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 ME 4096

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 OK 74146

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:

1 Foster Wheeler, dry bottom hopper boiler

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/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 2300500018 FRS #: 110000581406

SCC / Description 10100401 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 78 148 102 779 303 6 30

1 - Gases 0 78 148 102 779 303 6 1

1 - Metals 0 78 148 102 779 303 6 30

1 - PM 0 78 148 102 779 303 6 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

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 

Location Points Comments

1 - D/F 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

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

1 - D/F 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

2,3,3',4,4',5,5'-HpCB 

(PCB189)

1 - D/F Method 23 3 480 30

% 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

1 - Metals % 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

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.

1 - Metals 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

% 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 PM 4:43:00 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 AM 1:14:55 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, 

Residual

Oil, 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 AM 1:14:55 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, 

Residual

Oil, 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 AM 1:14:55 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, 

Residual

Oil, 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 AM 1:14:55 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, 

Residual

Oil, 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 AM 1:14:55 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, 

Residual

Oil, 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 AM 1:14:55 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, 

Residual

Oil, 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 

AM

11:27:00 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

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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 AM 7:39:00 

AM

7:53:00 AM

Run Finish Time 1:06:00 PM 1:16:00 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 154,545.9 150,601.7 146,898.0 150,681.867

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

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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

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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

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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

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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

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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

10 Residual Oil (No. 6) Burned 355520 gal/hr Method 027/028; 

Run PM-1; Date - 

3/2/2010; Start - 

07:41; End - 13:06

0

10 Average Heat Input 303 MMBtu/hr Method 027/028; 

Run PM-1; Date - 

3/2/2010; Start - 

07:41; End - 13:06

0

10 Steam Output 140 1000 lb Method 027/028; 

Run PM-1; Date - 

3/2/2010; Start - 

07:41; End - 13:06

0

10 Unit Gross Electrical Output 22 Mwe Method 027/028; 

Run PM-1; Date - 

3/2/2010; Start - 

07:41; End - 13:06

0

11 Residual Oil (No. 6) Burned 339913 gal/hr Method 027/028; 

Run PM-2; Date - 

3/3/2010; Start - 

07:39; End - 13:16

0

11 Average 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

11 Steam Output 212 1000 lb Method 027/028; 

Run PM-2; Date - 

3/3/2010; Start - 

07:39; End - 13:16

0

11 Unit Gross Electrical Output 22 Mwe Method 027/028; 

Run PM-2; Date - 

3/3/2010; Start - 

07:39; End - 13:16

0

12 Residual Oil (No. 6) Burned 333314 gal/hr Method 027/028; 

Run PM-3; Date - 

3/4/2010; Start - 

07:53; End - 13:28

0

12 Average Heat Input 284 MMBtu/hr Method 027/028; 

Run PM-3; Date - 

3/4/2010; Start - 

07:53; End - 13:28

0

12 Steam Output 102 1000 lb Method 027/028; 

Run PM-3; Date - 

3/4/2010; Start - 

07:53; End - 13:28

0

12 Unit 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 165 NOx Emissions 0

2 LOW NOX BURNERS 167 NOx Emissions 0

3 LOW NOX BURNERS 169 NOx Emissions 0

1 CYCLONE SEPARATORS 2 Opacity 0

2 CYCLONE SEPARATORS 2 Opacity 0

3 CYCLONE SEPARATORS 2 Opacity 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 18100 Btu/lb

2 Fuel Higher Heating Value 18200 Btu/lb

3 Fuel Higher Heating Value 18000 Btu/lb

1 Fuel Moisture 0.157 %

2 Fuel Moisture 0.272 %

3 Fuel Moisture 0.366 %

1 Fuel Mercury Content 0.0003 mg/kg

2 Fuel Mercury Content 0.0003 mg/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 0.0003 mg/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 0.014 mg/kg

1 Fuel Cadmium Content 0.007 mg/kg

2 Fuel Cadmium Content 0.006 mg/kg

3 Fuel Cadmium Content 0.006 mg/kg

1 Fuel Chromium Content 0.087 mg/kg

2 Fuel Chromium Content 0.089 mg/kg

3 Fuel Chromium Content 0.084 mg/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 0.022 mg/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 AM 8:23:00 AM 9:19:00 AM

Run Finish Time 4:57:00 PM 4:43:00 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

51385

0.183944288

018723

0.172432857

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 85,652.5 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

Percent Excess Air, % 82.4 78.4 79.0 79.933

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 148 148 148

Rectangular Duct Length, inches 78 78 78

Fw 10320 10320 10320 10,320.000

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 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM 1:14:55 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 91750 91,750.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Moisture, % 7.43 7.43 7.43 7.430

Analyzer Make THERMO THERMO THERMO

Analyzer Model 48i 48i 48i

Analyzer Serial Number INST-CO0015INST-CO0015INST-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 ALM031337 ALM031337 ALM031337

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 ALM031337 ALM031337 ALM031337

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, Residual Oil, Residual Oil, Residual

Fw 10320 10320 10320 10,320.000

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 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM 1:14:55 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 91750 91,750.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

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-TH0009INST-TH0009INST-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 ALM031337 ALM031337 ALM031337

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 ALM031337 ALM031337 ALM031337

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, Residual Oil, Residual Oil, Residual

Fw 10320 10320 10320 10,320.000

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 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM 1:14:55 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 91750 91,750.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

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 ALM031337 ALM031337 ALM031337

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 ALM031337 ALM031337 ALM031337

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, Residual Oil, Residual Oil, Residual

Fw 10320 10320 10320 10,320.000

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 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM 1:14:55 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 91750 91,750.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

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 ALM031337 ALM031337 ALM031337

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-

O2

AAL2058-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 ALM031337 ALM031337 ALM031337

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-

O2

AAL2058-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, Residual Oil, Residual Oil, Residual

Fw 10320 10320 10320 10,320.000

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 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM 1:14:55 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 91750 91,750.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

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 ALM031337 ALM031337 ALM031337

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 ALM031337 ALM031337 ALM031337

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, Residual Oil, Residual Oil, Residual

Fw 10320 10320 10320 10,320.000

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 AM 11:15:25 AM 1:37:25 PM

Run Finish Time 10:54:55 AM 1:14:55 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 91750 91,750.000

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

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 ALM031337 ALM031337 ALM031337

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 ALM057559 ALM057559 ALM057559

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 ALM031337 ALM031337 ALM031337

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 ALM057559 ALM057559 ALM057559

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, Residual Oil, Residual Oil, Residual

Fw 10320 10320 10320 10,320.000

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 AM 6:45:00 AM 7:03:00 AM

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

42176

0.208695122

274016

0.193298856

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 90,187.3 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

Percent Excess Air, % 82.4 78.4 79.0 79.933

F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 148 148 148

Rectangular Duct Length, inches 78 78 78

Fw 10320 10320 10320 10,320.000

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 AM 7:39:00 AM 7:53:00 AM

Run Finish Time 1:06:00 PM 1:16:00 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

91801

0.235468700

863922

0.220730716

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 90,459.8 94,728.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 154,545.9 150,601.7 146,898.0 150,681.867

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 9190 9,190.000

Round Duct Diameter, inches 0 0 0

Rectangular Duct Width, inches 148 148 148

Rectangular Duct Length, inches 78 78 78

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Thursday, February 24, 2011 Page 33 of 33