### Name: Jon Hays

Title: Environmental Specialist Company: Duke Energy Sign Date: 9/2/2010 Name: Pat Ford Title: project manager Company: AECOM Sign Date: 8/26/2010 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 01, 2011 Page 1 of 30

### 9/2/2010

Facility Information: IN_Wabash River Combined Cycle Station
450 Bolton Road

West Terre Haute IN 47885 Contact: Jon Hays
Phone: 317-838-4445
Fax: 317-8382490
Email: jon.hays@duke.energy.com Testing Company:
AECOM 2 Technology Park Drive

Westford MA 01886 Contact: Patrick Ford
Phone: 978-589-3427
Fax: 978-589-3100
Email: pat.ford@aecom.com

Air Permit Number: 167-26486-00147 Permitted Source ID/Name: Combustion Turbine Unit 1
Permitted Maximum Process Rate: 1709.1 Max. Normal Operation Process Rate: 1709.1 Target Process Test Rate 1709.1

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: This description should describe the process and associated controls to differentiate this facility from, or document similarity with others of same SCC. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 1816700147 FRS #: 330015654589

SCC / Description 20100201 Internal Combustion Engines - Electric Generation - Natural Gas - Turbine

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 216 8 2 4 0 16 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location
% H2O Method 1 - 4 3 60 0 Stack Exit Carbon Monoxide Method 10 3 120 0 Stack Exit 2,3,7,8-TCDD Method 23 3 416 0 Stack Exit 1,2,3,7,8-PeCDD Method 23 3 416 0 Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 416 0 Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 416 0 Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 416 0 Stack Exit



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

### 9/2/2010

The following describes any modifications and/or deviations to the applicable test methods. If alternative methods were requested, see the attachments for documentation of request AND approval, including dates.

1,2,3,4,6,7,8-HpCDD Method 23 3 416 0 Stack Exit OCDD Method 23 3 416 0 Stack Exit 2,3,7,8-TCDF Method 23 3 416 0 Stack Exit 1,2,3,7,8-PeCDF Method 23 3 416 0 Stack Exit 2,3,4,7,8-PeCDF Method 23 3 416 0 Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 416 0 Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 416 0 Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 416 0 Stack Exit 1,2,3,7,8,9-HxCDF Method 23 3 416 0 Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 416 0 Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 416 0 Stack Exit OCDF Method 23 3 416 0 Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 416 0 Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 416 0 Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 416 0 Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 416 0 Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 416 0 Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 416 0 Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 416 0 Stack Exit 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 416 0 Stack Exit

2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 416 0 Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 416 0 Stack Exit 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 416 0 Stack Exit

Total organic compounds

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

Hydrogen Chloride Method 26A 3 120 0 Stack Exit Hydrogen Fluoride Method 26A 3 120 0 Stack Exit Total PM2.5 OTM - 27/28 3 280 0 R1 299 Min, R2 329 Min, R3 318 Min Stack Exit

Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 280 0 R1 299 Min, R2 329 Min, R3 318 Min Stack Exit

Organic Condensible

Particulate OTM - 27/28 3 280 0 R1 299 Min, R2 329 Min, R3 318 Min Stack Exit

Filterable PM2.5 OTM - 27/28 3 280 0 R1 299 Min, R2 329 Min, R3 318 Min Stack Exit

Nickel Method 29 3 160 0 Stack Exit Manganese Method 29 3 160 0 Stack Exit Filterable Particulate Method 29 3 160 0 Stack Exit Antimony Method 29 3 160 0 Stack Exit Beryllium Method 29 3 160 0 Stack Exit Arsenic Method 29 3 160 0 Stack Exit Cobalt Method 29 3 160 0 Stack Exit Chromium Method 29 3 160 0 Stack Exit Selenium Method 29 3 160 0 Stack Exit Cadmium Method 29 3 160 0 Stack Exit Lead Method 29 3 160 0 Stack Exit O2 Method 3A O2 3 60 0 Stack Exit Co2 Method 3A CO2 3 60 0 Stack Exit Sulfur Dioxide Method 6C 3 60 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



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

### 9/2/2010

The following describes any modifications and/or deviations to the applicable test methods. If alternative methods were requested, see the attachments for documentation of request AND approval, including dates.



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

### 9/2/2010

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 6/28/2010 6/29/2010 6/30/2010
Run Start Time 9:08:00 AM 7:45:00 AM 7:43:00 AM

Run Finish Time 4:32:00 PM 2:51:00 PM 2:51:00 PM

Net Run Time, minutes 416 416 416 Dry Gas Meter Volume Sampled, dscf 299.239 296.408 299.996 298.548 Moisture Content of Stack Gas, % 14.62 13.48 12.03 13.377 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 8.3 9 9.3 8.867 Oxygen, % 14.1 13.5 13.5 13.700 Average Stack Gas Temperature, °F 381.38 380.73 380.42 380.843 Dry Volumetric Flow Rate, dry scfm 743,525.9 743,678.1 756,916.2 748,040.067 Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,424,364.8 1,398,561. 6 1,390,927.6 1,404,618.00 0 Percent Isokinetic of Sampling Rate, % 102.4 101.4 100.8 101.533 F-Factor, dscfm/MMBtu @ %O2
Fw
Fc 2341 2341 2341 2,341.000



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

### 9/2/2010

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 01, 2011 Page 6 of 30

### 9/2/2010

Location Stack Exit - Method 29 Average Run Number
Test Date
Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



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



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

### 9/2/2010

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



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

### 9/2/2010

Location Stack Exit - Method 7E Average Run Number
Test Date
Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



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



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

### 9/2/2010

Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run 1 2 3 Elb/hr 3.27E+00 2.95E+00 2.76E+00 2.993 lb/mmBtuCO2 1.85E-03 1.65E-03 1.54E-03 0.002 ppm 1.01E+00 9.02E-01 8.37E-01 0.916 ppm@7%O2 1.99E+00 1.78E+00 1.65E+00 1.807



### Location: Stack Exit - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.0000000037 0.0000000039 0.0000000056 0.000 Elb/hr 1.22E-09 1.29E-09 1.87E-09 0.000 lb/mmBtuCO2 7.69E-13 7.55E-13 1.04E-12 0.000 ug/dscm 4.37E-07 4.65E-07 6.59E-07 0.000 ug/dscm@7%O2 8.93E-07 8.73E-07 1.24E-06 0.000


### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000022 0.0000000044 0.0000000026 0.000 Elb/hr 7.23E-10 1.46E-09 8.68E-10 0.000 lb/mmBtuCO2 4.57E-13 8.51E-13 4.81E-13 0.000 ug/dscm 2.60E-07 5.24E-07 3.06E-07 0.000 ug/dscm@7%O2 5.31E-07 9.84E-07 5.75E-07 0.000


### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000029 0.0000000025 0.0000000035 0.000 Elb/hr 9.53E-10 8.30E-10 1.17E-09 0.000 lb/mmBtuCO2 6.03E-13 4.84E-13 6.47E-13 0.000 ug/dscm 3.42E-07 2.98E-07 4.12E-07 0.000 ug/dscm@7%O2 6.99E-07 5.60E-07 7.74E-07 0.000


### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000023 0.0000000022 0.0000000031 0.000 Elb/hr 7.56E-10 7.30E-10 1.03E-09 0.000 lb/mmBtuCO2 4.78E-13 4.26E-13 5.73E-13 0.000 ug/dscm 2.71E-07 2.62E-07 3.65E-07 0.000 ug/dscm@7%O2 5.54E-07 4.92E-07 6.86E-07 0.000


### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000022 0.0000000012 0.0000000016 0.000 Elb/hr 7.23E-10 3.98E-10 5.34E-10 0.000



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

### 9/2/2010
lb/mmBtuCO2 4.57E-13 2.32E-13 2.96E-13 0.000 ug/dscm 2.60E-07 1.43E-07 1.88E-07 0.000 ug/dscm@7%O2 5.31E-07 2.69E-07 3.53E-07 0.000


### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000023 0.0000000021 0.000000003 0.000 Elb/hr 7.56E-10 6.97E-10 1.00E-09 0.000 lb/mmBtuCO2 4.78E-13 4.06E-13 5.55E-13 0.000 ug/dscm 2.71E-07 2.50E-07 3.53E-07 0.000 ug/dscm@7%O2 5.54E-07 4.70E-07 6.63E-07 0.000


### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000011 0.0000000011 0.0000000014 0.000 Elb/hr 3.62E-10 3.65E-10 4.67E-10 0.000 lb/mmBtuCO2 2.29E-13 2.13E-13 2.59E-13 0.000 ug/dscm 1.30E-07 1.31E-07 1.65E-07 0.000 ug/dscm@7%O2 2.66E-07 2.46E-07 3.10E-07 0.000


### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000023 0.0000000022 0.000000003 0.000 Elb/hr 7.56E-10 7.30E-10 1.00E-09 0.000 lb/mmBtuCO2 4.78E-13 4.26E-13 5.55E-13 0.000 ug/dscm 2.71E-07 2.62E-07 3.53E-07 0.000 ug/dscm@7%O2 5.54E-07 4.92E-07 6.63E-07 0.000


### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000014 0.0000000013 0.0000000017 0.000 Elb/hr 4.60E-10 4.31E-10 5.67E-10 0.000 lb/mmBtuCO2 2.91E-13 2.52E-13 3.14E-13 0.000 ug/dscm 1.65E-07 1.55E-07 2.00E-07 0.000 ug/dscm@7%O2 3.37E-07 2.91E-07 3.76E-07 0.000


### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.0000000024 0.0000000021 0.0000000027 0.000 Elb/hr 7.89E-10 6.97E-10 9.01E-10 0.000 lb/mmBtuCO2 4.99E-13 4.06E-13 4.99E-13 0.000 ug/dscm 2.83E-07 2.50E-07 3.18E-07 0.000 ug/dscm@7%O2 5.78E-07 4.70E-07 5.97E-07 0.000


### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000018 0.0000000018 0.0000000023 0.000 Elb/hr 5.92E-10 5.97E-10 7.68E-10 0.000



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

### 9/2/2010
lb/mmBtuCO2 3.74E-13 3.48E-13 4.25E-13 0.000 ug/dscm 2.12E-07 2.14E-07 2.71E-07 0.000 ug/dscm@7%O2 4.33E-07 4.02E-07 5.09E-07 0.000


### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 2 3 Mass_mg 0.0000000109 0.0000000111 0.0000000154 0.000 Elb/hr 3.58E-09 3.68E-09 5.14E-09 0.000 lb/mmBtuCO2 2.26E-12 2.15E-12 2.85E-12 0.000 ug/dscm 1.29E-06 1.32E-06 1.81E-06 0.000 ug/dscm@7%O2 2.64E-06 2.48E-06 3.40E-06 0.000


### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 2 3 Mass_mg 0.00000007 0.000000054 0.00000033 0.000 Elb/hr 2.30E-08 1.79E-08 1.10E-07 0.000 lb/mmBtuCO2 1.45E-11 1.04E-11 6.10E-11 0.000 ug/dscm 8.26E-06 6.43E-06 3.89E-05 0.000 ug/dscm@7%O2 1.69E-05 1.21E-05 7.31E-05 0.000


### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 2 3 Mass_mg 0.00000015 0.000000131 0.00000092 0.000 Elb/hr 4.93E-08 4.35E-08 3.07E-07 0.000 lb/mmBtuCO2 3.12E-11 2.53E-11 1.70E-10 0.000 ug/dscm 1.77E-05 1.56E-05 1.08E-04 0.000 ug/dscm@7%O2 3.62E-05 2.93E-05 2.03E-04 0.000


### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 2 3 Mass_mg 0.000000014 0.000000015 0.0000000579 0.000 Elb/hr 4.60E-09 4.98E-09 1.93E-08 0.000 lb/mmBtuCO2 2.91E-12 2.90E-12 1.07E-11 0.000 ug/dscm 1.65E-06 1.79E-06 6.82E-06 0.000 ug/dscm@7%O2 3.37E-06 3.36E-06 1.28E-05 0.000


### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 2 3 Mass_mg 0.0000000114 0.0000000109 0.0000000469 0.000 Elb/hr 3.75E-09 3.62E-09 1.57E-08 0.000 lb/mmBtuCO2 2.37E-12 2.11E-12 8.68E-12 0.000 ug/dscm 1.35E-06 1.30E-06 5.52E-06 0.000 ug/dscm@7%O2 2.76E-06 2.44E-06 1.04E-05 0.000


### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 2 3 Mass_mg 0.000000364 0.000000288 0.00000191 0.000 Elb/hr 1.20E-07 9.56E-08 6.37E-07 0.000



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

### 9/2/2010
lb/mmBtuCO2 7.56E-11 5.57E-11 3.53E-10 0.000 ug/dscm 4.30E-05 3.43E-05 2.25E-04 0.000 ug/dscm@7%O2 8.79E-05 6.44E-05 4.23E-04 0.000


### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 2 3 Mass_mg 0.0000000129 0.0000000121 0.0000000314 0.000 Elb/hr 4.24E-09 4.02E-09 1.05E-08 0.000 lb/mmBtuCO2 2.68E-12 2.34E-12 5.81E-12 0.000 ug/dscm 1.52E-06 1.44E-06 3.70E-06 0.000 ug/dscm@7%O2 3.11E-06 2.70E-06 6.95E-06 0.000


### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000012 0.0000000011 0.0000000015 0.000 Elb/hr 3.94E-10 3.65E-10 5.01E-10 0.000 lb/mmBtuCO2 2.49E-13 2.13E-13 2.77E-13 0.000 ug/dscm 1.42E-07 1.31E-07 1.77E-07 0.000 ug/dscm@7%O2 2.90E-07 2.46E-07 3.32E-07 0.000


### Compound: 2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.000000002 0.0000000018 0.0000000023 0.000 Elb/hr 6.57E-10 5.97E-10 7.68E-10 0.000 lb/mmBtuCO2 4.16E-13 3.48E-13 4.25E-13 0.000 ug/dscm 2.36E-07 2.14E-07 2.71E-07 0.000 ug/dscm@7%O2 4.82E-07 4.02E-07 5.09E-07 0.000


### Compound: 2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000045 0.0000000052 0.000000006 0.000 Elb/hr 1.48E-09 1.73E-09 2.00E-09 0.000 lb/mmBtuCO2 9.35E-13 1.01E-12 1.11E-12 0.000 ug/dscm 5.31E-07 6.20E-07 7.06E-07 0.000 ug/dscm@7%O2 1.09E-06 1.16E-06 1.33E-06 0.000


### Compound: 2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.0000000094 0.0000000031 0.0000000036 0.000 Elb/hr 3.09E-09 1.03E-09 1.20E-09 0.000 lb/mmBtuCO2 1.95E-12 6.00E-13 6.66E-13 0.000 ug/dscm 1.11E-06 3.69E-07 4.24E-07 0.000 ug/dscm@7%O2 2.27E-06 6.93E-07 7.96E-07 0.000


### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 2 3 Mass_mg 0.000000075 0.0000000173 0.000000025 0.000 Elb/hr 2.47E-08 5.74E-09 8.34E-09 0.000



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

### 9/2/2010
lb/mmBtuCO2 1.56E-11 3.35E-12 4.62E-12 0.000 ug/dscm 8.85E-06 2.06E-06 2.94E-06 0.000 ug/dscm@7%O2 1.81E-05 3.87E-06 5.52E-06 0.000


### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 2 3 Mass_mg 0.000000013 0.0000000125 0.0000000206 0.000 Elb/hr 4.27E-09 4.15E-09 6.88E-09 0.000 lb/mmBtuCO2 2.70E-12 2.42E-12 3.81E-12 0.000 ug/dscm 1.53E-06 1.49E-06 2.43E-06 0.000 ug/dscm@7%O2 3.13E-06 2.80E-06 4.56E-06 0.000


### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 1 2 3 Mass_mg 0.000000068 0.0000000283 0.000000122 0.000 Elb/hr 2.23E-08 9.39E-09 4.07E-08 0.000 lb/mmBtuCO2 1.41E-11 5.48E-12 2.26E-11 0.000 ug/dscm 8.03E-06 3.37E-06 1.44E-05 0.000 ug/dscm@7%O2 1.64E-05 6.33E-06 2.70E-05 0.000


### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber 1 2 3 Mass_mg 0.0000000203 0.0000000165 0.0000000264 0.000 Elb/hr 6.67E-09 5.48E-09 8.81E-09 0.000 lb/mmBtuCO2 4.22E-12 3.19E-12 4.88E-12 0.000 ug/dscm 2.40E-06 1.97E-06 3.11E-06 0.000 ug/dscm@7%O2 4.91E-06 3.70E-06 5.84E-06 0.000


### Compound: OCDD Average RunNumber 1 2 3 Mass_mg 0.000000008 0.0000000078 0.000000015 0.000 Elb/hr 2.63E-09 2.59E-09 5.01E-09 0.000 lb/mmBtuCO2 1.66E-12 1.51E-12 2.77E-12 0.000 ug/dscm 9.44E-07 9.29E-07 1.77E-06 0.000 ug/dscm@7%O2 1.93E-06 1.75E-06 3.32E-06 0.000


### Compound: OCDF Average RunNumber 1 2 3 Mass_mg 0.0000000042 0.0000000057 0.0000000048 0.000 Elb/hr 1.38E-09 1.89E-09 1.60E-09 0.000 lb/mmBtuCO2 8.73E-13 1.10E-12 8.88E-13 0.000 ug/dscm 4.96E-07 6.79E-07 5.65E-07 0.000 ug/dscm@7%O2 1.01E-06 1.28E-06 1.06E-06 0.000



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average Run 1 2 3



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

### 9/2/2010
Elb/hr 5.86E-01 4.42E-01 1.40E+00 0.809 lb/mmBtuCO2 3.32E-04 2.48E-04 7.85E-04 0.000 ppm 1.15E-01 8.59E-02 2.71E-01 0.157 ppm@7%O2 2.26E-01 1.70E-01 5.34E-01 0.310



### Location: Stack Exit - Method 26A 

### Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 0.51 0.52 0.43 0.487 Elb/hr 5.20E-01 5.30E-01 4.44E-01 0.498 lb/mmBtuCO2 2.94E-04 3.08E-04 2.49E-04 0.000 mg/dscm 1.88E-01 1.95E-01 1.57E-01 0.180 mg/dscm@7%O2 3.71E-01 3.86E-01 3.10E-01 0.356


### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 0.31 0.31 0.26 0.293 Elb/hr 3.16E-01 3.16E-01 2.68E-01 0.300 lb/mmBtuCO2 1.79E-04 1.83E-04 1.50E-04 0.000 mg/dscm 1.14E-01 1.16E-01 9.48E-02 0.108 mg/dscm@7%O2 2.25E-01 2.29E-01 1.87E-01 0.214



### Location: Stack Exit - Method 29 Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.00003 0 0.00021 0.000 Elb/hr 2.31E-05 0.00E+00 1.65E-04 0.000 gr/dscf 3.57E-09 0.00E+00 2.51E-08 0.000 gr/dscf@7%O2 6.94E-09 0.00E+00 4.91E-08 0.000 lb/mmBtuCO2 1.32E-08 0.00E+00 9.21E-08 0.000 ug/dscm 8.16E-03 0.00E+00 5.74E-02 0.022 ug/dscm@7%O2 1.59E-02 0.00E+00 1.12E-01 0.043


### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.00045 0.00089 0.00119 0.001 Elb/hr 3.47E-04 6.97E-04 9.34E-04 0.001 gr/dscf 5.35E-08 1.08E-07 1.42E-07 0.000 gr/dscf@7%O2 1.04E-07 2.09E-07 2.78E-07 0.000 lb/mmBtuCO2 1.98E-07 3.96E-07 5.22E-07 0.000 ug/dscm 1.22E-01 2.48E-01 3.25E-01 0.232 ug/dscm@7%O2 2.37E-01 4.79E-01 6.36E-01 0.451


### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.00001 0.000017 0.000014 0.000 Elb/hr 7.70E-06 1.33E-05 1.10E-05 0.000 gr/dscf 1.19E-09 2.07E-09 1.67E-09 0.000



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

### 9/2/2010 gr/dscf@7%O2 2.31E-09 4.00E-09 3.27E-09 0.000 lb/mmBtuCO2 4.39E-09 7.56E-09 6.14E-09 0.000 ug/dscm 2.72E-03 4.74E-03 3.82E-03 0.004 ug/dscm@7%O2 5.29E-03 9.15E-03 7.48E-03 0.007


### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.0001 0.00011 0.00002 0.000 Elb/hr 7.70E-05 8.62E-05 1.57E-05 0.000 gr/dscf 1.19E-08 1.34E-08 2.39E-09 0.000 gr/dscf@7%O2 2.31E-08 2.59E-08 4.68E-09 0.000 lb/mmBtuCO2 4.39E-08 4.89E-08 8.77E-09 0.000 ug/dscm 2.72E-02 3.07E-02 5.46E-03 0.021 ug/dscm@7%O2 5.29E-02 5.93E-02 1.07E-02 0.041


### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.0037 0.0041 0.0043 0.004 Elb/hr 2.85E-03 3.21E-03 3.38E-03 0.003 gr/dscf 4.40E-07 4.99E-07 5.13E-07 0.000 gr/dscf@7%O2 8.55E-07 9.63E-07 1.00E-06 0.000 lb/mmBtuCO2 1.63E-06 1.82E-06 1.89E-06 0.000 ug/dscm 1.01E+00 1.14E+00 1.17E+00 1.107 ug/dscm@7%O2 1.96E+00 2.20E+00 2.29E+00 2.150


### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.00115 0.00002 0.00006 0.000 Elb/hr 8.86E-04 1.57E-05 4.71E-05 0.000 gr/dscf 1.37E-07 2.43E-09 7.16E-09 0.000 gr/dscf@7%O2 2.66E-07 4.69E-09 1.40E-08 0.000 lb/mmBtuCO2 5.05E-07 8.90E-09 2.63E-08 0.000 ug/dscm 3.13E-01 5.57E-03 1.64E-02 0.112 ug/dscm@7%O2 6.08E-01 1.08E-02 3.21E-02 0.217


### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 42.7 40.8 52.4 45.300 Elb/hr 3.29E+01 3.20E+01 4.11E+01 35.333 gr/dscf 5.08E-03 4.97E-03 6.26E-03 0.005 gr/dscf@7%O2 9.88E-03 9.59E-03 1.23E-02 0.011 lb/mmBtuCO2 1.88E-02 1.82E-02 2.30E-02 0.020 ug/dscm 1.16E+04 1.14E+04 1.43E+04 12,433.333 ug/dscm@7%O2 2.26E+04 2.20E+04 2.80E+04 24,200.000


### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.0005 0.0003 0.0008 0.001 Elb/hr 3.85E-04 2.35E-04 6.28E-04 0.000



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

### 9/2/2010 gr/dscf 5.94E-08 3.65E-08 9.55E-08 0.000 gr/dscf@7%O2 1.15E-07 7.05E-08 1.87E-07 0.000 lb/mmBtuCO2 2.20E-07 1.33E-07 3.51E-07 0.000 ug/dscm 1.36E-01 8.36E-02 2.19E-01 0.146 ug/dscm@7%O2 2.64E-01 1.61E-01 4.29E-01 0.285


### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.0038 0.0032 0.0034 0.003 Elb/hr 2.93E-03 2.51E-03 2.67E-03 0.003 gr/dscf 4.52E-07 3.90E-07 4.06E-07 0.000 gr/dscf@7%O2 8.79E-07 7.53E-07 7.95E-07 0.000 lb/mmBtuCO2 1.67E-06 1.42E-06 1.49E-06 0.000 ug/dscm 1.03E+00 8.92E-01 9.29E-01 0.950 ug/dscm@7%O2 2.00E+00 1.72E+00 1.82E+00 1.847


### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 0.00368 0.00328 0.0027 0.003 Elb/hr 2.84E-03 2.57E-03 2.12E-03 0.003 gr/dscf 4.38E-07 3.99E-07 3.22E-07 0.000 gr/dscf@7%O2 8.51E-07 7.70E-07 6.30E-07 0.000 lb/mmBtuCO2 1.62E-06 1.46E-06 1.18E-06 0.000 ug/dscm 1.00E+00 9.14E-01 7.38E-01 0.884 ug/dscm@7%O2 1.94E+00 1.76E+00 1.44E+00 1.713


### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 0.0305 0.0402 0.02859 0.033 Elb/hr 2.35E-02 3.15E-02 2.24E-02 0.026 gr/dscf 3.63E-06 4.89E-06 3.41E-06 0.000 gr/dscf@7%O2 7.06E-06 9.44E-06 6.68E-06 0.000 lb/mmBtuCO2 1.34E-05 1.79E-05 1.25E-05 0.000 ug/dscm 8.30E+00 1.12E+01 7.81E+00 9.103 ug/dscm@7%O2 1.61E+01 2.16E+01 1.53E+01 17.667



### Location: Stack Exit - Method 6C 

### Compound: Sulfur Dioxide Average Run 1 2 3 Elb/hr 1.81E+02 1.63E+02 1.61E+02 168.333 lb/mmBtuCO2 1.02E-01 9.40E-02 9.13E-02 0.096 ppm 2.46E+01 2.24E+01 2.16E+01 22.867 ppm@7%O2 4.85E+01 4.43E+01 4.27E+01 45.167



### Location: Stack Exit - Method 7E 

### Compound: Nitrogen oxides (NOx) Average Run 1 2 3 Elb/hr 1.22E+02 1.27E+02 1.27E+02 125.333



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

### 9/2/2010

Process Run Data lb/mmBtuCO2 6.90E-02 7.35E-02 7.18E-02 0.071 ppm 2.31E+01 2.44E+01 2.37E+01 23.733 ppm@7%O2 4.55E+01 4.82E+01 4.69E+01 46.867



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

### Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 9.8 11.2 9 10.000 Elb/hr 8.47E+00 9.21E+00 7.46E+00 8.380 gr/dscf 1.32E-03 1.37E-03 1.16E-03 0.001 gr/dscf@7%O2 2.57E-03 2.64E-03 2.27E-03 0.002 lb/mmBtuCO2 4.86E-03 5.02E-03 4.25E-03 0.005


### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 13.4 15.3 5.7 11.467 Elb/hr 1.16E+01 1.26E+01 4.73E+00 9.643 gr/dscf 1.80E-03 1.88E-03 7.33E-04 0.001 gr/dscf@7%O2 3.50E-03 3.63E-03 1.44E-03 0.003 lb/mmBtuCO2 6.65E-03 6.85E-03 2.69E-03 0.005


### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 17.2 19.5 16.6 17.767 Elb/hr 1.49E+01 1.60E+01 1.38E+01 14.900 gr/dscf 2.31E-03 2.39E-03 2.13E-03 0.002 gr/dscf@7%O2 4.49E-03 4.61E-03 4.17E-03 0.004 lb/mmBtuCO2 8.54E-03 8.73E-03 7.84E-03 0.008


### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 38.4 44 29.3 37.233 Elb/hr 3.32E+01 3.62E+01 2.43E+01 31.233 gr/dscf 5.16E-03 5.39E-03 3.77E-03 0.005 gr/dscf@7%O2 1.00E-02 1.04E-02 7.38E-03 0.009 lb/mmBtuCO2 1.91E-02 1.97E-02 1.38E-02 0.018



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

### 9/2/2010

Process Run Data

APCD Run Data 

### Run Name Value UOM Comments Target Value 1 Heat Input 1772 Million Btus/hr Run 1 PM/Metals 0


### 2 Heat Input 0 Million Btus/hr 0
3 Heat Input 0 Million Btus/hr 0
4 Heat Input 1753.9 Million Btus/hr Run 2 PM/Metals 0


### 1 Unit Gross Electrical Output 166 MW Run 1 PM/Metals 0
4 Unit Gross Electrical Output 165 MW Run 2 PM/Metals 0
5 Heat Input 1724.6 Million Btus/hr Run 3 PM/Metals 0


### 5 Unit Gross Electrical Output 160 MW Run 3 PM/Metals 0

6 Heat Input 1828.1 Million Btus/hr Run 1 Acid Gases 0

6 Unit Gross Electrical Output 164 MW Run 1 Acid Gases 0


### 7 Heat Input 1801.8 Million Btus/hr Run 2 Acid Gases 0
7 Unit Gross Electrical Output 164 MW Run 2 Acid Gases 0
8 Heat Input 1922.7 Million Btus/hr Run 3 Acid Gases 0


### 8 Unit Gross Electrical Output 164 MW Run 3 Acid Gases 0
9 Heat Input 1737.7 Million Btus/hr Run 1 Non-Dioxin Organics 0



### 9 Unit Gross Electrical Output 163 MW Run 1 Non-Dioxin Organics 0

10 Heat Input 1725.9 Million Btus/hr Run 2 Non-Dioxin Organics 0



### 10 Unit Gross Electrical Output 164 MW Run 2 Non-Dioxin Organics 0

11 Heat Input 1780.8 Million Btus/hr Run 3 Non-Dioxin Organics 0



### 11 Unit Gross Electrical Output 163 MW Run 3 Non-Dioxin Organics 0

12 Heat Input 1718.5 Million Btus/hr Run 1 Dioxin Organics 0



### 12 Unit Gross Electrical Output 167 MW Run 1 Dioxin Organics 0

13 Heat Input 1784.6 Million Btus/hr Run 2 Dioxin Organics 0



### 13 Unit Gross Electrical Output 168 MW Run 2 Dioxin Organics 0

14 Heat Input 1706.6 Million Btus/hr Run 3 Dioxin Organics 0

14 Unit Gross Electrical Output 168 MW Run 3 Dioxin Organics 0



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

### 9/2/2010

APCD Run Data

Process Lab Run Data 

### 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 Ultimate/Proximate Analysis 0 

### 1 Fuel Chlorine Content 0 mg/kg 1 Fuel Fluorine Content 0 mg/kg 1 Metals Content 0 mg/kg



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

### 9/2/2010

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 01, 2011 Page 21 of 30

### 9/2/2010

Location Stack Exit - Method 23 Average Run Number 1 2 3 Test Date 6/28/2010 6/29/2010 6/30/2010 Run Start Time 9:08:00 AM 7:45:00 AM 7:43:00 AM Run Finish Time 4:32:00 PM 2:51:00 PM 2:51:00 PM Net Traversing Points 64 64 64 Net Run Time, minutes 416 416 416 Nozzle Diameter, inches 0.21 0.21 0.21 0.210 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.016 1.016 1.016 1.016 Barometric Pressure, inches of Mercury 29.22 29.35 29.52 29.363 Average Orifice Meter Differential, inches H2O 1.82 1.78 1.77 1.790 Dry Gas Meter Volume Sampled, cubic feet 315.940 311.254 305.278 310.824 Average Dry Gas Meter Temperature, °F 95.67 95.05 80.97 90.563 Dry Gas Meter Volume Sampled, dscf 299.239 296.408 299.996 298.548 Total Moisture Liquid collected, g 1088.1 981.5 871.5 980.367 Volume of Water Vapor, standard cubic feet 51.22 46.20 41.02 46.147 Moisture Content of Stack Gas, % 14.62 13.48 12.03 13.377 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8538 0.8652 0.8797 0.866 Carbon Dioxide, % 8.3 9 9.3 8.867 Oxygen, % 14.1 13.5 13.5 13.700 Carbon Monoxide & Nitrogen, % 77.6 77.5 77.2 77.433 Fuel Factor 0.82 0.82 0.80 Dry Molecular Weight, lb/lb-Mole 29.89 29.98 30.03 29.967 Wet Molecular weight, lb/lb-Mole 28.15 28.37 28.58 28.367 Flue Gas Static Pressure, inches of H2O -0.97 -0.89 -0.76 -0.873 Absolute Flue Gas Pressure, inches of Mercury 29.15 29.28 29.46 29.297 Average Stack Gas Temperature, °F 381.38 380.73 380.42 380.843 Average Velocity Head, inches of H2O 1.6459382121 7781 1.607547958

94231 1.612445120

10911 1.622

Average Stack Gas Velocity, feet/second 93.29 91.60 91.10 91.997 Stack Cross-Sectional Area, square feet 254.469 254.469 254.469 254.469 Dry Volumetric Flow Rate, dry scfm 743,525.9 743,678.1 756,916.2 748,040.067 Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,424,364.8 1,398,561.6 1,390,927.6 1,404,618.0 00 Percent Isokinetic of Sampling Rate, % 102.4 101.4 100.8 101.533 Percent Excess Air, % 220.8 194.0 196.2 203.667 F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches 216 216 216 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw Fc 2341 2341 2341 2,341.000



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

### 9/2/2010

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 01, 2011 Page 23 of 30

### 9/2/2010

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 01, 2011 Page 24 of 30

### 9/2/2010

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 01, 2011 Page 25 of 30

### 9/2/2010

Location Stack Exit - Method 3A CO2 Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



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

### 9/2/2010

Location Stack Exit - Method 3A O2 Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



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

### 9/2/2010

Location Stack Exit - Method 6C Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



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

### 9/2/2010

Location Stack Exit - Method 7E Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



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

### 9/2/2010

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 01, 2011 Page 30 of 30