### 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: 4/27/2010 Permitted Facility Representative / Date Testing Company Representative / Date



## William F. Wyman Energy Center, Unit #2, 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 #2, Information Collection Request
5/5/2010 Facility Information: William F. Wyman Energy Center 677 Cousins Street

Yarmouth ME04096 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 2 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 2 - D/F 0 779 303 6 102 30 148 78 2 - Gases 0 779 303 6 102 1 148 78 2 - Metals 0 779 303 6 102 30 148 78 2 - 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 #2, Information Collection Request
5/5/2010 Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location % H2O Method 1 - 4 3 480 30 2 - D/F 2,3,7,8-TCDD Method 23 3 480 30 2 - D/F 1,2,3,7,8-PeCDD Method 23 3 480 30 2 - D/F 1,2,3,4,7,8-HxCDD Method 23 3 480 30 2 - D/F 1,2,3,6,7,8-HxCDD Method 23 3 480 30 2 - D/F 1,2,3,7,8,9-HxCDD Method 23 3 480 30 2 - D/F 1,2,3,4,6,7,8-HpCDD Method 23 3 480 30 2 - D/F OCDD Method 23 3 480 30 2 - D/F 2,3,7,8-TCDF Method 23 3 480 30 2 - D/F 1,2,3,7,8-PeCDF Method 23 3 480 30 2 - D/F 2,3,4,7,8-PeCDF Method 23 3 480 30 2 - D/F 1,2,3,4,7,8-HxCDF Method 23 3 480 30 2 - D/F 1,2,3,6,7,8-HxCDF Method 23 3 480 30 2 - D/F 2,3,4,6,7,8-HxCDF Method 23 3 480 30 2 - D/F 1,2,3,7,8,9-HxCDF Method 23 3 480 30 2 - D/F 1,2,3,4,6,7,8-HpCDF Method 23 3 480 30 2 - D/F 1,2,3,4,7,8,9-HpCDF Method 23 3 480 30 2 - D/F OCDF Method 23 3 480 30 2 - D/F Total Dioxins Method 23 3 480 30 2 - D/F Total Furans Method 23 3 480 30 2 - D/F 3,3',4,4'-TCB (PCB77) Method 23 3 480 30 2 - D/F 3,4,4',5-TCB (PCB81) Method 23 3 480 30 2 - D/F 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 30 2 - D/F 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 30 2 - D/F 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 30 2 - D/F 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 30 2 - D/F 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 30 2 - D/F 2,3,3',4,4',5/2,3,3',4,4',5'-

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

(PCB189) Method 23 3 480 30 2 - D/F

Co2 Method 3A CO2 3 480 30 2 - D/F O2 Method 3A O2 3 480 30 2 - D/F % H2O Method 1 - 4 3 120 1 Determined after initial stratification test 2 - Gases

Carbon Monoxide Method 10 3 120 1 Determined after initial stratification test 2 - Gases
Total organic compounds

(TOC) as Propane Method 25A 3 120 1 Determined after initial stratification test 2 - Gases

Co2 Method 3A CO2 3 120 1 Determined after initial stratification test 2 - Gases

O2 Method 3A O2 3 120 1 Determined after initial stratification test 2 - Gases

Sulfur Dioxide Method 6C 3 120 1 Determined after initial stratification test 2 - Gases
Nitrogen oxides (NOx) Method 7E 3 120 1 Determined after initial stratification test 2 - Gases

% H2O Method 1 - 4 3 240 30 2 - Metals Manganese Method 29 3 240 30 2 - Metals Chromium Method 29 3 240 30 2 - Metals


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

### William F. Wyman Energy Center, Unit #2, 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 - Dioxins pulled less than the required sample volume. RMB Consultants contacted EPA and received a variance to accept this pending proper sample volumes for Run 2 and Run 3. PM2.5 runs unable to pull required sample volumes due to excessive particulate matter plugging the cyclone and maximizing the sample vacuum.

Cobalt Method 29 3 240 30 2 - Metals Cadmium Method 29 3 240 30 2 - Metals Lead Method 29 3 240 30 2 - Metals Nickel Method 29 3 240 30 2 - Metals Selenium Method 29 3 240 30 2 - Metals Filterable Particulate Method 29 3 240 30 2 - Metals O2 Method 3A O2 3 240 30 2 - Metals Co2 Method 3A CO2 3 240 30 2 - Metals % H2O Method 1 - 4 3 315 12 Run times vary based on method calculations 2 - PM

Total PM2.5 OTM - 27/28 3 315 12 Run times vary based on method calculations 2 - PM
Organic Condensible

Particulate OTM - 27/28 3 315 12 Run times vary based on method calculations 2 - PM
Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 315 12 Run times vary based on method calculations 2 - PM

Filterable PM2.5 OTM - 27/28 3 315 12 Run times vary based on method calculations 2 - PM

Filterable Particulate OTM - 27/28 3 315 12 Run times vary based on method calculations 2 - PM

Total Particulate OTM - 27/28 3 315 12 Run times vary based on method calculations 2 - PM

Co2 Method 3A CO2 3 315 12 Run times vary based on method calculations 2 - PM

O2 Method 3A O2 3 315 12 Run times vary based on method calculations 2 - PM



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 Sampling / Stack Data Results Summary


### Location2 - D/F - Method 23 Average Run Number U2-23-1 U2-23-2 U2-23-3 Test Date 2/23/2010 2/24/2010 2/25/2010 Run Start Time 7:15:00 AM 8:03:00 AM 9:00:00 AM

Run Finish Time 3:48:00 PM4:55:00 PM 5:40:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 173.917 325.020 318.373 272.437 Moisture Content of Stack Gas, % 8.00 8.09 7.92 8.003 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 10.62 10.33 10.35 10.433 Oxygen, % 8.04 8.17 8.01 8.073 Average Stack Gas Temperature, °F 315.90 303.43 306.07 308.467 Dry Volumetric Flow Rate, dry scfm 86,850.7 78,343.3 74,855.9 80,016.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 137,759.0 123,328.9 118,663.2 126,583.700 Percent Isokinetic of Sampling Rate, % 98.1 98.0 100.5 98.867 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



### Location2 - Gases - Method 10 Average Run Number 2-CO-1 2-CO-2 2-CO-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM 11:13:21 AM 1:57:21 PM

Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Dry Volumetric Flow Rate, dry scfm 86888 86888 86888 86,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 8.01 8.01 8.01 8.010 Fuel Type Oil Oil Oil 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 #2, Information Collection Request
5/5/2010
Location2 - Gases - Method 25A Average Run Number 2-THC-1 2-THC-2 2-THC-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM 11:13:21 AM 1:57:21 PM

Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Dry Volumetric Flow Rate, dry scfm 86888 86888 86888 86,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 8.01 8.01 8.01 8.010 Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Location2 - Gases - Method 3A CO2 Average Run Number 2-CO2-1 2-CO2-2 2-CO2-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM 11:13:21 AM 1:57:21 PM

Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Dry Volumetric Flow Rate, dry scfm 86888 86888 86888 86,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 8.01 8.01 8.01 8.010 Fuel Type Oil Oil Oil 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 #2, Information Collection Request
5/5/2010
Location2 - Gases - Method 3A O2 Average Run Number 2-O2-1 2-O2-2 2-O2-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM 11:13:21 AM 1:57:21 PM

Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Dry Volumetric Flow Rate, dry scfm 86888 86888 86888 86,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 8.01 8.01 8.01 8.010 Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Location2 - Gases - Method 6C Average Run Number 2-SO2-1 2-SO2-2 2-SO2-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM 11:13:21 AM 1:57:21 PM

Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Dry Volumetric Flow Rate, dry scfm 86888 86888 86888 86,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 8.01 8.01 8.01 8.010 Fuel Type Oil Oil Oil 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 #2, Information Collection Request
5/5/2010
Location2 - Gases - Method 7E Average Run Number 2-NOx-1 2-NOx-2 2-NOx-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM 11:13:21 AM 1:57:21 PM

Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Dry Volumetric Flow Rate, dry scfm 86888 86888 86888 86,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 8.01 8.01 8.01 8.010 Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Location2 - Metals - Method 29 Average Run Number U2-29-1 U2-29-2 U2-29-3 Test Date 2/23/2010 2/24/2010 2/25/2010 Run Start Time 7:39:00 AM 8:24:00 AM 7:00:00 AM

Run Finish Time 2:09:00 PM 12:53:00 PM11:14:00 AM

Net Run Time, minutes 300 240 240 Dry Gas Meter Volume Sampled, dscf 139.126 161.906 167.028 156.020 Moisture Content of Stack Gas, % 11.57 9.30 8.47 9.780 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 10.62 10.33 10.35 10.433 Oxygen, % 8.04 8.17 8.01 8.073 Average Stack Gas Temperature, °F 316.80 306.50 307.20 310.167 Dry Volumetric Flow Rate, dry scfm 88,439.1 76,620.8 79,545.7 81,535.200 Actual Wet Volumetric Flue Gas Flow Rate, acfm 147,234.7 123,088.4 126,744.0 132,355.700 Percent Isokinetic of Sampling Rate, % 104.2 99.9 99.2 101.100 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 #2, Information Collection Request
5/5/2010
Location2 - PM - OTM - 27/28 Average Run Number U2-27/28-1U2-27/28-2 U2-27/28-3 Test Date 2/24/2010 2/25/2010 2/25/2010 Run Start Time 5:04:00 PM 7:54:00 AM 2:42:00 PM

Run Finish Time 10:21:00 PM1:50:00 PM 8:19:00 PM Net Run Time, minutes 294 322 308 Dry Gas Meter Volume Sampled, dscf 105.247 120.140 117.555 114.314 Moisture Content of Stack Gas, % 12.35 13.55 12.88 12.927 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 10.33 10.35 10.35 10.343 Oxygen, % 8.17 8.01 8.01 8.063 Average Stack Gas Temperature, °F 302.92 306.58 305.25 304.917 Dry Volumetric Flow Rate, dry scfm 78,704.1 76,932.3 78,866.8 78,167.733 Actual Wet Volumetric Flue Gas Flow Rate, acfm 129,918.6 129,678.1 132,756.6 130,784.433 Percent Isokinetic of Sampling Rate, % 104.4 111.4 111.1 108.967 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 #2, Information Collection Request
5/5/2010 Emissions Summary


### Location: 2 - D/F - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.000000016 0.000000042 0.0000000066 0.000 lb/mmBtuO2 3.03E-12 4.30E-12 6.81E-13 0.000 ng/dscm 3.25E-03 4.56E-03 7.32E-04 0.003 ng/dscm@7%O2 3.51E-03 4.98E-03 7.89E-04 0.003 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000015 0.00000001 0.0000000044 0.000 lb/mmBtuO2 2.84E-13 1.02E-12 4.54E-13 0.000 ng/dscm 3.05E-04 1.09E-03 4.88E-04 0.001 ng/dscm@7%O2 3.30E-04 1.19E-03 5.26E-04 0.001 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000054 0.0000000061 0.0000000038 0.000 lb/mmBtuO2 1.02E-12 6.24E-13 3.92E-13 0.000 ng/dscm 1.10E-03 6.63E-04 4.22E-04 0.001 ng/dscm@7%O2 1.19E-03 7.24E-04 4.55E-04 0.001 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000014 0.0000000064 0.0000000033 0.000 lb/mmBtuO2 2.65E-13 6.55E-13 3.41E-13 0.000 ng/dscm 2.84E-04 6.95E-04 3.66E-04 0.000 ng/dscm@7%O2 3.07E-04 7.59E-04 3.95E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.000000004 0.0000000064 0.0000000045 0.000 lb/mmBtuO2 7.57E-13 6.55E-13 4.64E-13 0.000 ng/dscm 8.12E-04 6.95E-04 4.99E-04 0.001 ng/dscm@7%O2 8.78E-04 7.59E-04 5.38E-04 0.001 

### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000014 0.0000000062 0.0000000033 0.000 lb/mmBtuO2 2.65E-13 6.35E-13 3.41E-13 0.000 ng/dscm 2.84E-04 6.74E-04 3.66E-04 0.000 ng/dscm@7%O2 3.07E-04 7.36E-04 3.95E-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 #2, Information Collection Request
5/5/2010 RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.00000000751 0.000000006 0.0000000042 0.000 lb/mmBtuO2 1.42E-12 6.14E-13 4.33E-13 0.000 ng/dscm 1.53E-03 6.52E-04 4.66E-04 0.001 ng/dscm@7%O2 1.65E-03 7.12E-04 5.03E-04 0.001 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000015 0.0000000064 0.0000000033 0.000 lb/mmBtuO2 2.84E-13 6.55E-13 3.41E-13 0.000 ng/dscm 3.05E-04 6.95E-04 3.66E-04 0.000 ng/dscm@7%O2 3.30E-04 7.59E-04 3.95E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000056 0.0000000068 0.0000000048 0.000 lb/mmBtuO2 1.06E-12 6.96E-13 4.95E-13 0.000 ng/dscm 1.14E-03 7.39E-04 5.33E-04 0.001 ng/dscm@7%O2 1.23E-03 8.07E-04 5.75E-04 0.001 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.00000000092 0.0000000032 0.0000000043 0.000 lb/mmBtuO2 1.74E-13 3.27E-13 4.44E-13 0.000 ng/dscm 1.87E-04 3.48E-04 4.77E-04 0.000 ng/dscm@7%O2 2.02E-04 3.80E-04 5.14E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000015 0.0000000033 0.0000000035 0.000 lb/mmBtuO2 2.84E-13 3.38E-13 3.61E-13 0.000 ng/dscm 3.05E-04 3.59E-04 3.88E-04 0.000 ng/dscm@7%O2 3.30E-04 3.92E-04 4.18E-04 0.000 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.00000000099 0.0000000215 0.0000000024 0.000 lb/mmBtuO2 1.87E-13 2.20E-12 2.48E-13 0.000 ng/dscm 2.01E-04 2.34E-03 2.66E-04 0.001 ng/dscm@7%O2 2.17E-04 2.56E-03 2.87E-04 0.001 

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000317 0.000000042 0.000000019 0.000 lb/mmBtuO2 6.00E-12 4.30E-12 1.96E-12 0.000 ng/dscm 6.44E-03 4.56E-03 2.11E-03 0.004 ng/dscm@7%O2 6.96E-03 4.98E-03 2.28E-03 0.005



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.00000171 0.00000236 0.00000127 0.000 lb/mmBtuO2 3.24E-10 2.42E-10 1.31E-10 0.000 ng/dscm 3.47E-01 2.56E-01 1.41E-01 0.248 ng/dscm@7%O2 3.75E-01 2.80E-01 1.52E-01 0.269 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.000000051 0.000000053 0.000000041 0.000 lb/mmBtuO2 9.66E-12 5.42E-12 4.23E-12 0.000 ng/dscm 1.04E-02 5.76E-03 4.55E-03 0.007 ng/dscm@7%O2 1.12E-02 6.29E-03 4.91E-03 0.007 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.00000011 0.000000184 0.000000099 0.000 lb/mmBtuO2 2.08E-11 1.88E-11 1.02E-11 0.000 ng/dscm 2.23E-02 2.00E-02 1.10E-02 0.018 ng/dscm@7%O2 2.41E-02 2.18E-02 1.19E-02 0.019 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.00000444 0.00000529 0.00000304 0.000 lb/mmBtuO2 8.41E-10 5.41E-10 3.14E-10 0.000 ng/dscm 9.02E-01 5.75E-01 3.37E-01 0.605 ng/dscm@7%O2 9.75E-01 6.28E-01 3.63E-01 0.655 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000001 0.000000135 0.0000000687 0.000 lb/mmBtuO2 1.89E-11 1.38E-11 7.09E-12 0.000 ng/dscm 2.03E-02 1.47E-02 7.62E-03 0.014 ng/dscm@7%O2 2.19E-02 1.61E-02 8.22E-03 0.015 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000038 0.0000000061 0.0000000043 0.000 lb/mmBtuO2 7.19E-13 6.24E-13 4.44E-13 0.000 ng/dscm 7.72E-04 6.63E-04 4.77E-04 0.001 ng/dscm@7%O2 8.34E-04 7.24E-04 5.14E-04 0.001 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000098 0.0000000078 0.0000000033 0.000 lb/mmBtuO2 1.86E-12 7.98E-13 3.41E-13 0.000



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 ng/dscm 1.99E-03 8.48E-04 3.66E-04 0.001 ng/dscm@7%O2 2.15E-03 9.26E-04 3.95E-04 0.001 

### Compound: 2,3,7,8-TCDD Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000067 0.0000000018 0.0000000063 0.000 lb/mmBtuO2 1.27E-12 1.84E-13 6.50E-13 0.000 ng/dscm 1.36E-03 1.96E-04 6.99E-04 0.001 ng/dscm@7%O2 1.47E-03 2.14E-04 7.54E-04 0.001 

### Compound: 2,3,7,8-TCDF Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000012 0.0000000057 0.0000000051 0.000 lb/mmBtuO2 2.27E-13 5.83E-13 5.26E-13 0.000 ng/dscm 2.44E-04 6.19E-04 5.66E-04 0.000 ng/dscm@7%O2 2.64E-04 6.76E-04 6.10E-04 0.001 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000066 0.0000000062 0.0000000037 0.000 lb/mmBtuO2 1.25E-12 6.35E-13 3.82E-13 0.000 ng/dscm 1.34E-03 6.74E-04 4.10E-04 0.001 ng/dscm@7%O2 1.45E-03 7.36E-04 4.42E-04 0.001 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.000000017 0.000000016 0.000000014 0.000 lb/mmBtuO2 3.22E-12 1.64E-12 1.44E-12 0.000 ng/dscm 3.45E-03 1.74E-03 1.55E-03 0.002 ng/dscm@7%O2 3.73E-03 1.90E-03 1.67E-03 0.002 

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.00000205 0.000002 0.00000111 0.000 lb/mmBtuO2 3.88E-10 2.05E-10 1.15E-10 0.000 ng/dscm 4.16E-01 2.17E-01 1.23E-01 0.252 ng/dscm@7%O2 4.50E-01 2.37E-01 1.33E-01 0.273 

### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000762 0.0000000959 0.000000053 0.000 lb/mmBtuO2 1.44E-11 9.81E-12 5.47E-12 0.000 ng/dscm 1.55E-02 1.04E-02 5.88E-03 0.011 ng/dscm@7%O2 1.68E-02 1.14E-02 6.34E-03 0.012 

### Compound: OCDD Average RunNumber U2-23-1 U2-23-2 U2-23-3


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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 Mass_mg 0.000000058 0.000000088 0.000000058 0.000 lb/mmBtuO2 1.10E-11 9.01E-12 5.98E-12 0.000 ng/dscm 1.18E-02 9.56E-03 6.43E-03 0.009 ng/dscm@7%O2 1.28E-02 1.04E-02 6.93E-03 0.010 

### Compound: OCDF Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.0000000058 0.0000000071 0.000000011 0.000 lb/mmBtuO2 1.10E-12 7.27E-13 1.14E-12 0.000 ng/dscm 1.18E-03 7.72E-04 1.22E-03 0.001 ng/dscm@7%O2 1.28E-03 8.43E-04 1.32E-03 0.001 

### Compound: Total Dioxins Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.00000008592 0.000000154 0.0000000851 0.000 lb/mmBtuO2 1.63E-11 1.58E-11 8.78E-12 0.000 ng/dscm 1.74E-02 1.67E-02 9.44E-03 0.015 ng/dscm@7%O2 1.88E-02 1.82E-02 1.02E-02 0.016 

### Compound: Total Furans Average RunNumber U2-23-1 U2-23-2 U2-23-3 Mass_mg 0.00000004611 0.0000000653 0.0000000489 0.000 lb/mmBtuO2 8.73E-12 6.68E-12 5.05E-12 0.000 ng/dscm 9.36E-03 7.10E-03 5.42E-03 0.007 ng/dscm@7%O2 1.01E-02 7.75E-03 5.84E-03 0.008



### Location: 2 - Gases - Method 10 Compound: Carbon Monoxide Average Run 2-CO-1 2-CO-2 2-CO-3 lb/mmBtuO2 7.63E-03 7.59E-03 8.04E-03 0.008 ppm 7.03E+00 6.99E+00 7.41E+00 7.143 ppm@7%O2 7.60E+00 7.56E+00 8.00E+00 7.720



### Location: 2 - Gases - Method 25A Compound: Total organic compounds (TOC) as Average Run 2-THC-1 2-THC-2 2-THC-3 lb/mmBtuO2 1.33E-03 1.24E-03 1.21E-03 0.001 ppm 7.80E-01 7.25E-01 7.09E-01 0.738 ppm@7%O2 8.43E-01 7.84E-01 7.65E-01 0.797



### Location: 2 - Gases - Method 6C Compound: Sulfur Dioxide Average Run 2-SO2-1 2-SO2-2 2-SO2-3 lb/mmBtuO2 6.73E-01 6.63E-01 6.77E-01 0.671 ppm 2.71E+02 2.67E+02 2.73E+02 270.333 ppm@7%O2 2.93E+02 2.89E+02 2.95E+02 292.333



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010

Location: 2 - Gases - Method 7E 

### Compound: Nitrogen oxides (NOx) Average Run 2-NOx-1 2-NOx-2 2-NOx-3 lb/mmBtuO2 2.77E-01 2.75E-01 2.74E-01 0.275 ppm 1.56E+02 1.54E+02 1.54E+02 154.667 ppm@7%O2 1.69E+02 1.66E+02 1.66E+02 167.000



### Location: 2 - Metals - Method 29 

### Compound: Antimony Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 0.578 0.758 0.821 0.719 Elb/hr 4.86E-02 4.75E-02 5.17E-02 0.049 lb/mmBtuO2 1.37E-04 1.56E-04 1.61E-04 0.000 mg/dscm 1.47E-01 1.65E-01 1.74E-01 0.162 mg/dscm@7%O2 1.59E-01 1.80E-01 1.88E-01 0.176 

### Compound: Arsenic Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 0.0123 0.0175 0.0182 0.016 Elb/hr 1.03E-03 1.10E-03 1.15E-03 0.001 lb/mmBtuO2 2.91E-06 3.60E-06 3.58E-06 0.000 mg/dscm 3.12E-03 3.82E-03 3.85E-03 0.004 mg/dscm@7%O2 3.37E-03 4.17E-03 4.15E-03 0.004 

### Compound: Beryllium Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 0.00158 0.00241 0.00256 0.002 Elb/hr 1.33E-04 1.51E-04 1.61E-04 0.000 lb/mmBtuO2 3.74E-07 4.95E-07 5.03E-07 0.000 mg/dscm 4.01E-04 5.26E-04 5.41E-04 0.000 mg/dscm@7%O2 4.33E-04 5.74E-04 5.83E-04 0.001 

### Compound: Cadmium Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 0.000364 0.00046 0.000755 0.001 Elb/hr 3.06E-05 2.88E-05 4.76E-05 0.000 lb/mmBtuO2 8.61E-08 9.45E-08 1.48E-07 0.000 mg/dscm 9.24E-05 1.00E-04 1.60E-04 0.000 mg/dscm@7%O2 9.99E-05 1.09E-04 1.73E-04 0.000 

### Compound: Chromium Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 0.0215 0.0195 0.0254 0.022 Elb/hr 1.81E-03 1.22E-03 1.60E-03 0.002 lb/mmBtuO2 5.09E-06 4.01E-06 5.00E-06 0.000 mg/dscm 5.46E-03 4.25E-03 5.37E-03 0.005



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 mg/dscm@7%O2 5.90E-03 4.64E-03 5.79E-03 0.005 

### Compound: Cobalt Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 0.113 0.158 0.232 0.168 Elb/hr 9.50E-03 9.89E-03 1.46E-02 0.011 lb/mmBtuO2 2.67E-05 3.25E-05 4.56E-05 0.000 mg/dscm 2.87E-02 3.45E-02 4.91E-02 0.037 mg/dscm@7%O2 3.10E-02 3.77E-02 5.29E-02 0.041 

### Compound: Filterable Particulate Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 192.7 163.5 191.53 182.577 Elb/hr 1.62E+01 1.02E+01 1.21E+01 12.833 lb/mmBtuO2 4.56E-02 3.36E-02 3.77E-02 0.039 mg/dscm 4.89E+01 3.57E+01 4.05E+01 41.700 mg/dscm@7%O2 5.29E+01 3.90E+01 4.37E+01 45.200 

### Compound: Lead Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 0.0315 0.0367 0.0431 0.037 Elb/hr 2.65E-03 2.30E-03 2.72E-03 0.003 lb/mmBtuO2 7.46E-06 7.54E-06 8.48E-06 0.000 mg/dscm 8.00E-03 8.01E-03 9.11E-03 0.008 mg/dscm@7%O2 8.65E-03 8.75E-03 9.82E-03 0.009 

### Compound: Manganese Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 0.195 0.291 0.342 0.276 Elb/hr 1.64E-02 1.82E-02 2.15E-02 0.019 lb/mmBtuO2 4.62E-05 5.98E-05 6.73E-05 0.000 mg/dscm 4.95E-02 6.35E-02 7.23E-02 0.062 mg/dscm@7%O2 5.35E-02 6.93E-02 7.80E-02 0.067 

### Compound: Nickel Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 3.1 4.07 4.64 3.937 Elb/hr 2.61E-01 2.55E-01 2.92E-01 0.269 lb/mmBtuO2 7.34E-04 8.36E-04 9.13E-04 0.001 mg/dscm 7.87E-01 8.88E-01 9.81E-01 0.885 mg/dscm@7%O2 8.51E-01 9.70E-01 1.06E+00 0.960 

### Compound: Selenium Average RunNumber U2-29-1 U2-29-2 U2-29-3 Mass_mg 0.0045 0.00345 0.00245 0.003 Elb/hr 3.78E-04 2.16E-04 1.54E-04 0.000 lb/mmBtuO2 1.07E-06 7.09E-07 4.82E-07 0.000 mg/dscm 1.14E-03 7.53E-04 5.18E-04 0.001


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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010

Process Run Data mg/dscm@7%O2 1.23E-03 8.22E-04 5.59E-04 0.001



### Location: 2 - PM - OTM - 27/28 Compound: Filterable Particulate Average RunNumber U2-27/28-1 U2-27/28-2 U2-27/28-3 Mass_mg 110.95 116.9 116.95 114.933 lb/mmBtuO2 3.51E-02 3.20E-02 3.27E-02 0.033 

### Compound: Filterable PM2.5 Average RunNumber U2-27/28-1 U2-27/28-2 U2-27/28-3 Mass_mg 83.85 83.425 82.125 83.133 lb/mmBtuO2 2.65E-02 2.28E-02 2.29E-02 0.024 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber U2-27/28-1 U2-27/28-2 U2-27/28-3 Mass_mg 4.614 4.128 2.132 3.625 lb/mmBtuO2 1.46E-03 1.13E-03 5.96E-04 0.001 

### Compound: Organic Condensible Particulate Average RunNumber U2-27/28-1 U2-27/28-2 U2-27/28-3 Mass_mg 4.538 7.038 0 3.859 lb/mmBtuO2 1.43E-03 1.92E-03 0.00E+00 0.001 

### Compound: Total Particulate Average RunNumber U2-27/28-1 U2-27/28-2 U2-27/28-3 Mass_mg 120.101 128.065 119.082 122.416 lb/mmBtuO2 3.80E-02 3.50E-02 3.33E-02 0.035 

### Compound: Total PM2.5 Average RunNumber U2-27/28-1 U2-27/28-2 U2-27/28-3 Mass_mg 93.001 94.59 84.257 90.616 lb/mmBtuO2 2.94E-02 2.59E-02 2.35E-02 0.026



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 Process Run Data



### Run Name Value UOM Comments Target Value 1 Residual Oil (No. 6) Burned 2238 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 2/23/2010; Start - 08:47; End - 10:46 0



### 1 Average Heat Input 279 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 2/23/2010; Start - 08:47; End - 10:46 0

1 Steam Output 183 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 2/23/2010; Start - 08:47; End - 10:46 0



### 1 Unit Gross Electrical Output 23 MWg Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 2/23/2010; Start - 08:47; End - 10:46 0

2 Residual Oil (No. 6) Burned 2233 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 2/23/2010; Start - 11:13; End - 13:12 0

2 Average Heat Input 278 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 2/23/2010; Start - 11:13; End - 13:12 0



### 2 Steam Output 183 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 2/23/2010; Start - 11:13; End - 13:12 0

2 Unit Gross Electrical Output 22 MWg Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 2/23/2010; Start - 11:13; End - 13:12 0



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 3 Residual Oil (No. 6) Burned 2240 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 2/23/2010; Start - 13:57; End - 15:56 0



### 3 Average Heat Input 279 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 2/23/2010; Start - 13:57; End - 15:56 0

3 Steam Output 183 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 2/23/2010; Start - 13:57; End - 15:56 0



### 3 Unit Gross Electrical Output 23 MWg Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 2/23/2010; Start - 13:57; End - 15:56 0

4 Residual Oil (No. 6) Burned 327845 gal/hr Method 23; Run D/F-1; Date - 2/23/2010; Start - 07:15; End - 15:48 0

4 Average Heat Input 279 MMBtu/hr Method 23; Run D/F-1; Date - 2/23/2010; Start - 07:15; End - 15:48 0

4 Steam Output 183 1000 lb Method 23; Run D/F-1; Date - 2/23/2010; Start - 07:15; End - 15:48 0

4 Unit Gross Electrical Output 23 MWg Method 23; Run D/F-1; Date - 2/23/2010; Start - 07:15; End - 15:48 0

5 Residual Oil (No. 6) Burned 297969 gal/hr Method 23; Run D/F-2; Date - 2/24/2010; Start - 08:03; End - 16:55 0

5 Average Heat Input 254 MMBtu/hr Method 23; Run D/F-2; Date - 2/24/2010; Start - 08:03; End - 16:55 0



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 5 Steam Output 171 1000 lb Method 23; Run D/F-2; Date - 2/24/2010; Start - 08:03; End - 16:55 0

5 Unit Gross Electrical Output 23 MWg Method 23; Run D/F-2; Date - 2/24/2010; Start - 08:03; End - 16:55 0

6 Residual Oil (No. 6) Burned 299120 gal/hr Method 23; Run D/F-3; Date - 2/25/2010; Start - 09:00; End - 16:40 0

6 Average Heat Input 255 MMBtu/hr Method 23; Run D/F-3; Date - 2/25/2010; Start - 09:00; End - 16:40 0

6 Steam Output 187 1000 lb Method 23; Run D/F-3; Date - 2/25/2010; Start - 09:00; End - 16:40 0

6 Unit Gross Electrical Output 23 MWg Method 23; Run D/F-3; Date - 2/25/2010; Start - 09:00; End - 16:40 0

7 Residual Oil (No. 6) Burned 327639 gal/hr Method 29; Run M-1; Date - 2/23/2010; Start - 07:39; End - 14:09 0

7 Average Heat Input 279 MMBtu/hr Method 29; Run M-1; Date - 2/23/2010; Start - 07:39; End - 14:09 0

7 Steam Output 183 1000 lb Method 29; Run M-1; Date - 2/23/2010; Start - 07:39; End - 14:09 0

7 Unit Gross Electrical Output 23 MWg Method 29; Run M-1; Date - 2/23/2010; Start - 07:39; End - 14:09 0

8 Residual Oil (No. 6) Burned 298824 gal/hr Method 29; Run M-2; Date - 2/24/2010; Start - 08:24; End - 12:53 0

8 Average Heat Input 255 MMBtu/hr Method 29; Run M-2; Date - 2/24/2010; Start - 08:24; End - 12:53 0



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 8 Steam Output 171 1000 lb Method 29; Run M-2; Date - 2/24/2010; Start - 08:24; End - 12:53 0

8 Unit Gross Electrical Output 23 MWg Method 29; Run M-2; Date - 2/24/2010; Start - 08:24; End - 12:53 0

9 Residual Oil (No. 6) Burned 299548 gal/hr Method 29; Run M-3; Date - 2/25/2010; Start - 07:00; End - 11:14 0

9 Average Heat Input 255 MMBtu/hr Method 29; Run M-3; Date - 2/25/2010; Start - 07:00; End - 11:14 0

9 Steam Output 187 1000 lb Method 29; Run M-3; Date - 2/25/2010; Start - 07:00; End - 11:14 0

9 Unit Gross Electrical Output 23 MWg Method 29; Run M-3; Date - 2/25/2010; Start - 07:00; End - 11:14 0

10Residual Oil (No. 6) Burned 296489 gal/hr Method 027/028; Run PM-1; Date - 2/24/2010; Start - 17:04; End - 22:21 0

10Average Heat Input 253 MMBtu/hr Method 027/028; Run PM-1; Date - 2/24/2010; Start - 17:04; End - 22:21 0

10Steam Output 171 1000 lb Method 027/028; Run PM-1; Date - 2/24/2010; Start - 17:04; End - 22:21 0

10Unit Gross Electrical Output 23 MWg Method 027/028; Run PM-1; Date - 2/24/2010; Start - 17:04; End - 22:21 0

11Residual Oil (No. 6) Burned 299263 gal/hr Method 027/028; Run PM-2; Date - 2/25/2010; Start - 07:54; End - 13:50 0

11Average Heat Input 255 MMBtu/hr Method 027/028; Run PM-2; Date - 2/25/2010; Start - 07:54; End - 13:50 0



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010

APCD Run Data

Process Lab Run Data 11Steam Output 187 1000 lb Method 027/028; Run PM-2; Date - 2/25/2010; Start - 07:54; End - 13:50 0

11Unit Gross Electrical Output 23 MWg Method 027/028; Run PM-2; Date - 2/25/2010; Start - 07:54; End - 13:50 0

12Residual Oil (No. 6) Burned 300772 gal/hr Method 027/028; Run PM-3; Date - 2/25/2010; Start - 14:42; End - 20:19 0

12Average Heat Input 256 MMBtu/hr Method 027/028; Run PM-3; Date - 2/25/2010; Start - 14:42; End - 20:19 0

12Steam Output 187 1000 lb Method 027/028; Run PM-3; Date - 2/25/2010; Start - 14:42; End - 20:19 0

12Unit Gross Electrical Output 23 MWg Method 027/028; Run PM-3; Date - 2/25/2010; Start - 14:42; End - 20:19 0



### Run Name Value UOM Comments Target Value 1 LOW NOX BURNERS 156NOx Emissions 0


### 2 LOW NOX BURNERS 154NOx Emissions 0
3 LOW NOX BURNERS 154NOx Emissions 0
1 CYCLONE SEPARATORS 6 Opacity 0


### 2 CYCLONE SEPARATORS 6 Opacity 0
3 CYCLONE SEPARATORS 6 Opacity 0

Run Name ValueUOM Comments 

### 2 Fuel Proximate Analysis (Oxygen) 0.5 % 2 Fuel Proximate Analysis (Sulfur) 0.694 % 3 Fuel Higher Heating Value 18300Btu/lb 3 Fuel Moisture 0.181 % 

### 3 Fuel Mercury Content 0.0004mg/kg 3 Fuel Chlorine Content 100 mg/kg 3 Fuel Fluorine Content 69 mg/kg 3 Fuel Antimony Content 3.3 mg/kg


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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 3 Fuel Arsenic Content 0.18 mg/kg 

### 3 Fuel Beryllium Content 0.013 mg/kg 3 Fuel Cadmium Content 0.006mg/kg 3 Fuel Chromium Content 0.087 mg/kg 3 Fuel Cobalt Content 0.83 mg/kg 

### 3 Fuel Lead Content 0.16 mg/kg 3 Fuel Manganese Content 1.6 mg/kg 3 Fuel Nickel Content 21.7 mg/kg 

### 3 Fuel Selenium Content 0.017 mg/kg 3 Fuel Sulfur Content 6400 mg/kg 3 Fuel Proximate Analysis (Carbon) 87.76 % 3 Fuel Proximate Analysis (Hydrogen) 10.24 % 

### 3 Fuel Proximate Analysis (Nitrogen) 1.43 % 3 Fuel Proximate Analysis (Oxygen) 0.5 % 3 Fuel Proximate Analysis (Sulfur) 0.7 % 

### 1 Fuel Higher Heating Value 18300Btu/lb 1 Fuel Moisture 0.33 % 1 Fuel Mercury Content 0.0004mg/kg 1 Fuel Chlorine Content 168 mg/kg 

### 1 Fuel Fluorine Content 59 mg/kg 1 Fuel Antimony Content 3.4 mg/kg 1 Fuel Arsenic Content 0.17 mg/kg 

### 1 Fuel Beryllium Content 0.013 mg/kg 1 Fuel Cadmium Content 0.063 mg/kg 1 Fuel Chromium Content 0.09 mg/kg 1 Fuel Cobalt Content 0.84 mg/kg 

### 1 Fuel Lead Content 0.17 mg/kg 1 Fuel Manganese Content 1.6 mg/kg 1 Fuel Nickel Content 21.6 mg/kg 

### 1 Fuel Selenium Content 0.022mg/kg 1 Fuel Sulfur Content 6250 mg/kg 1 Fuel Proximate Analysis (Carbon) 87.82 % 1 Fuel Proximate Analysis (Hydrogen) 10.49 % 

### 1 Fuel Proximate Analysis (Nitrogen) 1.33 % 1 Fuel Proximate Analysis (Oxygen) 0.5 % 1 Fuel Proximate Analysis (Sulfur) 0.706 % 

### 2 Fuel Higher Heating Value 18300Btu/lb 2 Fuel Moisture 0.365 % 2 Fuel Mercury Content 0.0004mg/kg 2 Fuel Chlorine Content 138 mg/kg 

### 2 Fuel Fluorine Content 74 mg/kg 2 Fuel Antimony Content 3.3 mg/kg 2 Fuel Arsenic Content 0.17 mg/kg



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 2 Fuel Beryllium Content 0.014 mg/kg 

### 2 Fuel Cadmium Content 0.007 mg/kg 2 Fuel Chromium Content 0.091 mg/kg 2 Fuel Cobalt Content 0.84 mg/kg 2 Fuel Lead Content 0.18 mg/kg 

### 2 Fuel Manganese Content 1.6 mg/kg 2 Fuel Nickel Content 21.6 mg/kg 2 Fuel Selenium Content 0.022mg/kg 

### 2 Fuel Sulfur Content 6160 mg/kg 2 Fuel Proximate Analysis (Carbon) 87.97 % 2 Fuel Proximate Analysis (Hydrogen) 10.5 % 2 Fuel Proximate Analysis (Nitrogen) 1.24 %



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010 Sampling / Stack Data Results Detail


### Location2 - D/F - Method 23 Average Run Number U2-23-1 U2-23-2 U2-23-3 Test Date 2/23/2010 2/24/2010 2/25/2010 Run Start Time 7:15:00 AM8:03:00 AM 9:00:00 AM Run Finish Time 3:48:00 PM4:55:00 PM 5:40:00 PM Net Traversing Points 30 30 30 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.25 0.36 0.36 0.323 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 30.21 29.98 29.82 30.003 Average Orifice Meter Differential, inches H2O 0.44 1.60 1.49 1.177 Dry Gas Meter Volume Sampled, cubic feet 181.446 341.458 334.599 285.834 Average Dry Gas Meter Temperature, °F 85.10 86.28 83.43 84.937 Dry Gas Meter Volume Sampled, dscf 173.917 325.020 318.373 272.437 Total Moisture Liquid collected, g 321.4 607.6 581.4 503.467 Volume of Water Vapor, standard cubic feet 15.13 28.60 27.37 23.700 Moisture Content of Stack Gas, % 8.00 8.09 7.92 8.003 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.92 0.9191 0.9208 0.920 Carbon Dioxide, % 10.62 10.33 10.35 10.433 Oxygen, % 8.04 8.17 8.01 8.073 Carbon Monoxide & Nitrogen, % 81.34 81.5 81.64 81.493 Fuel Factor 1.21 1.23 1.25 Dry Molecular Weight, lb/lb-Mole 30.02 29.98 29.98 29.993 Wet Molecular weight, lb/lb-Mole 29.06 29.01 29.03 29.033 Flue Gas Static Pressure, inches of H2O -1.1 -1.1 -1.1 -1.100 Absolute Flue Gas Pressure, inches of Mercury 30.13 29.90 29.74 29.923 Average Stack Gas Temperature, °F 315.90 303.43 306.07 308.467 Average Velocity Head, inches of H2O 0.1795418019 590720.144837135

4476690.133004104

672784 0.152
Average Stack Gas Velocity, feet/second 28.64 25.64 24.67 26.317 Stack Cross-Sectional Area, square feet 80.167 80.167 80.167 80.167 Dry Volumetric Flow Rate, dry scfm 86,850.7 78,343.3 74,855.980,016.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 137,759.0 123,328.9 118,663.2126,583.700 Percent Isokinetic of Sampling Rate, % 98.1 98.0 100.5 98.867 Percent Excess Air, % 59.8 61.2 59.1 60.033 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 #2, Information Collection Request
5/5/2010
Location2 - Gases - Method 10 Average Run Number 2-CO-1 2-CO-2 2-CO-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM11:13:21 AM 1:57:21 PM Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 86888 86888 8688886,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 8.01 8.01 8.01 8.010 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 0.2 0.28 0.26 0.247 Calibration Pre Zero Cylinder Bias 1.09 1.76 1.6 1.483 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID AAL4052 AAL4052 AAL4052 Calibration Pre High Cylinder Instrument Response 5.1 5.08 5.09 5.090 Calibration Pre High Cylinder Bias -0.08 -0.25 -0.17 -0.167 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response 0.28 0.26 0.21 0.250 Calibration Post Zero Cylinder Bias 1.76 1.6 1.18 1.513 Calibration Post Zero Cylinder Drift 0.67 0.16 0.42 0.417 Calibration Post High Cylinder ID AAL4052 AAL4052 AAL4052 Calibration Post High Cylinder Instrument Response 5.08 5.09 5.09 5.087 Calibration Post High Cylinder Bias -0.25 -0.17 -0.17 -0.197 Calibration Post High Cylinder Drift 0.17 0.08 0 0.083 Cavg 7.17 7.11 7.55 7.277 Cavg Units ppmvd ppmvd ppmvd Cgas 7.03 6.9892 7.4129 7.144 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil 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 #2, Information Collection Request
5/5/2010
Location2 - Gases - Method 25A Average Run Number 2-THC-1 2-THC-2 2-THC-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM11:13:21 AM 1:57:21 PM Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 86888 86888 8688886,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 8.01 8.01 8.01 8.010 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 -0.3 -0.64 0.25 -0.230 Calibration Pre Zero Cylinder Bias -0.84 -1.2 -0.26 -0.767 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID CC155655 CC155655 CC155655 Calibration Pre High Cylinder Instrument Response 25.39 24.8 24.98 25.057 Calibration Pre High Cylinder Bias 0 -0.62 -0.43 -0.350 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response -0.64 0.25 -0.7 -0.363 Calibration Post Zero Cylinder Bias -1.2 -0.26 -1.26 -0.907 Calibration Post Zero Cylinder Drift 0.36 0.94 1 0.767 Calibration Post High Cylinder ID CC155655 CC155655 CC155655 Calibration Post High Cylinder Instrument Response 24.8 24.98 25.18 24.987 Calibration Post High Cylinder Bias -0.62 -0.43 -0.22 -0.423 Calibration Post High Cylinder Drift 0.62 0.19 0.21 0.340 Cavg 0.27 0.48 0.44 0.397 Cavg Units ppmvw ppmvw ppmvw Cgas 0.7804 0.7254 0.7085 0.738 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0.7178564443 57520.667331074

347220.651728907

330567 0.679
Cgasw Units ppmvw ppmvw ppmvw



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

### William F. Wyman Energy Center, Unit #2, Information Collection Request
5/5/2010
Location2 - Gases - Method 3A CO2 Average Run Number 2-CO2-1 2-CO2-2 2-CO2-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM11:13:21 AM 1:57:21 PM Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 86888 86888 8688886,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 8.01 8.01 8.01 8.010 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 0.09 0.63 0.57 0.430 Calibration Pre Zero Cylinder Bias 0.46 3.25 2.94 2.217 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID AAL2058- CO2 AAL2058-

CO2 AAL2058-

CO2 Calibration Pre High Cylinder Instrument Response 9.13 9.18 9.22 9.177 Calibration Pre High Cylinder Bias -0.93 -0.67 -0.46 -0.687 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response 0.63 0.57 0.6 0.600 Calibration Post Zero Cylinder Bias 3.25 2.94 3.09 3.093 Calibration Post Zero Cylinder Drift 2.79 0.31 0.15 1.083 Calibration Post High Cylinder ID AAL2058- CO2 AAL2058-

CO2 AAL2058-

CO2 Calibration Post High Cylinder Instrument Response 9.18 9.22 9.45 9.283 Calibration Post High Cylinder Bias -0.67 -0.46 0.72 -0.137 Calibration Post High Cylinder Drift 0.26 0.21 1.18 0.550 Cavg 10.87 10.52 10.37 10.587 Cavg Units %vd %vd %vd Cgas 10.6235 10.2545 9.9416 10.273 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil 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 #2, Information Collection Request
5/5/2010
Location2 - Gases - Method 3A O2 Average Run Number 2-O2-1 2-O2-2 2-O2-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM11:13:21 AM 1:57:21 PM Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 86888 86888 8688886,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 8.01 8.01 8.01 8.010 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 0.4 0.09 0.05 0.180 Calibration Pre Zero Cylinder Bias 1.8 0.33 0.14 0.757 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID AAL2058-O2 AAL2058- O2AAL2058-O2
Calibration Pre High Cylinder Instrument Response 12.14 12.04 12.06 12.080 Calibration Pre High Cylinder Bias -0.05 -0.52 -0.43 -0.333 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response 0.09 0.05 0.13 0.090 Calibration Post Zero Cylinder Bias 0.33 0.14 0.52 0.330 Calibration Post Zero Cylinder Drift 1.47 0.19 0.38 0.680 Calibration Post High Cylinder ID AAL2058-O2 AAL2058- O2AAL2058-O2
Calibration Post High Cylinder Instrument Response 12.04 12.06 12.04 12.047 Calibration Post High Cylinder Bias -0.52 -0.43 -0.52 -0.490 Calibration Post High Cylinder Drift 0.47 0.09 0.09 0.217 Cavg 8.12 8.03 8.02 8.057 Cavg Units %vd %vd %vd Cgas 8.0445 8.0397 8.0228 8.036 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil 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 #2, Information Collection Request
5/5/2010
Location2 - Gases - Method 6C Average Run Number 2-SO2-1 2-SO2-2 2-SO2-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM11:13:21 AM 1:57:21 PM Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 86888 86888 8688886,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 8.01 8.01 8.01 8.010 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 2.44 8.87 6.27 5.860 Calibration Pre Zero Cylinder Bias 0.49 1.97 1.37 1.277 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID AL2793 AL2793 AL2793 Calibration Pre High Cylinder Instrument Response 247.57 255.52 258.75 253.947 Calibration Pre High Cylinder Bias -2.95 -1.12 -0.38 -1.483 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response 8.87 6.27 5.39 6.843 Calibration Post Zero Cylinder Bias 1.97 1.37 1.17 1.503 Calibration Post Zero Cylinder Drift 1.48 0.6 0.2 0.760 Calibration Post High Cylinder ID AL2793 AL2793 AL2793 Calibration Post High Cylinder Instrument Response 255.52 258.75 257.58 257.283 Calibration Post High Cylinder Bias -1.12 -0.38 -0.65 -0.717 Calibration Post High Cylinder Drift 1.83 0.74 0.27 0.947 Cavg 265.91 267.97 274.86 269.580 Cavg Units ppmvd ppmvd ppmvd Cgas 270.9556 267.1144 272.9375 270.336 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil 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 #2, Information Collection Request
5/5/2010
Location2 - Gases - Method 7E Average Run Number 2-NOx-1 2-NOx-2 2-NOx-3 Test Date 2/23/2010 2/23/2010 2/23/2010 Run Start Time 8:47:21 AM11:13:21 AM 1:57:21 PM Run Finish Time 10:46:51 AM1:12:51 PM 3:56:51 PM Carbon Dioxide, % 10.62 10.25 9.94 10.270 Oxygen, % 8.04 8.04 8.02 8.033 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 86888 86888 8688886,888.000 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 8.01 8.01 8.01 8.010 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 0.59 0.57 0.38 0.513 Calibration Pre Zero Cylinder Bias 0.18 0.17 0.09 0.147 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID ALM057559ALM057559ALM057559 Calibration Pre High Cylinder Instrument Response 105.24 106.74 105.68 105.887 Calibration Pre High Cylinder Bias -1.85 -1.24 -1.67 -1.587 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337ALM031337ALM031337 Calibration Post Zero Cylinder Instrument Response 0.57 0.38 0.64 0.530 Calibration Post Zero Cylinder Bias 0.17 0.09 0.2 0.153 Calibration Post Zero Cylinder Drift 9.9999999999 9998E-03 0.08 0.11 0.067
Calibration Post High Cylinder ID ALM057559ALM057559ALM057559 Calibration Post High Cylinder Instrument Response 106.74 105.68 106.42 106.280 Calibration Post High Cylinder Bias -1.24 -1.67 -1.37 -1.427 Calibration Post High Cylinder Drift 0.61 0.43 0.3 0.447 Cavg 148.34 147.61 146.85 147.600 Cavg Units ppmvd ppmvd ppmvd Cgas 155.5959 154.4615 153.9107 154.656 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil 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 #2, Information Collection Request
5/5/2010
Location2 - Metals - Method 29 Average Run Number U2-29-1 U2-29-2 U2-29-3 Test Date 2/23/2010 2/24/2010 2/25/2010 Run Start Time 7:39:00 AM8:24:00 AM 7:00:00 AM Run Finish Time 2:09:00 PM12:53:00 PM11:14:00 AM Net Traversing Points 30 30 30 Net Run Time, minutes 300 240 240 Nozzle Diameter, inches 0.272 0.36 0.36 0.331 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 29.98 29.89 29.89 29.920 Average Orifice Meter Differential, inches H2O 0.50 1.57 1.69 1.253 Dry Gas Meter Volume Sampled, cubic feet 143.205 166.905 172.387 160.832 Average Dry Gas Meter Temperature, °F 86.33 86.95 87.75 87.010 Dry Gas Meter Volume Sampled, dscf 139.126 161.906 167.028 156.020 Total Moisture Liquid collected, g 386.6 352.6 328.4 355.867 Volume of Water Vapor, standard cubic feet 18.20 16.60 15.46 16.753 Moisture Content of Stack Gas, % 11.57 9.30 8.47 9.780 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8843 0.907 0.9153 0.902 Carbon Dioxide, % 10.62 10.33 10.35 10.433 Oxygen, % 8.04 8.17 8.01 8.073 Carbon Monoxide & Nitrogen, % 81.34 81.5 81.64 81.493 Fuel Factor 1.21 1.23 1.25 Dry Molecular Weight, lb/lb-Mole 30.02 29.98 29.98 29.993 Wet Molecular weight, lb/lb-Mole 28.63 28.87 28.97 28.823 Flue Gas Static Pressure, inches of H2O -1.1 -1.1 -1.1 -1.100 Absolute Flue Gas Pressure, inches of Mercury 29.90 29.81 29.81 29.840 Average Stack Gas Temperature, °F 316.80 306.50 307.20 310.167 Average Velocity Head, inches of H2O 0.2001964738 802350.142588536

5392040.151528618

523797 0.165
Average Stack Gas Velocity, feet/second 30.61 25.59 26.35 27.517 Stack Cross-Sectional Area, square feet 80.167 80.167 80.167 80.167 Dry Volumetric Flow Rate, dry scfm 88,439.1 76,620.8 79,545.781,535.200 Actual Wet Volumetric Flue Gas Flow Rate, acfm 147,234.7 123,088.4 126,744.0132,355.700 Percent Isokinetic of Sampling Rate, % 104.2 99.9 99.2 101.100 Percent Excess Air, % 59.8 61.2 59.1 60.033 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 #2, Information Collection Request
5/5/2010
Location2 - PM - OTM - 27/28 Average Run Number U2-27/28-1 U2-27/28-2 U2-27/28-3 Test Date 2/24/2010 2/25/2010 2/25/2010 Run Start Time 5:04:00 PM7:54:00 AM 2:42:00 PM Run Finish Time 10:21:00 PM1:50:00 PM 8:19:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 294 322 308 Nozzle Diameter, inches 0.253 0.253 0.253 0.253 Pitot Tube Coefficient 0.8 0.8 0.8 0.800 Dry Gas Meter Calibration Factor 1.002 0.987 0.987 0.992 Barometric Pressure, inches of Mercury 29.96 29.89 29.65 29.833 Average Orifice Meter Differential, inches H2O 0.38 0.38 0.38 0.380 Dry Gas Meter Volume Sampled, cubic feet 108.000 123.939 121.269 117.736 Average Dry Gas Meter Temperature, °F 84.13 77.58 73.25 78.320 Dry Gas Meter Volume Sampled, dscf 105.247 120.140 117.555 114.314 Total Moisture Liquid collected, g 315 400.1 369.3 361.467 Volume of Water Vapor, standard cubic feet 14.83 18.83 17.38 17.013 Moisture Content of Stack Gas, % 12.35 13.55 12.88 12.927 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.8765 0.8645 0.8712 0.871 Carbon Dioxide, % 10.33 10.35 10.35 10.343 Oxygen, % 8.17 8.01 8.01 8.063 Carbon Monoxide & Nitrogen, % 81.5 81.64 81.64 81.593 Fuel Factor 1.23 1.25 1.25 Dry Molecular Weight, lb/lb-Mole 29.98 29.98 29.98 29.980 Wet Molecular weight, lb/lb-Mole 28.50 28.36 28.44 28.433 Flue Gas Static Pressure, inches of H2O -1.1 -1.1 -1.1 -1.100 Absolute Flue Gas Pressure, inches of Mercury 29.88 29.81 29.57 29.753 Average Stack Gas Temperature, °F 302.92 306.58 305.25 304.917 Average Velocity Head, inches of H2O 0.1740433571 842330.171327661

6100240.179031868

186227 0.175
Average Stack Gas Velocity, feet/second 27.01 26.96 27.60 27.190 Stack Cross-Sectional Area, square feet 80.167 80.167 80.167 80.167 Dry Volumetric Flow Rate, dry scfm 78,704.1 76,932.3 78,866.878,167.733 Actual Wet Volumetric Flue Gas Flow Rate, acfm 129,918.6 129,678.1 132,756.6130,784.433 Percent Isokinetic of Sampling Rate, % 104.4 111.4 111.1 108.967 Percent Excess Air, % 61.2 59.1 59.1 59.800 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