Name: Paul Plotkin

Title: General Manager

Company: Florida Power & Light Manatee Plant

Sign Date: 7/14/2010

Name: Thomas K. Graham

Title: Director of Operations

Company: Air Hygiene International, Inc.

Sign Date: 7/10/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Manatee 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.

Monday, February 14, 2011 Page 1 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Facility Information:

Manatee Energy Center

19050 State Road 62

Parrish FL 34219

Contact: Augie De La Vega

Phone: (305) 242-3896

Fax:

Email: augie.de.la.vega@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:

0810010-014-AV

Permitted Source ID/Name:

PMT2 Foster Wheeler, Wall Fired Boiler

Permitted Maximum Process Rate:

863.3 MW

Max. Normal Operation Process Rate:

800 MW

Target Process Test Rate

800 MW

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

Florida Power and Light Company (FPL) operates two oil fired electric utility steam generating units of Foster 

Wheeler design, designated as Units PMT1 and PMT2. The facility is located at 19050 State Road 62 in Parrish, 

Florida. Unit PMT1 and PMT2 are of identical design and consists of two wall fired boilers and ancillary equipment 

designed to generate 863.3 megawatts (MW) of electricity each with rated heat inputs of 8,650 million British 

thermal units per hour (MMBtu/hr) based on high heating value (HHV). Fuel oil consumption is rated at 600,000 

pounds per hour. Unit PMT1 and PMT2 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 platforms on the independent stacks of each unit.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 0810010 FRS #: 110000496776

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

PMT2 - D/F 357.4 0 0 0 4524 876 4 24

PMT2 - Gases 357.4 0 0 0 4524 876 4 1

PMT2 - Metals 357.4 0 0 0 4524 876 4 24

PMT2 - PM 357.4 0 0 0 4524 876 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Regulation Description Compound Limit Unit

Not applicable.

Monday, February 14, 2011 Page 2 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

PMT2 - D/F % H2O Method 1 - 4 3 480 24

PMT2 - D/F 2,3,7,8-TCDD Method 23 3 480 24

PMT2 - D/F 1,2,3,7,8-PeCDD Method 23 3 480 24

PMT2 - D/F 1,2,3,4,7,8-HxCDD Method 23 3 480 24

PMT2 - D/F 1,2,3,6,7,8-HxCDD Method 23 3 480 24

PMT2 - D/F 1,2,3,7,8,9-HxCDD Method 23 3 480 24

PMT2 - D/F 1,2,3,4,6,7,8-HpCDD Method 23 3 480 24

PMT2 - D/F OCDD Method 23 3 480 24

PMT2 - D/F 2,3,7,8-TCDF Method 23 3 480 24

PMT2 - D/F 1,2,3,7,8-PeCDF Method 23 3 480 24

PMT2 - D/F 2,3,4,7,8-PeCDF Method 23 3 480 24

PMT2 - D/F 1,2,3,4,7,8-HxCDF Method 23 3 480 24

PMT2 - D/F 1,2,3,6,7,8-HxCDF Method 23 3 480 24

PMT2 - D/F 2,3,4,6,7,8-HxCDF Method 23 3 480 24

PMT2 - D/F 1,2,3,7,8,9-HxCDF Method 23 3 480 24

PMT2 - D/F 1,2,3,4,6,7,8-HpCDF Method 23 3 480 24

PMT2 - D/F 1,2,3,4,7,8,9-HpCDF Method 23 3 480 24

PMT2 - D/F OCDF Method 23 3 480 24

PMT2 - D/F Total Dioxins Method 23 3 480 24

PMT2 - D/F Total Furans Method 23 3 480 24

PMT2 - D/F 3,3',4,4'-TCB (PCB77) Method 23 3 480 24

PMT2 - D/F 3,4,4',5-TCB (PCB81) Method 23 3 480 24

PMT2 - D/F 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 24

PMT2 - D/F 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 24

PMT2 - D/F 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 24

PMT2 - D/F 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 24

PMT2 - D/F 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 24

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

HxCB (PCBs156/157)

PMT2 - D/F Method 23 3 480 24

PMT2 - D/F 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 24

PMT2 - D/F 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 24

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

(PCB189)

PMT2 - D/F Method 23 3 480 24

PMT2 - D/F O2 Method 3A O2 3 480 24

PMT2 - D/F Co2 Method 3A CO2 3 480 24

% H2O Method 1 - 4 3 120 1 Determined after 

initial stratification test

PMT2 - Gases

Carbon Monoxide Method 10 3 120 1 Determined after 

initial stratification test

PMT2 - Gases

Total organic compounds 

(TOC) as Propane

Method 25A 3 120 1 Determined after 

initial stratification test

PMT2 - Gases

O2 Method 3A O2 3 120 1 Determined after 

initial stratification test

PMT2 - Gases

Co2 Method 3A CO2 3 120 1 Determined after 

initial stratification test

PMT2 - Gases

Sulfur Dioxide Method 6C 3 120 1 Determined after 

initial stratification test

PMT2 - Gases

Nitrogen oxides (NOx) Method 7E 3 120 1 Determined after 

initial stratification test

PMT2 - Gases

PMT2 - Metals % H2O Method 1 - 4 3 240 24

PMT2 - Metals Selenium Method 29 3 240 24

PMT2 - Metals Manganese Method 29 3 240 24

Monday, February 14, 2011 Page 3 of 34
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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.

PM Run All - reduced to 2 hour runs to avoid high vacuum, did not pull required volumes.
PM Run 3 - oily 

substance in organic backhalf.

PMT2 - Metals Lead Method 29 3 240 24

PMT2 - Metals Filterable Particulate Method 29 3 240 24

PMT2 - Metals Cobalt Method 29 3 240 24

PMT2 - Metals Cadmium Method 29 3 240 24

PMT2 - Metals Chromium Method 29 3 240 24

PMT2 - Metals Nickel Method 29 3 240 24

PMT2 - Metals Co2 Method 3A CO2 3 240 24

PMT2 - Metals O2 Method 3A O2 3 240 24

% H2O Method 1 - 4 3 120 12 Run times vary based 

on method calculations

PMT2 - PM

Filterable Particulate OTM - 27/28 3 120 12 Run times vary based 

on method calculations

PMT2 - PM

Filterable PM2.5 OTM - 27/28 3 120 12 Run times vary based 

on method calculations

PMT2 - PM

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 120 12 Run times vary based 

on method calculations

PMT2 - PM

Organic Condensible 

Particulate

OTM - 27/28 3 120 12 Run times vary based 

on method calculations

PMT2 - PM

Total PM2.5 OTM - 27/28 3 120 12 Run times vary based 

on method calculations

PMT2 - PM

Total Particulate OTM - 27/28 3 120 12 Run times vary based 

on method calculations

PMT2 - PM

O2 Method 3A O2 3 120 12 Run times vary based 

on method calculations

PMT2 - PM

Co2 Method 3A CO2 3 120 12 Run times vary based 

on method calculations

PMT2 - PM

Monday, February 14, 2011 Page 4 of 34
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Sampling / Stack Data Results Summary

Location PMT2 - D/F - Method 23

Average

Run Number PMT2-23-1 PMT2-23-2 PMT2-23-3

Test Date 5/11/2010 5/12/2010 5/13/2010

Run Start Time 12:58:00 PM 12:00:00 

PM

8:06:00 AM

Run Finish Time 8:58:00 PM 8:00:00 PM 4:06:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 365.205 374.736 379.425 373.122

Moisture Content of Stack Gas, % 9.20 9.09 8.71 9.000

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 12.59 12.9 12.7 12.730

Oxygen, % 4.99 5.04 5.11 5.047

Average Stack Gas Temperature, °F 320.08 321.71 321.63 321.140

Dry Volumetric Flow Rate, dry scfm 1,584,973.2 1,601,200.3 1,624,125.4 1,603,432.96

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,570,349.6 2,593,758.3 2,619,674.9 2,594,594.26

7

Percent Isokinetic of Sampling Rate, % 98.1 99.6 99.5 99.067

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 PMT2 - Gases - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Monday, February 14, 2011 Page 5 of 34
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Location PMT2 - Gases - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location PMT2 - Gases - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc PMT2 - 

Gases

PMT2 - 

Gases

PMT2 - 

Gases

Monday, February 14, 2011 Page 6 of 34
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Location PMT2 - Gases - Method 3A O2

Average

Run Number 2-O2-1 2-O2-2 2-O2-3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM

Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM

Carbon Dioxide, % 12.59 12.9 12.7 12.730

Oxygen, % 4.99 5.04 5.11 5.047

Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.00

0

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

Moisture, % 9.22 9.22 9.22 9.220

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location PMT2 - Gases - Method 6C

Average

Run Number 2-SO2-1 2-SO2-2 2-SO2-3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM

Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM

Carbon Dioxide, % 12.59 12.9 12.7 12.730

Oxygen, % 4.99 5.04 5.11 5.047

Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.00

0

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

Moisture, % 9.22 9.22 9.22 9.220

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 14, 2011 Page 7 of 34
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Location PMT2 - Gases - Method 7E

Average

Run Number 2-NOx-1 2-NOx-2 2-NOx-3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM

Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM

Carbon Dioxide, % 12.59 12.9 12.7 12.730

Oxygen, % 4.99 5.04 5.11 5.047

Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.00

0

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

Moisture, % 9.22 9.22 9.22 9.220

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location PMT2 - Metals - Method 29

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 14, 2011 Page 8 of 34
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Location PMT2 - PM - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Monday, February 14, 2011 Page 9 of 34
Manatee Energy Center, Unit #2, Information Collection Request

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Emissions Summary

Location: PMT2 - D/F - Method 23

Compound: 1,2,3,4,6,7,8-HpCDD

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000077 0.0000000037 0.0000000089 0.000

lb/mmBtuO2 5.61E-13 2.64E-13 6.29E-13 0.000

ng/dscm 7.45E-04 3.49E-04 8.28E-04 0.001

ng/dscm@7%O2 6.51E-04 3.06E-04 7.29E-04 0.001

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000042 0.000000003 0.0000000083 0.000

lb/mmBtuO2 3.06E-13 2.14E-13 5.87E-13 0.000

ng/dscm 4.06E-04 2.83E-04 7.73E-04 0.000

ng/dscm@7%O2 3.55E-04 2.48E-04 6.80E-04 0.000

Compound: 1,2,3,4,7,8,9-HpCDF

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000058 0.0000000041 0.000000006 0.000

lb/mmBtuO2 4.23E-13 2.92E-13 4.24E-13 0.000

ng/dscm 5.61E-04 3.86E-04 5.59E-04 0.001

ng/dscm@7%O2 4.90E-04 3.38E-04 4.92E-04 0.000

Compound: 1,2,3,4,7,8-HxCDD

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000069 0.0000000032 0.0000000049 0.000

lb/mmBtuO2 5.03E-13 2.28E-13 3.46E-13 0.000

ng/dscm 6.67E-04 3.02E-04 4.56E-04 0.000

ng/dscm@7%O2 5.83E-04 2.65E-04 4.01E-04 0.000

Compound: 1,2,3,4,7,8-HxCDF

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000047 0.0000000032 0.0000000029 0.000

lb/mmBtuO2 3.43E-13 2.28E-13 2.05E-13 0.000

ng/dscm 4.55E-04 3.02E-04 2.70E-04 0.000

ng/dscm@7%O2 3.98E-04 2.65E-04 2.38E-04 0.000

Compound: 1,2,3,6,7,8-HxCDD

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000057 0.0000000027 0.0000000041 0.000

lb/mmBtuO2 4.15E-13 1.92E-13 2.90E-13 0.000

ng/dscm 5.51E-04 2.54E-04 3.82E-04 0.000

ng/dscm@7%O2 4.81E-04 2.23E-04 3.36E-04 0.000

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

Average

Monday, February 14, 2011 Page 10 of 34
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RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000042 0.0000000028 0.0000000026 0.000

lb/mmBtuO2 3.06E-13 1.99E-13 1.84E-13 0.000

ng/dscm 4.06E-04 2.64E-04 2.42E-04 0.000

ng/dscm@7%O2 3.55E-04 2.31E-04 2.13E-04 0.000

Compound: 1,2,3,7,8,9-HxCDD

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.000000006 0.0000000028 0.0000000043 0.000

lb/mmBtuO2 4.37E-13 1.99E-13 3.04E-13 0.000

ng/dscm 5.80E-04 2.64E-04 4.00E-04 0.000

ng/dscm@7%O2 5.07E-04 2.31E-04 3.52E-04 0.000

Compound: 1,2,3,7,8,9-HxCDF

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000053 0.0000000036 0.0000000033 0.000

lb/mmBtuO2 3.86E-13 2.56E-13 2.33E-13 0.000

ng/dscm 5.13E-04 3.39E-04 3.07E-04 0.000

ng/dscm@7%O2 4.48E-04 2.97E-04 2.70E-04 0.000

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000054 0.0000000043 0.0000000052 0.000

lb/mmBtuO2 3.94E-13 3.06E-13 3.68E-13 0.000

ng/dscm 5.22E-04 4.05E-04 4.84E-04 0.000

ng/dscm@7%O2 4.56E-04 3.55E-04 4.26E-04 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000053 0.000000008 0.0000000045 0.000

lb/mmBtuO2 3.86E-13 5.70E-13 3.18E-13 0.000

ng/dscm 5.13E-04 7.54E-04 4.19E-04 0.001

ng/dscm@7%O2 4.48E-04 6.61E-04 3.69E-04 0.000

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.000000016 0.0000000023 0.0000000817 0.000

lb/mmBtuO2 1.17E-12 1.64E-13 5.77E-12 0.000

ng/dscm 1.55E-03 2.17E-04 7.61E-03 0.003

ng/dscm@7%O2 1.35E-03 1.90E-04 6.70E-03 0.003

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000659 0.0000000043 0.000000216 0.000

lb/mmBtuO2 4.80E-12 3.06E-13 1.53E-11 0.000

ng/dscm 6.37E-03 4.05E-04 2.01E-02 0.009

ng/dscm@7%O2 5.57E-03 3.55E-04 1.77E-02 0.008

Monday, February 14, 2011 Page 11 of 34
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Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.000000395 0.0000000996 0.00000137 0.000

lb/mmBtuO2 2.88E-11 7.10E-12 9.68E-11 0.000

ng/dscm 3.82E-02 9.39E-03 1.28E-01 0.059

ng/dscm@7%O2 3.34E-02 8.23E-03 1.13E-01 0.052

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000772 0.0000000023 0.00000031 0.000

lb/mmBtuO2 5.63E-12 1.64E-13 2.19E-11 0.000

ng/dscm 7.47E-03 2.17E-04 2.89E-02 0.012

ng/dscm@7%O2 6.53E-03 1.90E-04 2.54E-02 0.011

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.000000018 0.000000013 0.000000098 0.000

lb/mmBtuO2 1.31E-12 9.26E-13 6.93E-12 0.000

ng/dscm 1.74E-03 1.23E-03 9.12E-03 0.004

ng/dscm@7%O2 1.52E-03 1.08E-03 8.03E-03 0.004

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.00000105 0.00000027 0.00000301 0.000

lb/mmBtuO2 7.65E-11 1.92E-11 2.13E-10 0.000

ng/dscm 1.02E-01 2.54E-02 2.80E-01 0.136

ng/dscm@7%O2 8.91E-02 2.23E-02 2.46E-01 0.119

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.000000043 0.000000013 0.000000097 0.000

lb/mmBtuO2 3.13E-12 9.26E-13 6.86E-12 0.000

ng/dscm 4.16E-03 1.23E-03 9.03E-03 0.005

ng/dscm@7%O2 3.63E-03 1.08E-03 7.95E-03 0.004

Compound: 2,3,4,6,7,8-HxCDF

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000045 0.000000003 0.0000000028 0.000

lb/mmBtuO2 3.28E-13 2.14E-13 1.98E-13 0.000

ng/dscm 4.35E-04 2.83E-04 2.61E-04 0.000

ng/dscm@7%O2 3.80E-04 2.48E-04 2.30E-04 0.000

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.000000005 0.0000000077 0.0000000043 0.000

lb/mmBtuO2 3.64E-13 5.49E-13 3.04E-13 0.000

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ng/dscm 4.84E-04 7.26E-04 4.00E-04 0.001

ng/dscm@7%O2 4.23E-04 6.36E-04 3.52E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000069 0.0000000082 0.0000000042 0.000

lb/mmBtuO2 5.03E-13 5.84E-13 2.97E-13 0.000

ng/dscm 6.67E-04 7.73E-04 3.91E-04 0.001

ng/dscm@7%O2 5.83E-04 6.77E-04 3.44E-04 0.001

Compound: 2,3,7,8-TCDF

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000068 0.0000000057 0.0000000042 0.000

lb/mmBtuO2 4.96E-13 4.06E-13 2.97E-13 0.000

ng/dscm 6.58E-04 5.37E-04 3.91E-04 0.001

ng/dscm@7%O2 5.75E-04 4.71E-04 3.44E-04 0.000

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000039 0.0000000022 0.000000012 0.000

lb/mmBtuO2 2.84E-13 1.57E-13 8.48E-13 0.000

ng/dscm 3.77E-04 2.07E-04 1.12E-03 0.001

ng/dscm@7%O2 3.29E-04 1.81E-04 9.86E-04 0.000

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.000000023 0.000000016 0.0000000587 0.000

lb/mmBtuO2 1.68E-12 1.14E-12 4.15E-12 0.000

ng/dscm 2.22E-03 1.51E-03 5.46E-03 0.003

ng/dscm@7%O2 1.94E-03 1.32E-03 4.81E-03 0.003

Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000974 0.00000003 0.000000292 0.000

lb/mmBtuO2 7.10E-12 2.14E-12 2.06E-11 0.000

ng/dscm 9.42E-03 2.83E-03 2.72E-02 0.013

ng/dscm@7%O2 8.23E-03 2.48E-03 2.39E-02 0.012

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000082 0.0000000078 0.0000000184 0.000

lb/mmBtuO2 5.98E-13 5.56E-13 1.30E-12 0.000

ng/dscm 7.93E-04 7.35E-04 1.71E-03 0.001

ng/dscm@7%O2 6.93E-04 6.44E-04 1.51E-03 0.001

Compound: OCDD

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Monday, February 14, 2011 Page 13 of 34
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Mass_mg 0.000000024 0.000000006 0.0000000514 0.000

lb/mmBtuO2 1.75E-12 4.27E-13 3.63E-12 0.000

ng/dscm 2.32E-03 5.66E-04 4.78E-03 0.003

ng/dscm@7%O2 2.03E-03 4.96E-04 4.21E-03 0.002

Compound: OCDF

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000059 0.0000000031 0.000000011 0.000

lb/mmBtuO2 4.30E-13 2.21E-13 7.77E-13 0.000

ng/dscm 5.71E-04 2.92E-04 1.02E-03 0.001

ng/dscm@7%O2 4.99E-04 2.56E-04 8.98E-04 0.001

Compound: Total Dioxins

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000626 0.0000000309 0.000000083 0.000

lb/mmBtuO2 4.56E-12 2.20E-12 5.87E-12 0.000

ng/dscm 6.05E-03 2.91E-03 7.73E-03 0.006

ng/dscm@7%O2 5.29E-03 2.55E-03 6.80E-03 0.005

Compound: Total Furans

Average

RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3

Mass_mg 0.0000000517 0.0000000442 0.0000000499 0.000

lb/mmBtuO2 3.77E-12 3.15E-12 3.53E-12 0.000

ng/dscm 5.00E-03 4.17E-03 4.65E-03 0.005

ng/dscm@7%O2 4.37E-03 3.65E-03 4.09E-03 0.004

Location: PMT2 - Gases - Method 10

Compound: Carbon Monoxide

Average

Run 2-CO-1 2-CO-2 2-CO-3

lb/mmBtuO2 1.73E-01 1.62E-01 1.85E-01 0.173

ppm 1.97E+02 1.84E+02 2.09E+02 196.667

ppm@7%O2 1.72E+02 1.61E+02 1.84E+02 172.333

Location: PMT2 - Gases - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 2-THC-1 2-THC-2 2-THC-3

lb/mmBtuO2 0.00E+00 3.68E-04 0.00E+00 0.000

ppm 0.00E+00 2.65E-01 0.00E+00 0.088

ppm@7%O2 0.00E+00 2.32E-01 0.00E+00 0.077

Location: PMT2 - Gases - Method 6C

Compound: Sulfur Dioxide

Average

Run 2-SO2-1 2-SO2-2 2-SO2-3

lb/mmBtuO2 9.19E-01 9.03E-01 9.37E-01 0.920

ppm 4.58E+02 4.49E+02 4.63E+02 456.667

ppm@7%O2 4.00E+02 3.94E+02 4.08E+02 400.667

Monday, February 14, 2011 Page 14 of 34
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Location: PMT2 - Gases - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 2-NOx-1 2-NOx-2 2-NOx-3

lb/mmBtuO2 2.38E-01 2.42E-01 2.39E-01 0.240

ppm 1.65E+02 1.67E+02 1.65E+02 165.667

ppm@7%O2 1.44E+02 1.46E+02 1.45E+02 145.000

Location: PMT2 - Metals - Method 29

Compound: Antimony

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 0.159 0.167 0.0584 0.128

Elb/hr 1.85E-01 1.93E-01 6.66E-02 0.148

lb/mmBtuO2 2.35E-05 2.46E-05 8.34E-06 0.000

mg/dscm 3.12E-02 3.25E-02 1.10E-02 0.025

mg/dscm@7%O2 2.73E-02 2.85E-02 9.64E-03 0.022

Compound: Arsenic

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 0.0125 0.0157 0.00538 0.011

Elb/hr 1.45E-02 1.82E-02 6.13E-03 0.013

lb/mmBtuO2 1.85E-06 2.31E-06 7.68E-07 0.000

mg/dscm 2.45E-03 3.05E-03 1.02E-03 0.002

mg/dscm@7%O2 2.14E-03 2.67E-03 8.94E-04 0.002

Compound: Beryllium

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 0.0003 0.000344 0.000227 0.000

Elb/hr 3.49E-04 3.98E-04 2.59E-04 0.000

lb/mmBtuO2 4.44E-08 5.06E-08 3.24E-08 0.000

mg/dscm 5.89E-05 6.69E-05 4.29E-05 0.000

mg/dscm@7%O2 5.15E-05 5.86E-05 3.76E-05 0.000

Compound: Cadmium

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 0.000346 0.000466 0.000166 0.000

Elb/hr 4.02E-04 5.39E-04 1.89E-04 0.000

lb/mmBtuO2 5.12E-08 6.85E-08 2.37E-08 0.000

mg/dscm 6.79E-05 9.07E-05 3.13E-05 0.000

mg/dscm@7%O2 5.93E-05 7.95E-05 2.74E-05 0.000

Compound: Chromium

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 0.0301 0.0356 0.0147 0.027

Elb/hr 3.50E-02 4.12E-02 1.68E-02 0.031

lb/mmBtuO2 4.45E-06 5.24E-06 2.10E-06 0.000

mg/dscm 5.91E-03 6.93E-03 2.78E-03 0.005

Monday, February 14, 2011 Page 15 of 34
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mg/dscm@7%O2 5.16E-03 6.07E-03 2.44E-03 0.005

Compound: Cobalt

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 0.185 0.222 0.0846 0.164

Elb/hr 2.15E-01 2.57E-01 9.65E-02 0.190

lb/mmBtuO2 2.74E-05 3.26E-05 1.21E-05 0.000

mg/dscm 3.63E-02 4.32E-02 1.60E-02 0.032

mg/dscm@7%O2 3.17E-02 3.79E-02 1.40E-02 0.028

Compound: Filterable Particulate

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 165.1 185.3 60.6 137.000

Elb/hr 1.92E+02 2.14E+02 6.91E+01 158.367

lb/mmBtuO2 2.44E-02 2.73E-02 8.65E-03 0.020

mg/dscm 3.24E+01 3.61E+01 1.14E+01 26.633

mg/dscm@7%O2 2.83E+01 3.16E+01 9.99E+00 23.297

Compound: Lead

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 0.0359 0.0436 0.0161 0.032

Elb/hr 4.18E-02 5.04E-02 1.84E-02 0.037

lb/mmBtuO2 5.31E-06 6.41E-06 2.30E-06 0.000

mg/dscm 7.05E-03 8.48E-03 3.04E-03 0.006

mg/dscm@7%O2 6.16E-03 7.43E-03 2.66E-03 0.005

Compound: Manganese

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 0.0712 0.0844 0.036 0.064

Elb/hr 8.28E-02 9.76E-02 4.11E-02 0.074

lb/mmBtuO2 1.05E-05 1.24E-05 5.14E-06 0.000

mg/dscm 1.40E-02 1.64E-02 6.80E-03 0.012

mg/dscm@7%O2 1.22E-02 1.44E-02 5.96E-03 0.011

Compound: Nickel

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 4.06 4.41 1.52 3.330

Elb/hr 4.72E+00 5.10E+00 1.73E+00 3.850

lb/mmBtuO2 6.00E-04 6.49E-04 2.17E-04 0.000

mg/dscm 7.97E-01 8.58E-01 2.87E-01 0.647

mg/dscm@7%O2 6.96E-01 7.52E-01 2.52E-01 0.567

Compound: Selenium

Average

RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3

Mass_mg 0.00416 0.002 0.002 0.003

Elb/hr 4.84E-03 2.31E-03 2.28E-03 0.003

lb/mmBtuO2 6.15E-07 2.94E-07 2.85E-07 0.000

mg/dscm 8.16E-04 3.89E-04 3.78E-04 0.001

Monday, February 14, 2011 Page 16 of 34
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Process Run Data

mg/dscm@7%O2 7.13E-04 3.41E-04 3.31E-04 0.000

Location: PMT2 - PM - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber PMT2-27/28-2 PMT2-27/28-3 PMT2-27/28-1

Mass_mg 12.597 43.997 70.747 42.447

lb/mmBtuO2 7.37E-03 2.66E-02 4.35E-02 0.026

Compound: Filterable PM2.5

Average

RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3

Mass_mg 43.314 8.672 31.772 27.919

lb/mmBtuO2 2.67E-02 5.08E-03 1.92E-02 0.017

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3

Mass_mg 0.254 1.309 7.771 3.111

lb/mmBtuO2 1.56E-04 7.66E-04 4.70E-03 0.002

Compound: Organic Condensible Particulate

Average

RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3

Mass_mg 1.725 0.54 274.91 92.392

lb/mmBtuO2 1.06E-03 3.16E-04 1.66E-01 0.056

Compound: Total Particulate

Average

RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3

Mass_mg 75.49 15.393 327.274 139.386

lb/mmBtuO2 4.65E-02 9.01E-03 1.98E-01 0.085

Compound: Total PM2.5

Average

RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3

Mass_mg 45.293 10.521 314.452 123.422

lb/mmBtuO2 2.79E-02 6.16E-03 1.90E-01 0.075

Monday, February 14, 2011 Page 17 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Residual Oil (No. 6) Burned 60065 gal/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/11/2010; 

Start - 12:47; 

End - 14:47

0

10 Residual Oil (No. 6) Burned 59941 gal/hr Method 027/028; 

Run PM-1; Date - 

5/11/2010; Start - 

08:49; End - 12:36

0

11 Residual Oil (No. 6) Burned 60117 gal/hr Method 027/028; 

Run PM-2; Date - 

5/11/2010; Start - 

18:33; End - 21:33

0

12 Residual Oil (No. 6) Burned 60000 gal/hr Method 027/028; 

Run PM-3; Date - 

5/12/2010; Start - 

08:23; End - 11:32

0

2 Residual Oil (No. 6) Burned 60080 gal/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/11/2010; 

Start - 15:09; 

End - 17:09

0

3 Residual Oil (No. 6) Burned 60124 gal/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/11/2010; 

Start - 17:33; 

End - 19:33

0

4 Residual Oil (No. 6) Burned 60088 gal/hr Method 23; Run 

D/F-1; Date - 

5/11/2010; Start - 

12:58; End - 22:36

0

5 Residual Oil (No. 6) Burned 60059 gal/hr Method 23; Run 

D/F-2; Date - 

5/12/2010; Start - 

12:00; End - 21:05

0

6 Residual Oil (No. 6) Burned 60161 gal/hr Method 23; Run 

D/F-3; Date - 

5/13/2010; Start - 

08:06; End - 17:07

0

7 Residual Oil (No. 6) Burned 60073 gal/hr Method 29; Run 

M-1; Date - 

5/11/2010; Start - 

13:18; End - 18:11

0

Monday, February 14, 2011 Page 18 of 34
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8 Residual Oil (No. 6) Burned 59985 gal/hr Method 29; Run 

M-2; Date - 

5/12/2010; Start - 

08:22; End - 13:04

0

9 Residual Oil (No. 6) Burned 60088 gal/hr Method 29; Run 

M-3; Date - 

5/12/2010; Start - 

13:32; End - 18:13

0

1 Average Heat Input 7506 MMBtu/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/11/2010; 

Start - 12:47; 

End - 14:47

0

10 Average Heat Input 7492 MMBtu/hr Method 027/028; 

Run PM-1; Date - 

5/11/2010; Start - 

08:49; End - 12:36

0

11 Average Heat Input 7514 MMBtu/hr Method 027/028; 

Run PM-2; Date - 

5/11/2010; Start - 

18:33; End - 21:33

0

12 Average Heat Input 7499 MMBtu/hr Method 027/028; 

Run PM-3; Date - 

5/12/2010; Start - 

08:23; End - 11:32

0

2 Average Heat Input 7508 MMBtu/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/11/2010; 

Start - 15:09; 

End - 17:09

0

3 Average Heat Input 7514 MMBtu/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/11/2010; 

Start - 17:33; 

End - 19:33

0

4 Average Heat Input 7511 MMBtu/hr Method 23; Run 

D/F-1; Date - 

5/11/2010; Start - 

12:58; End - 22:36

0

5 Average Heat Input 7507 MMBtu/hr Method 23; Run 

D/F-2; Date - 

5/12/2010; Start - 

12:00; End - 21:05

0

6 Average Heat Input 7520 MMBtu/hr Method 23; Run 

D/F-3; Date - 

5/13/2010; Start - 

08:06; End - 17:07

0

Monday, February 14, 2011 Page 19 of 34
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7 Average Heat Input 7509 MMBtu/hr Method 29; Run 

M-1; Date - 

5/11/2010; Start - 

13:18; End - 18:11

0

8 Average Heat Input 7498 MMBtu/hr Method 29; Run 

M-2; Date - 

5/12/2010; Start - 

08:22; End - 13:04

0

9 Average Heat Input 7510 MMBtu/hr Method 29; Run 

M-3; Date - 

5/12/2010; Start - 

13:32; End - 18:13

0

1 Steam Output 5327 1000 lb Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/11/2010; 

Start - 12:47; 

End - 14:47

0

10 Steam Output 5319 1000 lb Method 027/028; 

Run PM-1; Date - 

5/11/2010; Start - 

08:49; End - 12:36

0

11 Steam Output 5330 1000 lb Method 027/028; 

Run PM-2; Date - 

5/11/2010; Start - 

18:33; End - 21:33

0

12 Steam Output 5316 1000 lb Method 027/028; 

Run PM-3; Date - 

5/12/2010; Start - 

08:23; End - 11:32

0

2 Steam Output 5325 1000 lb Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/11/2010; 

Start - 15:09; 

End - 17:09

0

3 Steam Output 5329 1000 lb Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/11/2010; 

Start - 17:33; 

End - 19:33

0

4 Steam Output 5328 1000 lb Method 23; Run 

D/F-1; Date - 

5/11/2010; Start - 

12:58; End - 22:36

0

5 Steam Output 5325 1000 lb Method 23; Run 

D/F-2; Date - 

5/12/2010; Start - 

12:00; End - 21:05

0

Monday, February 14, 2011 Page 20 of 34
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6 Steam Output 5324 1000 lb Method 23; Run 

D/F-3; Date - 

5/13/2010; Start - 

08:06; End - 17:07

0

7 Steam Output 5327 1000 lb Method 29; Run 

M-1; Date - 

5/11/2010; Start - 

13:18; End - 18:11

0

8 Steam Output 5317 1000 lb Method 29; Run 

M-2; Date - 

5/12/2010; Start - 

08:22; End - 13:04

0

9 Steam Output 5326 1000 lb Method 29; Run 

M-3; Date - 

5/12/2010; Start - 

13:32; End - 18:13

0

1 Unit Gross Electrical Output 798 MWg Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/11/2010; 

Start - 12:47; 

End - 14:47

0

10 Unit Gross Electrical Output 798 MWg Method 027/028; 

Run PM-1; Date - 

5/11/2010; Start - 

08:49; End - 12:36

0

11 Unit Gross Electrical Output 798 MWg Method 027/028; 

Run PM-2; Date - 

5/11/2010; Start - 

18:33; End - 21:33

0

12 Unit Gross Electrical Output 798 MWg Method 027/028; 

Run PM-3; Date - 

5/12/2010; Start - 

08:23; End - 11:32

0

2 Unit Gross Electrical Output 798 MWg Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/11/2010; 

Start - 15:09; 

End - 17:09

0

3 Unit Gross Electrical Output 798 MWg Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/11/2010; 

Start - 17:33; 

End - 19:33

0

4 Unit Gross Electrical Output 798 MWg Method 23; Run 

D/F-1; Date - 

5/11/2010; Start - 

12:58; End - 22:36

0

Monday, February 14, 2011 Page 21 of 34
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7/14/2010

5 Unit Gross Electrical Output 798 MWg Method 23; Run 

D/F-2; Date - 

5/12/2010; Start - 

12:00; End - 21:05

0

6 Unit Gross Electrical Output 798 MWg Method 23; Run 

D/F-3; Date - 

5/13/2010; Start - 

08:06; End - 17:07

0

7 Unit Gross Electrical Output 798 MWg Method 29; Run 

M-1; Date - 

5/11/2010; Start - 

13:18; End - 18:11

0

8 Unit Gross Electrical Output 798 MWg Method 29; Run 

M-2; Date - 

5/12/2010; Start - 

08:22; End - 13:04

0

9 Unit Gross Electrical Output 798 MWg Method 29; Run 

M-3; Date - 

5/12/2010; Start - 

13:32; End - 18:13

0

1 Unit Net Electric Generation 766 MWn Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/11/2010; 

Start - 12:47; 

End - 14:47

0

10 Unit Net Electric Generation 766 MWn Method 027/028; 

Run PM-1; Date - 

5/11/2010; Start - 

08:49; End - 12:36

0

11 Unit Net Electric Generation 766 MWn Method 027/028; 

Run PM-2; Date - 

5/11/2010; Start - 

18:33; End - 21:33

0

12 Unit Net Electric Generation 767 MWn Method 027/028; 

Run PM-3; Date - 

5/12/2010; Start - 

08:23; End - 11:32

0

2 Unit Net Electric Generation 766 MWn Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/11/2010; 

Start - 15:09; 

End - 17:09

0

3 Unit Net Electric Generation 766 MWn Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/11/2010; 

Start - 17:33; 

End - 19:33

0

Monday, February 14, 2011 Page 22 of 34
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7/14/2010

APCD Run Data

Process Lab Run Data

4 Unit Net Electric Generation 766 MWn Method 23; Run 

D/F-1; Date - 

5/11/2010; Start - 

12:58; End - 22:36

0

5 Unit Net Electric Generation 766 MWn Method 23; Run 

D/F-2; Date - 

5/12/2010; Start - 

12:00; End - 21:05

0

6 Unit Net Electric Generation 766 MWn Method 23; Run 

D/F-3; Date - 

5/13/2010; Start - 

08:06; End - 17:07

0

7 Unit Net Electric Generation 766 MWn Method 29; Run 

M-1; Date - 

5/11/2010; Start - 

13:18; End - 18:11

0

8 Unit Net Electric Generation 767 MWn Method 29; Run 

M-2; Date - 

5/12/2010; Start - 

08:22; End - 13:04

0

9 Unit Net Electric Generation 766 MWn Method 29; Run 

M-3; Date - 

5/12/2010; Start - 

13:32; End - 18:13

0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 164 NOx Emissions 0

2 LOW NOX BURNERS 166 NOx Emissions 0

3 LOW NOX BURNERS 165 NOx Emissions 0

1 CYCLONE SEPARATORS 14.8 Opacity 0

2 CYCLONE SEPARATORS 16 Opacity 0

3 CYCLONE SEPARATORS 15.4 Opacity 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 17800 Btu/lb

1 Fuel Moisture 0.096 %

1 Fuel Mercury Content 0.002 mg/kg

1 Fuel Chlorine Content 145 mg/kg

1 Fuel Fluorine Content 76 mg/kg

1 Fuel Antimony Content 0.8 mg/kg

1 Fuel Arsenic Content 0.067 mg/kg

1 Fuel Beryllium Content 0.008 mg/kg

Monday, February 14, 2011 Page 23 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

1 Fuel Cadmium Content 0.009 mg/kg

1 Fuel Chromium Content 0.088 mg/kg

1 Fuel Cobalt Content 1.1 mg/kg

1 Fuel Lead Content 0.15 mg/kg

1 Fuel Manganese Content 0.3 mg/kg

1 Fuel Nickel Content 22.8 mg/kg

1 Fuel Selenium Content 0.03 mg/kg

1 Fuel Sulfur Content 11800 mg/kg

1 Fuel Proximate Analysis (Carbon) 88.31 %

1 Fuel Proximate Analysis (Hydrogen) 10.02 %

1 Fuel Proximate Analysis (Nitrogen) 0.67 %

1 Fuel Proximate Analysis (Oxygen) 0.5 %

1 Fuel Proximate Analysis (Sulfur) 1.13 %

2 Fuel Higher Heating Value 17700 Btu/lb

2 Fuel Moisture 0.114 %

2 Fuel Mercury Content 0.002 mg/kg

2 Fuel Chlorine Content 261 mg/kg

2 Fuel Fluorine Content 76 mg/kg

2 Fuel Antimony Content 0.8 mg/kg

2 Fuel Arsenic Content 0.06 mg/kg

2 Fuel Beryllium Content 0.008 mg/kg

2 Fuel Cadmium Content 0.008 mg/kg

2 Fuel Chromium Content 0.078 mg/kg

2 Fuel Cobalt Content 1.1 mg/kg

2 Fuel Lead Content 0.14 mg/kg

2 Fuel Manganese Content 0.3 mg/kg

2 Fuel Nickel Content 22.3 mg/kg

2 Fuel Selenium Content 0.03 mg/kg

2 Fuel Sulfur Content 10100 mg/kg

2 Fuel Proximate Analysis (Carbon) 88.27 %

2 Fuel Proximate Analysis (Hydrogen) 10.1 %

2 Fuel Proximate Analysis (Nitrogen) 0.66 %

2 Fuel Proximate Analysis (Oxygen) 0.5 %

2 Fuel Proximate Analysis (Sulfur) 1.09 %

3 Fuel Higher Heating Value 17900 Btu/lb

3 Fuel Moisture 0.111 %

3 Fuel Mercury Content 0.001 mg/kg

3 Fuel Chlorine Content 255 mg/kg

3 Fuel Fluorine Content 72 mg/kg

3 Fuel Antimony Content 0.7 mg/kg

3 Fuel Arsenic Content 0.049 mg/kg

3 Fuel Beryllium Content 0.008 mg/kg

3 Fuel Cadmium Content 0.009 mg/kg

Monday, February 14, 2011 Page 24 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

3 Fuel Chromium Content 0.1 mg/kg

3 Fuel Cobalt Content 1.1 mg/kg

3 Fuel Lead Content 0.14 mg/kg

3 Fuel Manganese Content 0.3 mg/kg

3 Fuel Nickel Content 22.1 mg/kg

3 Fuel Selenium Content 0.03 mg/kg

3 Fuel Sulfur Content 10500 mg/kg

3 Fuel Proximate Analysis (Carbon) 87.97 %

3 Fuel Proximate Analysis (Hydrogen) 9.95 %

3 Fuel Proximate Analysis (Nitrogen) 0.72 %

3 Fuel Proximate Analysis (Oxygen) 0.5 %

3 Fuel Proximate Analysis (Sulfur) 1.12 %

Monday, February 14, 2011 Page 25 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Sampling / Stack Data Results Detail

Location PMT2 - D/F - Method 23

Average

Run Number PMT2-23-1 PMT2-23-2 PMT2-23-3

Test Date 5/11/2010 5/12/2010 5/13/2010

Run Start Time 12:58:00 PM 12:00:00 PM 8:06:00 AM

Run Finish Time 8:58:00 PM 8:00:00 PM 4:06:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.25 0.25 0.25 0.250

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.987 0.987 0.987 0.987

Barometric Pressure, inches of Mercury 30.14 30.2 30.2 30.180

Average Orifice Meter Differential, inches H2O 2.16 2.20 2.25 2.203

Dry Gas Meter Volume Sampled, cubic feet 373.520 381.680 385.720 380.307

Average Dry Gas Meter Temperature, °F 79.75 78.63 77.67 78.683

Dry Gas Meter Volume Sampled, dscf 365.205 374.736 379.425 373.122

Total Moisture Liquid collected, g 786.3 796.1 769.1 783.833

Volume of Water Vapor, standard cubic feet 37.01 37.47 36.20 36.893

Moisture Content of Stack Gas, % 9.20 9.09 8.71 9.000

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.908 0.9091 0.9129 0.910

Carbon Dioxide, % 12.59 12.9 12.7 12.730

Oxygen, % 4.99 5.04 5.11 5.047

Carbon Monoxide & Nitrogen, % 82.42 82.06 82.19 82.223

Fuel Factor 1.26 1.23 1.24

Dry Molecular Weight, lb/lb-Mole 30.21 30.27 30.24 30.240

Wet Molecular weight, lb/lb-Mole 29.09 29.15 29.17 29.137

Flue Gas Static Pressure, inches of H2O -1.6 -1.6 -1.6 -1.600

Absolute Flue Gas Pressure, inches of Mercury 30.02 30.08 30.08 30.060

Average Stack Gas Temperature, °F 320.08 321.71 321.63 321.140

Average Velocity Head, inches of H2O 0.8208445492

94092

0.837588525

270098

0.854896842

115147

0.838

Average Stack Gas Velocity, feet/second 61.49 62.05 62.67 62.070

Stack Cross-Sectional Area, square feet 696.685 696.685 696.685 696.685

Dry Volumetric Flow Rate, dry scfm 1,584,973.2 1,601,200.3 1,624,125.4 1,603,432.9

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,570,349.6 2,593,758.3 2,619,674.9 2,594,594.2

67

Percent Isokinetic of Sampling Rate, % 98.1 99.6 99.5 99.067

Percent Excess Air, % 29.8 30.3 30.8 30.300

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

Round Duct Diameter, inches 357.4 357.4 357.4

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 14, 2011 Page 26 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Location PMT2 - Gases - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 14, 2011 Page 27 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Location PMT2 - Gases - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Monday, February 14, 2011 Page 28 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Location PMT2 - Gases - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor Method 3A 

CO2

Method 3A 

CO2

Method 3A 

CO2

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc PMT2 - Gases PMT2 - 

Gases

PMT2 - Gases

Cgasw 2-CO2-1 2-CO2-2 2-CO2-3

Cgasw Units 5/11/2010 5/11/2010 5/11/2010

Monday, February 14, 2011 Page 29 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Location PMT2 - Gases - Method 3A O2

Average

Run Number 2-O2-1 2-O2-2 2-O2-3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM

Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM

Carbon Dioxide, % 12.59 12.9 12.7 12.730

Oxygen, % 4.99 5.04 5.11 5.047

Fuel Factor 1.32 1.32 1.32

Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.0

00

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

Moisture, % 9.22 9.22 9.22 9.220

Analyzer Make THERMO THERMO THERMO

Analyzer Model 42i-HL 42i-HL 42i-HL

Analyzer Serial Number INST-N2-0002 INST-N2-

0002

INST-N2-

0002

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 0.37 0.37 0.37 0.370

Calibration Pre Zero Cylinder Bias 1.47 1.47 1.47 1.470

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID AAL12025-O2 AAL12025-

O2

AAL12025-

O2

Calibration Pre High Cylinder Instrument Response 12.02 11.91 11.9 11.943

Calibration Pre High Cylinder Bias 0.05 -0.47 -0.52 -0.313

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Post Zero Cylinder Instrument Response 0.37 0.37 0.36 0.367

Calibration Post Zero Cylinder Bias 1.47 1.47 1.42 1.453

Calibration Post Zero Cylinder Drift 0 0 0.05 0.017

Calibration Post High Cylinder ID AAL12025-O2 AAL12025-

O2

AAL12025-

O2

Calibration Post High Cylinder Instrument Response 11.91 11.9 11.88 11.897

Calibration Post High Cylinder Bias -0.47 -0.52 -0.62 -0.537

Calibration Post High Cylinder Drift 0.52 0.05 0.1 0.223

Cavg 5.15 5.18 5.23 5.187

Cavg Units %vd %vd %vd

Cgas 4.9882 5.0456 5.1077 5.047

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

Monday, February 14, 2011 Page 30 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Location PMT2 - Gases - Method 6C

Average

Run Number 2-SO2-1 2-SO2-2 2-SO2-3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM

Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM

Carbon Dioxide, % 12.59 12.9 12.7 12.730

Oxygen, % 4.99 5.04 5.11 5.047

Fuel Factor 1.32 1.32 1.32

Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.0

00

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

Moisture, % 9.22 9.22 9.22 9.220

Analyzer Make THERMO THERMO THERMO

Analyzer Model 43i-HL 43i-HL 43i-HL

Analyzer Serial Number INST-S2-0005 INST-S2-

0005

INST-S2-

0005

Operating Range 959 959 959 959.000

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 2.05 3.71 2.96 2.907

Calibration Pre Zero Cylinder Bias 0.17 0.34 0.26 0.257

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID CC66246 CC66246 CC66246

Calibration Pre High Cylinder Instrument Response 406.28 402.58 406.32 405.060

Calibration Pre High Cylinder Bias -1.48 -1.87 -1.48 -1.610

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Post Zero Cylinder Instrument Response 3.71 2.96 3.18 3.283

Calibration Post Zero Cylinder Bias 0.34 0.26 0.28 0.293

Calibration Post Zero Cylinder Drift 0.17 0.08 0.02 0.090

Calibration Post High Cylinder ID CC66246 CC66246 CC66246

Calibration Post High Cylinder Instrument Response 402.58 406.32 405.99 404.963

Calibration Post High Cylinder Bias -1.87 -1.48 -1.51 -1.620

Calibration Post High Cylinder Drift 0.39 0.39 0.03 0.270

Cavg 432.44 423.73 439.23 431.800

Cavg Units ppmvd ppmvd ppmvd

Cgas 457.855 448.5723 463.1194 456.516

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

Monday, February 14, 2011 Page 31 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Location PMT2 - Gases - Method 7E

Average

Run Number 2-NOx-1 2-NOx-2 2-NOx-3

Test Date 5/11/2010 5/11/2010 5/11/2010

Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM

Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM

Carbon Dioxide, % 12.59 12.9 12.7 12.730

Oxygen, % 4.99 5.04 5.11 5.047

Fuel Factor 1.32 1.32 1.32

Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.0

00

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

Moisture, % 9.22 9.22 9.22 9.220

Analyzer Make THERMO THERMO THERMO

Analyzer Model 42i-HL 42i-HL 42i-HL

Analyzer Serial Number INST-N2-0002 INST-N2-

0002

INST-N2-

0002

Operating Range 1110 1110 1110 1,110.000

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 1.19 2.24 1.91 1.780

Calibration Pre Zero Cylinder Bias 0.02 0.11 0.08 0.070

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID ALM042523-

NOx

ALM042523

-NOx

ALM042523-

NOx

Calibration Pre High Cylinder Instrument Response 536.28 531.09 531.7 533.023

Calibration Pre High Cylinder Bias -1.81 -2.27 -2.22 -2.100

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Post Zero Cylinder Instrument Response 2.24 1.91 1.93 2.027

Calibration Post Zero Cylinder Bias 0.11 0.08 0.09 0.093

Calibration Post Zero Cylinder Drift 0.09 0.03 0.01 0.043

Calibration Post High Cylinder ID ALM042523-

NOx

ALM042523

-NOx

ALM042523-

NOx

Calibration Post High Cylinder Instrument Response 531.09 531.7 530.29 531.027

Calibration Post High Cylinder Bias -2.27 -2.22 -2.35 -2.280

Calibration Post High Cylinder Drift 0.46 4.999999999

99998E-02

0.13 0.213

Cavg 162.64 164.16 161.36 162.720

Cavg Units ppmvd ppmvd ppmvd

Cgas 165.4717 167.4989 164.8418 165.937

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

Monday, February 14, 2011 Page 32 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Location PMT2 - Metals - Method 29

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 14, 2011 Page 33 of 34
Manatee Energy Center, Unit #2, Information Collection Request

7/14/2010

Location PMT2 - PM - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Monday, February 14, 2011 Page 34 of 34