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 ME 04096

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:

2 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

2 - D/F 0 78 148 102 779 303 6 30

2 - Gases 0 78 148 102 779 303 6 1

2 - Metals 0 78 148 102 779 303 6 30

2 - 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 #2, Information Collection Request

5/5/2010

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

2 - D/F % 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

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

HxCB (PCBs156/157)

2 - D/F 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

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

(PCB189)

2 - D/F 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

% 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

2 - Metals % H2O Method 1 - 4 3 240 30

2 - Metals Manganese Method 29 3 240 30

2 - Metals Chromium Method 29 3 240 30

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.

2 - Metals 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

% 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

Location 2 - 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 PM 4:55:00 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

Location 2 - 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 AM 1:12:51 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

Location 2 - 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 AM 1:12:51 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

Location 2 - 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 AM 1:12:51 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

Location 2 - 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 AM 1:12:51 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

Location 2 - 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 AM 1:12:51 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

Location 2 - 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 AM 1:12:51 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

Location 2 - 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 

PM

11:14:00 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

Location 2 - 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 PM 7:54:00 

AM

2:42:00 PM

Run Finish Time 10:21:00 PM 1:50:00 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

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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

10 Residual Oil (No. 6) Burned 296489 gal/hr Method 027/028; 

Run PM-1; Date - 

2/24/2010; Start - 

17:04; End - 22:21

0

10 Average Heat Input 253 MMBtu/hr Method 027/028; 

Run PM-1; Date - 

2/24/2010; Start - 

17:04; End - 22:21

0

10 Steam Output 171 1000 lb Method 027/028; 

Run PM-1; Date - 

2/24/2010; Start - 

17:04; End - 22:21

0

10 Unit Gross Electrical Output 23 MWg Method 027/028; 

Run PM-1; Date - 

2/24/2010; Start - 

17:04; End - 22:21

0

11 Residual Oil (No. 6) Burned 299263 gal/hr Method 027/028; 

Run PM-2; Date - 

2/25/2010; Start - 

07:54; End - 13:50

0

11 Average 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

11 Steam Output 187 1000 lb Method 027/028; 

Run PM-2; Date - 

2/25/2010; Start - 

07:54; End - 13:50

0

11 Unit Gross Electrical Output 23 MWg Method 027/028; 

Run PM-2; Date - 

2/25/2010; Start - 

07:54; End - 13:50

0

12 Residual Oil (No. 6) Burned 300772 gal/hr Method 027/028; 

Run PM-3; Date - 

2/25/2010; Start - 

14:42; End - 20:19

0

12 Average Heat Input 256 MMBtu/hr Method 027/028; 

Run PM-3; Date - 

2/25/2010; Start - 

14:42; End - 20:19

0

12 Steam Output 187 1000 lb Method 027/028; 

Run PM-3; Date - 

2/25/2010; Start - 

14:42; End - 20:19

0

12 Unit 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 156 NOx Emissions 0

2 LOW NOX BURNERS 154 NOx Emissions 0

3 LOW NOX BURNERS 154 NOx Emissions 0

1 CYCLONE SEPARATORS 6 Opacity 0

2 CYCLONE SEPARATORS 6 Opacity 0

3 CYCLONE SEPARATORS 6 Opacity 0

Run Name Value UOM Comments

2 Fuel Proximate Analysis (Oxygen) 0.5 %

2 Fuel Proximate Analysis (Sulfur) 0.694 %

3 Fuel Higher Heating Value 18300 Btu/lb

3 Fuel Moisture 0.181 %

3 Fuel Mercury Content 0.0004 mg/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 0.006 mg/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 18300 Btu/lb

1 Fuel Moisture 0.33 %

1 Fuel Mercury Content 0.0004 mg/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 0.022 mg/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 18300 Btu/lb

2 Fuel Moisture 0.365 %

2 Fuel Mercury Content 0.0004 mg/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 0.022 mg/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

Location 2 - 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 PM 4:55:00 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

59072

0.144837135

447669

0.133004104

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 74,855.9 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

Percent Excess Air, % 59.8 61.2 59.1 60.033

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 #2, Information Collection Request

5/5/2010

Location 2 - 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 AM 1:12:51 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 86888 86,888.000

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

Moisture, % 8.01 8.01 8.01 8.010

Analyzer Make THERMO THERMO THERMO

Analyzer Model 48i 48i 48i

Analyzer Serial Number INST-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 0.2 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 ALM031337 ALM031337 ALM031337

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 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 #2, Information Collection Request

5/5/2010

Location 2 - 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 AM 1:12:51 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 86888 86,888.000

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

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-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 -0.3 -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 ALM031337 ALM031337 ALM031337

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 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Cgasw 0.7178564443

5752

0.667331074

34722

0.651728907

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

Location 2 - 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 AM 1:12:51 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 86888 86,888.000

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

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 ALM031337 ALM031337 ALM031337

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 ALM031337 ALM031337 ALM031337

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 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 #2, Information Collection Request

5/5/2010

Location 2 - 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 AM 1:12:51 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 86888 86,888.000

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

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 ALM031337 ALM031337 ALM031337

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-

O2

AAL2058-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 ALM031337 ALM031337 ALM031337

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-

O2

AAL2058-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 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 #2, Information Collection Request

5/5/2010

Location 2 - 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 AM 1:12:51 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 86888 86,888.000

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

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 ALM031337 ALM031337 ALM031337

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 ALM031337 ALM031337 ALM031337

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 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 #2, Information Collection Request

5/5/2010

Location 2 - 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 AM 1:12:51 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 86888 86,888.000

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

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 ALM031337 ALM031337 ALM031337

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 ALM057559 ALM057559 ALM057559

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 ALM031337 ALM031337 ALM031337

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 ALM057559 ALM057559 ALM057559

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 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 #2, Information Collection Request

5/5/2010

Location 2 - 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 PM 11:14:00 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

80235

0.142588536

539204

0.151528618

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 79,545.7 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

Percent Excess Air, % 59.8 61.2 59.1 60.033

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 #2, Information Collection Request

5/5/2010

Location 2 - 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 PM 7:54:00 AM 2:42:00 PM

Run Finish Time 10:21:00 PM 1:50:00 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

84233

0.171327661

610024

0.179031868

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 78,866.8 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

Percent Excess Air, % 61.2 59.1 59.1 59.800

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