### Name: Mark Mediros

Title: Principal Engineer Company: Taunton Municipal Light Plant Sign Date: 11/24/2010 Name: Michael Kelley Title: Project Manager Company: CK Environmental, Inc Sign Date: 11/24/2010 Permitted Facility Representative / Date Testing Company Representative / Date Final Test Report for

/ / Based on information and belief formed after reasonable inquiry, I certify that the statements and information in this test report are true, accurate, and complete. I have reviewed all testing details and results in this test report and hereby certify that the test report is authentic and accurate.

Saturday, February 26, 2011 Page 1 of 34

### 11/24/2010

Facility Information: Cleary Flood Station (TMLP)
1314 Somerset Avenue

Taunton MA 02780 Contact: Bill Lyons Phone: 508-824-3166 Fax: 508-822-3782 Email: williamlyons@tmlp.com Testing Company: CK Environmental, Inc. 1020 Turnpike Street
Suite #8
Canton MA 02021 Contact: Michael Kelley Phone: 781-828-5200 Fax: 781-828-5380 Email: mkelley@ckenvironmental.com

Air Permit Number: 01682 Permitted Source ID/Name: Unit #8 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: Unit No. 8 is a 398 MMBtu/hr Combustion Engineering wall fired boiler. It has a gross generating capacity of approximately 29 megawatts (MW). Unit No. 8 is a peaking unit which fires 1 percent sulfur residual oil and small amounts of distillate oil when needed. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: FRS #: 110024570533

SCC / Description 10100405 External Combustion Boilers - Electric Generation - Residual Oil - Grade 5 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 Exit 106 1054 384 2 106 6 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



### Saturday, February 26, 2011 Page 2 of 34

### 11/24/2010 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 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 organic compounds

(TOC) as Propane Method 25A 3 120 0 Stack Exit
Hydrogen Chloride Method 26A 3 60 0 Stack Exit Hydrogen Fluoride Method 26A 3 60 0 Stack Exit Hydrogen Fluoride Method 26 3 60 0 Stack Exit Hydrogen Chloride Method 26 3 60 0 Stack Exit Total PM2.5 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

Inorganic (Aqueous)

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

Organic Condensible

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

Cadmium Method 29 3 240 0 Stack Exit Copper Method 29 0 Stack Exit Silver Method 29 0 Stack Exit Chromium Method 29 3 240 0 Stack Exit Beryllium Method 29 3 240 0 Stack Exit Phosphorus (yellow or white) Method 29 0 Stack Exit Zinc Method 29 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit


### Saturday, February 26, 2011 Page 3 of 34

### 11/24/2010

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

Selenium Method 29 3 240 0 Stack Exit Nickel Method 29 3 240 0 Stack Exit Mercury Method 29 3 240 0 Stack Exit Manganese Method 29 3 240 0 Stack Exit Lead Method 29 3 240 0 Stack Exit Barium Method 29 0 Stack Exit Co2 Method 3A CO2 3 120 0 Stack Exit O2 Method 3A O2 3 120 0 Stack Exit Sulfur Dioxide Method 6C 3 120 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 120 0 Stack Exit



### Saturday, February 26, 2011 Page 4 of 34

### 11/24/2010

Sampling / Stack Data Results Summary



### Location Stack Exit - Method 0011 Average Run Number Run # 3 Run #1 Run #2
Test Date 9/24/2010 9/24/2010 9/24/2010 Run Start Time 12:19:00 PM 7:32:00 AM 9:51:00 AM

Run Finish Time 2:27:00 PM 9:41:00 AM 11:59:00 AM

Net Run Time, minutes 120 120 120 Dry Gas Meter Volume Sampled, dscf 67.508 67.385 66.171 67.021 Moisture Content of Stack Gas, % 6.34 7.67 8.40 7.470 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 10.3 9.5 9.5 9.767 Oxygen, % 8.9 8.9 8.9 8.900 Average Stack Gas Temperature, °F 254.63 254.63 254.83 254.697 Dry Volumetric Flow Rate, dry scfm 59,599.9 59,000.5 58,623.4 59,074.600 Actual Wet Volumetric Flue Gas Flow Rate, acfm 85,526.6 85,857.5 86,041.3 85,808.467 Percent Isokinetic of Sampling Rate, % 108.3 109.2 107.9 108.467 F-Factor, dscfm/MMBtu @ %O2 9203 9203 9203 9,203.000
Fw 0 0 0 0.000
Fc 1399 1399 1399 1,399.000



### 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



### Saturday, February 26, 2011 Page 5 of 34

### 11/24/2010

Location Stack Exit - Method 23 Average Run Number
Test Date Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Location Stack Exit - Method 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



### Saturday, February 26, 2011 Page 6 of 34

### 11/24/2010

Location Stack Exit - Method 26A Average Run Number
Test Date Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### 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



### Saturday, February 26, 2011 Page 7 of 34

### 11/24/2010

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 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



### Saturday, February 26, 2011 Page 8 of 34

### 11/24/2010

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



### Saturday, February 26, 2011 Page 9 of 34

### 11/24/2010

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



### Saturday, February 26, 2011 Page 10 of 34

### 11/24/2010

Emissions Summary



### Location: Stack Exit - Method 0011 Compound: Formaldehyde Average RunNumber Run #1 Run #2 Run # 3 Mass_mg 0.037 0.23 0.034 0.100 lb/mmBtuO2 1.94E-05 1.23E-04 1.78E-05 0.000 ppm 1.55E-02 9.83E-02 1.42E-02 0.043 ppm@7%O2 1.80E-02 1.14E-01 1.64E-02 0.049



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run Run #1 Run #2 Run #3 lb/mmBtuO2 5.61E-04 1.06E-03 3.13E-03 0.002 ppm 5.06E-01 9.50E-01 2.73E+00 1.395 ppm@7%O2 5.59E-01 1.06E+00 3.11E+00 1.576



### Location: Stack Exit - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.000000015 0.00000001 0.000000016 0.000 lb/mmBtuO2 2.15E-12 1.33E-12 2.22E-12 0.000 ng/dscm 2.20E-03 1.45E-03 2.38E-03 0.002 ng/dscm@7%O2 2.50E-03 1.54E-03 2.57E-03 0.002 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000004 0.000000021 0.000000023 0.000 lb/mmBtuO2 5.74E-12 2.79E-12 3.20E-12 0.000 ng/dscm 5.86E-03 3.04E-03 3.42E-03 0.004 ng/dscm@7%O2 6.65E-03 3.23E-03 3.70E-03 0.005 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000000087 0.0000000048 0.0000000028 0.000 lb/mmBtuO2 1.25E-12 6.38E-13 3.89E-13 0.000 ng/dscm 1.27E-03 6.95E-04 4.17E-04 0.001 ng/dscm@7%O2 1.44E-03 7.39E-04 4.51E-04 0.001 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000000018 0.0000000019 0.000000002 0.000 lb/mmBtuO2 2.58E-13 2.52E-13 2.78E-13 0.000 ng/dscm 2.64E-04 2.75E-04 2.98E-04 0.000 ng/dscm@7%O2 3.00E-04 2.92E-04 3.22E-04 0.000



### Saturday, February 26, 2011 Page 11 of 34

### 11/24/2010

Compound: 1,2,3,4,7,8-HxCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000000022 0.000000008 0.000000008 0.000 lb/mmBtuO2 3.16E-13 1.06E-12 1.11E-12 0.000 ng/dscm 3.22E-04 1.16E-03 1.19E-03 0.001 ng/dscm@7%O2 3.65E-04 1.23E-03 1.29E-03 0.001 

### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000000016 0.0000000017 0.0000000019 0.000 lb/mmBtuO2 2.30E-13 2.26E-13 2.64E-13 0.000 ng/dscm 2.34E-04 2.46E-04 2.83E-04 0.000 ng/dscm@7%O2 2.66E-04 2.61E-04 3.06E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.000000004 0.000000003 0.0000000031 0.000 lb/mmBtuO2 5.74E-13 3.99E-13 4.31E-13 0.000 ng/dscm 5.86E-04 4.34E-04 4.61E-04 0.000 ng/dscm@7%O2 6.65E-04 4.61E-04 4.98E-04 0.001 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000000016 0.0000000033 0.000000002 0.000 lb/mmBtuO2 2.30E-13 4.38E-13 2.78E-13 0.000 ng/dscm 2.34E-04 4.78E-04 2.98E-04 0.000 ng/dscm@7%O2 2.66E-04 5.08E-04 3.22E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000000019 0.0000000024 0.0000000019 0.000 lb/mmBtuO2 2.73E-13 3.19E-13 2.64E-13 0.000 ng/dscm 2.78E-04 3.47E-04 2.83E-04 0.000 ng/dscm@7%O2 3.15E-04 3.69E-04 3.06E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000000024 0.0000000019 0.0000000016 0.000 lb/mmBtuO2 3.44E-13 2.52E-13 2.22E-13 0.000 ng/dscm 3.51E-04 2.75E-04 2.38E-04 0.000 ng/dscm@7%O2 3.98E-04 2.92E-04 2.57E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.000000003 0.0000000018 0.000000002 0.000 lb/mmBtuO2 4.31E-13 2.39E-13 2.78E-13 0.000



### Saturday, February 26, 2011 Page 12 of 34

### 11/24/2010 ng/dscm 4.39E-04 2.61E-04 2.98E-04 0.000 ng/dscm@7%O2 4.98E-04 2.77E-04 3.22E-04 0.000 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000002 0.00000015 0.00000017 0.000 lb/mmBtuO2 2.87E-11 1.99E-11 2.36E-11 0.000 ng/dscm 2.93E-02 2.17E-02 2.53E-02 0.025 ng/dscm@7%O2 3.32E-02 2.31E-02 2.73E-02 0.028 

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000014 0.00000012 0.00000013 0.000 lb/mmBtuO2 2.01E-11 1.59E-11 1.81E-11 0.000 ng/dscm 2.05E-02 1.74E-02 1.93E-02 0.019 ng/dscm@7%O2 2.33E-02 1.85E-02 2.09E-02 0.021 

### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000013 0.00000018 0.0000002 0.000 lb/mmBtuO2 1.87E-11 2.39E-11 2.78E-11 0.000 ng/dscm 1.90E-02 2.61E-02 2.98E-02 0.025 ng/dscm@7%O2 2.16E-02 2.77E-02 3.22E-02 0.027 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000014 0.00000012 0.00000013 0.000 lb/mmBtuO2 2.01E-11 1.59E-11 1.81E-11 0.000 ng/dscm 2.05E-02 1.74E-02 1.93E-02 0.019 ng/dscm@7%O2 2.33E-02 1.85E-02 2.09E-02 0.021 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000011 0.0000001 0.0000001 0.000 lb/mmBtuO2 1.58E-11 1.33E-11 1.39E-11 0.000 ng/dscm 1.61E-02 1.45E-02 1.49E-02 0.015 ng/dscm@7%O2 1.83E-02 1.54E-02 1.61E-02 0.017 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000045 0.00000056 0.00000067 0.000 lb/mmBtuO2 6.46E-11 7.44E-11 9.31E-11 0.000 ng/dscm 6.59E-02 8.11E-02 9.97E-02 0.082 ng/dscm@7%O2 7.48E-02 8.62E-02 1.08E-01 0.090 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber Run #1 Run #2 Run #3


### Saturday, February 26, 2011 Page 13 of 34

### 11/24/2010 Mass_mg 0.00000011 0.00000011 0.0000001 0.000 lb/mmBtuO2 1.58E-11 1.46E-11 1.39E-11 0.000 ng/dscm 1.61E-02 1.59E-02 1.49E-02 0.016 ng/dscm@7%O2 1.83E-02 1.69E-02 1.61E-02 0.017 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.000000007 0.000000006 0.000000005 0.000 lb/mmBtuO2 1.00E-12 7.97E-13 6.95E-13 0.000 ng/dscm 1.02E-03 8.68E-04 7.44E-04 0.001 ng/dscm@7%O2 1.16E-03 9.22E-04 8.04E-04 0.001 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000000069 0.000000006 0.0000000064 0.000 lb/mmBtuO2 9.90E-13 7.97E-13 8.89E-13 0.000 ng/dscm 1.01E-03 8.68E-04 9.52E-04 0.001 ng/dscm@7%O2 1.15E-03 9.22E-04 1.03E-03 0.001 

### Compound: 2,3,7,8-TCDD Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000000026 0.0000000038 0.0000000024 0.000 lb/mmBtuO2 3.73E-13 5.05E-13 3.33E-13 0.000 ng/dscm 3.81E-04 5.50E-04 3.57E-04 0.000 ng/dscm@7%O2 4.32E-04 5.84E-04 3.86E-04 0.000 

### Compound: 2,3,7,8-TCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.000000007 0.000000006 0.0000000049 0.000 lb/mmBtuO2 1.00E-12 7.97E-13 6.81E-13 0.000 ng/dscm 1.02E-03 8.68E-04 7.29E-04 0.001 ng/dscm@7%O2 1.16E-03 9.22E-04 7.88E-04 0.001 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000014 0.00000013 0.00000014 0.000 lb/mmBtuO2 2.01E-11 1.73E-11 1.94E-11 0.000 ng/dscm 2.05E-02 1.88E-02 2.08E-02 0.020 ng/dscm@7%O2 2.33E-02 2.00E-02 2.25E-02 0.022 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000011 0.00000011 0.0000001 0.000 lb/mmBtuO2 1.58E-11 1.46E-11 1.39E-11 0.000 ng/dscm 1.61E-02 1.59E-02 1.49E-02 0.016 ng/dscm@7%O2 1.83E-02 1.69E-02 1.61E-02 0.017



### Saturday, February 26, 2011 Page 14 of 34

### 11/24/2010

Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000014 0.00000013 0.00000017 0.000 lb/mmBtuO2 2.01E-11 1.73E-11 2.36E-11 0.000 ng/dscm 2.05E-02 1.88E-02 2.53E-02 0.022 ng/dscm@7%O2 2.33E-02 2.00E-02 2.73E-02 0.024 

### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00000013 0.00000012 0.00000016 0.000 lb/mmBtuO2 1.87E-11 1.59E-11 2.22E-11 0.000 ng/dscm 1.90E-02 1.74E-02 2.38E-02 0.020 ng/dscm@7%O2 2.16E-02 1.85E-02 2.57E-02 0.022 

### Compound: OCDD Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.000000077 0.000000068 0.00000006 0.000 lb/mmBtuO2 1.10E-11 9.03E-12 8.34E-12 0.000 ng/dscm 1.13E-02 9.84E-03 8.93E-03 0.010 ng/dscm@7%O2 1.28E-02 1.05E-02 9.65E-03 0.011 

### Compound: OCDF Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.000000015 0.000000017 0.000000014 0.000 lb/mmBtuO2 2.15E-12 2.26E-12 1.94E-12 0.000 ng/dscm 2.20E-03 2.46E-03 2.08E-03 0.002 ng/dscm@7%O2 2.50E-03 2.61E-03 2.25E-03 0.002 

### Compound: Total Dioxins Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0000001247 0.0000001055 0.0000001 0.000 lb/mmBtuO2 1.79E-11 1.40E-11 1.39E-11 0.000 ng/dscm 1.83E-02 1.53E-02 1.49E-02 0.016 ng/dscm@7%O2 2.08E-02 1.63E-02 1.61E-02 0.018 

### Compound: Total Furans Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.000000124 0.000000087 0.000000066 0.000 lb/mmBtuO2 1.78E-11 1.16E-11 9.17E-12 0.000 ng/dscm 1.82E-02 1.26E-02 9.82E-03 0.014 ng/dscm@7%O2 2.07E-02 1.34E-02 1.06E-02 0.015



### Location: Stack Exit - Method 25A 

### Compound: Total organic compounds (TOC) as Average Run Run #1 Run #2 Run #3 lb/mmBtuO2 9.65E-03 8.01E-03 8.02E-03 0.009


### Saturday, February 26, 2011 Page 15 of 34

### 11/24/2010

ppm 5.48E+00 4.59E+00 4.60E+00 4.890 ppm@7%O2 6.10E+00 5.06E+00 5.07E+00 5.410



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber Run #1 Run #2 Run #3 Mass_mg 1.9 0.68 0.76 1.113 Elb/hr 1.68E-01 1.84E-01 1.96E-01 0.183 lb/mmBtuO2 7.75E-04 8.79E-04 8.81E-04 0.001 mg/dscm 8.15E-01 9.15E-01 9.32E-01 0.887 mg/dscm@7%O2 8.97E-01 1.02E+00 1.02E+00 0.979 

### Compound: Hydrogen Fluoride Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.25 0.2 0.2 0.217 Elb/hr 2.21E-02 5.40E-02 5.16E-02 0.043 lb/mmBtuO2 1.02E-04 2.59E-04 2.32E-04 0.000 mg/dscm 1.07E-01 2.69E-01 2.45E-01 0.207 mg/dscm@7%O2 1.18E-01 2.99E-01 2.68E-01 0.228



### Location: Stack Exit - Method 29 Compound: Arsenic Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.01004 0.01082 0.01183 0.011 Elb/hr 6.35E-04 6.78E-04 7.50E-04 0.001 lb/mmBtuO2 3.13E-06 3.13E-06 3.62E-06 0.000 mg/dscm 3.31E-03 3.28E-03 3.70E-03 0.003 mg/dscm@7%O2 3.62E-03 3.62E-03 4.19E-03 0.004 

### Compound: Barium Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.143 0.155 0.1125 0.137 Elb/hr 9.04E-03 9.71E-03 7.13E-03 0.009 lb/mmBtuO2 4.46E-05 4.49E-05 3.44E-05 0.000 mg/dscm 4.72E-02 4.70E-02 3.52E-02 0.043 mg/dscm@7%O2 5.16E-02 5.19E-02 3.99E-02 0.048 

### Compound: Beryllium Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0012 0.0012 0.0012 0.001 Elb/hr 7.59E-05 7.52E-05 7.61E-05 0.000 lb/mmBtuO2 3.74E-07 3.47E-07 3.67E-07 0.000 mg/dscm 3.96E-04 3.64E-04 3.75E-04 0.000 mg/dscm@7%O2 4.33E-04 4.02E-04 4.25E-04 0.000 

### Compound: Cadmium Average RunNumber Run #1 Run #2 Run #3


### Saturday, February 26, 2011 Page 16 of 34

### 11/24/2010 Mass_mg 0.00137 0.00161 0.00144 0.001 Elb/hr 8.67E-05 1.01E-04 9.13E-05 0.000 lb/mmBtuO2 4.27E-07 4.66E-07 4.41E-07 0.000 mg/dscm 4.52E-04 4.89E-04 4.50E-04 0.000 mg/dscm@7%O2 4.94E-04 5.40E-04 5.10E-04 0.001 

### Compound: Chromium Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.028 0.0493 0.0349 0.037 Elb/hr 1.77E-03 3.09E-03 2.21E-03 0.002 lb/mmBtuO2 8.72E-06 1.43E-05 1.07E-05 0.000 mg/dscm 9.24E-03 1.50E-02 1.09E-02 0.012 mg/dscm@7%O2 1.01E-02 1.66E-02 1.24E-02 0.013 

### Compound: Copper Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0982 0.1026 0.1085 0.103 Elb/hr 6.21E-03 6.43E-03 6.88E-03 0.007 lb/mmBtuO2 3.06E-05 2.97E-05 3.32E-05 0.000 mg/dscm 3.24E-02 3.11E-02 3.39E-02 0.032 mg/dscm@7%O2 3.54E-02 3.43E-02 3.84E-02 0.036 

### Compound: Lead Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0427 0.062 0.0392 0.048 Elb/hr 2.70E-03 3.88E-03 2.48E-03 0.003 lb/mmBtuO2 1.33E-05 1.79E-05 1.20E-05 0.000 mg/dscm 1.41E-02 1.88E-02 1.23E-02 0.015 mg/dscm@7%O2 1.54E-02 2.08E-02 1.39E-02 0.017 

### Compound: Manganese Average RunNumber Run #1 Run #2 Run #3 Mass_mg 4.3008 0.0509 0.21 1.521 Elb/hr 2.72E-01 3.19E-03 1.33E-02 0.096 lb/mmBtuO2 1.34E-03 1.47E-05 6.43E-05 0.000 mg/dscm 1.42E+00 1.54E-02 6.57E-02 0.500 mg/dscm@7%O2 1.55E+00 1.70E-02 7.45E-02 0.547 

### Compound: Mercury Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.0003596 0.0003739 0.0003329 0.000 Elb/hr 2.27E-05 2.34E-05 2.11E-05 0.000 lb/mmBtuO2 1.12E-07 1.08E-07 1.02E-07 0.000 mg/dscm 1.19E-04 1.13E-04 1.04E-04 0.000 mg/dscm@7%O2 1.30E-04 1.25E-04 1.18E-04 0.000 

### Compound: Nickel Average RunNumber Run #1 Run #2 Run #3


### Saturday, February 26, 2011 Page 17 of 34

### 11/24/2010 Mass_mg 2.25 2.4132 2.245 2.303 Elb/hr 1.42E-01 1.51E-01 1.42E-01 0.145 lb/mmBtuO2 7.01E-04 6.98E-04 6.87E-04 0.001 mg/dscm 7.42E-01 7.32E-01 7.02E-01 0.725 mg/dscm@7%O2 8.11E-01 8.08E-01 7.96E-01 0.805 

### Compound: Phosphorus (yellow or white) Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.628 0.658 0.637 0.641 Elb/hr 3.97E-02 4.12E-02 4.04E-02 0.040 lb/mmBtuO2 1.96E-04 1.90E-04 1.95E-04 0.000 mg/dscm 2.07E-01 2.00E-01 1.99E-01 0.202 mg/dscm@7%O2 2.26E-01 2.21E-01 2.26E-01 0.224 

### Compound: Selenium Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.012 0.0127 0.0157 0.013 Elb/hr 7.59E-04 7.96E-04 9.95E-04 0.001 lb/mmBtuO2 3.74E-06 3.68E-06 4.81E-06 0.000 mg/dscm 3.96E-03 3.85E-03 4.91E-03 0.004 mg/dscm@7%O2 4.33E-03 4.25E-03 5.57E-03 0.005 

### Compound: Silver Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.00315 0.00333 0.00245 0.003 Elb/hr 1.99E-04 2.09E-04 1.55E-04 0.000 lb/mmBtuO2 9.81E-07 9.64E-07 7.50E-07 0.000 mg/dscm 1.04E-03 1.01E-03 7.66E-04 0.001 mg/dscm@7%O2 1.14E-03 1.12E-03 8.68E-04 0.001 

### Compound: Zinc Average RunNumber Run #1 Run #2 Run #3 Mass_mg 0.702 0.761 0.647 0.703 Elb/hr 4.44E-02 4.77E-02 4.10E-02 0.044 lb/mmBtuO2 2.19E-04 2.20E-04 1.98E-04 0.000 mg/dscm 2.32E-01 2.31E-01 2.02E-01 0.222 mg/dscm@7%O2 2.54E-01 2.55E-01 2.29E-01 0.246



### Location: Stack Exit - Method 6C Compound: Sulfur Dioxide Average Run Run #1 Run #2 Run #3 Elb/hr 1.88E+02 1.94E+02 1.79E+02 187.000 lb/mmBtuO2 8.75E-01 8.94E-01 8.67E-01 0.879 mg/dscm 9.11E+02 9.39E+02 8.83E+02 911.000 mg/dscm@7%O2 1.01E+03 1.03E+03 1.00E+03 1,013.333 ppm 3.42E+02 3.53E+02 3.31E+02 342.000 ppm@7%O2 3.81E+02 3.89E+02 3.77E+02 382.333



### Saturday, February 26, 2011 Page 18 of 34

### 11/24/2010

Process Run Data Location: Stack Exit - Method 7E 

### Compound: Nitrogen oxides (NOx) Average Run Run #1 Run #2 Run #3 Elb/hr 5.88E+01 5.93E+01 8.01E+01 66.067 lb/mmBtuO2 2.74E-01 2.73E-01 3.89E-01 0.312 mg/dscm 2.85E+02 2.87E+02 3.96E+02 322.667 mg/dscm@7%O2 3.17E+02 3.16E+02 4.50E+02 361.000 ppm 1.49E+02 1.50E+02 2.07E+02 168.667 ppm@7%O2 1.66E+02 1.65E+02 2.35E+02 188.667



### Location: Stack Exit - OTM - 27/28 Compound: Filterable PM2.5 Average RunNumber Run #1 Run #2 Run #3 Mass_mg 104.4 114.3 115.4 111.367 lb/mmBtuO2 3.59E-02 3.78E-02 3.90E-02 0.038 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber Run #1 Run #2 Run #3 Mass_mg 9.5 14 18 13.833 lb/mmBtuO2 3.27E-03 4.63E-03 6.08E-03 0.005 

### Compound: Organic Condensible Particulate Average RunNumber Run #1 Run #2 Run #3 Mass_mg 2.5 2.3 1.8 2.200 lb/mmBtuO2 8.61E-04 7.60E-04 6.08E-04 0.001 

### Compound: Total PM2.5 Average RunNumber Run #1 Run #2 Run #3 Mass_mg 116.4 130.6 135.2 127.400 lb/mmBtuO2 4.01E-02 4.32E-02 4.57E-02 0.043



### Saturday, February 26, 2011 Page 19 of 34

### 11/24/2010

Process Run Data



### Run Name Value UOM Comments Target Value 1 Residual Oil Burned 0 1000 Gallons/hr 0


### 2 Residual Oil Burned 0 1000 Gallons/hr 0
3 Residual Oil Burned 0 1000 Gallons/hr 0
1 Average Heat Input 168 MMBtu/hr Methods 29, 25A, 26A - 9/20/10 0



### 2 Average Heat Input 169 MMBtu/hr Methods 29, 23, 25A - 9/21/10 0

3 Average Heat Input 172 MMBtu/hr Methods OTM27/28, 23, 031, 10 - 9/22/10 0

1 Steam Output 0 1000 lb steam/hr 0


### 2 Steam Output 0 1000 lb steam/hr 0
3 Steam Output 0 1000 lb steam/hr 0
1 Synfuel Firing Rate 0 0


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


### 2 Coal Gas Firing Rate 0 0
3 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
1 Flue Gas Flow Rate 0 dscfm 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



### Saturday, February 26, 2011 Page 20 of 34

### 11/24/2010

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 0 MW 0


### 1 Unit Net Electric Generation 0 MWh 0
1 MW 0 MW 0
2 Flue Gas Flow Rate 0 dscfm 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 0 MW 0
2 Unit Net Electric Generation 0 MWh 0
2 MW 0 MW 0


### 3 Flue Gas Flow Rate 0 dscfm 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



### 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 0 MW 0
3 Unit Net Electric Generation 0 MWh 0



### Saturday, February 26, 2011 Page 21 of 34

### 11/24/2010

3 MW 0 MW 0


### 1 MW 15.6 MW Methods 29, 25A, 26A - 9/20/10 0

2 MW 15.6 MW Methods 29, 23, 25A - 9/21/10 0



### 3 MW 16 MW Methods OTM27/28, 23, 031, 10 - 9/22/10 0

4 Residual Oil Burned 0 1000 Gallons/hr 0
4 Average Heat Input 173 MMBtu/hr Methods OTM27/28, 23 - 9/23/10 0

4 Steam Output 0 1000 lb steam/hr 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 0 dscfm 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 0 MW 0


### 4 Unit Net Electric Generation 0 MWh 0
4 MW 0 MW 0
4 MW 16 MW Methods OTM27/28, 23 - 9/23/10 0

5 Residual Oil Burned 0 1000 Gallons/hr 0
5 Average Heat Input 186 MMBtu/hr Methods RCRA011, 10 - 9/24/10 0

5 Steam Output 0 1000 lb steam/hr 0
5 Synfuel Firing Rate 0 0



### Saturday, February 26, 2011 Page 22 of 34

### 11/24/2010

APCD Run Data

Process Lab Run Data 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 0 dscfm 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 0 MW 0
5 Unit Net Electric Generation 0 MWh 0
5 MW 0 MW 0


### 5 MW 16.1 MW Methods RCRA011, 10 - 9/24/10 0

Run Name Value UOM Comments Target Value 

### 1 List all emissions control devices in order of process flow. Choose from 0 0

1 drop down lists. If not on list add description and provide detailed 0 0



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

Run Name Value UOM Comments 1 See 4b Comments.(Refer to Fuel Analysis Spreadsheet) 0



### Saturday, February 26, 2011 Page 23 of 34

### 11/24/2010

Sampling / Stack Data Results Detail



### Location Stack Exit - Method 0011 Average Run Number Run # 3 Run #1 Run #2 Test Date 9/24/2010 9/24/2010 9/24/2010 Run Start Time 12:19:00 PM 7:32:00 AM 9:51:00 AM Run Finish Time 2:27:00 PM 9:41:00 AM 11:59:00 AM Net Traversing Points 24 24 24 Net Run Time, minutes 120 120 120 Nozzle Diameter, inches 0.313 0.313 0.313 0.313 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.0207 1.0207 1.0207 1.021 Barometric Pressure, inches of Mercury 30.12 30.13 30.12 30.123 Average Orifice Meter Differential, inches H2O 0.90 0.90 0.90 0.900 Dry Gas Meter Volume Sampled, cubic feet 65.018 64.176 63.679 64.291 Average Dry Gas Meter Temperature, °F 63.67 58.00 63.25 61.640 Dry Gas Meter Volume Sampled, dscf 67.508 67.385 66.171 67.021 Total Moisture Liquid collected, g 97 119 129 115.000 Volume of Water Vapor, standard cubic feet 4.57 5.60 6.07 5.413 Moisture Content of Stack Gas, % 6.34 7.67 8.40 7.470 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9366 0.9233 0.916 0.925 Carbon Dioxide, % 10.3 9.5 9.5 9.767 Oxygen, % 8.9 8.9 8.9 8.900 Carbon Monoxide & Nitrogen, % 80.8 81.6 81.6 81.333 Fuel Factor 1.17 1.26 1.26 Dry Molecular Weight, lb/lb-Mole 30.00 29.88 29.88 29.920 Wet Molecular weight, lb/lb-Mole 29.24 28.97 28.88 29.030 Flue Gas Static Pressure, inches of H2O 0.08 0.08 0.08 0.080 Absolute Flue Gas Pressure, inches of Mercury 30.13 30.14 30.13 30.133 Average Stack Gas Temperature, °F 254.63 254.63 254.83 254.697 Average Velocity Head, inches of H2O 0.1293322494 25224 0.129189130

210234 0.129233774

694275 0.129
Average Stack Gas Velocity, feet/second 23.26 23.35 23.40 23.337 Stack Cross-Sectional Area, square feet 61.283 61.283 61.283 61.283 Dry Volumetric Flow Rate, dry scfm 59,599.9 59,000.5 58,623.4 59,074.600 Actual Wet Volumetric Flue Gas Flow Rate, acfm 85,526.6 85,857.5 86,041.3 85,808.467 Percent Isokinetic of Sampling Rate, % 108.3 109.2 107.9 108.467 Percent Excess Air, % 71.6 70.4 70.4 70.800 F-Factor, dscfm/MMBtu @ %O2 9203 9203 9203 9,203.000 Round Duct Diameter, inches 106 106 106 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 0 0 0 0.000 Fc 1399 1399 1399 1,399.000



### Saturday, February 26, 2011 Page 24 of 34

### 11/24/2010

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



### Saturday, February 26, 2011 Page 25 of 34

### 11/24/2010

Location Stack Exit - Method 23 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



### Saturday, February 26, 2011 Page 26 of 34

### 11/24/2010

Location Stack Exit - Method 25A Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



### Saturday, February 26, 2011 Page 27 of 34

### 11/24/2010

Location Stack Exit - Method 26A Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Saturday, February 26, 2011 Page 28 of 34

### 11/24/2010

Location Stack Exit - Method 29 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Saturday, February 26, 2011 Page 29 of 34

### 11/24/2010

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



### Saturday, February 26, 2011 Page 30 of 34

### 11/24/2010

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



### Saturday, February 26, 2011 Page 31 of 34

### 11/24/2010

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



### Saturday, February 26, 2011 Page 32 of 34

### 11/24/2010

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



### Saturday, February 26, 2011 Page 33 of 34

### 11/24/2010

Location Stack Exit - OTM - 27/28 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Saturday, February 26, 2011 Page 34 of 34