### 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 15

### Facility Information:

Harding Street 3700 S. Harding Street

Indianapolis IN46217 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: 60 60 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 !!!!UPDATE NEEDED!!! Industry/SCC/NAIS221112

Sampling Location Information:

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

SCC / Description10100212 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous Coal - Pulverized Coal: Dry Bottom (Tangential) (Bituminous Coal)

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 116 232 928 4 0 3 0 0

Target Parameter Test Method Number of

Test RunsTest Run

DurationSample

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 151,2,3,7,8,9-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 15

### 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 15

### Sampling / Stack Data Results Summary



### LocationStack Exit - Method 29 Average Run Number 1 2 3 Test Date 3/13/2010 3/13/2010 3/14/2010 Run Start Time 9:05:00 AM4:10:00 PM9:00:00 AM Run Finish Time 3:19:00 PM 10:26:00 PM3:15:00 PM

Net Run Time, minutes 360 360 360 Dry Gas Meter Volume Sampled, dscf 273.193 265.504 263.965 267.554 Moisture Content of Stack Gas, % 9.07 9.28 9.20 9.183 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 11.6 11.1 11.3 11.333 Oxygen, % 6.2 6.9 6.7 6.600 Average Stack Gas Temperature, °F 342.01 341.96 340.04 341.337 Dry Volumetric Flow Rate, dry scfm 262,261.1 255,435.1 259,395.0259,030.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 434,181.2 423,833.0 442,327.6433,447.267 Percent Isokinetic of Sampling Rate, % 102.4 102.2 100.0 101.533 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000



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

### LocationStack 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 6 of 15

### Emissions Summary



### Location: Stack Exit - Method 29 Compound:Antimony Average RunNumber 1 2 3 Mass_mg 0.0082 0.0081 0.0089 0.008 Elb/hr 1.04E-03 1.03E-03 1.16E-03 0.001 lb/mmBtuO2 9.20E-07 9.82E-07 1.07E-06 0.000 mg/dscm 1.06E-03 1.08E-03 1.19E-03 0.001 mg/dscm@7%O2 1.00E-03 1.07E-03 1.16E-03 0.001 

### Compound:Arsenic Average RunNumber 1 2 3 Mass_mg 0.0919 0.1368 0.1217 0.117 Elb/hr 1.17E-02 1.74E-02 1.58E-02 0.015 lb/mmBtuO2 1.03E-05 1.66E-05 1.46E-05 0.000 mg/dscm 1.19E-02 1.82E-02 1.63E-02 0.015 mg/dscm@7%O2 1.13E-02 1.81E-02 1.60E-02 0.015 

### Compound:Beryllium Average RunNumber 1 2 3 Mass_mg 0.0053 0.0054 0.006 0.006 Elb/hr 6.73E-04 6.87E-04 7.80E-04 0.001 lb/mmBtuO2 5.95E-07 6.55E-07 7.21E-07 0.000 mg/dscm 6.85E-04 7.18E-04 8.03E-04 0.001 mg/dscm@7%O2 6.48E-04 7.13E-04 7.86E-04 0.001 

### Compound:Cadmium Average RunNumber 1 2 3 Mass_mg 0.0031 0.0028 0.0035 0.003 Elb/hr 3.94E-04 3.56E-04 4.55E-04 0.000 lb/mmBtuO2 3.48E-07 3.39E-07 4.21E-07 0.000 mg/dscm 4.01E-04 3.72E-04 4.68E-04 0.000 mg/dscm@7%O2 3.79E-04 3.69E-04 4.58E-04 0.000 

### Compound:Chromium Average RunNumber 1 2 3 Mass_mg 0.0219 0.0186 0.031 0.024 Elb/hr 2.78E-03 2.37E-03 4.03E-03 0.003 lb/mmBtuO2 2.46E-06 2.25E-06 3.73E-06 0.000 mg/dscm 2.83E-03 2.47E-03 4.15E-03 0.003 mg/dscm@7%O2 2.68E-03 2.45E-03 4.06E-03 0.003 

### Compound:Cobalt Average RunNumber 1 2 3 Mass_mg 0.01 0.0101 0.0112 0.010 Elb/hr 1.27E-03 1.29E-03 1.46E-03 0.001



### Tuesday, February 15, 2011 Page 7 of 15lb/mmBtuO2 1.12E-06 1.22E-06 1.35E-06 0.000 mg/dscm 1.29E-03 1.34E-03 1.50E-03 0.001 mg/dscm@7%O2 1.22E-03 1.33E-03 1.47E-03 0.001 

### Compound:Filterable Particulate Average RunNumber 1 2 3 Mass_mg 93.8 93.2 156.8 114.600 Elb/hr 1.19E+01 1.19E+01 2.04E+01 14.733 lb/mmBtuO2 1.05E-02 1.13E-02 1.89E-02 0.014 mg/dscm 1.21E+01 1.24E+01 2.10E+01 15.167 mg/dscm@7%O2 1.14E+01 1.23E+01 2.06E+01 14.767 

### Compound:Lead Average RunNumber 1 2 3 Mass_mg 0.0543 0.0597 0.0614 0.058 Elb/hr 6.90E-03 7.60E-03 7.98E-03 0.007 lb/mmBtuO2 6.09E-06 7.24E-06 7.38E-06 0.000 mg/dscm 7.02E-03 7.94E-03 8.22E-03 0.008 mg/dscm@7%O2 6.64E-03 7.88E-03 8.05E-03 0.008 

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

### Compound:Manganese Average RunNumber 1 2 3 Mass_mg 0.0193 0.0203 0.0228 0.021 Elb/hr 2.45E-03 2.58E-03 2.96E-03 0.003 lb/mmBtuO2 2.17E-06 2.46E-06 2.74E-06 0.000 mg/dscm 2.50E-03 2.70E-03 3.05E-03 0.003 mg/dscm@7%O2 2.36E-03 2.68E-03 2.99E-03 0.003 

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

### Compound:Nickel Average RunNumber 1 2 3 Mass_mg 0.053 0.05 0.0585 0.054 Elb/hr 6.73E-03 6.36E-03 7.60E-03 0.007 

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

### Process Run Data lb/mmBtuO2 5.95E-06 6.06E-06 7.03E-06 0.000 mg/dscm 6.85E-03 6.65E-03 7.83E-03 0.007 mg/dscm@7%O2 6.48E-03 6.60E-03 7.66E-03 0.007 

### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 1.1764 0.8553 0.9822 1.005 Elb/hr 1.49E-01 1.09E-01 1.28E-01 0.129 lb/mmBtuO2 1.32E-04 1.04E-04 1.18E-04 0.000 mg/dscm 1.52E-01 1.14E-01 1.31E-01 0.132 mg/dscm@7%O2 1.44E-01 1.13E-01 1.28E-01 0.128



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

### Compound:Filterable Particulate Average RunNumber 1 2 3 Mass_mg 85.8 100.5 75.3 87.200 lb/mmBtuO2 1.95E-02 2.32E-02 1.73E-02 0.020 

### Compound:Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 37.3 47.1 42.8 42.400 lb/mmBtuO2 8.46E-03 1.09E-02 9.83E-03 0.010 

### Compound:Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 43.1 161 125 109.700 lb/mmBtuO2 9.78E-03 3.71E-02 2.87E-02 0.025 

### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 101 72.4 38.7 70.700 lb/mmBtuO2 2.29E-02 1.67E-02 8.89E-03 0.016 

### Compound:Total Particulate Average RunNumber 1 2 3 Mass_mg 229.9 333.9 239 267.600 lb/mmBtuO2 5.22E-02 7.70E-02 5.49E-02 0.061 

### Compound:Total PM2.5 Average RunNumber 1 2 3 Mass_mg 181.4 280.5 206.5 222.800 lb/mmBtuO2 4.12E-02 6.46E-02 4.74E-02 0.051



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

### Process Run Data



### Run Name Value UOM Comments Target Value 1 Bituminous Coal Burned 0 Tons/hr 0 

### 2 Bituminous Coal Burned 0 Tons/hr 0 3 Bituminous Coal Burned 0 Tons/hr 0 4 Bituminous Coal Burned 0 Tons/hr 0 

### 5 Bituminous Coal Burned 0 Tons/hr 0 6 Bituminous Coal Burned 0 Tons/hr 0 1 Average Heat Input 936.76MMBtu/hr 0 

### 2 Average Heat Input 947.33MMBtu/hr 0 3 Average Heat Input 970.11MMBtu/hr 0 4 Average Heat Input 1063.4MMBtu/hr 0 

### 5 Average Heat Input 783.04MMBtu/hr 0 6 Average Heat Input 1072.6MMBtu/hr 0 1 Steam Output 755.851000 lb steam/hr 0 

### 2 Steam Output 753.21000 lb steam/hr 0 3 Steam Output 762.431000 lb steam/hr 0 4 Steam Output 804.21000 lb steam/hr 0 

### 5 Steam Output 578.511000 lb steam/hr 0 6 Steam Output 751.821000 lb steam/hr 0 1 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 

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

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

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



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

### 4 Coal Gas Firing Rate 0 0



### 5 Coal Gas Firing Rate 0 0 6 Coal Gas Firing Rate 0 0 1 Fuel Oil Firing Rate 0 0 

### 2Fuel 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 1 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 

### 1 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 1 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 

### 1 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 1 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

1 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 1 Flue Gas Carbon Dioxide Content 0 % 0



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

### APCD Run Data

4 Flue Gas Carbon Dioxide Content 0 % 0 

### 5 Flue Gas Carbon Dioxide Content 0 % 0 6 Flue Gas Carbon Dioxide Content 0 % 0 1 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 

### 1 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 1 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 1 Standard Pressure 0 atm 0 

### 4 Standard Pressure 0 atm 0 5 Standard Pressure 0 atm 0 6 Standard Pressure 0 atm 0 

### 1 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 1 Unit Gross Electrical Output 103.63 MW 0 

### 4 Unit Gross Electrical Output 109.89 MW 0 5 Unit Gross Electrical Output 79.97 MW 0 6 Unit Gross Electrical Output 103.4 MW 0 

### 1 Unit Net Electric Generation 98.61 MWh 0 4 Unit Net Electric Generation 104.68 MWh 0 5 Unit Net Electric Generation 75.41 MWh 0 

### 6 Unit Net Electric Generation 98.35 MWh 0

Run Name Value UOM Comments Target Value 1 LOW NOX BURNERS 0 0 1 OVERFIRE AIR 0 0



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

### Process Lab Run Data

1 SELECTIVE NONCATALYTIC REDUCTION FOR NOX 0 0



### 1 ELECTROSTATIC PRECIPITATOR 0 0

Run Name ValueUOM 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 1 Fuel Manganese Content 0 ppm 1 Fuel Chlorine Content 0 ppm 

### 1 Fuel Fluorine Content 0 ppm

Tuesday, February 15, 2011 Page 13 of 15

### Sampling / Stack Data Results Detail



### LocationStack Exit - Method 29 Average Run Number 1 2 3 Test Date 3/13/2010 3/13/2010 3/14/2010 Run Start Time 9:05:00 AM4:10:00 PM9:00:00 AM Run Finish Time 3:19:00 PM10:26:00 PM3:15:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 360 360 360 Nozzle Diameter, inches 0.195 0.195 0.195 0.195 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9925 0.9925 0.9925 0.993 Barometric Pressure, inches of Mercury 29.67 29.67 28.77 29.370 Average Orifice Meter Differential, inches H2O 1.98 1.87 1.99 1.947 Dry Gas Meter Volume Sampled, cubic feet 272.481 265.255 269.510 269.082 Average Dry Gas Meter Temperature, °F 60.85 61.58 57.10 59.843 Dry Gas Meter Volume Sampled, dscf 273.193 265.504 263.965 267.554 Total Moisture Liquid collected, g 578.8 576.9 567.9 574.533 Volume of Water Vapor, standard cubic feet 27.24 27.15 26.73 27.040 Moisture Content of Stack Gas, % 9.07 9.28 9.20 9.183 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9093 0.9072 0.908 0.908 Carbon Dioxide, % 11.6 11.1 11.3 11.333 Oxygen, % 6.2 6.9 6.7 6.600 Carbon Monoxide & Nitrogen, % 82.2 82 82 82.067 Fuel Factor 1.27 1.26 1.26 Dry Molecular Weight, lb/lb-Mole 30.10 30.05 30.08 30.077 Wet Molecular weight, lb/lb-Mole 29.00 28.93 28.97 28.967 Flue Gas Static Pressure, inches of H2O 7.1 7.1 7 7.067 Absolute Flue Gas Pressure, inches of Mercury 30.19 30.19 29.28 29.887 Average Stack Gas Temperature, °F 342.01 341.96 340.04 341.337 Average Velocity Head, inches of H2O 2.0580368800 23851.956386724

390422.074705522

24057 2.030 Average Stack Gas Velocity, feet/second 98.60 96.25 100.45 98.433 Stack Cross-Sectional Area, square feet 73.391 73.391 73.391 73.391 Dry Volumetric Flow Rate, dry scfm 262,261.1 255,435.1 259,395.0259,030.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 434,181.2 423,833.0 442,327.6433,447.267 Percent Isokinetic of Sampling Rate, % 102.4 102.2 100.0 101.533 Percent Excess Air, % 40.0 46.8 44.8 43.867 F-Factor, dscfm/MMBtu @ %O2 9780 9780 97809,780.000 Round Duct Diameter, inches 116 116 116 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10640 10640 1064010,640.000 Fc 1800 1800 18001,800.000



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

### LocationStack 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 15 of 15