### 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.

Friday, January 14, 2011 Page 1 of 33

### Facility Information:

AES Hawaii, INC 91-086 Kaomi Loop

Kapolei HI 96707 Contact: Sabrina Guanio Phone: (808) 682-3412 Fax: Email: Sabrina.Guanio@aes.com Testing Company: URS Corporation
1600 Perimeter Park
Suite 400
Morrisville NC 27560 Contact: Brad Justus Phone: 919-461-1326 Fax: 919-461-1415 Email: Brad_Justus@urscorp.com

Air Permit Number: 10673 Permitted Source ID/Name: BLRA BLRA 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: 198 MW, circulating fluidized bed combustor, selective non-catalytic reduction, and a baghouse Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: FRS #: 110037260923

SCC / Description 10100218 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous Coal - Atmospheric Fluidized Bed Combustion: Circulating Bed (Bitum. 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 0 235 59 6 0 5 109 127.5

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



### Friday, January 14, 2011 Page 2 of 331,2,3,7,8,9-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 3 375 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Filterable PM2.5 OTM - 27/28 3 375 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Organic Condensible

Particulate OTM - 27/28 3 375 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit



### Friday, January 14, 2011 Page 3 of 33

### 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 3 375 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Total Particulate OTM - 27/28 3 375 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Filterable Particulate OTM - 27/28 3 375 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 3 240 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



### Friday, January 14, 2011 Page 4 of 33

### 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



### Friday, January 14, 2011 Page 5 of 33

### Location Stack Exit - Method 26A Average

Run Number 1 2 3
Test Date 4/5/2010 4/6/2010 4/7/2010 Run Start Time 2:03:00 PM 7:25:00 AM 2:06:00 PM

Run Finish Time 5:10:00 PM 10:30:00 AM 5:11:00 PM

Net Run Time, minutes 180 180 180 Dry Gas Meter Volume Sampled, dscf 129.193 122.721 125.634 125.849 Moisture Content of Stack Gas, % 9.36 9.63 9.74 9.577 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 14.3 14.3 14.2 14.267 Oxygen, % 5.4 5.4 5.5 5.433 Average Stack Gas Temperature, °F 299.13 296.67 300.37 298.723 Dry Volumetric Flow Rate, dry scfm 232,722.3 227,885.0 234,540.6 231,715.967 Actual Wet Volumetric Flue Gas Flow Rate, acfm 384,437.9 377,662.9 388,491.4 383,530.733 Percent Isokinetic of Sampling Rate, % 106.5 103.3 102.8 104.200 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



### Friday, January 14, 2011 Page 6 of 33

### 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



### Friday, January 14, 2011 Page 7 of 33

### 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



### Friday, January 14, 2011 Page 8 of 33

### 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



### Friday, January 14, 2011 Page 9 of 33

### 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



### Friday, January 14, 2011 Page 10 of 33

### Emissions Summary



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 gr/dscf 1.83E-02 1.59E-02 1.60E-02 0.017 lb/mmBtuO2 3.41E-02 2.97E-02 2.98E-02 0.031 mg/dscm 4.18E+01 3.63E+01 3.66E+01 38.233 ppm 3.59E+01 3.12E+01 3.15E+01 32.867 ppm@7%O2 3.19E+01 2.78E+01 2.79E+01 29.200



### Location: Stack Exit - Method 25A 

### Compound: Total organic compounds (TOC) as Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.000 gr/dscf 2.42E-04 2.46E-04 2.33E-04 0.000 lb/mmBtuO2 4.51E-04 4.59E-04 4.33E-04 0.000 mg/dscm 5.53E-01 5.62E-01 5.32E-01 0.549 ppm 3.02E-01 3.07E-01 2.90E-01 0.300 ppm@7%O2 2.68E-01 2.73E-01 2.57E-01 0.266



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 13.37 12.355 11.801 12.509 Elb/hr 3.19E+00 3.03E+00 2.91E+00 3.043 lb/mmBtuO2 3.01E-03 2.93E-03 2.75E-03 0.003 mg/dscm 3.66E+00 3.56E+00 3.32E+00 3.513 mg/dscm@7%O2 3.28E+00 3.19E+00 3.00E+00 3.157 

### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 0.279 0.26 0.266 0.268 Elb/hr 6.65E-02 6.39E-02 6.57E-02 0.065 lb/mmBtuO2 6.28E-05 6.16E-05 6.20E-05 0.000 mg/dscm 7.63E-02 7.48E-02 7.48E-02 0.075 mg/dscm@7%O2 6.84E-02 6.71E-02 6.75E-02 0.068



### Location: Stack Exit - Method 29 Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.0000054 0.0000354 0.000055 0.000 Elb/hr 9.76E-07 6.49E-06 1.03E-05 0.000 lb/mmBtuO2 9.35E-10 6.12E-09 9.82E-09 0.000 mg/dscm 1.14E-06 7.43E-06 1.19E-05 0.000 mg/dscm@7%O2 1.02E-06 6.66E-06 1.07E-05 0.000


### Friday, January 14, 2011 Page 11 of 33

### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.00015 0.00015 0.00015 0.000 Elb/hr 2.71E-05 2.75E-05 2.81E-05 0.000 lb/mmBtuO2 2.60E-08 2.59E-08 2.68E-08 0.000 mg/dscm 3.15E-05 3.15E-05 3.25E-05 0.000 mg/dscm@7%O2 2.82E-05 2.82E-05 2.91E-05 0.000 

### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.000024 0.000024 0.000024 0.000 Elb/hr 4.34E-06 4.40E-06 4.50E-06 0.000 lb/mmBtuO2 4.15E-09 4.15E-09 4.29E-09 0.000 mg/dscm 5.05E-06 5.04E-06 5.21E-06 0.000 mg/dscm@7%O2 4.53E-06 4.52E-06 4.67E-06 0.000 

### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.000086 0.000122 0.000069 0.000 Elb/hr 1.55E-05 2.24E-05 1.29E-05 0.000 lb/mmBtuO2 1.49E-08 2.11E-08 1.23E-08 0.000 mg/dscm 1.81E-05 2.56E-05 1.50E-05 0.000 mg/dscm@7%O2 1.62E-05 2.30E-05 1.35E-05 0.000 

### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.19867 0.00469 0.00207 0.068 Elb/hr 3.59E-02 8.59E-04 3.88E-04 0.012 lb/mmBtuO2 3.44E-05 8.11E-07 3.70E-07 0.000 mg/dscm 4.18E-02 9.85E-04 4.49E-04 0.014 mg/dscm@7%O2 3.75E-02 8.83E-04 4.03E-04 0.013 

### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.000909 0.000249 0.000123 0.000 Elb/hr 1.64E-04 4.56E-05 2.31E-05 0.000 lb/mmBtuO2 1.57E-07 4.30E-08 2.20E-08 0.000 mg/dscm 1.91E-04 5.23E-05 2.67E-05 0.000 mg/dscm@7%O2 1.71E-04 4.69E-05 2.39E-05 0.000 

### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 11 4.4 3.2 6.200 Elb/hr 1.99E+00 8.06E-01 6.00E-01 1.132 lb/mmBtuO2 1.90E-03 7.61E-04 5.71E-04 0.001 mg/dscm 2.31E+00 9.24E-01 6.94E-01 1.309 mg/dscm@7%O2 2.07E+00 8.29E-01 6.22E-01 1.174


### Friday, January 14, 2011 Page 12 of 33

### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.00058 0.00225 0.00162 0.001 Elb/hr 1.05E-04 4.12E-04 3.04E-04 0.000 lb/mmBtuO2 1.00E-07 3.89E-07 2.89E-07 0.000 mg/dscm 1.22E-04 4.73E-04 3.51E-04 0.000 mg/dscm@7%O2 1.09E-04 4.24E-04 3.15E-04 0.000 

### 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 0.008821 0.002031 0.000871 0.004 Elb/hr 1.59E-03 3.72E-04 1.63E-04 0.001 lb/mmBtuO2 1.53E-06 3.51E-07 1.56E-07 0.000 mg/dscm 1.86E-03 4.27E-04 1.89E-04 0.001 mg/dscm@7%O2 1.67E-03 3.83E-04 1.69E-04 0.001 

### 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 0.033693 0.006713 0.004633 0.015 Elb/hr 6.09E-03 1.23E-03 8.68E-04 0.003 lb/mmBtuO2 5.83E-06 1.16E-06 8.27E-07 0.000 mg/dscm 7.09E-03 1.41E-03 1.01E-03 0.003 mg/dscm@7%O2 6.36E-03 1.26E-03 9.06E-04 0.003 

### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 0.00026 0.00032 0.00033 0.000 Elb/hr 4.70E-05 5.86E-05 6.19E-05 0.000 lb/mmBtuO2 4.50E-08 5.53E-08 5.89E-08 0.000 mg/dscm 5.47E-05 6.72E-05 7.16E-05 0.000 mg/dscm@7%O2 4.91E-05 6.03E-05 6.42E-05 0.000


### Friday, January 14, 2011 Page 13 of 33

### Process Run Data



### Location: Stack Exit - OTM - 27/28 Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 2.5 7.7 2.1 4.100 lb/mmBtuO2 5.38E-04 1.70E-03 4.60E-04 0.001 

### Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 1.1 3.4 1 1.833 lb/mmBtuO2 2.37E-04 7.51E-04 2.19E-04 0.000 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 17.1 18.6 17.3 17.667 lb/mmBtuO2 3.68E-03 4.11E-03 3.79E-03 0.004 

### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 4.4 3.5 3.8 3.900 lb/mmBtuO2 9.47E-04 7.73E-04 8.33E-04 0.001 

### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 24 29.8 23.2 25.667 lb/mmBtuO2 5.17E-03 6.58E-03 5.08E-03 0.006 

### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 22.6 25.5 22.1 23.400 lb/mmBtuO2 4.86E-03 5.63E-03 4.84E-03 0.005



### Friday, January 14, 2011 Page 14 of 33

### Process Run Data



### Run Name Value UOM Comments Target Value 1 Bituminous Coal Burned 1087.3 Tons/hr 0


### 2 Bituminous Coal Burned 1089.6 Tons/hr 0
3 Bituminous Coal Burned 1095.4 Tons/hr 0
4 Bituminous Coal Burned 1079.8 Tons/hr 0


### 5 Bituminous Coal Burned 1093.6 Tons/hr 0
6 Bituminous Coal Burned 1095.3 Tons/hr 0
7 Bituminous Coal Burned 1079.8 Tons/hr 0


### 8 Bituminous Coal Burned 1081.1 Tons/hr 0
9 Bituminous Coal Burned 1080.6 Tons/hr 0
1 Average Heat Input 0 MMBtu/hr 0


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


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


### 8 Average Heat Input 0 MMBtu/hr 0
9 Average Heat Input 0 MMBtu/hr 0
1 Steam Output 669 1000 lb steam/hr 0


### 2 Steam Output 663.71 1000 lb steam/hr 0
3 Steam Output 666.76 1000 lb steam/hr 0
4 Steam Output 662.98 1000 lb steam/hr 0


### 5 Steam Output 667.07 1000 lb steam/hr 0
6 Steam Output 667.08 1000 lb steam/hr 0


### 7 Steam Output 671.3 1000 lb steam/hr 0
8 Steam Output 678.35 1000 lb steam/hr 0
9 Steam Output 679.47 1000 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



### Friday, January 14, 2011 Page 15 of 33

### 7 Synfuel Firing Rate 0 0



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


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


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


### 8 Petroleum Coke Firing Rate 0 0
9 Petroleum 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
4 Coal Gas Firing Rate 0 0


### 5 Coal Gas Firing Rate 0 0
6 Coal Gas Firing Rate 0 0
7 Coal Gas Firing Rate 0 0


### 8 Coal Gas Firing Rate 0 0
9 Coal Gas Firing Rate 0 0


### 1 Fuel Oil Firing Rate 0 0
2 Fuel Oil Firing Rate 0 0
3 Fuel Oil Firing Rate 0 0


### 4 Fuel Oil Firing Rate 0 0
5 Fuel Oil Firing Rate 0 0
6 Fuel Oil Firing Rate 0 0


### 7 Fuel Oil Firing Rate 0 0
8 Fuel Oil Firing Rate 0 0
9 Fuel Oil Firing Rate 0 0


### 1 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
7 Flue Gas Flow Rate 0 dscfm 0
8 Flue Gas Flow Rate 0 dscfm 0



### Friday, January 14, 2011 Page 16 of 33

### 9 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
7 Pressure Drop Across FGD (if applicable) 0 in H20 0
8 Pressure Drop Across FGD (if applicable) 0 in H20 0


### 9 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
7 FGD Scrubber Liquor pH 0 pH 0


### 8 FGD Scrubber Liquor pH 0 pH 0
9 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


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


### 9 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

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



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

9 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



### Friday, January 14, 2011 Page 17 of 33

### 6 Flue Gas Oxygen Content 0 % 0



### 7 Flue Gas Oxygen Content 0 % 0
8 Flue Gas Oxygen Content 0 % 0
9 Flue Gas Oxygen Content 0 % 0


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


### 6 Flue Gas Carbon Dioxide Content 0 % 0
7 Flue Gas Carbon Dioxide Content 0 % 0
8 Flue Gas Carbon Dioxide Content 0 % 0


### 9 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
7 Flue Gas Moisture Content 0 % 0


### 8 Flue Gas Moisture Content 0 % 0
9 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
7 Flue Gas Sampling Point Temperature 0 Deg F 0
8 Flue Gas Sampling Point Temperature 0 Deg F 0


### 9 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
7 Flue Gas Pressure 0 atm 0


### 8 Flue Gas Pressure 0 atm 0
9 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



### Friday, January 14, 2011 Page 18 of 33

### APCD Run Data

Process Lab Run Data 7 Standard Pressure 0 atm 0


### 8 Standard Pressure 0 atm 0
9 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


### 7 Standard Temperature 0 Deg F 0
8 Standard Temperature 0 Deg F 0
9 Standard Temperature 0 Deg F 0


### 1 Unit Gross Electrical Output 197.1 MW 0
4 Unit Gross Electrical Output 197.37 MW 0
5 Unit Gross Electrical Output 196.69 MW 0


### 6 Unit Gross Electrical Output 197.07 MW 0
7 Unit Gross Electrical Output 196.96 MW 0
8 Unit Gross Electrical Output 196.89 MW 0


### 9 Unit Gross Electrical Output 196.76 MW 0
1 Unit Net Electric Generation 0 MWh 0
4 Unit Net Electric Generation 0 MWh 0


### 5 Unit Net Electric Generation 0 MWh 0
6 Unit Net Electric Generation 0 MWh 0


### 7 Unit Net Electric Generation 0 MWh 0
8 Unit Net Electric Generation 0 MWh 0
9 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments Target Value 

### 1 SELECTIVE NONCATALYTIC REDUCTION FOR NOX 0 0

1 BAGHOUSE 0 0


### 1 desription in section 5a. 0 0

Run Name Value UOM Comments 1 Fuel Higher Heating Value 12179 Btu/lb 2 Fuel Higher Heating Value 11962 Btu/lb



### Friday, January 14, 2011 Page 19 of 33

### 3 Fuel Higher Heating Value 12096 Btu/lb



### 4 Fuel Higher Heating Value 11905 Btu/lb 5 Fuel Higher Heating Value 12032 Btu/lb 6 Fuel Higher Heating Value 12231 Btu/lb 7 Fuel Higher Heating Value 11863 Btu/lb 

### 8 Fuel Higher Heating Value 11812 Btu/lb 9 Fuel Higher Heating Value 11795 Btu/lb 1 Fuel Moisture 14 % 

### 2 Fuel Moisture 14 % 3 Fuel Moisture 15 % 4 Fuel Moisture 15 % 5 Fuel Moisture 17 % 

### 6 Fuel Moisture 16 % 7 Fuel Moisture 16 % 8 Fuel Moisture 16 % 

### 9 Fuel Moisture 17 % 1 Fuel Mercury Content 0.040 ppm 2 Fuel Mercury Content 0.055 ppm 3 Fuel Mercury Content 0.067 ppm 

### 4 Fuel Mercury Content 0.044 ppm 5 Fuel Mercury Content 0.075 ppm 6 Fuel Mercury Content 0.055 ppm 

### 7 Fuel Mercury Content 0 ppm 8 Fuel Mercury Content 0 ppm 9 Fuel Mercury Content 0 ppm 1 Fuel Cadmium Content 0 ppm 

### 2 Fuel Cadmium Content 0 ppm 3 Fuel Cadmium Content 0 ppm 4 Fuel Cadmium Content 0 ppm 

### 5 Fuel Cadmium Content 0.49 ppm 6 Fuel Cadmium Content 0 ppm 7 Fuel Cadmium Content 0 ppm 8 Fuel Cadmium Content 0 ppm 

### 9 Fuel Cadmium Content 0 ppm 1 Ultimate/Proximate Analysis 0 2 Ultimate/Proximate Analysis 0 

### 3 Ultimate/Proximate Analysis 0 4 Ultimate/Proximate Analysis 0 5 Ultimate/Proximate Analysis 0 6 Ultimate/Proximate Analysis 0 

### 7 Ultimate/Proximate Analysis 0 8 Ultimate/Proximate Analysis 0 9 Ultimate/Proximate Analysis 0



### Friday, January 14, 2011 Page 20 of 33

### 1 Fuel Nickel Content 7.9 ppm



### 2 Fuel Nickel Content 8.1 ppm 3 Fuel Nickel Content 7.4 ppm 4 Fuel Nickel Content 7.7 ppm 5 Fuel Nickel Content 11 ppm 

### 6 Fuel Nickel Content 7.6 ppm 7 Fuel Nickel Content 0 ppm 8 Fuel Nickel Content 0 ppm 

### 9 Fuel Nickel Content 0 ppm 1 Fuel Arsenic Content 2.1 ppm 2 Fuel Arsenic Content 1.4 ppm 3 Fuel Arsenic Content 1.6 ppm 

### 4 Fuel Arsenic Content 1.6 ppm 5 Fuel Arsenic Content 1.7 ppm 6 Fuel Arsenic Content 1.7 ppm 

### 7 Fuel Arsenic Content 0 ppm 8 Fuel Arsenic Content 0 ppm 9 Fuel Arsenic Content 0 ppm 1 Fuel Chromium Content 5.3 ppm 

### 2 Fuel Chromium Content 6.9 ppm 3 Fuel Chromium Content 5.7 ppm 4 Fuel Chromium Content 5.3 ppm 

### 5 Fuel Chromium Content 7 ppm 6 Fuel Chromium Content 5.6 ppm 7 Fuel Chromium Content 0 ppm 8 Fuel Chromium Content 0 ppm 

### 9 Fuel Chromium Content 0 ppm 1 Fuel Beryllium Content 0.44 ppm 2 Fuel Beryllium Content 0.6 ppm 

### 3 Fuel Beryllium Content 0.6 ppm 4 Fuel Beryllium Content 0.4 ppm 5 Fuel Beryllium Content 0.7 ppm 6 Fuel Beryllium Content 0.6 ppm 

### 7 Fuel Beryllium Content 0 ppm 8 Fuel Beryllium Content 0 ppm 9 Fuel Beryllium Content 0 ppm 

### 1 Fuel Lead Content 3.8 ppm 2 Fuel Lead Content 4.3 ppm 3 Fuel Lead Content 3.9 ppm 4 Fuel Lead Content 4.3 ppm 

### 5 Fuel Lead Content 11 ppm 6 Fuel Lead Content 4.5 ppm 7 Fuel Lead Content 0 ppm



### Friday, January 14, 2011 Page 21 of 33

### 8 Fuel Lead Content 0 ppm



### 9 Fuel Lead Content 0 ppm 1 Fuel Manganese Content 39 ppm 2 Fuel Manganese Content 45 ppm 3 Fuel Manganese Content 57 ppm 

### 4 Fuel Manganese Content 37 ppm 5 Fuel Manganese Content 149 ppm 6 Fuel Manganese Content 44 ppm 

### 7 Fuel Manganese Content 0 ppm 8 Fuel Manganese Content 0 ppm 9 Fuel Manganese Content 0 ppm 1 Fuel Chlorine Content 74 ppm 

### 2 Fuel Chlorine Content 74 ppm 3 Fuel Chlorine Content 68 ppm 4 Fuel Chlorine Content 63 ppm 

### 5 Fuel Chlorine Content 67 ppm 6 Fuel Chlorine Content 63 ppm 7 Fuel Chlorine Content 63 ppm 8 Fuel Chlorine Content 62 ppm 

### 9 Fuel Chlorine Content 61 ppm 1 Fuel Fluorine Content 0 ppm 2 Fuel Fluorine Content 0 ppm 

### 3 Fuel Fluorine Content 0 ppm 4 Fuel Fluorine Content 0 ppm 5 Fuel Fluorine Content 0 ppm 6 Fuel Fluorine Content 0 ppm 

### 7 Fuel Fluorine Content 56 ppm 8 Fuel Fluorine Content 67 ppm 9 Fuel Fluorine Content 61 ppm



### Friday, January 14, 2011 Page 22 of 33

### 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



### Friday, January 14, 2011 Page 23 of 33

### 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



### Friday, January 14, 2011 Page 24 of 33

### Location Stack Exit - Method 26A Average

Run Number 1 2 3 Test Date 4/5/2010 4/6/2010 4/7/2010 Run Start Time 2:03:00 PM 7:25:00 AM 2:06:00 PM Run Finish Time 5:10:00 PM 10:30:00 AM 5:11:00 PM Net Traversing Points 31 31 31 Net Run Time, minutes 180 180 180 Nozzle Diameter, inches 0.226333333 0.226333333 0.226333333 0.226 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.994 0.994 0.994 0.994 Barometric Pressure, inches of Mercury 30.27 30.25 30.25 30.257 Average Orifice Meter Differential, inches H2O 1.50 0.93 0.98 1.137 Dry Gas Meter Volume Sampled, cubic feet 131.162 125.543 128.626 128.444 Average Dry Gas Meter Temperature, °F 81.03 84.05 84.55 83.210 Dry Gas Meter Volume Sampled, dscf 129.193 122.721 125.634 125.849 Total Moisture Liquid collected, g 283.4 277.8 287.8 283.000 Volume of Water Vapor, standard cubic feet 13.34 13.08 13.55 13.323 Moisture Content of Stack Gas, % 9.36 9.63 9.74 9.577 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9064 0.9037 0.9026 0.904 Carbon Dioxide, % 14.3 14.3 14.2 14.267 Oxygen, % 5.4 5.4 5.5 5.433 Carbon Monoxide & Nitrogen, % 80.3 80.3 80.3 80.300 Fuel Factor 1.08 1.08 1.08 Dry Molecular Weight, lb/lb-Mole 30.50 30.50 30.49 30.497 Wet Molecular weight, lb/lb-Mole 29.33 29.30 29.27 29.300 Flue Gas Static Pressure, inches of H2O -21 -22 -19.5 -20.833 Absolute Flue Gas Pressure, inches of Mercury 28.73 28.63 28.82 28.727 Average Stack Gas Temperature, °F 299.13 296.67 300.37 298.723 Average Velocity Head, inches of H2O 0.9488209474 22606 0.914494742

728271 0.968222668

83143 0.944
Average Stack Gas Velocity, feet/second 66.39 65.22 67.09 66.233 Stack Cross-Sectional Area, square feet 96.510 96.510 96.510 96.510 Dry Volumetric Flow Rate, dry scfm 232,722.3 227,885.0 234,540.6 231,715.967 Actual Wet Volumetric Flue Gas Flow Rate, acfm 384,437.9 377,662.9 388,491.4 383,530.733 Percent Isokinetic of Sampling Rate, % 106.5 103.3 102.8 104.200 Percent Excess Air, % 34.2 34.2 35.0 34.467 F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000 Round Duct Diameter, inches 0 0 0 Rectangular Duct Width, inches 109 109 109 Rectangular Duct Length, inches 127.5 127.5 127.5 Fw 10640 10640 10640 10,640.000 Fc 1800 1800 1800 1,800.000



### Friday, January 14, 2011 Page 25 of 33

### 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



### Friday, January 14, 2011 Page 26 of 33

### 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



### Friday, January 14, 2011 Page 27 of 33

### 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



### Friday, January 14, 2011 Page 28 of 33

### 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



### Friday, January 14, 2011 Page 29 of 33

### 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



### Friday, January 14, 2011 Page 30 of 33

### 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



### Friday, January 14, 2011 Page 31 of 33

### 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



### Friday, January 14, 2011 Page 32 of 33

### 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



### Friday, January 14, 2011 Page 33 of 33