### Name: Chuck French

Title: General Manager Company: FPL Energy Wyman, LLC Sign Date: 5/5/2010 Name: Thomas K. Graham Title: Director of Operations Company:Air Hygiene International, Inc. Sign Date: 4/23/2010 Permitted Facility Representative / Date Testing Company Representative / Date



## William F. Wyman Energy Center, Unit #1, Information Collection Request 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.

Thursday, February 24, 2011 Page 1 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 Facility Information: William F. Wyman Energy Center 677 Cousins Street

Yarmouth ME4096 Contact:Stephen Hofacker Phone:(207) 846-8129 Fax: (207) 846-0521 Email: stephen.a.hofacker@fpl.com Testing Company: Air Hygiene International, Inc. 5634 S. 122nd East Ave, Suite F

Tulsa OK74146 Contact:Thomas Graham Phone:(918) 307-8865 Fax: (918) 307-9131 Email:tom@airhygiene.com

Air Permit Number: A-388-70-A-I Permitted Source ID/Name: Foster Wheeler, dry bottom hopper boiler 1 Permitted Maximum Process Rate: 55 MW Max. Normal Operation Process Rate: 22 MW Target Process Test Rate 22 MW

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: Florida Power & Light (FPL) Energy Wyman, LLC (Wyman) operates two oil fired electric utility steam generating units of Foster Wheeler design, designated as Units 1 and 2. The facility is located at 677 Cousins Street in Yarmouth, Maine. Unit 1 and 2 are of identical design and consists of two dry bottom hopper boilers with super heat and no reheat and ancillary equipment designed to generate 55 megawatts (MW) of electricity each with rated heat inputs of 630 million British thermal units per hour (MMBtu/hr) based on high heating value (HHV). Fuel oil consumption is rated at 4,200 gallons per hour. Unit 1 and 2 utilize low nitrogen oxide (NOx) burner technology to control NOx emissions and cyclone separators to control particulate matter (PM) emissions. Emission testing will be conducted from vertical ductwork prior to the stack breaching for each unit. Industry/SCC/NAIS221112

Sampling Location Information:

Test Parameter Information: AFS #:2300500018 FRS #:110000581406

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 1 - D/F 0 779 303 6 102 30 148 78 1 - Gases 0 779 303 6 102 1 148 78 1 - Metals 0 779 303 6 102 30 148 78 1 - PM 0 779 303 6 102 12 148 78

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location Regulation Description Compound Limit Unit Not applicable.



### Thursday, February 24, 2011 Page 2 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location 2,3,7,8-TCDD Method 23 3 480 30 1 - D/F 1,2,3,7,8-PeCDD Method 23 3 480 30 1 - D/F 1,2,3,4,7,8-HxCDD Method 23 3 480 30 1 - D/F 1,2,3,6,7,8-HxCDD Method 23 3 480 30 1 - D/F 1,2,3,7,8,9-HxCDD Method 23 3 480 30 1 - D/F 1,2,3,4,6,7,8-HpCDD Method 23 3 480 30 1 - D/F OCDD Method 23 3 480 30 1 - D/F 2,3,7,8-TCDF Method 23 3 480 30 1 - D/F 1,2,3,7,8-PeCDF Method 23 3 480 30 1 - D/F 2,3,4,7,8-PeCDF Method 23 3 480 30 1 - D/F 1,2,3,4,7,8-HxCDF Method 23 3 480 30 1 - D/F 1,2,3,6,7,8-HxCDF Method 23 3 480 30 1 - D/F 2,3,4,6,7,8-HxCDF Method 23 3 480 30 1 - D/F 1,2,3,7,8,9-HxCDF Method 23 3 480 30 1 - D/F 1,2,3,4,6,7,8-HpCDF Method 23 3 480 30 1 - D/F 1,2,3,4,7,8,9-HpCDF Method 23 3 480 30 1 - D/F OCDF Method 23 3 480 30 1 - D/F Total Dioxins Method 23 3 480 30 1 - D/F Total Furans Method 23 3 480 30 1 - D/F 3,3',4,4'-TCB (PCB77) Method 23 3 480 30 1 - D/F 3,4,4',5-TCB (PCB81) Method 23 3 480 30 1 - D/F 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 30 1 - D/F 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 30 1 - D/F 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 30 1 - D/F 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 30 1 - D/F 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 30 1 - D/F 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 480 30 1 - D/F
2,3',4,4',5,5'-HxCB (PCB167)Method 23 3 480 30 1 - D/F 3,3',4,4',5,5'-HxCB (PCB169)Method 23 3 480 30 1 - D/F 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 30 1 - D/F

% H2O Method 1 - 4 3 120 1 Determined after initial stratification test 1 - Gases

Carbon Monoxide Method 10 3 120 1 Determined after initial stratification test 1 - Gases
Total organic compounds

(TOC) as Propane Method 25A 3 120 1 Determined after initial stratification test 1 - Gases

Co2 Method 3A CO2 3 120 1 Determined after initial stratification test 1 - Gases

O2 Method 3A O2 3 120 1 Determined after initial stratification test 1 - Gases

Sulfur Dioxide Method 6C 3 120 1 Determined after initial stratification test 1 - Gases
Nitrogen oxides (NOx) Method 7E 3 120 1 Determined after initial stratification test 1 - Gases

% H2O Method 1 - 4 3 240 30 1 - Metals % H2O Method 1 - 4 3 480 30 1 - Metals Chromium Method 29 3 240 30 1 - Metals Cadmium Method 29 3 240 30 1 - Metals Filterable Particulate Method 29 3 240 30 1 - Metals Selenium Method 29 3 240 30 1 - Metals


### Thursday, February 24, 2011 Page 3 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010

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. Run 1 - PM2.5 pulled less than the required sample volume.

Nickel Method 29 3 240 30 1 - Metals Cobalt Method 29 3 240 30 1 - Metals Manganese Method 29 3 240 30 1 - Metals Lead Method 29 3 240 30 1 - Metals Co2 Method 3A CO2 3 240 30 1 - Metals O2 Method 3A O2 3 240 30 1 - Metals O2 Method 3A O2 3 480 30 1 - Metals Co2 Method 3A CO2 3 480 30 1 - Metals % H2O Method 1 - 4 3 315 12 Run times vary based on method calculations 1 - PM

Filterable PM2.5 OTM - 27/28 3 315 12 Run times vary based on method calculations 1 - PM
Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 315 12 Run times vary based on method calculations 1 - PM
Organic Condensible

Particulate OTM - 27/28 3 315 12 Run times vary based on method calculations 1 - PM

Total PM2.5 OTM - 27/28 3 315 12 Run times vary based on method calculations 1 - PM

Total Particulate OTM - 27/28 3 315 12 Run times vary based on method calculations 1 - PM

Filterable Particulate OTM - 27/28 3 315 12 Run times vary based on method calculations 1 - PM

O2 Method 3A O2 3 315 12 Run times vary based on method calculations 1 - PM

Co2 Method 3A CO2 3 315 12 Run times vary based on method calculations 1 - PM



### Thursday, February 24, 2011 Page 4 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 Sampling / Stack Data Results Summary


### Location 1 - D/F - Method 23 Average Run Number U1-23-1 U1-23-2 U1-23-3 Test Date 3/2/2010 3/3/2010 3/4/2010 Run Start Time 8:29:00 AM 8:23:00 AM 9:19:00 AM

Run Finish Time 4:57:00 PM4:43:00 PM 6:03:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 379.744 304.591 376.353 353.563 Moisture Content of Stack Gas, % 7.41 7.62 7.10 7.377 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 9.06 9.27 9.18 9.170 Oxygen, % 9.69 9.43 9.48 9.533 Average Stack Gas Temperature, °F 312.27 304.77 307.20 308.080 Dry Volumetric Flow Rate, dry scfm 91,758.8 88,492.9 85,652.5 88,634.733 Actual Wet Volumetric Flue Gas Flow Rate, acfm 142,520.9 139,634.9 135,690.7 139,282.167 Percent Isokinetic of Sampling Rate, % 97.8 102.9 95.7 98.800 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Location 1 - Gases - Method 10 Average Run Number 1-CO-1 1-CO-2 1-CO-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Dry Volumetric Flow Rate, dry scfm 91750 91750 91750 91,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 7.43 7.43 7.43 7.430 Fuel Type Oil, Residual Oil, ResidualOil, Residual

Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Thursday, February 24, 2011 Page 5 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Gases - Method 25A Average Run Number 1-THC-1 1-THC-2 1-THC-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Dry Volumetric Flow Rate, dry scfm 91750 91750 91750 91,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 7.43 7.43 7.43 7.430 Fuel Type Oil, Residual Oil, ResidualOil, Residual

Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Location 1 - Gases - Method 3A CO2 Average Run Number 1-CO2-1 1-CO2-2 1-CO2-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Dry Volumetric Flow Rate, dry scfm 91750 91750 91750 91,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 7.43 7.43 7.43 7.430 Fuel Type Oil, Residual Oil, ResidualOil, Residual

Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Thursday, February 24, 2011 Page 6 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Gases - Method 3A O2 Average Run Number 1-O2-1 1-O2-2 1-O2-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Dry Volumetric Flow Rate, dry scfm 91750 91750 91750 91,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 7.43 7.43 7.43 7.430 Fuel Type Oil, Residual Oil, ResidualOil, Residual

Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Location 1 - Gases - Method 6C Average Run Number 1-SO2-1 1-SO2-2 1-SO2-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Dry Volumetric Flow Rate, dry scfm 91750 91750 91750 91,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 7.43 7.43 7.43 7.430 Fuel Type Oil, Residual Oil, ResidualOil, Residual

Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Thursday, February 24, 2011 Page 7 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Gases - Method 7E Average Run Number 1-NOx-1 1-NOx-2 1-NOx-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Dry Volumetric Flow Rate, dry scfm 91750 91750 91750 91,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 7.43 7.43 7.43 7.430 Fuel Type Oil, Residual Oil, ResidualOil, Residual

Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Location 1 - Metals - Method 29 Average Run Number U1-29-1 U1-29-2 U1-29-3 Test Date 3/2/2010 3/3/2010 3/4/2010 Run Start Time 6:44:00 AM 6:45:00 AM 7:03:00 AM

Run Finish Time 11:11:00 AM 11:03:00 AM11:27:00 AM

Net Run Time, minutes 240 240 240 Dry Gas Meter Volume Sampled, dscf 208.049 161.059 210.332 193.147 Moisture Content of Stack Gas, % 7.43 7.53 7.79 7.583 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 9.06 9.27 9.18 9.170 Oxygen, % 9.69 9.43 9.48 9.533 Average Stack Gas Temperature, °F 311.40 305.93 305.50 307.610 Dry Volumetric Flow Rate, dry scfm 99,803.0 94,100.2 90,187.3 94,696.833 Actual Wet Volumetric Flue Gas Flow Rate, acfm 155,026.9 149,014.4 143,819.6 149,286.967 Percent Isokinetic of Sampling Rate, % 98.5 102.4 101.6 100.833 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Thursday, February 24, 2011 Page 8 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - PM - OTM - 27/28 Average Run Number U1-27/28-1U1-27/28-2 U1-27/28-3 Test Date 3/2/2010 3/3/2010 3/4/2010 Run Start Time 7:41:00 AM 7:39:00 AM 7:53:00 AM

Run Finish Time 1:06:00 PM1:16:00 PM 1:28:00 PM Net Run Time, minutes 318 317 316 Dry Gas Meter Volume Sampled, dscf 114.494 122.568 122.225 119.762 Moisture Content of Stack Gas, % 8.22 8.24 9.42 8.627 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 9.06 9.27 9.18 9.170 Oxygen, % 9.69 9.43 9.48 9.533 Average Stack Gas Temperature, °F 311.25 304.50 305.75 307.167 Dry Volumetric Flow Rate, dry scfm 98,858.2 94,867.9 90,459.8 94,728.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 154,545.9 150,601.7 146,898.0150,681.867 Percent Isokinetic of Sampling Rate, % 97.8 109.4 114.8 107.333 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Thursday, February 24, 2011 Page 9 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 Emissions Summary


### Location: 1 - D/F - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000255 0.000000014 0.000000019 0.000 lb/mmBtuO2 2.54E-12 1.70E-12 1.87E-12 0.000 ng/dscm 2.37E-03 1.62E-03 1.78E-03 0.002 ng/dscm@7%O2 2.94E-03 1.96E-03 2.17E-03 0.002 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000029 0.0000000031 0.0000000079 0.000 lb/mmBtuO2 2.88E-13 3.76E-13 7.78E-13 0.000 ng/dscm 2.70E-04 3.59E-04 7.41E-04 0.000 ng/dscm@7%O2 3.35E-04 4.35E-04 9.02E-04 0.001 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000037 0.0000000027 0.00000001 0.000 lb/mmBtuO2 3.68E-13 3.27E-13 9.85E-13 0.000 ng/dscm 3.44E-04 3.13E-04 9.38E-04 0.001 ng/dscm@7%O2 4.27E-04 3.79E-04 1.14E-03 0.001 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000027 0.0000000025 0.0000000044 0.000 lb/mmBtuO2 2.69E-13 3.03E-13 4.33E-13 0.000 ng/dscm 2.51E-04 2.90E-04 4.13E-04 0.000 ng/dscm@7%O2 3.11E-04 3.51E-04 5.03E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000019 0.0000000016 0.0000000081 0.000 lb/mmBtuO2 1.89E-13 1.94E-13 7.98E-13 0.000 ng/dscm 1.77E-04 1.86E-04 7.60E-04 0.000 ng/dscm@7%O2 2.19E-04 2.25E-04 9.25E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000027 0.0000000025 0.0000000043 0.000 lb/mmBtuO2 2.69E-13 3.03E-13 4.24E-13 0.000 ng/dscm 2.51E-04 2.90E-04 4.04E-04 0.000 ng/dscm@7%O2 3.11E-04 3.51E-04 4.92E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDF Average



### Thursday, February 24, 2011 Page 10 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000018 0.0000000015 0.0000000055 0.000 lb/mmBtuO2 1.79E-13 1.82E-13 5.42E-13 0.000 ng/dscm 1.67E-04 1.74E-04 5.16E-04 0.000 ng/dscm@7%O2 2.07E-04 2.11E-04 6.28E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000027 0.0000000026 0.0000000044 0.000 lb/mmBtuO2 2.69E-13 3.15E-13 4.33E-13 0.000 ng/dscm 2.51E-04 3.01E-04 4.13E-04 0.000 ng/dscm@7%O2 3.11E-04 3.65E-04 5.03E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000021 0.0000000017 0.0000000063 0.000 lb/mmBtuO2 2.09E-13 2.06E-13 6.21E-13 0.000 ng/dscm 1.95E-04 1.97E-04 5.91E-04 0.000 ng/dscm@7%O2 2.42E-04 2.39E-04 7.19E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000026 0.0000000031 0.0000000026 0.000 lb/mmBtuO2 2.59E-13 3.76E-13 2.56E-13 0.000 ng/dscm 2.42E-04 3.59E-04 2.44E-04 0.000 ng/dscm@7%O2 3.00E-04 4.35E-04 2.97E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000017 0.0000000032 0.0000000039 0.000 lb/mmBtuO2 1.69E-13 3.88E-13 3.84E-13 0.000 ng/dscm 1.58E-04 3.71E-04 3.66E-04 0.000 ng/dscm@7%O2 1.96E-04 4.50E-04 4.45E-04 0.000 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000086 0.0000000022 0.0000000063 0.000 lb/mmBtuO2 8.55E-13 2.67E-13 6.21E-13 0.000 ng/dscm 8.00E-04 2.55E-04 5.91E-04 0.001 ng/dscm@7%O2 9.92E-04 3.09E-04 7.19E-04 0.001 

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.00000003 0.000000011 0.0000000129 0.000 lb/mmBtuO2 2.98E-12 1.33E-12 1.27E-12 0.000 ng/dscm 2.79E-03 1.28E-03 1.21E-03 0.002 ng/dscm@7%O2 3.46E-03 1.55E-03 1.47E-03 0.002



### Thursday, February 24, 2011 Page 11 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.00000143 0.000000795 0.000000813 0.000 lb/mmBtuO2 1.42E-10 9.64E-11 8.01E-11 0.000 ng/dscm 1.33E-01 9.22E-02 7.63E-02 0.101 ng/dscm@7%O2 1.65E-01 1.12E-01 9.29E-02 0.123 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.000000053 0.000000023 0.000000041 0.000 lb/mmBtuO2 5.27E-12 2.79E-12 4.04E-12 0.000 ng/dscm 4.93E-03 2.67E-03 3.85E-03 0.004 ng/dscm@7%O2 6.11E-03 3.24E-03 4.69E-03 0.005 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.000000081 0.00000007 0.0000000529 0.000 lb/mmBtuO2 8.06E-12 8.48E-12 5.21E-12 0.000 ng/dscm 7.53E-03 8.12E-03 4.96E-03 0.007 ng/dscm@7%O2 9.34E-03 9.84E-03 6.04E-03 0.008 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.00000327 0.00000201 0.00000194 0.000 lb/mmBtuO2 3.25E-10 2.44E-10 1.91E-10 0.000 ng/dscm 3.04E-01 2.33E-01 1.82E-01 0.240 ng/dscm@7%O2 3.77E-01 2.82E-01 2.22E-01 0.294 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.000000075 0.00000005 0.0000000419 0.000 lb/mmBtuO2 7.46E-12 6.06E-12 4.13E-12 0.000 ng/dscm 6.98E-03 5.80E-03 3.93E-03 0.006 ng/dscm@7%O2 8.65E-03 7.03E-03 4.78E-03 0.007 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000018 0.0000000016 0.0000000056 0.000 lb/mmBtuO2 1.79E-13 1.94E-13 5.52E-13 0.000 ng/dscm 1.67E-04 1.86E-04 5.26E-04 0.000 ng/dscm@7%O2 2.07E-04 2.25E-04 6.40E-04 0.000 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000074 0.000000003 0.0000000036 0.000 lb/mmBtuO2 7.36E-13 3.64E-13 3.55E-13 0.000



### Thursday, February 24, 2011 Page 12 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 ng/dscm 6.88E-04 3.48E-04 3.38E-04 0.000 ng/dscm@7%O2 8.53E-04 4.22E-04 4.11E-04 0.001 

### Compound: 2,3,7,8-TCDD Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000024 0.0000000043 0.0000000039 0.000 lb/mmBtuO2 2.39E-13 5.21E-13 3.84E-13 0.000 ng/dscm 2.23E-04 4.99E-04 3.66E-04 0.000 ng/dscm@7%O2 2.77E-04 6.05E-04 4.45E-04 0.000 

### Compound: 2,3,7,8-TCDF Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000038 0.0000000043 0.0000000065 0.000 lb/mmBtuO2 3.78E-13 5.21E-13 6.40E-13 0.000 ng/dscm 3.53E-04 4.99E-04 6.10E-04 0.000 ng/dscm@7%O2 4.38E-04 6.05E-04 7.42E-04 0.001 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000037 0.0000000046 0.0000000023 0.000 lb/mmBtuO2 3.68E-13 5.58E-13 2.27E-13 0.000 ng/dscm 3.44E-04 5.33E-04 2.16E-04 0.000 ng/dscm@7%O2 4.27E-04 6.46E-04 2.63E-04 0.000 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000083 0.0000000035 0.0000000071 0.000 lb/mmBtuO2 8.26E-13 4.24E-13 7.00E-13 0.000 ng/dscm 7.72E-04 4.06E-04 6.66E-04 0.001 ng/dscm@7%O2 9.57E-04 4.92E-04 8.11E-04 0.001 

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.00000111 0.000000599 0.000000474 0.000 lb/mmBtuO2 1.10E-10 7.26E-11 4.67E-11 0.000 ng/dscm 1.03E-01 6.95E-02 4.45E-02 0.072 ng/dscm@7%O2 1.28E-01 8.42E-02 5.42E-02 0.089 

### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.000000049 0.0000000308 0.000000033 0.000 lb/mmBtuO2 4.87E-12 3.73E-12 3.25E-12 0.000 ng/dscm 4.56E-03 3.57E-03 3.10E-03 0.004 ng/dscm@7%O2 5.65E-03 4.33E-03 3.77E-03 0.005 

### Compound: OCDD Average RunNumber U1-23-1 U1-23-2 U1-23-3


### Thursday, February 24, 2011 Page 13 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 Mass_mg 0.0000000394 0.000000029 0.000000949 0.000 lb/mmBtuO2 3.92E-12 3.51E-12 9.35E-11 0.000 ng/dscm 3.66E-03 3.36E-03 8.91E-02 0.032 ng/dscm@7%O2 4.54E-03 4.07E-03 1.08E-01 0.039 

### Compound: OCDF Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000064 0.0000000043 0.000000049 0.000 lb/mmBtuO2 6.37E-13 5.21E-13 4.83E-12 0.000 ng/dscm 5.95E-04 4.99E-04 4.60E-03 0.002 ng/dscm@7%O2 7.38E-04 6.05E-04 5.60E-03 0.002 

### Compound: Total Dioxins Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.000000078 0.000000058 0.0000009876 0.000 lb/mmBtuO2 7.76E-12 7.03E-12 9.73E-11 0.000 ng/dscm 7.25E-03 6.73E-03 9.27E-02 0.036 ng/dscm@7%O2 8.99E-03 8.16E-03 1.13E-01 0.043 

### Compound: Total Furans Average RunNumber U1-23-1 U1-23-2 U1-23-3 Mass_mg 0.0000000335 0.000000027 0.0000001064 0.000 lb/mmBtuO2 3.33E-12 3.27E-12 1.05E-11 0.000 ng/dscm 3.12E-03 3.13E-03 9.99E-03 0.005 ng/dscm@7%O2 3.87E-03 3.79E-03 1.22E-02 0.007



### Location: 1 - Gases - Method 10 Compound: Carbon Monoxide Average Run 1-CO-1 1-CO-2 1-CO-3 lb/mmBtuO2 4.49E-04 1.92E-03 6.49E-04 0.001 ppm 3.61E-01 1.54E+00 5.22E-01 0.808 ppm@7%O2 4.46E-01 1.91E+00 6.47E-01 1.001



### Location: 1 - Gases - Method 25A Compound: Total organic compounds (TOC) as Average Run 1-THC-1 1-THC-2 1-THC-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: 1 - Gases - Method 6C Compound: Sulfur Dioxide Average Run 1-SO2-1 1-SO2-2 1-SO2-3 lb/mmBtuO2 7.04E-01 7.14E-01 7.11E-01 0.710 ppm 2.48E+02 2.50E+02 2.50E+02 249.333 ppm@7%O2 3.07E+02 3.11E+02 3.10E+02 309.333



### Thursday, February 24, 2011 Page 14 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010

Location: 1 - Gases - Method 7E 

### Compound: Nitrogen oxides (NOx) Average Run 1-NOx-1 1-NOx-2 1-NOx-3 lb/mmBtuO2 3.37E-01 3.41E-01 3.46E-01 0.341 ppm 1.65E+02 1.67E+02 1.69E+02 167.000 ppm@7%O2 2.04E+02 2.07E+02 2.09E+02 206.667



### Location: 1 - Metals - Method 29 

### Compound: Antimony Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 0.738 0.588 0.818 0.715 Elb/hr 4.68E-02 4.54E-02 4.64E-02 0.046 lb/mmBtuO2 1.34E-04 1.35E-04 1.44E-04 0.000 mg/dscm 1.25E-01 1.29E-01 1.37E-01 0.130 mg/dscm@7%O2 1.55E-01 1.56E-01 1.67E-01 0.159 

### Compound: Arsenic Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 0.015 0.0125 0.0193 0.016 Elb/hr 9.52E-04 9.66E-04 1.09E-03 0.001 lb/mmBtuO2 2.72E-06 2.87E-06 3.40E-06 0.000 mg/dscm 2.55E-03 2.74E-03 3.24E-03 0.003 mg/dscm@7%O2 3.16E-03 3.32E-03 3.94E-03 0.003 

### Compound: Beryllium Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 0.00247 0.00192 0.00262 0.002 Elb/hr 1.57E-04 1.48E-04 1.49E-04 0.000 lb/mmBtuO2 4.48E-07 4.40E-07 4.62E-07 0.000 mg/dscm 4.19E-04 4.21E-04 4.40E-04 0.000 mg/dscm@7%O2 5.20E-04 5.10E-04 5.36E-04 0.001 

### Compound: Cadmium Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 0.000373 0.000275 0.000324 0.000 Elb/hr 2.37E-05 2.13E-05 1.84E-05 0.000 lb/mmBtuO2 6.77E-08 6.30E-08 5.71E-08 0.000 mg/dscm 6.33E-05 6.03E-05 5.44E-05 0.000 mg/dscm@7%O2 7.85E-05 7.31E-05 6.62E-05 0.000 

### Compound: Chromium Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 0.0144 0.012 0.0124 0.013 Elb/hr 9.14E-04 9.27E-04 7.03E-04 0.001 lb/mmBtuO2 2.61E-06 2.75E-06 2.19E-06 0.000 mg/dscm 2.44E-03 2.63E-03 2.08E-03 0.002



### Thursday, February 24, 2011 Page 15 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 mg/dscm@7%O2 3.03E-03 3.19E-03 2.53E-03 0.003 

### Compound: Cobalt Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 0.151 0.13 0.174 0.152 Elb/hr 9.58E-03 1.00E-02 9.87E-03 0.010 lb/mmBtuO2 2.74E-05 2.98E-05 3.07E-05 0.000 mg/dscm 2.56E-02 2.85E-02 2.92E-02 0.028 mg/dscm@7%O2 3.17E-02 3.45E-02 3.55E-02 0.034 

### Compound: Filterable Particulate Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 150 115.1 144.5 136.533 Elb/hr 9.52E+00 8.90E+00 8.20E+00 8.873 lb/mmBtuO2 2.72E-02 2.64E-02 2.55E-02 0.026 mg/dscm 2.55E+01 2.52E+01 2.43E+01 25.000 mg/dscm@7%O2 3.16E+01 3.05E+01 2.96E+01 30.567 

### Compound: Lead Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 0.0374 0.0271 0.0343 0.033 Elb/hr 2.37E-03 2.09E-03 1.95E-03 0.002 lb/mmBtuO2 6.79E-06 6.21E-06 6.05E-06 0.000 mg/dscm 6.35E-03 5.94E-03 5.76E-03 0.006 mg/dscm@7%O2 7.87E-03 7.20E-03 7.01E-03 0.007 

### Compound: Manganese Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 0.259 0.228 0.302 0.263 Elb/hr 1.64E-02 1.76E-02 1.71E-02 0.017 lb/mmBtuO2 4.70E-05 5.23E-05 5.32E-05 0.000 mg/dscm 4.40E-02 5.00E-02 5.07E-02 0.048 mg/dscm@7%O2 5.46E-02 6.06E-02 6.17E-02 0.059 

### Compound: Nickel Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 3.74 3.04 4.4 3.727 Elb/hr 2.37E-01 2.35E-01 2.50E-01 0.241 lb/mmBtuO2 6.79E-04 6.97E-04 7.76E-04 0.001 mg/dscm 6.35E-01 6.67E-01 7.39E-01 0.680 mg/dscm@7%O2 7.87E-01 8.08E-01 8.99E-01 0.831 

### Compound: Selenium Average RunNumber U1-29-1 U1-29-2 U1-29-3 Mass_mg 0.00414 0.002 0.00208 0.003 Elb/hr 2.63E-04 1.55E-04 1.18E-04 0.000 lb/mmBtuO2 7.52E-07 4.58E-07 3.67E-07 0.000 mg/dscm 7.03E-04 4.39E-04 3.49E-04 0.000


### Thursday, February 24, 2011 Page 16 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010

Process Run Data mg/dscm@7%O2 8.72E-04 5.32E-04 4.25E-04 0.001



### Location: 1 - PM - OTM - 27/28 Compound: Filterable Particulate Average RunNumber U1-27/28-1 U1-27/28-2 U1-27/28-3 Mass_mg 90.375 98.8 90.35 93.175 lb/mmBtuO2 2.98E-02 2.98E-02 2.74E-02 0.029 

### Compound: Filterable PM2.5 Average RunNumber U1-27/28-1 U1-27/28-2 U1-27/28-3 Mass_mg 50.5 58.1 50.325 52.975 lb/mmBtuO2 1.67E-02 1.75E-02 1.53E-02 0.017 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber U1-27/28-1 U1-27/28-2 U1-27/28-3 Mass_mg 8.612 1.973 2.874 4.486 lb/mmBtuO2 2.84E-03 5.94E-04 8.72E-04 0.001 

### Compound: Organic Condensible Particulate Average RunNumber U1-27/28-1 U1-27/28-2 U1-27/28-3 Mass_mg 6.663 0.788 1.013 2.821 lb/mmBtuO2 2.20E-03 2.37E-04 3.07E-04 0.001 

### Compound: Total Particulate Average RunNumber U1-27/28-1 U1-27/28-2 U1-27/28-3 Mass_mg 105.649 101.561 94.237 100.482 lb/mmBtuO2 3.49E-02 3.06E-02 2.86E-02 0.031 

### Compound: Total PM2.5 Average RunNumber U1-27/28-1 U1-27/28-2 U1-27/28-3 Mass_mg 65.774 60.861 54.212 60.282 lb/mmBtuO2 2.17E-02 1.83E-02 1.64E-02 0.019



### Thursday, February 24, 2011 Page 17 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 Process Run Data



### Run Name Value UOM Comments Target Value 1 Residual Oil (No. 6) Burned 2429 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 3/2/2010; Start - 08:55; End - 10:54 0



### 1 Average Heat Input 303 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 3/2/2010; Start - 08:55; End - 10:54 0

1 Steam Output 140 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 3/2/2010; Start - 08:55; End - 10:54 0



### 1 Unit Gross Electrical Output 22 Mwe Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 3/2/2010; Start - 08:55; End - 10:54 0

2 Residual Oil (No. 6) Burned 2417 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 3/2/2010; Start - 11:15; End - 13:14 0

2 Average Heat Input 301 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 3/2/2010; Start - 11:15; End - 13:14 0



### 2 Steam Output 140 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 3/2/2010; Start - 11:15; End - 13:14 0

2 Unit Gross Electrical Output 22 Mwe Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 3/2/2010; Start - 11:15; End - 13:14 0



### Thursday, February 24, 2011 Page 18 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 3 Residual Oil (No. 6) Burned 2402 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 3/2/2010; Start - 13:37; End - 15:36 0



### 3 Average Heat Input 299 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 3/2/2010; Start - 13:37; End - 15:36 0

3 Steam Output 140 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 3/2/2010; Start - 13:37; End - 15:36 0



### 3 Unit Gross Electrical Output 22 Mwe Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 3/2/2010; Start - 13:37; End - 15:36 0

4 Residual Oil (No. 6) Burned 353612 gal/hr Method 23; Run D/F-1; Date - 3/2/2010; Start - 08:29; End - 16:57 0

4 Average Heat Input 301 MMBtu/hr Method 23; Run D/F-1; Date - 3/2/2010; Start - 08:29; End - 16:57 0

4 Steam Output 140 1000 lb Method 23; Run D/F-1; Date - 3/2/2010; Start - 08:29; End - 16:57 0

4 Unit Gross Electrical Output 22 Mwe Method 23; Run D/F-1; Date - 3/2/2010; Start - 08:29; End - 16:57 0

5 Residual Oil (No. 6) Burned 338246 gal/hr Method 23; Run D/F-2; Date - 3/3/2010; Start - 08:23; End - 16:43 0

5 Average Heat Input 288 MMBtu/hr Method 23; Run D/F-2; Date - 3/3/2010; Start - 08:23; End - 16:43 0



### Thursday, February 24, 2011 Page 19 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 5 Steam Output 212 1000 lb Method 23; Run D/F-2; Date - 3/3/2010; Start - 08:23; End - 16:43 0

5 Unit Gross Electrical Output 22 Mwe Method 23; Run D/F-2; Date - 3/3/2010; Start - 08:23; End - 16:43 0

6 Residual Oil (No. 6) Burned 333571 gal/hr Method 23; Run D/F-3; Date - 3/4/2010; Start - 09:19; End - 18:03 0

6 Average Heat Input 284 MMBtu/hr Method 23; Run D/F-3; Date - 3/4/2010; Start - 09:19; End - 18:03 0

6 Steam Output 102 1000 lb Method 23; Run D/F-3; Date - 3/4/2010; Start - 09:19; End - 18:03 0

6 Unit Gross Electrical Output 22 Mwe Method 23; Run D/F-3; Date - 3/4/2010; Start - 09:19; End - 18:03 0

7 Residual Oil (No. 6) Burned 357780 gal/hr Method 29; Run M-1; Date - 3/2/2010; Start - 06:44; End - 11:11 0

7 Average Heat Input 305 MMBtu/hr Method 29; Run M-1; Date - 3/2/2010; Start - 06:44; End - 11:11 0

7 Steam Output 140 1000 lb Method 29; Run M-1; Date - 3/2/2010; Start - 06:44; End - 11:11 0

7 Unit Gross Electrical Output 22 Mwe Method 29; Run M-1; Date - 3/2/2010; Start - 06:44; End - 11:11 0

8 Residual Oil (No. 6) Burned 346100 gal/hr Method 29; Run M-2; Date - 3/3/2010; Start - 06:45; End - 11:03 0

8 Average Heat Input 295 MMBtu/hr Method 29; Run M-2; Date - 3/3/2010; Start - 06:45; End - 11:03 0



### Thursday, February 24, 2011 Page 20 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 8 Steam Output 212 1000 lb Method 29; Run M-2; Date - 3/3/2010; Start - 06:45; End - 11:03 0

8 Unit Gross Electrical Output 22 Mwe Method 29; Run M-2; Date - 3/3/2010; Start - 06:45; End - 11:03 0

9 Residual Oil (No. 6) Burned 333518 gal/hr Method 29; Run M-3; Date - 3/4/2010; Start - 07:03; End - 11:27 0

9 Average Heat Input 284 MMBtu/hr Method 29; Run M-3; Date - 3/4/2010; Start - 07:03; End - 11:27 0

9 Steam Output 102 1000 lb Method 29; Run M-3; Date - 3/4/2010; Start - 07:03; End - 11:27 0

9 Unit Gross Electrical Output 22 Mwe Method 29; Run M-3; Date - 3/4/2010; Start - 07:03; End - 11:27 0

10Residual Oil (No. 6) Burned 355520 gal/hr Method 027/028; Run PM-1; Date - 3/2/2010; Start - 07:41; End - 13:06 0

10Average Heat Input 303 MMBtu/hr Method 027/028; Run PM-1; Date - 3/2/2010; Start - 07:41; End - 13:06 0

10Steam Output 140 1000 lb Method 027/028; Run PM-1; Date - 3/2/2010; Start - 07:41; End - 13:06 0

10Unit Gross Electrical Output 22 Mwe Method 027/028; Run PM-1; Date - 3/2/2010; Start - 07:41; End - 13:06 0

11Residual Oil (No. 6) Burned 339913 gal/hr Method 027/028; Run PM-2; Date - 3/3/2010; Start - 07:39; End - 13:16 0

11Average Heat Input 290 MMBtu/hr Method 027/028; Run PM-2; Date - 3/3/2010; Start - 07:39; End - 13:16 0



### Thursday, February 24, 2011 Page 21 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010

APCD Run Data

Process Lab Run Data 11Steam Output 212 1000 lb Method 027/028; Run PM-2; Date - 3/3/2010; Start - 07:39; End - 13:16 0

11Unit Gross Electrical Output 22 Mwe Method 027/028; Run PM-2; Date - 3/3/2010; Start - 07:39; End - 13:16 0

12Residual Oil (No. 6) Burned 333314 gal/hr Method 027/028; Run PM-3; Date - 3/4/2010; Start - 07:53; End - 13:28 0

12Average Heat Input 284 MMBtu/hr Method 027/028; Run PM-3; Date - 3/4/2010; Start - 07:53; End - 13:28 0

12Steam Output 102 1000 lb Method 027/028; Run PM-3; Date - 3/4/2010; Start - 07:53; End - 13:28 0

12Unit Gross Electrical Output 22 Mwe Method 027/028; Run PM-3; Date - 3/4/2010; Start - 07:53; End - 13:28 0



### Run Name Value UOM Comments Target Value 1 LOW NOX BURNERS 165NOx Emissions 0


### 2 LOW NOX BURNERS 167NOx Emissions 0
3 LOW NOX BURNERS 169NOx Emissions 0
1 CYCLONE SEPARATORS 2 Opacity 0


### 2 CYCLONE SEPARATORS 2 Opacity 0
3 CYCLONE SEPARATORS 2 Opacity 0

Run Name ValueUOM Comments 

### 1 Fuel Higher Heating Value 18100Btu/lb 2 Fuel Higher Heating Value 18200Btu/lb 3 Fuel Higher Heating Value 18000Btu/lb 1 Fuel Moisture 0.157 % 

### 2 Fuel Moisture 0.272 % 3 Fuel Moisture 0.366 % 1 Fuel Mercury Content 0.0003mg/kg 2 Fuel Mercury Content 0.0003mg/kg


### Thursday, February 24, 2011 Page 22 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 3 Fuel Mercury Content 0.0003mg/kg 

### 1 Fuel Chlorine Content 100 mg/kg 2 Fuel Chlorine Content 207 mg/kg 3 Fuel Chlorine Content 229 mg/kg 1 Fuel Fluorine Content 68 mg/kg 

### 2 Fuel Fluorine Content 76 mg/kg 3 Fuel Fluorine Content 71 mg/kg 1 Fuel Antimony Content 3.3 mg/kg 

### 2 Fuel Antimony Content 3.3 mg/kg 3 Fuel Antimony Content 3.2 mg/kg 1 Fuel Arsenic Content 0.18 mg/kg 2 Fuel Arsenic Content 0.17 mg/kg 

### 3 Fuel Arsenic Content 0.17 mg/kg 1 Fuel Beryllium Content 0.013 mg/kg 2 Fuel Beryllium Content 0.013 mg/kg 

### 3 Fuel Beryllium Content 0.014mg/kg 1 Fuel Cadmium Content 0.007 mg/kg 2 Fuel Cadmium Content 0.006mg/kg 3 Fuel Cadmium Content 0.006mg/kg 

### 1 Fuel Chromium Content 0.087 mg/kg 2 Fuel Chromium Content 0.089 mg/kg 3 Fuel Chromium Content 0.084mg/kg 

### 1 Fuel Cobalt Content 0.83 mg/kg 2 Fuel Cobalt Content 0.81 mg/kg 3 Fuel Cobalt Content 0.8 mg/kg 1 Fuel Lead Content 0.18 mg/kg 

### 2 Fuel Lead Content 0.16 mg/kg 3 Fuel Lead Content 0.16 mg/kg 1 Fuel Manganese Content 1.6 mg/kg 

### 2 Fuel Manganese Content 1.6 mg/kg 3 Fuel Manganese Content 1.6 mg/kg 1 Fuel Nickel Content 21.5 mg/kg 2 Fuel Nickel Content 21.2 mg/kg 

### 3 Fuel Nickel Content 20.9 mg/kg 1 Fuel Selenium Content 0.022mg/kg 2 Fuel Selenium Content 0.017 mg/kg 

### 3 Fuel Selenium Content 0.017 mg/kg 1 Fuel Sulfur Content 6140 mg/kg 2 Fuel Sulfur Content 6460 mg/kg 3 Fuel Sulfur Content 6650 mg/kg 

### 1 Fuel Proximate Analysis (Carbon) 87.28 % 2 Fuel Proximate Analysis (Carbon) 87.19 % 3 Fuel Proximate Analysis (Carbon) 87.3 %



### Thursday, February 24, 2011 Page 23 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 1 Fuel Proximate Analysis (Hydrogen) 10.35 % 

### 2 Fuel Proximate Analysis (Hydrogen) 10.42 % 3 Fuel Proximate Analysis (Hydrogen) 10.46 % 1 Fuel Proximate Analysis (Nitrogen) 1.54 % 2 Fuel Proximate Analysis (Nitrogen) 1.49 % 

### 3 Fuel Proximate Analysis (Nitrogen) 1.28 % 1 Fuel Proximate Analysis (Oxygen) 0.89 % 2 Fuel Proximate Analysis (Oxygen) 0.56 % 

### 3 Fuel Proximate Analysis (Oxygen) 0.74 % 1 Fuel Proximate Analysis (Sulfur) 0.677 % 2 Fuel Proximate Analysis (Sulfur) 0.682 % 3 Fuel Proximate Analysis (Sulfur) 0.685 %



### Thursday, February 24, 2011 Page 24 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010 Sampling / Stack Data Results Detail


### Location 1 - D/F - Method 23 Average Run Number U1-23-1 U1-23-2 U1-23-3 Test Date 3/2/2010 3/3/2010 3/4/2010 Run Start Time 8:29:00 AM8:23:00 AM 9:19:00 AM Run Finish Time 4:57:00 PM4:43:00 PM 6:03:00 PM Net Traversing Points 30 30 30 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.36 0.32 0.375 0.352 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.979 0.979 0.979 0.979 Barometric Pressure, inches of Mercury 30.5 29.8 29.61 29.970 Average Orifice Meter Differential, inches H2O 2.17 1.32 2.35 1.947 Dry Gas Meter Volume Sampled, cubic feet 389.273 321.730 404.154 371.719 Average Dry Gas Meter Temperature, °F 82.98 85.58 92.55 87.037 Dry Gas Meter Volume Sampled, dscf 379.744 304.591 376.353 353.563 Total Moisture Liquid collected, g 646.1 534.1 611.3 597.167 Volume of Water Vapor, standard cubic feet 30.41 25.14 28.77 28.107 Moisture Content of Stack Gas, % 7.41 7.62 7.10 7.377 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9259 0.9238 0.929 0.926 Carbon Dioxide, % 9.06 9.27 9.18 9.170 Oxygen, % 9.69 9.43 9.48 9.533 Carbon Monoxide & Nitrogen, % 81.25 81.3 81.34 81.297 Fuel Factor 1.24 1.24 1.24 Dry Molecular Weight, lb/lb-Mole 29.84 29.86 29.85 29.850 Wet Molecular weight, lb/lb-Mole 28.96 28.96 29.01 28.977 Flue Gas Static Pressure, inches of H2O -1 -1 -1 -1.000 Absolute Flue Gas Pressure, inches of Mercury 30.43 29.73 29.54 29.900 Average Stack Gas Temperature, °F 312.27 304.77 307.20 308.080 Average Velocity Head, inches of H2O 0.1942438531 513850.183944288

0187230.172432857

643409 0.184
Average Stack Gas Velocity, feet/second 29.63 29.03 28.21 28.957 Stack Cross-Sectional Area, square feet 80.167 80.167 80.167 80.167 Dry Volumetric Flow Rate, dry scfm 91,758.8 88,492.9 85,652.588,634.733 Actual Wet Volumetric Flue Gas Flow Rate, acfm 142,520.9 139,634.9 135,690.7139,282.167 Percent Isokinetic of Sampling Rate, % 97.8 102.9 95.7 98.800 Percent Excess Air, % 82.4 78.4 79.0 79.933 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 0 0 0 Rectangular Duct Width, inches 148 148 148 Rectangular Duct Length, inches 78 78 78 Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000



### Thursday, February 24, 2011 Page 25 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Gases - Method 10 Average Run Number 1-CO-1 1-CO-2 1-CO-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM11:15:25 AM 1:37:25 PM Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 91750 91750 9175091,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 7.43 7.43 7.43 7.430 Analyzer Make THERMO THERMO THERMO Analyzer Model 48i 48i 48i Analyzer Serial Number INST-CO0015 INST-CO0015 INST-CO0015 Operating Range 11.9 11.9 11.9 11.900 Operating Units ppm ppm ppm No. Readings/Avg. 240 240 240 240.000 Calibration Set 5 5 5 5.000 Calibration Pre Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Pre Zero Cylinder Instrument Response -0.06 0.1 0.07 0.037 Calibration Pre Zero Cylinder Bias -1.09 0.25 0 -0.280 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID AAL4052 AAL4052 AAL4052 Calibration Pre High Cylinder Instrument Response 5.11 5.01 5.29 5.137 Calibration Pre High Cylinder Bias 0.59 -0.25 2.1 0.813 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response 0.1 0.07 -0.04 0.043 Calibration Post Zero Cylinder Bias 0.25 0 -0.92 -0.223 Calibration Post Zero Cylinder Drift 1.34 0.25 0.92 0.837 Calibration Post High Cylinder ID AAL4052 AAL4052 AAL4052 Calibration Post High Cylinder Instrument Response 5.01 5.29 5.02 5.107 Calibration Post High Cylinder Bias -0.25 2.1 -0.17 0.560 Calibration Post High Cylinder Drift 0.84 2.35 2.27 1.820 Cavg 0.39 1.67 0.56 0.873 Cavg Units ppmvd ppmvd ppmvd Cgas 0.3612 1.5396 0.5217 0.808 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil, ResidualOil, ResidualOil, Residual Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units ppmvw ppmvw ppmvw



### Thursday, February 24, 2011 Page 26 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Gases - Method 25A Average Run Number 1-THC-1 1-THC-2 1-THC-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM11:15:25 AM 1:37:25 PM Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 91750 91750 9175091,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 7.43 7.43 7.43 7.430 Analyzer Make THERMO THERMO THERMO Analyzer Model 51C-HT 51C-HT 51C-HT Analyzer Serial Number INST-TH0009 INST-TH0009 INST-TH0009 Operating Range 95 95 95 95.000 Operating Units ppm ppm ppm No. Readings/Avg. 240 240 240 240.000 Calibration Set 6 6 6 6.000 Calibration Pre Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Pre Zero Cylinder Instrument Response -0.11 -0.74 -0.41 -0.420 Calibration Pre Zero Cylinder Bias 0 -0.66 -0.32 -0.327 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID CC155655 CC155655 CC155655 Calibration Pre High Cylinder Instrument Response 25.3 25 25.15 25.150 Calibration Pre High Cylinder Bias 0 -0.32 -0.16 -0.160 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response -0.74 -0.41 -0.73 -0.627 Calibration Post Zero Cylinder Bias -0.66 -0.32 -0.65 -0.543 Calibration Post Zero Cylinder Drift 0.66 0.34 0.33 0.443 Calibration Post High Cylinder ID CC155655 CC155655 CC155655 Calibration Post High Cylinder Instrument Response 25 25.15 24.48 24.877 Calibration Post High Cylinder Bias -0.32 -0.16 -0.86 -0.447 Calibration Post High Cylinder Drift 0.32 0.16 0.7 0.393 Cavg -0.37 -0.35 -0.45 -0.390 Cavg Units ppmvw ppmvw ppmvw Cgas 0 0 0 0.000 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil, ResidualOil, ResidualOil, Residual Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units ppmvw ppmvw ppmvw



### Thursday, February 24, 2011 Page 27 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Gases - Method 3A CO2 Average Run Number 1-CO2-1 1-CO2-2 1-CO2-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM11:15:25 AM 1:37:25 PM Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 91750 91750 9175091,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 7.43 7.43 7.43 7.430 Analyzer Make THERMO THERMO THERMO Analyzer Model 410i 410i 410i Analyzer Serial Number INST-C2-0009 INST-C2- 0009 INST-C2-

0009 Operating Range 19.4 19.4 19.4 19.400 Operating Units % % % No. Readings/Avg. 240 240 240 240.000 Calibration Set 2 2 2 2.000 Calibration Pre Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Pre Zero Cylinder Instrument Response 0.01 0.5 0.3 0.270 Calibration Pre Zero Cylinder Bias -0.26 2.27 1.24 1.083 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID AAL2058- CO2 AAL2058-

CO2 AAL2058-

CO2 Calibration Pre High Cylinder Instrument Response 8.86 9.31 8.97 9.047 Calibration Pre High Cylinder Bias -2.58 -0.26 -2.01 -1.617 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response 0.5 0.3 0.6 0.467 Calibration Post Zero Cylinder Bias 2.27 1.24 2.78 2.097 Calibration Post Zero Cylinder Drift 2.53 1.03 1.54 1.700 Calibration Post High Cylinder ID AAL2058- CO2 AAL2058-

CO2 AAL2058-

CO2 Calibration Post High Cylinder Instrument Response 9.31 8.97 8.93 9.070 Calibration Post High Cylinder Bias -0.26 -2.01 -2.22 -1.497 Calibration Post High Cylinder Drift 2.32 1.75 0.21 1.427 Cavg 9.04 9.58 9.06 9.227 Cavg Units %vd %vd %vd Cgas 8.8447 9.3376 9.005 9.062 Cgas Units %vd %vd %vd Fuel Type Oil, ResidualOil, ResidualOil, Residual Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units %vw %vw %vw



### Thursday, February 24, 2011 Page 28 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Gases - Method 3A O2 Average Run Number 1-O2-1 1-O2-2 1-O2-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM11:15:25 AM 1:37:25 PM Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 91750 91750 9175091,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 7.43 7.43 7.43 7.430 Analyzer Make THERMO THERMO THERMO Analyzer Model 42i-HL 42i-HL 42i-HL Analyzer Serial Number INST-N2-0001 INST-N2- 0001 INST-N2-

0001 Operating Range 21.1 21.1 21.1 21.100 Operating Units % % % No. Readings/Avg. 240 240 240 240.000 Calibration Set 1 1 1 1.000 Calibration Pre Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Pre Zero Cylinder Instrument Response 0.04 -0.01 0.09 0.040 Calibration Pre Zero Cylinder Bias -0.09 -0.33 0.14 -0.093 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID AAL2058-O2 AAL2058- O2AAL2058-O2
Calibration Pre High Cylinder Instrument Response 11.93 11.82 11.83 11.860 Calibration Pre High Cylinder Bias -0.81 -1.33 -1.28 -1.140 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response -0.01 0.09 -0.02 0.020 Calibration Post Zero Cylinder Bias -0.33 0.14 -0.38 -0.190 Calibration Post Zero Cylinder Drift 0.24 0.47 0.52 0.410 Calibration Post High Cylinder ID AAL2058-O2 AAL2058- O2AAL2058-O2
Calibration Post High Cylinder Instrument Response 11.82 11.83 11.82 11.823 Calibration Post High Cylinder Bias -1.33 -1.28 -1.33 -1.313 Calibration Post High Cylinder Drift 0.52 0.05 0.05 0.207 Cavg 9.49 9.5 9.47 9.487 Cavg Units %vd %vd %vd Cgas 9.6667 9.7129 9.6831 9.688 Cgas Units %vd %vd %vd Fuel Type Oil, ResidualOil, ResidualOil, Residual Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units %vw %vw %vw



### Thursday, February 24, 2011 Page 29 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Gases - Method 6C Average Run Number 1-SO2-1 1-SO2-2 1-SO2-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM11:15:25 AM 1:37:25 PM Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 91750 91750 9175091,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 7.43 7.43 7.43 7.430 Analyzer Make THERMO THERMO THERMO Analyzer Model 43i-HL 43i-HL 43i-HL Analyzer Serial Number INST-S2-0004 INST-S2- 0004 INST-S2-

0004 Operating Range 434 434 434 434.000 Operating Units ppm ppm ppm No. Readings/Avg. 240 240 240 240.000 Calibration Set 3 3 3 3.000 Calibration Pre Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Pre Zero Cylinder Instrument Response 0.42 8.1 8.27 5.597 Calibration Pre Zero Cylinder Bias 0.01 1.78 1.82 1.203 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID AL2793 AL2793 AL2793 Calibration Pre High Cylinder Instrument Response 247.59 244.86 243.22 245.223 Calibration Pre High Cylinder Bias -1.41 -2.04 -2.42 -1.957 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response 8.1 8.27 2.75 6.373 Calibration Post Zero Cylinder Bias 1.78 1.82 0.55 1.383 Calibration Post Zero Cylinder Drift 1.77 0.04 1.27 1.027 Calibration Post High Cylinder ID AL2793 AL2793 AL2793 Calibration Post High Cylinder Instrument Response 244.86 243.22 244.98 244.353 Calibration Post High Cylinder Bias -2.04 -2.42 -2.02 -2.160 Calibration Post High Cylinder Drift 0.63 0.38 0.4 0.470 Cavg 238.39 238.55 238.44 238.460 Cavg Units ppmvd ppmvd ppmvd Cgas 247.7105 250.0411 249.927 249.226 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil, ResidualOil, ResidualOil, Residual Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units ppmvw ppmvw ppmvw



### Thursday, February 24, 2011 Page 30 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Gases - Method 7E Average Run Number 1-NOx-1 1-NOx-2 1-NOx-3 Test Date 3/2/2010 3/2/2010 3/2/2010 Run Start Time 8:55:25 AM11:15:25 AM 1:37:25 PM Run Finish Time 10:54:55 AM1:14:55 PM 3:36:55 PM Carbon Dioxide, % 8.85 9.34 9.01 9.067 Oxygen, % 9.66 9.71 9.68 9.683 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 91750 91750 9175091,750.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 7.43 7.43 7.43 7.430 Analyzer Make THERMO THERMO THERMO Analyzer Model 42i-HL 42i-HL 42i-HL Analyzer Serial Number INST-N2-0001 INST-N2- 0001 INST-N2-

0001 Operating Range 244 244 244 244.000 Operating Units ppm ppm ppm No. Readings/Avg. 240 240 240 240.000 Calibration Set 4 4 4 4.000 Calibration Pre Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Pre Zero Cylinder Instrument Response 0.4 0.67 0.79 0.620 Calibration Pre Zero Cylinder Bias 0.09 0.2 0.25 0.180 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID ALM057559ALM057559ALM057559 Calibration Pre High Cylinder Instrument Response 109.59 109.3 108.54 109.143 Calibration Pre High Cylinder Bias -0.22 -0.34 -0.65 -0.403 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response 0.67 0.79 0.77 0.743 Calibration Post Zero Cylinder Bias 0.2 0.25 0.24 0.230 Calibration Post Zero Cylinder Drift 0.11 0.05 0.01 0.057 Calibration Post High Cylinder ID ALM057559ALM057559ALM057559 Calibration Post High Cylinder Instrument Response 109.3 108.54 108.13 108.657 Calibration Post High Cylinder Bias -0.34 -0.65 -0.82 -0.603 Calibration Post High Cylinder Drift 0.12 0.31 0.17 0.200 Cavg 162.48 163.1 164.96 163.513 Cavg Units ppmvd ppmvd ppmvd Cgas 165.0527 166.5872 169.4387 167.026 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil, ResidualOil, ResidualOil, Residual Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units ppmvw ppmvw ppmvw



### Thursday, February 24, 2011 Page 31 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - Metals - Method 29 Average Run Number U1-29-1 U1-29-2 U1-29-3 Test Date 3/2/2010 3/3/2010 3/4/2010 Run Start Time 6:44:00 AM6:45:00 AM 7:03:00 AM Run Finish Time 11:11:00 AM11:03:00 AM11:27:00 AM Net Traversing Points 30 30 30 Net Run Time, minutes 240 240 240 Nozzle Diameter, inches 0.36 0.32 0.375 0.352 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.002 1.002 1.002 1.002 Barometric Pressure, inches of Mercury 30.47 29.71 29.57 29.917 Average Orifice Meter Differential, inches H2O 2.70 1.58 2.78 2.353 Dry Gas Meter Volume Sampled, cubic feet 209.030 166.990 219.867 198.629 Average Dry Gas Meter Temperature, °F 84.85 86.82 90.35 87.340 Dry Gas Meter Volume Sampled, dscf 208.049 161.059 210.332 193.147 Total Moisture Liquid collected, g 354.6 278.5 377.8 336.967 Volume of Water Vapor, standard cubic feet 16.69 13.11 17.78 15.860 Moisture Content of Stack Gas, % 7.43 7.53 7.79 7.583 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9257 0.9247 0.9221 0.924 Carbon Dioxide, % 9.06 9.27 9.18 9.170 Oxygen, % 9.69 9.43 9.48 9.533 Carbon Monoxide & Nitrogen, % 81.25 81.3 81.34 81.297 Fuel Factor 1.24 1.24 1.24 Dry Molecular Weight, lb/lb-Mole 29.84 29.86 29.85 29.850 Wet Molecular weight, lb/lb-Mole 28.96 28.97 28.93 28.953 Flue Gas Static Pressure, inches of H2O -1 -1 -1 -1.000 Absolute Flue Gas Pressure, inches of Mercury 30.40 29.64 29.50 29.847 Average Stack Gas Temperature, °F 311.40 305.93 305.50 307.610 Average Velocity Head, inches of H2O 0.2298709089 421760.208695122

2740160.193298856

095001 0.211
Average Stack Gas Velocity, feet/second 32.23 30.98 29.90 31.037 Stack Cross-Sectional Area, square feet 80.167 80.167 80.167 80.167 Dry Volumetric Flow Rate, dry scfm 99,803.0 94,100.2 90,187.394,696.833 Actual Wet Volumetric Flue Gas Flow Rate, acfm 155,026.9 149,014.4 143,819.6149,286.967 Percent Isokinetic of Sampling Rate, % 98.5 102.4 101.6 100.833 Percent Excess Air, % 82.4 78.4 79.0 79.933 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 0 0 0 Rectangular Duct Width, inches 148 148 148 Rectangular Duct Length, inches 78 78 78 Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000



### Thursday, February 24, 2011 Page 32 of 33

### William F. Wyman Energy Center, Unit #1, Information Collection Request
5/5/2010
Location 1 - PM - OTM - 27/28 Average Run Number U1-27/28-1 U1-27/28-2 U1-27/28-3 Test Date 3/2/2010 3/3/2010 3/4/2010 Run Start Time 7:41:00 AM7:39:00 AM 7:53:00 AM Run Finish Time 1:06:00 PM1:16:00 PM 1:28:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 318 317 316 Nozzle Diameter, inches 0.234 0.234 0.234 0.234 Pitot Tube Coefficient 0.8 0.8 0.8 0.800 Dry Gas Meter Calibration Factor 0.987 0.987 0.987 0.987 Barometric Pressure, inches of Mercury 30.53 29.81 29.57 29.970 Average Orifice Meter Differential, inches H2O 0.41 0.41 0.41 0.410 Dry Gas Meter Volume Sampled, cubic feet 115.276 126.656 127.940 123.291 Average Dry Gas Meter Temperature, °F 75.92 77.08 79.67 77.557 Dry Gas Meter Volume Sampled, dscf 114.494 122.568 122.225 119.762 Total Moisture Liquid collected, g 217.7 233.9 270 240.533 Volume of Water Vapor, standard cubic feet 10.25 11.01 12.71 11.323 Moisture Content of Stack Gas, % 8.22 8.24 9.42 8.627 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9178 0.9176 0.9058 0.914 Carbon Dioxide, % 9.06 9.27 9.18 9.170 Oxygen, % 9.69 9.43 9.48 9.533 Carbon Monoxide & Nitrogen, % 81.25 81.3 81.34 81.297 Fuel Factor 1.24 1.24 1.24 Dry Molecular Weight, lb/lb-Mole 29.84 29.86 29.85 29.850 Wet Molecular weight, lb/lb-Mole 28.87 28.88 28.73 28.827 Flue Gas Static Pressure, inches of H2O -1 -1 -1 -1.000 Absolute Flue Gas Pressure, inches of Mercury 30.46 29.74 29.50 29.900 Average Stack Gas Temperature, °F 311.25 304.50 305.75 307.167 Average Velocity Head, inches of H2O 0.2517173165 918010.235468700

8639220.220730716

766518 0.236
Average Stack Gas Velocity, feet/second 32.13 31.31 30.54 31.327 Stack Cross-Sectional Area, square feet 80.167 80.167 80.167 80.167 Dry Volumetric Flow Rate, dry scfm 98,858.2 94,867.9 90,459.894,728.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 154,545.9 150,601.7 146,898.0150,681.867 Percent Isokinetic of Sampling Rate, % 97.8 109.4 114.8 107.333 Percent Excess Air, % 82.4 78.4 79.0 79.933 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 0 0 0 Rectangular Duct Width, inches 148 148 148 Rectangular Duct Length, inches 78 78 78 Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000



### Thursday, February 24, 2011 Page 33 of 33