 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



### Wednesday, February 16, 2011 Page 31 of 45

### 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



### Wednesday, February 16, 2011 Page 32 of 45

### 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



### Wednesday, February 16, 2011 Page 33 of 45

### 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



### Wednesday, February 16, 2011 Page 34 of 45

### 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



### Wednesday, February 16, 2011 Page 35 of 45

### 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



### Wednesday, February 16, 2011 Page 36 of 45

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

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



### Wednesday, February 16, 2011 Page 37 of 45

### 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



### Wednesday, February 16, 2011 Page 38 of 45

### 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



### Wednesday, February 16, 2011 Page 39 of 45

### 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



### Wednesday, February 16, 2011 Page 40 of 45

### 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



### Wednesday, February 16, 2011 Page 41 of 45

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

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



### Wednesday, February 16, 2011 Page 42 of 45

### 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



### Wednesday, February 16, 2011 Page 43 of 45

### 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



### Wednesday, February 16, 2011 Page 44 of 45

### 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



### Wednesday, February 16, 2011 Page 45 of 45