### Name:

Title: Company: Sign Date: Name: Title: Company: Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date 

## 1241 La Cygne 2 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 36

### 1241 La Cygne 2

Facility Information: 1241 La Cygne Generating Station
25166 East 2200 Road

La Cygne KS 66040 Contact: Theresa Goin Phone: (913)757-4451 x5436 Fax: Email: Theresa.Goin@kcpl.com Testing Company: Civil & Environmental Consultants, Inc.
4848 Park 370 Blvd.

Hazelwood MO 63042 Contact: Franklin M. Stevens Phone: (314)656-4566 Fax: (314)656-4595 Email: fstevens@cecinc.com

Air Permit Number: 1241 Permitted Source ID/Name: Enter the Boiler ID of the tested boiler (left) 2 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: KCPL La Cygne Generating Station Unit 2 is designed for firing pulverized coal and is a dry bottom wall-fired boiler. Unit 2 has a 685 megawatt average gross load that is fired with 100% sub-bituminous Powder River Basin (PRB) coal and uses fuel oil for startup. Unit 2 uses an electrostatic precipitator for particulate control. The generating station is located approximately 40 miles south of Kansas City, Kansas. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: Enter ARS ID FRS #: 1241

SCC / Description 10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous Coal - Pulverized Coal: Dry Bottom (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 288 4800 2148 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 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


### Wednesday, February 16, 2011 Page 2 of 36

### 1241 La Cygne 2

1,2,3,7,8,9-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 Organic Condensible

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

Inorganic (Aqueous)

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



### Wednesday, February 16, 2011 Page 3 of 36

### 1241 La Cygne 2

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. 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 PM2.5 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 Nickel Method 29 3 240 0 Stack Exit Cobalt Method 29 3 240 0 Stack Exit Antimony Method 29 3 240 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit Filterable Particulate Method 29 3 240 0 Stack Exit Chromium Method 29 3 240 0 Stack Exit Lead Method 29 3 240 0 Stack Exit Cadmium Method 29 3 240 0 Stack Exit O2 Method 3A O2 3 120 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 3 180 0 Stack Exit Co2 Method 3A CO2 3 180 0 Stack Exit Co2 Method 3A CO2 3 240 0 Stack Exit Organic Condensible

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

Inorganic (Aqueous)

Condensible Part. 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



### Wednesday, February 16, 2011 Page 4 of 36

### 1241 La Cygne 2

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 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



### Wednesday, February 16, 2011 Page 5 of 36

### 1241 La Cygne 2

Location Stack Exit - Method 26A Average Run Number 1 2 3
Test Date 5/20/2010 5/20/2010 5/21/2010 Run Start Time 10:48:00 AM 2:43:00 PM 7:15:00 AM
Run Finish Time 2:11:00 PM 5:59:00 PM 7:15:00 AM Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf 121.642 122.333 119.032 121.002 Moisture Content of Stack Gas, % 13.08 13.22 12.82 13.040 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 14.092 14.162 13.974 14.076 Oxygen, % 5.333 5.326 5.434 5.364 Average Stack Gas Temperature, °F 297.92 299.00 290.92 295.947 Dry Volumetric Flow Rate, dry scfm 1,599,472.2 1,591,733.5 1,563,475.2 1,584,893.63 3 Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,778,935.1 2,787,621.0 2,688,005.0 2,751,520.36 7 Percent Isokinetic of Sampling Rate, % 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



### 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



### Wednesday, February 16, 2011 Page 6 of 36

### 1241 La Cygne 2

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



### 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



### Wednesday, February 16, 2011 Page 7 of 36

### 1241 La Cygne 2

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



### 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



### Wednesday, February 16, 2011 Page 8 of 36

### 1241 La Cygne 2

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



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



### Wednesday, February 16, 2011 Page 9 of 36

### 1241 La Cygne 2

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



### 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



### Wednesday, February 16, 2011 Page 10 of 36

### 1241 La Cygne 2

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 11 of 36

### 1241 La Cygne 2

Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run 1 2 3 lb/mmBtuO2 4.01E-01 2.82E-01 3.78E-01 0.354 ppm 4.20E+02 2.94E+02 3.96E+02 370.000 ppm@7%O2 3.75E+02 2.64E+02 3.54E+02 331.000



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average Run 1 2 3 lb/mmBtuO2 1.60E-03 4.79E-04 7.24E-04 0.001 ppm 1.06E+00 3.17E-01 4.82E-01 0.620 ppm@7%O2 9.48E-01 2.84E-01 4.30E-01 0.554



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 2.794 3.461 2.899 3.051 Elb/hr 4.86E+00 5.96E+00 5.04E+00 5.287 lb/mmBtuO2 6.65E-04 8.19E-04 7.10E-04 0.001 mg/dscm 8.11E-01 9.99E-01 8.60E-01 0.890 mg/dscm@7%O2 7.24E-01 8.92E-01 7.73E-01 0.796 

### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 3.012 2.805 4.135 3.317 Elb/hr 5.24E+00 4.83E+00 7.18E+00 5.750 lb/mmBtuO2 7.17E-04 6.63E-04 1.01E-03 0.001 mg/dscm 8.75E-01 8.10E-01 1.23E+00 0.972 mg/dscm@7%O2 7.81E-01 7.23E-01 1.11E+00 0.871



### Location: Stack Exit - Method 29 Compound: Antimony Average RunNumber 3 1 2 Mass_mg 0.02893 0.00992 0.00086 0.013 Elb/hr 3.71E-02 1.29E-02 1.12E-03 0.017 lb/mmBtuO2 5.26E-06 1.77E-06 1.55E-07 0.000 mg/dscm 6.56E-03 2.17E-03 1.90E-04 0.003 mg/dscm@7%O2 5.73E-03 1.93E-03 1.69E-04 0.003 

### Compound: Arsenic Average RunNumber 3 1 2 Mass_mg 0.00413 0.00507 0.00393 0.004 Elb/hr 5.30E-03 6.60E-03 5.10E-03 0.006


### Wednesday, February 16, 2011 Page 12 of 36

### 1241 La Cygne 2

lb/mmBtuO2 7.51E-07 9.06E-07 7.07E-07 0.000 mg/dscm 9.37E-04 1.11E-03 8.67E-04 0.001 mg/dscm@7%O2 8.19E-04 9.89E-04 7.69E-04 0.001 

### Compound: Beryllium Average RunNumber 3 1 2 Mass_mg 0.00044 0.00028 0.0003 0.000 Elb/hr 5.64E-04 3.64E-04 3.89E-04 0.000 lb/mmBtuO2 8.00E-08 5.00E-08 5.39E-08 0.000 mg/dscm 9.98E-05 6.12E-05 6.62E-05 0.000 mg/dscm@7%O2 8.72E-05 5.45E-05 5.87E-05 0.000 

### Compound: Cadmium Average RunNumber 3 1 2 Mass_mg 0.00053 0.00144 0.00079 0.001 Elb/hr 6.80E-04 1.87E-03 1.02E-03 0.001 lb/mmBtuO2 9.64E-08 2.57E-07 1.42E-07 0.000 mg/dscm 1.20E-04 3.15E-04 1.74E-04 0.000 mg/dscm@7%O2 1.05E-04 2.81E-04 1.54E-04 0.000 

### Compound: Chromium Average RunNumber 3 1 2 Mass_mg 0.01095 0.01179 0.02207 0.015 Elb/hr 1.40E-02 1.53E-02 2.86E-02 0.019 lb/mmBtuO2 1.99E-06 2.11E-06 3.97E-06 0.000 mg/dscm 2.48E-03 2.58E-03 4.87E-03 0.003 mg/dscm@7%O2 2.17E-03 2.30E-03 4.32E-03 0.003 

### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.00343 0.005 0.00109 0.003 Elb/hr 4.46E-03 6.48E-03 1.40E-03 0.004 lb/mmBtuO2 6.13E-07 8.99E-07 1.98E-07 0.000 mg/dscm 7.49E-04 1.10E-03 2.47E-04 0.001 mg/dscm@7%O2 6.67E-04 9.76E-04 2.16E-04 0.001 

### Compound: Filterable Particulate Average RunNumber 2 3 1 Mass_mg 34.1 19.2 32.5 28.600 Elb/hr 4.42E+01 2.46E+01 4.23E+01 37.033 lb/mmBtuO2 6.13E-03 3.49E-03 5.81E-03 0.005 mg/dscm 7.53E+00 4.35E+00 7.10E+00 6.327 mg/dscm@7%O2 6.68E+00 3.80E+00 6.33E+00 5.603 

### Compound: Lead Average RunNumber 3 1 2 Mass_mg 0.01659 0.03299 0.01337 0.021 Elb/hr 2.13E-02 4.29E-02 1.73E-02 0.027


### Wednesday, February 16, 2011 Page 13 of 36

### 1241 La Cygne 2

lb/mmBtuO2 3.02E-06 5.89E-06 2.40E-06 0.000 mg/dscm 3.76E-03 7.21E-03 2.95E-03 0.005 mg/dscm@7%O2 3.29E-03 6.42E-03 2.62E-03 0.004 

### Compound: Manganese Average RunNumber 3 1 2 Mass_mg 0.00991 0.01755 0.01605 0.015 Elb/hr 1.27E-02 2.28E-02 2.08E-02 0.019 lb/mmBtuO2 1.80E-06 3.13E-06 2.89E-06 0.000 mg/dscm 2.25E-03 3.83E-03 3.54E-03 0.003 mg/dscm@7%O2 1.97E-03 3.41E-03 3.14E-03 0.003 

### Compound: Nickel Average RunNumber 3 1 2 Mass_mg 0.01006 0.00978 0.02581 0.015 Elb/hr 1.29E-02 1.27E-02 3.35E-02 0.020 lb/mmBtuO2 1.83E-06 1.75E-06 4.64E-06 0.000 mg/dscm 2.28E-03 2.14E-03 5.70E-03 0.003 mg/dscm@7%O2 1.99E-03 1.91E-03 5.06E-03 0.003 

### Compound: Selenium Average RunNumber 2 3 1 Mass_mg 0.0028 0.0148 0.02337 0.014 Elb/hr 3.63E-03 1.90E-02 3.04E-02 0.018 lb/mmBtuO2 5.03E-07 2.69E-06 4.17E-06 0.000 mg/dscm 6.18E-04 3.36E-03 5.11E-03 0.003 mg/dscm@7%O2 5.48E-04 2.94E-03 4.55E-03 0.003



### Location: Stack Exit - Method 6C 

### Compound: Sulfur Dioxide Average Run 1 2 3 Elb/hr 4.97E+03 5.02E+03 4.93E+03 4,973.333 lb/mmBtuO2 6.79E-01 6.90E-01 6.94E-01 0.688 mg/dscm 8.29E+02 8.42E+02 8.41E+02 837.333 mg/dscm@7%O2 7.40E+02 7.51E+02 7.56E+02 749.000 ppm 3.11E+02 3.16E+02 3.16E+02 314.333 ppm@7%O2 2.78E+02 2.82E+02 2.84E+02 281.333



### Location: Stack Exit - Method 7E Compound: Nitrogen oxides (NOx) Average Run 1 2 3 Elb/hr 2.44E+03 2.46E+03 2.58E+03 2,493.333 lb/mmBtuO2 3.33E-01 3.38E-01 3.63E-01 0.345 mg/dscm 4.07E+02 4.13E+02 4.40E+02 420.000 mg/dscm@7%O2 3.63E+02 3.69E+02 3.95E+02 375.667 ppm 2.13E+02 2.16E+02 2.30E+02 219.667 ppm@7%O2 1.90E+02 1.93E+02 2.07E+02 196.667



### Wednesday, February 16, 2011 Page 14 of 36

### 1241 La Cygne 2

Process Run Data Location: Stack Exit - OTM - 27/28 

### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 21.2 15 12.9 16.367 lb/mmBtuO2 7.30E-03 5.13E-03 4.29E-03 0.006 

### Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 14.3 12 10 12.100 lb/mmBtuO2 4.92E-03 4.11E-03 3.33E-03 0.004 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 14.6 16 17 15.867 lb/mmBtuO2 5.03E-03 5.48E-03 5.66E-03 0.005 

### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 4.4 3.9 3.3 3.867 lb/mmBtuO2 1.52E-03 1.33E-03 1.10E-03 0.001 

### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 40.2 34.9 33.2 36.100 lb/mmBtuO2 1.38E-02 1.19E-02 1.10E-02 0.012 

### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 33.3 31.9 30.3 31.833 lb/mmBtuO2 1.15E-02 1.09E-02 1.01E-02 0.011



### Wednesday, February 16, 2011 Page 15 of 36

### 1241 La Cygne 2

Process Run Data



### Run Name Value UOM Comments Target Value 1 Coal Firing Rate 392.9 daily avg tons/hour Organic HAP Run 1 0



### 1 Average Heat Input 6759.8 MMBtu/hr Organic HAP Run 1 0

1 Steam Output 4288 1000 lb steam/hr Organic HAP Run 1 0



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


### 1 Coal Gas Firing Rate 0 0
1 Fuel Oil Firing Rate 0 0
1 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg Moisture 12.8%. Organic HAP Run 1 0

1 Pressure Drop Across FGD (if applicable) 0 in H20 0


### 1 FGD Scrubber Liquor pH 0 pH 0
1 FGD Scrubber Liquor Flow Rate 0 gal/min 0
1 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



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


### 1 Flue Gas Moisture Content 0 % 0
1 Flue Gas Sampling Point Temperature 0 Deg F 0
1 Flue Gas Pressure 0 atm 0


### 1 Standard Pressure 0 atm 0
1 Standard Temperature 0 Deg F 0
1 Unit Gross Electrical Output 683.5 MW Organic HAP Run 1 0



### 1 Unit Net Electric Generation 653.3 MWh Organic HAP Run 1 0

2 Coal Firing Rate 392.9 daily avg tons/hour Organic HAP Run 2 0



### 2 Average Heat Input 6759.8 MMBtu/hr Organic HAP Run 2 0

2 Steam Output 4288 1000 lb steam/hr Organic HAP Run 2 0



### 2 Synfuel Firing Rate 0 0
2 Petroleum Coke Firing Rate 0 0



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

### 1241 La Cygne 2

2 Coal Gas Firing Rate 0 0


### 2 Fuel Oil Firing Rate 0 0
2 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg Moisture 12.8%. Organic HAP Run 2 0

2 Pressure Drop Across FGD (if applicable) 0 in H20 0
2 FGD Scrubber Liquor pH 0 pH 0


### 2 FGD Scrubber Liquor Flow Rate 0 gal/min 0
2 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 2 Flue Gas Oxygen Content 0 % 0
2 Flue Gas Carbon Dioxide Content 0 % 0
2 Flue Gas Moisture Content 0 % 0


### 2 Flue Gas Sampling Point Temperature 0 Deg F 0
2 Flue Gas Pressure 0 atm 0
2 Standard Pressure 0 atm 0


### 2 Standard Temperature 0 Deg F 0
2 Unit Gross Electrical Output 683.5 MW Organic HAP Run 2 0



### 2 Unit Net Electric Generation 653.3 MWh Organic HAP Run 2 0

3 Coal Firing Rate 392.9 daily avg tons/hour Organic HAP Run 3 0



### 3 Average Heat Input 6759.8 MMBtu/hr Organic HAP Run 3 0

3 Steam Output 4288 1000 lb steam/hr Organic HAP Run 3 0



### 3 Synfuel Firing Rate 0 0
3 Petroleum Coke Firing Rate 0 0
3 Coal Gas Firing Rate 0 0


### 3 Fuel Oil Firing Rate 0 0
3 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg Moisture 12.8%. Organic HAP Run 3 0

3 Pressure Drop Across FGD (if applicable) 0 in H20 0
3 FGD Scrubber Liquor pH 0 pH 0


### 3 FGD Scrubber Liquor Flow Rate 0 gal/min 0
3 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### Wednesday, February 16, 2011 Page 17 of 36

### 1241 La Cygne 2

3 Flue Gas Oxygen Content 0 % 0


### 3 Flue Gas Carbon Dioxide Content 0 % 0
3 Flue Gas Moisture Content 0 % 0
3 Flue Gas Sampling Point Temperature 0 Deg F 0


### 3 Flue Gas Pressure 0 atm 0
3 Standard Pressure 0 atm 0
3 Standard Temperature 0 Deg F 0


### 3 Unit Gross Electrical Output 683.5 MW Organic HAP Run 3 0

3 Unit Net Electric Generation 653.3 MWh Organic HAP Run 3 0



### 4 Coal Firing Rate 409.2 daily avg tons/hour Acid Gas HAP Run 1 0

4 Average Heat Input 6827.9 MMBtu/hr Acid Gas HAP Run 1 0



### 4 Steam Output 4271 1000 lb steam/hr Acid Gas HAP Run 1 0

4 Synfuel Firing Rate 0 0


### 4 Petroleum Coke Firing Rate 0 0
4 Coal Gas Firing Rate 0 0
4 Fuel Oil Firing Rate 0 0


### 4 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg Moisture 12.8%. Acid Gas HAP Run 1 0

4 Pressure Drop Across FGD (if applicable) 0 in H20 0
4 FGD Scrubber Liquor pH 0 pH 0
4 FGD Scrubber Liquor Flow Rate 0 gal/min 0


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

4 Flue Gas Oxygen Content 0 % 0


### 4 Flue Gas Carbon Dioxide Content 0 % 0
4 Flue Gas Moisture Content 0 % 0
4 Flue Gas Sampling Point Temperature 0 Deg F 0


### 4 Flue Gas Pressure 0 atm 0
4 Standard Pressure 0 atm 0
4 Standard Temperature 0 Deg F 0


### 4 Unit Gross Electrical Output 683.5 MW Acid Gas HAP Run 1 0

4 Unit Net Electric Generation 653.3 MWh Acid Gas HAP Run 1 0



### Wednesday, February 16, 2011 Page 18 of 36

### 1241 La Cygne 2

5 Coal Firing Rate 409.2 daily avg tons/hour Acid Gas HAP Run 2 0



### 5 Average Heat Input 6827.9 MMBtu/hr Acid Gas HAP Run 2 0

5 Steam Output 4271 1000 lb steam/hr Acid Gas HAP Run 2 0

5 Synfuel Firing Rate 0 0
5 Petroleum Coke Firing Rate 0 0


### 5 Coal Gas Firing Rate 0 0
5 Fuel Oil Firing Rate 0 0
5 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg Moisture 12.8%. Acid Gas HAP Run 2 0

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


### 5 FGD Scrubber Liquor pH 0 pH 0
5 FGD Scrubber Liquor Flow Rate 0 gal/min 0
5 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 5 Flue Gas Oxygen Content 0 % 0
5 Flue Gas Carbon Dioxide Content 0 % 0


### 5 Flue Gas Moisture Content 0 % 0
5 Flue Gas Sampling Point Temperature 0 Deg F 0
5 Flue Gas Pressure 0 atm 0


### 5 Standard Pressure 0 atm 0
5 Standard Temperature 0 Deg F 0
5 Unit Gross Electrical Output 683.5 MW Acid Gas HAP Run 2 0



### 5 Unit Net Electric Generation 653.3 MWh Acid Gas HAP Run 2 0

6 Coal Firing Rate 391.4 daily avg tons/hour Acid Gas HAP Run 3 0



### 6 Average Heat Input 6772.3 MMBtu/hr Acid Gas HAP Run 3 0

6 Steam Output 4329 1000 lb steam/hr Acid Gas HAP Run 3 0



### 6 Synfuel Firing Rate 0 0
6 Petroleum Coke Firing Rate 0 0


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



### Wednesday, February 16, 2011 Page 19 of 36

### 1241 La Cygne 2

6 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg Moisture 12.8%. Acid Gas HAP Run 3 0

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


### 6 FGD Scrubber Liquor pH 0 pH 0
6 FGD Scrubber Liquor Flow Rate 0 gal/min 0
6 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



### 6 Flue Gas Oxygen Content 0 % 0
6 Flue Gas Carbon Dioxide Content 0 % 0


### 6 Flue Gas Moisture Content 0 % 0
6 Flue Gas Sampling Point Temperature 0 Deg F 0
6 Flue Gas Pressure 0 atm 0


### 6 Standard Pressure 0 atm 0
6 Standard Temperature 0 Deg F 0
6 Unit Gross Electrical Output 691.1 MW Acid Gas HAP Run 3 0



### 6 Unit Net Electric Generation 661.7 MWh Acid Gas HAP Run 3 0

7 Coal Firing Rate 391.4 daily avg tons/hour Metals/PM Run 1 0


### 7 Average Heat Input 6772.3 MMBtu/hr Metals/PM Run 1 0
7 Steam Output 4329 1000 lb steam/hr Metals/PM Run 1 0
7 Synfuel Firing Rate 0 0


### 7 Petroleum Coke Firing Rate 0 0
7 Coal Gas Firing Rate 0 0
7 Fuel Oil Firing Rate 0 0


### 7 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg Moisture 12.8%. Metals/PM Run 1 0

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


### 7 FGD Scrubber Liquor pH 0 pH 0
7 FGD Scrubber Liquor Flow Rate 0 gal/min 0


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

7 Flue Gas Oxygen Content 0 % 0
7 Flue Gas Carbon Dioxide Content 0 % 0


### 7 Flue Gas Moisture Content 0 % 0
7 Flue Gas Sampling Point Temperature 0 Deg F 0
7 Flue Gas Pressure 0 atm 0



### Wednesday, February 16, 2011 Page 20 of 36

### 1241 La Cygne 2

7 Standard Pressure 0 atm 0


### 7 Standard Temperature 0 Deg F 0
7 Unit Gross Electrical Output 691.1 MW Metals/PM Run 1 0
7 Unit Net Electric Generation 661.7 MWh Metals/PM Run 1 0


### 8 Coal Firing Rate 391.4 daily avg tons/hour Metals/PM Run 2 0
8 Average Heat Input 6772.3 MMBtu/hr Metals/PM Run 2 0
8 Steam Output 4329 1000 lb steam/hr Metals/PM Run 2 0


### 8 Synfuel Firing Rate 0 0
8 Petroleum Coke Firing Rate 0 0
8 Coal Gas Firing Rate 0 0


### 8 Fuel Oil Firing Rate 0 0
8 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg Moisture 12.8%. Metals/PM Run 2 0



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


### 8 FGD Scrubber Liquor Flow Rate 0 gal/min 0
8 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

8 Flue Gas Oxygen Content 0 % 0


### 8 Flue Gas Carbon Dioxide Content 0 % 0
8 Flue Gas Moisture Content 0 % 0
8 Flue Gas Sampling Point Temperature 0 Deg F 0


### 8 Flue Gas Pressure 0 atm 0
8 Standard Pressure 0 atm 0
8 Standard Temperature 0 Deg F 0


### 8 Unit Gross Electrical Output 691.1 MW Metals/PM Run 2 0
8 Unit Net Electric Generation 661.7 MWh Metals/PM Run 2 0
9 Coal Firing Rate 355.9 daily avg tons/hour Metals/PM Run 3 0


### 9 Average Heat Input 6368.5 MMBtu/hr Metals/PM Run 3 0
9 Steam Output 4018 1000 lb steam/hr Metals/PM Run 3 0


### 9 Synfuel Firing Rate 0 0
9 Petroleum Coke Firing Rate 0 0
9 Coal Gas Firing Rate 0 0


### 9 Fuel Oil Firing Rate 0 0
9 Flue Gas Flow Rate 1E+06 dscfm Used M29 Avg Moisture 12.8%. Metals/PM Run 3 0

Wednesday, February 16, 2011 Page 21 of 36

### 1241 La Cygne 2

APCD Run Data

Process Lab Run Data 9 Pressure Drop Across FGD (if applicable) 0 in H20 0


### 9 FGD Scrubber Liquor pH 0 pH 0
9 FGD Scrubber Liquor Flow Rate 0 gal/min 0
9 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0



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


### 9 Flue Gas Moisture Content 0 % 0
9 Flue Gas Sampling Point Temperature 0 Deg F 0
9 Flue Gas Pressure 0 atm 0


### 9 Standard Pressure 0 atm 0
9 Standard Temperature 0 Deg F 0
9 Unit Gross Electrical Output 644.4 MW Metals/PM Run 3 0


### 9 Unit Net Electric Generation 613.5 MWh Metals/PM Run 3 0

Run Name Value UOM Comments Target Value 1 ELECTROSTATIC PRECIPITATOR 317.78 Primary Voltage 0


### 2 ELECTROSTATIC PRECIPITATOR 317.78 Primary Voltage 0
3 ELECTROSTATIC PRECIPITATOR 317.78 Primary Voltage 0
4 ELECTROSTATIC PRECIPITATOR 316.69 Primary Voltage 0


### 5 ELECTROSTATIC PRECIPITATOR 316.69 Primary Voltage 0
6 ELECTROSTATIC PRECIPITATOR 319.88 Primary Voltage 0
7 ELECTROSTATIC PRECIPITATOR 319.88 Primary Voltage 0


### 8 ELECTROSTATIC PRECIPITATOR 319.88 Primary Voltage 0
9 ELECTROSTATIC PRECIPITATOR 334.91 Primary Voltage 0

Run Name Value UOM Comments 1 Fuel Higher Heating Value (as received) Btu/lb 

### 1 Fuel Moisture (as received) % 1 Fuel Mercury Content ppm 1 Fuel Cadmium Content ppm 1 Ultimate/Proximate Analysis 

### 1 Fuel Nickel Content ppm 1 Fuel Arsenic Content ppm 1 Fuel Chromium Content ppm



### Wednesday, February 16, 2011 Page 22 of 36

### 1241 La Cygne 2

1 Fuel Beryllium Content ppm 

### 1 Fuel Lead Content ppm 1 Fuel Manganese Content ppm 1 Fuel Chlorine Content ppm 1 Fuel Fluorine Content ppm 

### 1 Proximate - Ash % weight 1 Proximate - Volatile % weight 1 Proximate - Fixed Carbon % weight 

### 1 Ultimate - Carbon % weight 1 Ultimate - Nitrogen % weight 1 Ultimate - Sulfur % weight 1 Ultimate - Oxygen % weight



### Wednesday, February 16, 2011 Page 23 of 36

### 1241 La Cygne 2

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 24 of 36

### 1241 La Cygne 2

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 25 of 36

### 1241 La Cygne 2

Location Stack Exit - Method 26A Average Run Number 1 2 3 Test Date 5/20/2010 5/20/2010 5/21/2010 Run Start Time 10:48:00 AM 2:43:00 PM 7:15:00 AM Run Finish Time 2:11:00 PM 5:59:00 PM 7:15:00 AM Net Traversing Points 12 12 12 Net Run Time, minutes Nozzle Diameter, inches 0.187 0.187 0.187 0.187 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9779 0.9779 0.9779 0.978 Barometric Pressure, inches of Mercury 28.64 28.5 28.59 28.577 Average Orifice Meter Differential, inches H2O 1.78 1.77 1.68 1.743 Dry Gas Meter Volume Sampled, cubic feet 133.740 136.471 130.500 133.570 Average Dry Gas Meter Temperature, °F 85.88 91.17 83.25 86.767 Dry Gas Meter Volume Sampled, dscf 121.642 122.333 119.032 121.002 Total Moisture Liquid collected, g 388.9 396 371.8 385.567 Volume of Water Vapor, standard cubic feet 18.31 18.64 17.50 18.150 Moisture Content of Stack Gas, % 13.08 13.22 12.82 13.040 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8692 0.8678 0.8718 0.870 Carbon Dioxide, % 14.092 14.162 13.974 14.076 Oxygen, % 5.333 5.326 5.434 5.364 Carbon Monoxide & Nitrogen, % 80.575 80.512 80.592 80.560 Fuel Factor 1.10 1.10 1.11 Dry Molecular Weight, lb/lb-Mole 30.47 30.48 30.45 30.467 Wet Molecular weight, lb/lb-Mole 28.84 28.83 28.85 28.840 Flue Gas Static Pressure, inches of H2O -2.7 -2.7 -2.7 -2.700 Absolute Flue Gas Pressure, inches of Mercury 28.44 28.30 28.39 28.377 Average Stack Gas Temperature, °F 297.92 299.00 290.92 295.947 Average Velocity Head, inches of H2O 2.1994314876 6317 2.198468950

6087 2.074179278

13561 2.157
Average Stack Gas Velocity, feet/second 102.38 102.70 99.03 101.370 Stack Cross-Sectional Area, square feet 452.389 452.389 452.389 452.389 Dry Volumetric Flow Rate, dry scfm 1,599,472.2 1,591,733.5 1,563,475.2 1,584,893.6 33 Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,778,935.1 2,787,621.0 2,688,005.0 2,751,520.3 67 Percent Isokinetic of Sampling Rate, % Percent Excess Air, % 33.5 33.4 34.3 33.733 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Round Duct Diameter, inches 288 288 288 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000



### Wednesday, February 16, 2011 Page 26 of 36

### 1241 La Cygne 2

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 27 of 36

### 1241 La Cygne 2

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 28 of 36

### 1241 La Cygne 2

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 29 of 36

### 1241 La Cygne 2

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 30 of 36

### 1241 La Cygne 2

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 31 of 36

### 1241 La Cygne 2

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 32 of 36

### 1241 La Cygne 2

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 33 of 36

### 1241 La Cygne 2

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 34 of 36

### 1241 La Cygne 2

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 35 of 36

### 1241 La Cygne 2

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 36 of 36