### Name: Shih Chieh Lin

Title: Plant General Manager Company: TEMES (Cabras No. 1 & 2 PMC) Sign Date: Name: Tony Wong Title: President Company: AirKinetics Inc. Sign Date: Permitted Facility Representative / Date Testing Company Representative / Date 

## Emissions Testing Unit 1 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, July 06, 2011 Page 1 of 19

### Emissions Testing Unit 1

Facility Information:
Cabras Power Plant No. 322 Cabras Hwy, Route 11

Piti GU96915 Contact:Melinda R. Camacho Phone: (671) 648-2312 Fax: (671) 648-3167 Email: plant.mgr@temes.com.tw Testing Company:
AirKinetics Inc.
1308 S. Allec

Anaheim CA92805 Contact:Tony Wong Phone: (714) 245-1945 Fax: (714) 956-2350 Email: wongt@airkineticsinc.com

Air Permit Number: FO-002 Permitted Source ID/Name: Boiler Unit # 1 Cabras # 1 Permitted Maximum Process Rate: Title V Air Permit has no limit on MM Max. Normal Operation Process Rate: 481 MMBtu/hr Target Process Test Rat N/A

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: N/A FRS #: N/A

SCC / Description10100401 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: Normal Firing

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 113.69 480 1212 2 113.69 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location Carbon Monoxide Method 10 3 120 0 stack Total organic compounds

(TOC) as Carbon Method 25A 3 120 0 stack

Total PM2.5 OTM - 27/28 3 367 0 stack Filterable PM2.5 OTM - 27/28 3 367 0 stack Regulation Description Compound Limit Unit



### Wednesday, July 06, 2011 Page 2 of 19

### Emissions Testing Unit 1

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 Organic Condensible

Particulate OTM - 27/28 3 367 0 stack
Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 367 0 stack

Total Particulate OTM - 27/28 3 367 0 stack Filterable Particulate OTM - 27/28 3 367 0 stack Arsenic Method 29 3 240 0 stack Antimony Method 29 3 240 0 stack Beryllium Method 29 3 240 0 stack Cadmium Method 29 3 240 0 stack Chromium Method 29 3 240 0 stack Cobalt Method 29 3 240 0 stack Lead Method 29 3 240 0 stack Manganese Method 29 3 240 0 stack Nickel Method 29 3 240 0 stack Selenium Method 29 3 240 0 stack O2 Method 3A O2 3 120 0 stack Co2 Method 3A CO2 3 120 0 stack Filterable Particulate Method 5 240 0 stack Sulfur Dioxide Method 6C 3 120 0 stack Nitrogen oxides (NOx) Method 7E 3 120 0 stack



### Wednesday, July 06, 2011 Page 3 of 19

### Emissions Testing Unit 1

Sampling / Stack Data Results Summary

Location stack - Method 10 Average Run Number 1 2 3
Test Date 1/20/2011 1/20/2011 1/21/2011 Run Start Time 11:13:00 AM 1:48:00 PM 10:01:00 AM Run Finish Time 1:13:00 PM 3:48:00 PM 12:01:00 PM Carbon Dioxide, % 11.74 11.72 11.65 11.703 Oxygen, % 6.2 6.27 6.24 6.237 Dry Volumetric Flow Rate, dry scfm 136576 128782 137514 134,290.667 F-Factor, dscfm/MMBtu @ %O2 9258 9258 9305 9,273.667 Moisture, % 12.41 12.83 12.12 12.453 Fuel Type Override Override Override
Fw
Fc



### Location stack - Method 25A Average Run Number 1 2 3
Test Date 1/20/2011 1/20/2011 1/21/2011 Run Start Time 11:13:00 AM 1:48:00 PM 10:01:00 AM Run Finish Time 1:13:00 PM 3:48:00 PM 12:01:00 PM Carbon Dioxide, % 11.74 11.72 11.65 11.703 Oxygen, % 6.2 6.27 6.24 6.237 Dry Volumetric Flow Rate, dry scfm 136576 128782 137514 134,290.667 F-Factor, dscfm/MMBtu @ %O2 9258 9258 9305 9,273.667 Moisture, % 12.41 12.83 12.12 12.453 Fuel Type Override Override Override
Fw
Fc



### Wednesday, July 06, 2011 Page 4 of 19

### Emissions Testing Unit 1

Location stack - Method 29 Average Run Number 2 3 4
Test Date 1/19/2011 1/20/2011 1/21/2011 Run Start Time 12:10:00 PM 12:18:00 PM 3:30:00 PM

Run Finish Time 4:27:00 PM 4:57:00 PM 7:46:00 PM Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 165.672 163.327 170.534 166.511 Moisture Content of Stack Gas, % 12.27 12.82 12.43 12.507 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 11.72 11.74 11.49 11.650 Oxygen, % 6.27 6.26 6.29 6.273 Average Stack Gas Temperature, °F 354.17 357.71 358.17 356.683 Dry Volumetric Flow Rate, dry scfm 129,023.3 128,777.7 133,174.8 130,325.267 Actual Wet Volumetric Flue Gas Flow Rate, acfm 226,929.8 228,917.9 235,812.5 230,553.400 Percent Isokinetic of Sampling Rate, % 101.5 101.0 101.2 101.233 F-Factor, dscfm/MMBtu @ %O2 9688 9258 9305 9,417.000
Fw
Fc



### Wednesday, July 06, 2011 Page 5 of 19

### Emissions Testing Unit 1

Location stack - Method 5 Average Run Number 2 3 4
Test Date 1/19/2011 1/20/2011 1/21/2011 Run Start Time 12:10:00 PM 12:18:00 PM 11:49:00 AM

Run Finish Time 4:27:00 PM 4:57:00 PM 7:46:00 PM Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 165.672 163.327 170.534 166.511 Moisture Content of Stack Gas, % 12.27 12.82 12.43 12.507 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 11.72 11.74 11.49 11.650 Oxygen, % 6.27 6.26 6.29 6.273 Average Stack Gas Temperature, °F 354.17 357.71 358.17 356.683 Dry Volumetric Flow Rate, dry scfm 129,023.3 128,777.7 133,174.8 130,325.267 Actual Wet Volumetric Flue Gas Flow Rate, acfm 226,929.8 228,917.9 235,812.5 230,553.400 Percent Isokinetic of Sampling Rate, % 101.5 101.0 101.2 101.233 F-Factor, dscfm/MMBtu @ %O2 9688 9258 9305 9,417.000
Fw
Fc



### Location stack - Method 6C Average Run Number 1 2 3
Test Date 1/21/2011 1/21/2011 1/21/2011 Run Start Time 10:01:00 AM 1:01:00 PM 3:47:00 PM Run Finish Time 12:01:00 PM 3:01:00 PM 5:47:00 PM Carbon Dioxide, % 11.65 11.69 11.65 11.663 Oxygen, % 6.24 6.22 6.28 6.247 Dry Volumetric Flow Rate, dry scfm 137514 137514 133190 136,072.667 F-Factor, dscfm/MMBtu @ %O2 9305 9305 9305 9,305.000 Moisture, % 12.12 12.12 12.43 12.223 Fuel Type Override Override Override
Fw
Fc



### Wednesday, July 06, 2011 Page 6 of 19

### Emissions Testing Unit 1

Location stack - Method 7E Average Run Number 1 2 3
Test Date 1/21/2011 1/21/2011 1/21/2011 Run Start Time 10:01:00 AM 1:01:00 PM 3:47:00 PM Run Finish Time 12:01:00 PM 3:01:00 PM 5:47:00 PM Carbon Dioxide, % 11.65 11.69 11.65 11.663 Oxygen, % 6.24 6.22 6.28 6.247 Dry Volumetric Flow Rate, dry scfm 137514 137514 133190 136,072.667 F-Factor, dscfm/MMBtu @ %O2 9305 9305 9305 9,305.000 Moisture, % 12.12 12.12 12.43 12.223 Fuel Type Override Override Override
Fw
Fc



### Location stack - OTM - 27/28 Average Run Number 2 3 4
Test Date 1/19/2011 1/20/2011 1/21/2011 Run Start Time 7:40:00 AM 7:31:00 AM 9:06:00 AM

Run Finish Time 2:17:00 PM 2:48:00 PM 3:37:00 PM Net Run Time, minutes 364.7141317 368.264478 1 371.5

Dry Gas Meter Volume Sampled, dscf 123.433 128.568 129.865 127.289 Moisture Content of Stack Gas, % 12.08 12.41 12.11 12.200 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 11.76 11.74 11.67 11.723 Oxygen, % 6.28 6.26 6.23 6.257 Average Stack Gas Temperature, °F 349.25 353.92 356.00 353.057 Dry Volumetric Flow Rate, dry scfm 136,078.0 136,566.8 138,031.4 136,892.067 Actual Wet Volumetric Flue Gas Flow Rate, acfm 237,377.5 240,507.6 242,876.3 240,253.800 Percent Isokinetic of Sampling Rate, % 92.9 95.5 94.6 94.333 F-Factor, dscfm/MMBtu @ %O2 9688 9258 9305 9,417.000
Fw
Fc



### Wednesday, July 06, 2011 Page 7 of 19

### Emissions Testing Unit 1

Emissions Summary

Location: stack - Method 10 Compound: Carbon Monoxide Average Run 1 2 3 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 ppm 0.00E+00 0.00E+00 0.00E+00 0.000 ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000



### Location: stack - Method 25A Compound: Total organic compounds (TOC) as Average Run 1 2 3 lb/mmBtuO2 3.73E-04 3.48E-04 4.83E-04 0.000 ppm 9.10E-01 8.44E-01 1.17E+00 0.975 ppm@7%O2 8.60E-01 8.02E-01 1.11E+00 0.924



### Location: stack - Method 29 Compound: Antimony Average RunNumber 4 2 3 Mass_mg 0.328983 0.201963 0.402913 0.311 lb/mmBtuO2 5.66E-05 3.72E-05 7.19E-05 0.000 

### Compound: Arsenic Average RunNumber 4 2 3 Mass_mg 0.024403 0.021873 0.030363 0.026 lb/mmBtuO2 4.20E-06 4.03E-06 5.42E-06 0.000 

### Compound: Beryllium Average RunNumber 4 2 3 Mass_mg 0.00039 0.00036 0.00041 0.000 lb/mmBtuO2 6.71E-08 6.63E-08 7.31E-08 0.000 

### Compound: Cadmium Average RunNumber 4 2 3 Mass_mg 0.001653 0.001273 0.012 0.005 lb/mmBtuO2 2.84E-07 2.34E-07 2.14E-06 0.000 

### Compound: Chromium Average RunNumber 4 2 3 Mass_mg 0.01805 0.0253 0.021 0.021 lb/mmBtuO2 3.11E-06 4.66E-06 3.75E-06 0.000 

### Compound: Cobalt Average RunNumber 4 2 3



### Wednesday, July 06, 2011 Page 8 of 19

### Emissions Testing Unit 1

Mass_mg 0.121905 0.110901 0.12895 0.121 lb/mmBtuO2 2.10E-05 2.04E-05 2.30E-05 0.000 

### Compound: Lead Average RunNumber 4 2 3 Mass_mg 0.02426 0.01776 0.02061 0.021 lb/mmBtuO2 4.17E-06 3.27E-06 3.68E-06 0.000 

### Compound: Manganese Average RunNumber 4 2 3 Mass_mg 0.03513 0.0305 0.04324 0.036 lb/mmBtuO2 6.05E-06 5.62E-06 7.71E-06 0.000 

### Compound: Nickel Average RunNumber 4 2 3 Mass_mg 4.46186 3.67116 4.59296 4.242 lb/mmBtuO2 7.68E-04 6.76E-04 8.19E-04 0.001 

### Compound: Selenium Average RunNumber 4 2 3 Mass_mg 0.0184 0.0208 0.0187 0.019 lb/mmBtuO2 3.17E-06 3.83E-06 3.34E-06 0.000



### Location: stack - Method 5 Compound: Filterable Particulate Average RunNumber 2 3 4 Mass_mg 353.4 467.6 469.5 430.167 lb/mmBtuO2 6.51E-02 8.34E-02 8.08E-02 0.076



### Location: stack - Method 6C Compound: Sulfur Dioxide Average Run 1 2 3 lb/mmBtuO2 1.47E+00 1.45E+00 1.45E+00 1.457 ppm 6.68E+02 6.59E+02 6.57E+02 661.333 ppm@7%O2 6.33E+02 6.24E+02 6.25E+02 627.333



### Location: stack - Method 7E Compound: Nitrogen oxides (NOx) Average Run 1 2 3 lb/mmBtuO2 4.89E-01 4.80E-01 4.78E-01 0.482 ppm 3.08E+02 3.04E+02 3.01E+02 304.333 ppm@7%O2 2.92E+02 2.88E+02 2.86E+02 288.667



### Location: stack - OTM - 27/28

Wednesday, July 06, 2011 Page 9 of 19

### Emissions Testing Unit 1

Compound: Filterable Particulate Average RunNumber 2 3 4 Mass_mg 110.8 157.4 145.3 137.833 lb/mmBtuO2 2.74E-02 3.57E-02 3.27E-02 0.032 

### Compound: Filterable PM2.5 Average RunNumber 2 3 4 Mass_mg 90.2 132 144 122.067 lb/mmBtuO2 2.23E-02 2.99E-02 3.24E-02 0.028 

### Compound: Inorganic (Aqueous) Condensible P Average RunNumber 2 3 4 Mass_mg 212.5 162.3 128.4 167.733 lb/mmBtuO2 5.26E-02 3.68E-02 2.89E-02 0.039 

### Compound: Organic Condensible Particulate Average RunNumber 2 3 4 Mass_mg 113.5 172.8 83.2 123.167 lb/mmBtuO2 2.81E-02 3.92E-02 1.87E-02 0.029 

### Compound: Total Particulate Average RunNumber 2 3 4 Mass_mg 492.1 533.5 395.4 473.667 lb/mmBtuO2 1.22E-01 1.21E-01 8.90E-02 0.111 

### Compound: Total PM2.5 Average RunNumber 2 3 4 Mass_mg 414.2 465.1 353.6 410.967 lb/mmBtuO2 1.02E-01 1.05E-01 7.96E-02 0.096



### Wednesday, July 06, 2011 Page 10 of 19

### Emissions Testing Unit 1

Process Run Data

Run Name Value UOM Comments Target Value 2 0
2 0


### 2 0
2 0


### 2 0
2 Residual Oil (No. 6) Burned 34521000 Gallons/hr 3086


### 2 0
2 Unit Gross Electric Generation 45.2 Mwe EPA Method 10 and 25A: Run 4 and Run 5 43



### 2 Unit Net Electric Generation 42.3 MWh EPA Method OTM 27/28: OTM27/28-3 40

2 Steam Output 3891,000 lbs steam/hr EPA Method 5/29: M5/29-3 360

2 Average Heat Input 516 MMBtu/hr January 20, 2011 Test Day 460

3 0
3 0
3 0


### 3 0
3 0


### 3 Residual Oil (No. 6) Burned 3205 1000 Gallons/hr 3086
3 0 EPA Method 3A, 6C, and 7E: Run 1, Run 2, and Run 3 

### 3 Unit Gross Electric Generation 44.4 Mwe EPA Method 10 and 25A: Run 6 43

3 Unit Net Electric Generation 41.5 MWh EPA Method OTM 27/28: OTM27/28-4 40

3 Steam Output 3881,000 lbs steam/hr EPA Method 5/29: M5/29-4 360

3 Average Heat Input 479 MMBtu/hr January 21, 2011 Test Day 460

1 0
1 0


### 1 0

Wednesday, July 06, 2011 Page 11 of 19

### Emissions Testing Unit 1

APCD Run Data

Process Lab Run Data 1 0
1 0


### 1 Residual Oil (No. 6) Burned 31661000 Gallons/hr 3086
1 0
1 Unit Gross Electric Generation 44.5 Mwe 43
1 Unit Net Electric Generation 41.6 MWh EPA Method OTM 27/28: OTM27/28-2 40

1 Steam Output 3861,000 lbs steam/hr EPA Method 5/29: M5/29-2 360



### 1 Average Heat Input 473 MMBtu/hr January 19, 2011 Test Day 460

Run Name Value UOM Comments Target Value 

### 1 None 0
1 0


### 1 0
1 0



### Run Name Value UOM Comments 1 none 0 

### 1 0 1 0 1 0 1 0



### Wednesday, July 06, 2011 Page 12 of 19

### Emissions Testing Unit 1

Sampling / Stack Data Results Detail

Location stack - Method 10 Average Run Number 1 2 3 Test Date 1/20/2011 1/20/2011 1/21/2011 Run Start Time 11:13:00 AM 1:48:00 PM 10:01:00 AM Run Finish Time 1:13:00 PM 3:48:00 PM 12:01:00 PM Carbon Dioxide, % 11.74 11.72 11.65 11.703 Oxygen, % 6.2 6.27 6.24 6.237 Fuel Factor 1.25 1.25 1.26 Dry Volumetric Flow Rate, dry scfm 136576 128782 137514134,290.667 F-Factor, dscfm/MMBtu @ %O2 9258 9258 9305 9,273.667 Moisture, % 12.41 12.83 12.12 12.453 Analyzer Make Thermo Electron Thermo

Electron Thermo

Electron Analyzer Model 48 48 48 48.000 Analyzer Serial Number Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 0 0 0 0.000 Calibration Pre Zero Cylinder ID Nitrogen Nitrogen Nitrogen Calibration Pre Zero Cylinder Instrument Response 0.13 -0.17 0.01 -0.010 Calibration Pre Zero Cylinder Bias 0.32 -0.95 0.21 -0.140 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID COCC149350- Diluted2 COCC149350- Diluted2 COCC116748- Diluted2 Calibration Pre High Cylinder Instrument Response 9.16 9.48 9.35 9.330 Calibration Pre High Cylinder Bias -1.53 -0.16 -455.91 -152.533 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Nitrogen Nitrogen Nitrogen Calibration Post Zero Cylinder Instrument Response -0.17 0.25 0.12 0.067 Calibration Post Zero Cylinder Bias -1.27 1.27 0.79 0.263 Calibration Post Zero Cylinder Drift 1.59 2.22 0.58 1.463 Calibration Post High Cylinder ID COCC149350- Diluted2 COCC149350- Diluted2 COCC116748- Diluted2 Calibration Post High Cylinder Instrument Response 9.48 9.3 9.38 9.387 Calibration Post High Cylinder Bias 0.16 -1.11 -455.76 -152.237 Calibration Post High Cylinder Drift 1.69 0.950.1500000000 00034 0.930
Cavg -0.29 -0.06 -0.18 -0.177 Cavg Units ppmvd ppmvd ppmvd Cgas 0 0 0 0.000 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw Fc Cgasw 0 0 0 0.000 Cgasw Units



### Wednesday, July 06, 2011 Page 13 of 19

### Emissions Testing Unit 1

Location stack - Method 25A Average Run Number 1 2 3 Test Date 1/20/2011 1/20/2011 1/21/2011 Run Start Time 11:13:00 AM 1:48:00 PM 10:01:00 AM Run Finish Time 1:13:00 PM 3:48:00 PM 12:01:00 PM Carbon Dioxide, % 11.74 11.72 11.65 11.703 Oxygen, % 6.2 6.27 6.24 6.237 Fuel Factor 1.25 1.25 1.26 Dry Volumetric Flow Rate, dry scfm 136576 128782 137514134,290.667 F-Factor, dscfm/MMBtu @ %O2 9258 9258 9305 9,273.667 Moisture, % 12.41 12.83 12.12 12.453 Analyzer Make VIG VIG VIG Analyzer Model 20 20 20 20.000 Analyzer Serial Number Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 1 1 1 1.000 Calibration Pre Zero Cylinder ID Nitrogen Nitrogen Nitrogen Calibration Pre Zero Cylinder Instrument Response -0.01 0.08 0.04 0.037 Calibration Pre Zero Cylinder Bias 0 0 0 0.000 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID THCCC74957- Diluted1 THCCC74957- Diluted1 THCCC74957- Diluted1 Calibration Pre High Cylinder Instrument Response 2.47 2.42 2.57 2.487 Calibration Pre High Cylinder Bias 0 0 0 0.000 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Nitrogen Nitrogen Nitrogen Calibration Post Zero Cylinder Instrument Response 0.08 0.07 0.11 0.087 Calibration Post Zero Cylinder Bias 0.9 -0.12 0.84 0.540 Calibration Post Zero Cylinder Drift 0.9 0.12 0.84 0.620 Calibration Post High Cylinder ID THCCC74957- Diluted1 THCCC74957- Diluted1 THCCC74957- Diluted1 Calibration Post High Cylinder Instrument Response 2.42 2.54 2.49 2.483 Calibration Post High Cylinder Bias -0.6 1.43 -0.95 -0.040 Calibration Post High Cylinder Drift 0.6 1.43 0.95 0.993 Cavg 0.8 0.78 1.08 0.887 Cavg Units ppmvw ppmvw ppmvw Cgas 0.9096 0.8441 1.1692 0.974 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw Fc Cgasw 0.7967427385 892120.735779625

7796261.0275152749

4908 0.853
Cgasw Units ppmvw ppmvw ppmvw



### Wednesday, July 06, 2011 Page 14 of 19

### Emissions Testing Unit 1

Location stack - Method 29 Average Run Number 2 3 4 Test Date 1/19/2011 1/20/2011 1/21/2011 Run Start Time 12:10:00 PM 12:18:00 PM 3:30:00 PM Run Finish Time 4:27:00 PM 4:57:00 PM 7:46:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.261 0.26 0.261 0.261 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.02 1.02 1.02 1.020 Barometric Pressure, inches of Mercury 29.9 29.9 29.9 29.900 Average Orifice Meter Differential, inches H2O 1.70 1.66 1.75 1.703 Dry Gas Meter Volume Sampled, cubic feet 173.103 169.164 176.870 173.046 Average Dry Gas Meter Temperature, °F 104.69 99.71 100.60 101.667 Dry Gas Meter Volume Sampled, dscf 165.672 163.327 170.534 166.511 Total Moisture Liquid collected, g 492.2 510.3 514.1 505.533 Volume of Water Vapor, standard cubic feet 23.17 24.02 24.20 23.797 Moisture Content of Stack Gas, % 12.27 12.82 12.43 12.507 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8773 0.8718 0.8757 0.875 Carbon Dioxide, % 11.72 11.74 11.49 11.650 Oxygen, % 6.27 6.26 6.29 6.273 Carbon Monoxide & Nitrogen, % 82.01 82 82.22 82.077 Fuel Factor 1.25 1.25 1.27 Dry Molecular Weight, lb/lb-Mole 30.13 30.13 30.09 30.117 Wet Molecular weight, lb/lb-Mole 28.64 28.57 28.59 28.600 Flue Gas Static Pressure, inches of H2O 0.05 0.05 0.05 0.050 Absolute Flue Gas Pressure, inches of Mercury 29.90 29.90 29.90 29.900 Average Stack Gas Temperature, °F 354.17 357.71 358.17 356.683 Average Velocity Head, inches of H2O 0.5871343392 42741 0.593452660

6036190.6297239915

08873 0.603
Average Stack Gas Velocity, feet/second 53.65 54.12 55.75 54.507 Stack Cross-Sectional Area, square feet 70.497 70.497 70.497 70.497 Dry Volumetric Flow Rate, dry scfm 129,023.3 128,777.7 133,174.8130,325.267 Actual Wet Volumetric Flue Gas Flow Rate, acfm 226,929.8 228,917.9 235,812.5230,553.400 Percent Isokinetic of Sampling Rate, % 101.5 101.0 101.2 101.233 Percent Excess Air, % 40.8 40.7 40.8 40.767 F-Factor, dscfm/MMBtu @ %O2 9688 9258 9305 9,417.000 Round Duct Diameter, inches 113.69 113.69 113.69 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw Fc



### Wednesday, July 06, 2011 Page 15 of 19

### Emissions Testing Unit 1

Location stack - Method 5 Average Run Number 2 3 4 Test Date 1/19/2011 1/20/2011 1/21/2011 Run Start Time 12:10:00 PM 12:18:00 PM 11:49:00 AM Run Finish Time 4:27:00 PM 4:57:00 PM 7:46:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.261 0.26 0.261 0.261 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.02 1.02 1.02 1.020 Barometric Pressure, inches of Mercury 29.9 29.9 29.9 29.900 Average Orifice Meter Differential, inches H2O 1.70 1.66 1.75 1.703 Dry Gas Meter Volume Sampled, cubic feet 173.103 169.164 176.870 173.046 Average Dry Gas Meter Temperature, °F 104.69 99.71 100.60 101.667 Dry Gas Meter Volume Sampled, dscf 165.672 163.327 170.534 166.511 Total Moisture Liquid collected, g 492.2 510.3 514.1 505.533 Volume of Water Vapor, standard cubic feet 23.17 24.02 24.20 23.797 Moisture Content of Stack Gas, % 12.27 12.82 12.43 12.507 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8773 0.8718 0.8757 0.875 Carbon Dioxide, % 11.72 11.74 11.49 11.650 Oxygen, % 6.27 6.26 6.29 6.273 Carbon Monoxide & Nitrogen, % 82.01 82 82.22 82.077 Fuel Factor 1.25 1.25 1.27 Dry Molecular Weight, lb/lb-Mole 30.13 30.13 30.09 30.117 Wet Molecular weight, lb/lb-Mole 28.64 28.57 28.59 28.600 Flue Gas Static Pressure, inches of H2O 0.05 0.05 0.05 0.050 Absolute Flue Gas Pressure, inches of Mercury 29.90 29.90 29.90 29.900 Average Stack Gas Temperature, °F 354.17 357.71 358.17 356.683 Average Velocity Head, inches of H2O 0.5871343392 42741 0.593452660

6036190.6297239915

08873 0.603
Average Stack Gas Velocity, feet/second 53.65 54.12 55.75 54.507 Stack Cross-Sectional Area, square feet 70.497 70.497 70.497 70.497 Dry Volumetric Flow Rate, dry scfm 129,023.3 128,777.7 133,174.8130,325.267 Actual Wet Volumetric Flue Gas Flow Rate, acfm 226,929.8 228,917.9 235,812.5230,553.400 Percent Isokinetic of Sampling Rate, % 101.5 101.0 101.2 101.233 Percent Excess Air, % 40.8 40.7 40.8 40.767 F-Factor, dscfm/MMBtu @ %O2 9688 9258 9305 9,417.000 Round Duct Diameter, inches 113.69 113.69 113.69 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw Fc



### Wednesday, July 06, 2011 Page 16 of 19

### Emissions Testing Unit 1

Location stack - Method 6C Average Run Number 1 2 3 Test Date 1/21/2011 1/21/2011 1/21/2011 Run Start Time 10:01:00 AM 1:01:00 PM 3:47:00 PM Run Finish Time 12:01:00 PM 3:01:00 PM 5:47:00 PM Carbon Dioxide, % 11.65 11.69 11.65 11.663 Oxygen, % 6.24 6.22 6.28 6.247 Fuel Factor 1.26 1.26 1.25 Dry Volumetric Flow Rate, dry scfm 137514 137514 133190136,072.667 F-Factor, dscfm/MMBtu @ %O2 9305 9305 9305 9,305.000 Moisture, % 12.12 12.12 12.43 12.223 Analyzer Make Analyzer Model Analyzer Serial Number Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 3 3 3 3.000 Calibration Pre Zero Cylinder ID Nitrogen Nitrogen Nitrogen Calibration Pre Zero Cylinder Instrument Response -1 0 1 0.000 Calibration Pre Zero Cylinder Bias 0.11 0.17 0.33 0.203 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID SO2- CC207182- Diluted1 SO2-

CC207182- Diluted1 SO2-

CC207182- Diluted1 Calibration Pre High Cylinder Instrument Response 897.47 894.17 896.03 895.890 Calibration Pre High Cylinder Bias -1.16 -1.21 -0.79 -1.053 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Nitrogen Nitrogen Nitrogen Calibration Post Zero Cylinder Instrument Response 0 1 0 0.333 Calibration Post Zero Cylinder Bias 0.22 0.28 0.22 0.240 Calibration Post Zero Cylinder Drift 0.11 0.11 0.11 0.110 Calibration Post High Cylinder ID SO2- CC207182- Diluted1 SO2-

CC207182- Diluted1 SO2-

CC207182- Diluted1 Calibration Post High Cylinder Instrument Response 894.17 896.03 893.67 894.623 Calibration Post High Cylinder Bias -1.52 -1.01 -1.05 -1.193 Calibration Post High Cylinder Drift 0.36 0.2 0.26 0.273 Cavg 661.19 652.73 650.11 654.677 Cavg Units ppmvd ppmvd ppmvd Cgas 667.7287 659.4478 656.9824 661.386 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw Fc Cgasw 0 0 0 0.000 Cgasw Units



### Wednesday, July 06, 2011 Page 17 of 19

### Emissions Testing Unit 1

Location stack - Method 7E Average Run Number 1 2 3 Test Date 1/21/2011 1/21/2011 1/21/2011 Run Start Time 10:01:00 AM 1:01:00 PM 3:47:00 PM Run Finish Time 12:01:00 PM 3:01:00 PM 5:47:00 PM Carbon Dioxide, % 11.65 11.69 11.65 11.663 Oxygen, % 6.24 6.22 6.28 6.247 Fuel Factor 1.26 1.26 1.25 Dry Volumetric Flow Rate, dry scfm 137514 137514 133190136,072.667 F-Factor, dscfm/MMBtu @ %O2 9305 9305 9305 9,305.000 Moisture, % 12.12 12.12 12.43 12.223 Analyzer Make CAI Model CAI Model Analyzer Model 600 600 600.000 Analyzer Serial Number Operating Range 0 0 0 0.000 Operating Units No. Readings/Avg. 0 0 0 0.000 Calibration Set 4 4 4 4.000 Calibration Pre Zero Cylinder ID Nitrogen Nitrogen Nitrogen Calibration Pre Zero Cylinder Instrument Response 1 1 2 1.333 Calibration Pre Zero Cylinder Bias 0 0 0.11 0.037 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID NOxCC199835- Diluted1 NOxCC199835- Diluted1 NOxCC199835- Diluted1 Calibration Pre High Cylinder Instrument Response 452 455 452.92 453.307 Calibration Pre High Cylinder Bias -0.78 -0.45 -0.68 -0.637 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Nitrogen Nitrogen Nitrogen Calibration Post Zero Cylinder Instrument Response 1 2 1 1.333 Calibration Post Zero Cylinder Bias 0 0.11 0 0.037 Calibration Post Zero Cylinder Drift 0 0.11 0.11 0.073 Calibration Post High Cylinder ID NOxCC199835- Diluted1 NOxCC199835- Diluted1 NOxCC199835- Diluted1 Calibration Post High Cylinder Instrument Response 455 452.92 455.5 454.473 Calibration Post High Cylinder Bias -0.45 -0.68 -0.4 -0.510 Calibration Post High Cylinder Drift 0.33 0.23 0.28 0.280 Cavg 308.77 304.52 302.07 305.120 Cavg Units ppmvd ppmvd ppmvd Cgas 308.4502 303.7165 301.0945 304.420 Cgas Units ppmvd ppmvd ppmvd Fuel Type Override Override Override Fw Fc Cgasw 0 0 0 0.000 Cgasw Units



### Wednesday, July 06, 2011 Page 18 of 19

### Emissions Testing Unit 1

Location stack - OTM - 27/28 Average Run Number 2 3 4 Test Date 1/19/2011 1/20/2011 1/21/2011 Run Start Time 7:40:00 AM 7:31:00 AM 9:06:00 AM Run Finish Time 2:17:00 PM 2:48:00 PM 3:37:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 364.7141317 368.2644781 371.5 Nozzle Diameter, inches 0.186 0.186 0.186 0.186 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990 Barometric Pressure, inches of Mercury 29.9 29.9 29.9 29.900 Average Orifice Meter Differential, inches H2O 0.50 0.50 0.49 0.497 Dry Gas Meter Volume Sampled, cubic feet 130.696 135.406 137.200 134.434 Average Dry Gas Meter Temperature, °F 93.79 90.83 92.54 92.387 Dry Gas Meter Volume Sampled, dscf 123.433 128.568 129.865 127.289 Total Moisture Liquid collected, g 360.4 386.9 380.2 375.833 Volume of Water Vapor, standard cubic feet 16.96 18.21 17.90 17.690 Moisture Content of Stack Gas, % 12.08 12.41 12.11 12.200 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8792 0.8759 0.8789 0.878 Carbon Dioxide, % 11.76 11.74 11.67 11.723 Oxygen, % 6.28 6.26 6.23 6.257 Carbon Monoxide & Nitrogen, % 81.96 82 82.1 82.020 Fuel Factor 1.24 1.25 1.26 Dry Molecular Weight, lb/lb-Mole 30.13 30.13 30.12 30.127 Wet Molecular weight, lb/lb-Mole 28.66 28.62 28.65 28.643 Flue Gas Static Pressure, inches of H2O 0.05 0.05 0.05 0.050 Absolute Flue Gas Pressure, inches of Mercury 29.90 29.90 29.90 29.900 Average Stack Gas Temperature, °F 349.25 353.92 356.00 353.057 Average Velocity Head, inches of H2O 0.6466074894 87560.659257694

9459860.6712826861

25964 0.659
Average Stack Gas Velocity, feet/second 56.12 56.86 57.42 56.800 Stack Cross-Sectional Area, square feet 70.497 70.497 70.497 70.497 Dry Volumetric Flow Rate, dry scfm 136,078.0 136,566.8 138,031.4136,892.067 Actual Wet Volumetric Flue Gas Flow Rate, acfm 237,377.5 240,507.6 242,876.3240,253.800 Percent Isokinetic of Sampling Rate, % 92.9 95.5 94.6 94.333 Percent Excess Air, % 40.9 40.7 40.3 40.633 F-Factor, dscfm/MMBtu @ %O2 9688 9258 9305 9,417.000 Round Duct Diameter, inches 113.69 113.69 113.69 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw Fc



### Wednesday, July 06, 2011 Page 19 of 19