Name: Paul Plotkin

Title: Plant General Manager

Company: Florida Power & Light

Sign Date: 8/23/2010

Name: Thomas K. Graham

Title: Director of Operations

Company: Air Hygiene International, Inc.

Sign Date: 7/27/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Manatee Energy Center, Unit #1, Information Collection Request

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Monday, February 14, 2011 Page 1 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

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:

PMT1 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

PMT1 - D/F 357.4 0 0 0 4524 876 4 24

PMT1 - Gases 357.4 0 0 0 4524 876 4 1

PMT1 - Metals 357.4 0 0 0 4524 876 4 24

PMT1 - 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 32
Manatee Energy Center, Unit #1, Information Collection Request

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Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

PMT1 - D/F % H2O Method 1 - 4 3 480 24

PMT1 - D/F 2,3,7,8-TCDD Method 23 3 480 24

PMT1 - D/F 1,2,3,7,8-PeCDD Method 23 3 480 24

PMT1 - D/F 1,2,3,4,7,8-HxCDD Method 23 3 480 24

PMT1 - D/F 1,2,3,6,7,8-HxCDD Method 23 3 480 24

PMT1 - D/F 1,2,3,7,8,9-HxCDD Method 23 3 480 24

PMT1 - D/F 1,2,3,4,6,7,8-HpCDD Method 23 3 480 24

PMT1 - D/F OCDD Method 23 3 480 24

PMT1 - D/F 2,3,7,8-TCDF Method 23 3 480 24

PMT1 - D/F 1,2,3,7,8-PeCDF Method 23 3 480 24

PMT1 - D/F 2,3,4,7,8-PeCDF Method 23 3 480 24

PMT1 - D/F 1,2,3,4,7,8-HxCDF Method 23 3 480 24

PMT1 - D/F 1,2,3,6,7,8-HxCDF Method 23 3 480 24

PMT1 - D/F 2,3,4,6,7,8-HxCDF Method 23 3 480 24

PMT1 - D/F 1,2,3,7,8,9-HxCDF Method 23 3 480 24

PMT1 - D/F 1,2,3,4,6,7,8-HpCDF Method 23 3 480 24

PMT1 - D/F 1,2,3,4,7,8,9-HpCDF Method 23 3 480 24

PMT1 - D/F OCDF Method 23 3 480 24

PMT1 - D/F Total Dioxins Method 23 3 480 24

PMT1 - D/F Total Furans Method 23 3 480 24

PMT1 - D/F 3,3',4,4'-TCB (PCB77) Method 23 3 480 24

PMT1 - D/F 3,4,4',5-TCB (PCB81) Method 23 3 480 24

PMT1 - D/F 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 24

PMT1 - D/F 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 24

PMT1 - D/F 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 24

PMT1 - D/F 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 24

PMT1 - 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)

PMT1 - D/F Method 23 3 480 24

PMT1 - D/F 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 24

PMT1 - D/F 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 24

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

(PCB189)

PMT1 - D/F Method 23 3 480 24

PMT1 - D/F O2 Method 3A O2 3 480 24

PMT1 - D/F Co2 Method 3A CO2 3 480 24

% H2O Method 1 - 4 3 120 1 Determined after 

initial stratification test

PMT1 - Gases

Carbon Monoxide Method 10 3 120 1 Determined after 

initial stratification test

PMT1 - Gases

Total organic compounds 

(TOC) as Propane

Method 25A 3 120 1 Determined after 

initial stratification test

PMT1 - Gases

Co2 Method 3A CO2 3 120 1 Determined after 

initial stratification test

PMT1 - Gases

O2 Method 3A O2 3 120 1 Determined after 

initial stratification test

PMT1 - Gases

Sulfur Dioxide Method 6C 3 120 1 Determined after 

initial stratification test

PMT1 - Gases

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

initial stratification test

PMT1 - Gases

PMT1 - Metals % H2O Method 1 - 4 3 240 24

PMT1 - Metals Nickel Method 29 3 240 24

PMT1 - Metals Filterable Particulate Method 29 3 240 24

Monday, February 14, 2011 Page 3 of 32
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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.

PMT1 - Metals Cobalt Method 29 3 240 24

PMT1 - Metals Chromium Method 29 3 240 24

PMT1 - Metals Cadmium Method 29 3 240 24

PMT1 - Metals Manganese Method 29 3 240 24

PMT1 - Metals Selenium Method 29 3 240 24

PMT1 - Metals Lead Method 29 3 240 24

PMT1 - Metals Co2 Method 3A CO2 3 240 24

PMT1 - Metals O2 Method 3A O2 3 240 24

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

on method calculations

PMT1 - PM

Inorganic (Aqueous) 

Condensible Part.

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

on method calculations

PMT1 - PM

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

on method calculations

PMT1 - PM

Organic Condensible 

Particulate

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

on method calculations

PMT1 - PM

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

on method calculations

PMT1 - PM

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

on method calculations

PMT1 - PM

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

on method calculations

PMT1 - PM

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

on method calculations

PMT1 - PM

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

on method calculations

PMT1 - PM

Monday, February 14, 2011 Page 4 of 32
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Sampling / Stack Data Results Summary

Location PMT1 - D/F - Method 23

Average

Run Number PMT1-23-1 PMT1-23-2 PMT1-23-3

Test Date 5/17/2010 5/18/2010 5/20/2010

Run Start Time 9:37:00 AM 11:05:00 

AM

11:10:00 AM

Run Finish Time 5:37:00 PM 7:05:00 PM 7:10:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 370.084 370.760 356.228 365.691

Moisture Content of Stack Gas, % 9.26 9.44 9.07 9.257

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

Carbon Dioxide, % 12.79 12.66 12.86 12.770

Oxygen, % 5.26 5.36 5.28 5.300

Average Stack Gas Temperature, °F 323.33 328.50 329.38 327.070

Dry Volumetric Flow Rate, dry scfm 1,577,964.0 1,598,210.6 1,558,820.1 1,578,331.56

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,580,799.9 2,636,395.4 2,573,275.7 2,596,823.66

7

Percent Isokinetic of Sampling Rate, % 99.9 98.8 97.3 98.667

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 PMT1 - 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 32
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Location PMT1 - 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 PMT1 - 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

Monday, February 14, 2011 Page 6 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - Gases - Method 3A O2

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 PMT1 - Gases - Method 6C

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 7 of 32
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8/23/2010

Location PMT1 - Gases - Method 7E

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 PMT1 - 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 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - 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 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Emissions Summary

Location: PMT1 - D/F - Method 23

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000072 0.0000000099 0.000000007 0.000

lb/mmBtuO2 5.27E-13 7.28E-13 5.33E-13 0.000

ng/dscm 6.87E-04 9.43E-04 6.94E-04 0.001

ng/dscm@7%O2 6.11E-04 8.43E-04 6.18E-04 0.001

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000037 0.0000000056 0.000000003 0.000

lb/mmBtuO2 2.71E-13 4.12E-13 2.28E-13 0.000

ng/dscm 3.53E-04 5.33E-04 2.97E-04 0.000

ng/dscm@7%O2 3.14E-04 4.77E-04 2.64E-04 0.000

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000051 0.0000000077 0.0000000041 0.000

lb/mmBtuO2 3.73E-13 5.66E-13 3.12E-13 0.000

ng/dscm 4.87E-04 7.34E-04 4.07E-04 0.001

ng/dscm@7%O2 4.33E-04 6.57E-04 3.62E-04 0.000

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000052 0.0000000049 0.0000000073 0.000

lb/mmBtuO2 3.80E-13 3.60E-13 5.56E-13 0.000

ng/dscm 4.96E-04 4.67E-04 7.24E-04 0.001

ng/dscm@7%O2 4.41E-04 4.18E-04 6.44E-04 0.001

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.000000012 0.0000000027 0.0000000037 0.000

lb/mmBtuO2 8.78E-13 1.98E-13 2.82E-13 0.000

ng/dscm 1.15E-03 2.57E-04 3.67E-04 0.001

ng/dscm@7%O2 1.02E-03 2.30E-04 3.27E-04 0.001

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000044 0.0000000041 0.0000000061 0.000

lb/mmBtuO2 3.22E-13 3.01E-13 4.64E-13 0.000

ng/dscm 4.20E-04 3.91E-04 6.05E-04 0.000

ng/dscm@7%O2 3.73E-04 3.50E-04 5.38E-04 0.000

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

Average

Monday, February 14, 2011 Page 10 of 32
Manatee Energy Center, Unit #1, Information Collection Request

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RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000021 0.0000000024 0.0000000033 0.000

lb/mmBtuO2 1.54E-13 1.76E-13 2.51E-13 0.000

ng/dscm 2.00E-04 2.29E-04 3.27E-04 0.000

ng/dscm@7%O2 1.78E-04 2.05E-04 2.91E-04 0.000

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000046 0.0000000042 0.0000000063 0.000

lb/mmBtuO2 3.37E-13 3.09E-13 4.79E-13 0.000

ng/dscm 4.39E-04 4.00E-04 6.25E-04 0.000

ng/dscm@7%O2 3.90E-04 3.58E-04 5.56E-04 0.000

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000027 0.0000000031 0.0000000042 0.000

lb/mmBtuO2 1.98E-13 2.28E-13 3.20E-13 0.000

ng/dscm 2.58E-04 2.95E-04 4.16E-04 0.000

ng/dscm@7%O2 2.29E-04 2.64E-04 3.70E-04 0.000

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000051 0.0000000072 0.0000000047 0.000

lb/mmBtuO2 3.73E-13 5.29E-13 3.58E-13 0.000

ng/dscm 4.87E-04 6.86E-04 4.66E-04 0.001

ng/dscm@7%O2 4.33E-04 6.14E-04 4.15E-04 0.000

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.00000003 0.0000000052 0.0000000063 0.000

lb/mmBtuO2 2.19E-12 3.82E-13 4.79E-13 0.000

ng/dscm 2.86E-03 4.95E-04 6.25E-04 0.001

ng/dscm@7%O2 2.54E-03 4.43E-04 5.56E-04 0.001

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.000000053 0.0000000022 0.000000066 0.000

lb/mmBtuO2 3.88E-12 1.62E-13 5.02E-12 0.000

ng/dscm 5.06E-03 2.10E-04 6.54E-03 0.004

ng/dscm@7%O2 4.50E-03 1.88E-04 5.82E-03 0.004

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.000000159 0.0000000278 0.00000017 0.000

lb/mmBtuO2 1.16E-11 2.04E-12 1.29E-11 0.000

ng/dscm 1.52E-02 2.65E-03 1.69E-02 0.012

ng/dscm@7%O2 1.35E-02 2.37E-03 1.50E-02 0.010

Monday, February 14, 2011 Page 11 of 32
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Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.000000855 0.000000271 0.00000144 0.000

lb/mmBtuO2 6.25E-11 1.99E-11 1.10E-10 0.000

ng/dscm 8.16E-02 2.58E-02 1.43E-01 0.083

ng/dscm@7%O2 7.25E-02 2.31E-02 1.27E-01 0.074

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.000000223 0.000000026 0.00000024 0.000

lb/mmBtuO2 1.63E-11 1.91E-12 1.83E-11 0.000

ng/dscm 2.13E-02 2.48E-03 2.38E-02 0.016

ng/dscm@7%O2 1.89E-02 2.22E-03 2.12E-02 0.014

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000412 0.000000017 0.000000105 0.000

lb/mmBtuO2 3.01E-12 1.25E-12 7.99E-12 0.000

ng/dscm 3.93E-03 1.62E-03 1.04E-02 0.005

ng/dscm@7%O2 3.49E-03 1.45E-03 9.25E-03 0.005

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.00000205 0.000000693 0.00000291 0.000

lb/mmBtuO2 1.50E-10 5.09E-11 2.21E-10 0.000

ng/dscm 1.96E-01 6.60E-02 2.89E-01 0.184

ng/dscm@7%O2 1.74E-01 5.90E-02 2.57E-01 0.163

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000342 0.000000028 0.0000000666 0.000

lb/mmBtuO2 2.50E-12 2.06E-12 5.07E-12 0.000

ng/dscm 3.26E-03 2.67E-03 6.60E-03 0.004

ng/dscm@7%O2 2.90E-03 2.39E-03 5.87E-03 0.004

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000023 0.0000000026 0.0000000035 0.000

lb/mmBtuO2 1.68E-13 1.91E-13 2.66E-13 0.000

ng/dscm 2.20E-04 2.48E-04 3.47E-04 0.000

ng/dscm@7%O2 1.96E-04 2.22E-04 3.09E-04 0.000

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000047 0.000000005 0.000000006 0.000

lb/mmBtuO2 3.44E-13 3.67E-13 4.57E-13 0.000

Monday, February 14, 2011 Page 12 of 32
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ng/dscm 4.49E-04 4.76E-04 5.95E-04 0.001

ng/dscm@7%O2 3.99E-04 4.26E-04 5.29E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000041 0.0000000062 0.0000000057 0.000

lb/mmBtuO2 3.00E-13 4.56E-13 4.34E-13 0.000

ng/dscm 3.91E-04 5.91E-04 5.65E-04 0.001

ng/dscm@7%O2 3.48E-04 5.29E-04 5.03E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000362 0.0000000051 0.000000006 0.000

lb/mmBtuO2 2.65E-12 3.75E-13 4.57E-13 0.000

ng/dscm 3.45E-03 4.86E-04 5.95E-04 0.002

ng/dscm@7%O2 3.07E-03 4.35E-04 5.29E-04 0.001

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000063 0.0000000027 0.0000000071 0.000

lb/mmBtuO2 4.61E-13 1.98E-13 5.40E-13 0.000

ng/dscm 6.01E-04 2.57E-04 7.04E-04 0.001

ng/dscm@7%O2 5.34E-04 2.30E-04 6.26E-04 0.000

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.00000001 0.000000021 0.0000000483 0.000

lb/mmBtuO2 7.32E-13 1.54E-12 3.68E-12 0.000

ng/dscm 9.54E-04 2.00E-03 4.79E-03 0.003

ng/dscm@7%O2 8.48E-04 1.79E-03 4.26E-03 0.002

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.000000148 0.000000037 0.000000282 0.000

lb/mmBtuO2 1.08E-11 2.72E-12 2.15E-11 0.000

ng/dscm 1.41E-02 3.52E-03 2.80E-02 0.015

ng/dscm@7%O2 1.25E-02 3.15E-03 2.49E-02 0.014

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

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000211 0.000000007 0.0000000183 0.000

lb/mmBtuO2 1.54E-12 5.14E-13 1.39E-12 0.000

ng/dscm 2.01E-03 6.67E-04 1.81E-03 0.001

ng/dscm@7%O2 1.79E-03 5.97E-04 1.61E-03 0.001

Compound: OCDD

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Monday, February 14, 2011 Page 13 of 32
Manatee Energy Center, Unit #1, Information Collection Request

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Mass_mg 0.00000006 0.000000036 0.000000018 0.000

lb/mmBtuO2 4.39E-12 2.65E-12 1.37E-12 0.000

ng/dscm 5.73E-03 3.43E-03 1.78E-03 0.004

ng/dscm@7%O2 5.09E-03 3.07E-03 1.58E-03 0.003

Compound: OCDF

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.000000022 0.0000000089 0.000000016 0.000

lb/mmBtuO2 1.61E-12 6.54E-13 1.22E-12 0.000

ng/dscm 2.10E-03 8.48E-04 1.59E-03 0.002

ng/dscm@7%O2 1.87E-03 7.59E-04 1.41E-03 0.001

Compound: Total Dioxins

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000000906 0.0000000725 0.0000000551 0.000

lb/mmBtuO2 6.63E-12 5.33E-12 4.19E-12 0.000

ng/dscm 8.65E-03 6.91E-03 5.46E-03 0.007

ng/dscm@7%O2 7.69E-03 6.18E-03 4.86E-03 0.006

Compound: Total Furans

Average

RunNumber PMT1-23-1 PMT1-23-2 PMT1-23-3

Mass_mg 0.0000001208 0.0000000483 0.0000000561 0.000

lb/mmBtuO2 8.84E-12 3.55E-12 4.27E-12 0.000

ng/dscm 1.15E-02 4.60E-03 5.56E-03 0.007

ng/dscm@7%O2 1.02E-02 4.11E-03 4.95E-03 0.006

Location: PMT1 - Gases - Method 10

Compound: Carbon Monoxide

Average

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

lb/mmBtuO2 1.06E-01 9.59E-02 5.35E-02 0.085

ppm 1.18E+02 1.07E+02 5.95E+01 94.833

ppm@7%O2 1.05E+02 9.52E+01 5.32E+01 84.467

Location: PMT1 - Gases - Method 25A

Compound: Total organic compounds (TOC) as 

Average

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

lb/mmBtuO2 4.70E-05 0.00E+00 0.00E+00 0.000

ppm 3.35E-02 0.00E+00 0.00E+00 0.011

ppm@7%O2 2.97E-02 0.00E+00 0.00E+00 0.010

Location: PMT1 - Gases - Method 6C

Compound: Sulfur Dioxide

Average

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

lb/mmBtuO2 8.31E-01 8.10E-01 9.44E-01 0.862

ppm 4.08E+02 3.96E+02 4.59E+02 421.000

ppm@7%O2 3.62E+02 3.52E+02 4.11E+02 375.000

Monday, February 14, 2011 Page 14 of 32
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Process Run Data

Location: PMT1 - Gases - Method 7E

Compound: Nitrogen oxides (NOx)

Average

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

lb/mmBtuO2 0.000

ppm 0.000

ppm@7%O2 #Num!

Monday, February 14, 2011 Page 15 of 32
Manatee Energy Center, Unit #1, Information Collection Request

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Process Run Data

Run Name Value UOM Comments

Target

Value

1 Residual Oil (No. 6) Burned 59626 gal/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/17/2010; 

Start - 13:28; 

End - 15:27

0

10 Residual Oil (No. 6) Burned 59619 gal/hr Method 027/028; 

Run PM-1; Date - 

5/17/2010; Start - 

18:31; End - 21:39

0

11 Residual Oil (No. 6) Burned 59927 gal/hr Method 027/028; 

Run PM-2; Date - 

5/19/2010; Start - 

16:43; End - 18:15

0

12 Residual Oil (No. 6) Burned 59736 gal/hr Method 027/028; 

Run PM-3; Date - 

5/20/2010; Start - 

15:22; End - 18:00

0

2 Residual Oil (No. 6) Burned 59685 gal/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/17/2010; 

Start - 15:52; 

End - 17:52

0

3 Residual Oil (No. 6) Burned 59714 gal/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/18/2010; 

Start - 13:04; 

End - 15:03

0

4 Residual Oil (No. 6) Burned 59649 gal/hr Method 23; Run 

D/F-1; Date - 

5/17/2010; Start - 

09:37; End - 20:16

0

5 Residual Oil (No. 6) Burned 59722 gal/hr Method 23; Run 

D/F-2; Date - 

5/18/2010; Start - 

11:05; End - 19:58

0

6 Residual Oil (No. 6) Burned 59985 gal/hr Method 23; Run 

D/F-3; Date - 

5/20/2010; Start - 

11:10; End - 20:03

0

7 Residual Oil (No. 6) Burned 59649 gal/hr Method 29; Run 

M-1; Date - 

5/17/2010; Start - 

13:16; End - 17:59

0

Monday, February 14, 2011 Page 16 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

8 Residual Oil (No. 6) Burned 59649 gal/hr Method 29; Run 

M-2; Date - 

5/18/2010; Start - 

08:02; End - 12:42

0

9 Residual Oil (No. 6) Burned 59736 gal/hr Method 29; Run 

M-3; Date - 

5/18/2010; Start - 

12:57; End - 17:32

0

1 Average Heat Input 7426 MMBtu/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/17/2010; 

Start - 13:28; 

End - 15:27

0

10 Average Heat Input 7427 MMBtu/hr Method 027/028; 

Run PM-1; Date - 

5/17/2010; Start - 

18:31; End - 21:39

0

11 Average Heat Input 7465 MMBtu/hr Method 027/028; 

Run PM-2; Date - 

5/19/2010; Start - 

16:43; End - 18:15

0

12 Average Heat Input 7441 MMBtu/hr Method 027/028; 

Run PM-3; Date - 

5/20/2010; Start - 

15:22; End - 18:00

0

2 Average Heat Input 7433 MMBtu/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/17/2010; 

Start - 15:52; 

End - 17:52

0

3 Average Heat Input 7438 MMBtu/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/18/2010; 

Start - 13:04; 

End - 15:03

0

4 Average Heat Input 7430 MMBtu/hr Method 23; Run 

D/F-1; Date - 

5/17/2010; Start - 

09:37; End - 20:16

0

5 Average Heat Input 7440 MMBtu/hr Method 23; Run 

D/F-2; Date - 

5/18/2010; Start - 

11:05; End - 19:58

0

6 Average Heat Input 7471 MMBtu/hr Method 23; Run 

D/F-3; Date - 

5/20/2010; Start - 

11:10; End - 20:03

0

Monday, February 14, 2011 Page 17 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

7 Average Heat Input 7430 MMBtu/hr Method 29; Run 

M-1; Date - 

5/17/2010; Start - 

13:16; End - 17:59

0

8 Average Heat Input 7429 MMBtu/hr Method 29; Run 

M-2; Date - 

5/18/2010; Start - 

08:02; End - 12:42

0

9 Average Heat Input 7442 MMBtu/hr Method 29; Run 

M-3; Date - 

5/18/2010; Start - 

12:57; End - 17:32

0

1 Steam Output 5353 1000 lb Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/17/2010; 

Start - 13:28; 

End - 15:27

0

10 Steam Output 5351 1000 lb Method 027/028; 

Run PM-1; Date - 

5/17/2010; Start - 

18:31; End - 21:39

0

11 Steam Output 5362 1000 lb Method 027/028; 

Run PM-2; Date - 

5/19/2010; Start - 

16:43; End - 18:15

0

12 Steam Output 5354 1000 lb Method 027/028; 

Run PM-3; Date - 

5/20/2010; Start - 

15:22; End - 18:00

0

2 Steam Output 5356 1000 lb Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/17/2010; 

Start - 15:52; 

End - 17:52

0

3 Steam Output 5366 1000 lb Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/18/2010; 

Start - 13:04; 

End - 15:03

0

4 Steam Output 5354 1000 lb Method 23; Run 

D/F-1; Date - 

5/17/2010; Start - 

09:37; End - 20:16

0

5 Steam Output 5365 1000 lb Method 23; Run 

D/F-2; Date - 

5/18/2010; Start - 

11:05; End - 19:58

0

Monday, February 14, 2011 Page 18 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

6 Steam Output 5354 1000 lb Method 23; Run 

D/F-3; Date - 

5/20/2010; Start - 

11:10; End - 20:03

0

7 Steam Output 5354 1000 lb Method 29; Run 

M-1; Date - 

5/17/2010; Start - 

13:16; End - 17:59

0

8 Steam Output 5363 1000 lb Method 29; Run 

M-2; Date - 

5/18/2010; Start - 

08:02; End - 12:42

0

9 Steam Output 5367 1000 lb Method 29; Run 

M-3; Date - 

5/18/2010; Start - 

12:57; End - 17:32

0

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

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/17/2010; 

Start - 13:28; 

End - 15:27

0

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

Run PM-1; Date - 

5/17/2010; Start - 

18:31; End - 21:39

0

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

Run PM-2; Date - 

5/19/2010; Start - 

16:43; End - 18:15

0

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

Run PM-3; Date - 

5/20/2010; Start - 

15:22; End - 18:00

0

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

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/17/2010; 

Start - 15:52; 

End - 17:52

0

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

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/18/2010; 

Start - 13:04; 

End - 15:03

0

4 Unit Gross Electrical Output 798 MWg Method 23; Run 

D/F-1; Date - 

5/17/2010; Start - 

09:37; End - 20:16

0

Monday, February 14, 2011 Page 19 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

5 Unit Gross Electrical Output 798 MWg Method 23; Run 

D/F-2; Date - 

5/18/2010; Start - 

11:05; End - 19:58

0

6 Unit Gross Electrical Output 798 MWg Method 23; Run 

D/F-3; Date - 

5/20/2010; Start - 

11:10; End - 20:03

0

7 Unit Gross Electrical Output 798 MWg Method 29; Run 

M-1; Date - 

5/17/2010; Start - 

13:16; End - 17:59

0

8 Unit Gross Electrical Output 798 MWg Method 29; Run 

M-2; Date - 

5/18/2010; Start - 

08:02; End - 12:42

0

9 Unit Gross Electrical Output 798 MWg Method 29; Run 

M-3; Date - 

5/18/2010; Start - 

12:57; End - 17:32

0

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

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 5/17/2010; 

Start - 13:28; 

End - 15:27

0

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

Run PM-1; Date - 

5/17/2010; Start - 

18:31; End - 21:39

0

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

Run PM-2; Date - 

5/19/2010; Start - 

16:43; End - 18:15

0

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

Run PM-3; Date - 

5/20/2010; Start - 

15:22; End - 18:00

0

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

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 5/17/2010; 

Start - 15:52; 

End - 17:52

0

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

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 5/18/2010; 

Start - 13:04; 

End - 15:03

0

Monday, February 14, 2011 Page 20 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

APCD Run Data

Process Lab Run Data

4 Unit Net Electric Generation 766 MWn Method 23; Run 

D/F-1; Date - 

5/17/2010; Start - 

09:37; End - 20:16

0

5 Unit Net Electric Generation 766 MWn Method 23; Run 

D/F-2; Date - 

5/18/2010; Start - 

11:05; End - 19:58

0

6 Unit Net Electric Generation 766 MWn Method 23; Run 

D/F-3; Date - 

5/20/2010; Start - 

11:10; End - 20:03

0

7 Unit Net Electric Generation 766 MWn Method 29; Run 

M-1; Date - 

5/17/2010; Start - 

13:16; End - 17:59

0

8 Unit Net Electric Generation 766 MWn Method 29; Run 

M-2; Date - 

5/18/2010; Start - 

08:02; End - 12:42

0

9 Unit Net Electric Generation 766 MWn Method 29; Run 

M-3; Date - 

5/18/2010; Start - 

12:57; End - 17:32

0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 165 NOx Emissions 0

2 LOW NOX BURNERS 168 NOx Emissions 0

3 LOW NOX BURNERS 154 NOx Emissions 0

1 CYCLONE SEPARATORS 13.9 Opacity 0

2 CYCLONE SEPARATORS 15.2 Opacity 0

3 CYCLONE SEPARATORS 11.4 Opacity 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 17800 Btu/lb

1 Fuel Moisture 0.112 %

1 Fuel Mercury Content 0.001 mg/kg

1 Fuel Chlorine Content 194 mg/kg

1 Fuel Fluorine Content 74 mg/kg

1 Fuel Antimony Content 0.87 mg/kg

1 Fuel Arsenic Content 0.08 mg/kg

1 Fuel Beryllium Content 0.008 mg/kg

Monday, February 14, 2011 Page 21 of 32
Manatee Energy Center, Unit #1, Information Collection Request

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1 Fuel Cadmium Content 0.008 mg/kg

1 Fuel Chromium Content 0.083 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 22.3 mg/kg

1 Fuel Selenium Content 0.03 mg/kg

1 Fuel Sulfur Content 10700 mg/kg

1 Fuel Proximate Analysis (Carbon) 88.51 %

1 Fuel Proximate Analysis (Hydrogen) 10.06 %

1 Fuel Proximate Analysis (Nitrogen) 0.57 %

1 Fuel Proximate Analysis (Oxygen) 0.5 %

1 Fuel Proximate Analysis (Sulfur) 1.06 %

2 Fuel Higher Heating Value 17800 Btu/lb

2 Fuel Moisture 0.083 %

2 Fuel Mercury Content 0.002 mg/kg

2 Fuel Chlorine Content 217 mg/kg

2 Fuel Fluorine Content 78 mg/kg

2 Fuel Antimony Content 1 mg/kg

2 Fuel Arsenic Content 0.069 mg/kg

2 Fuel Beryllium Content 0.008 mg/kg

2 Fuel Cadmium Content 0.008 mg/kg

2 Fuel Chromium Content 0.092 mg/kg

2 Fuel Cobalt Content 1 mg/kg

2 Fuel Lead Content 0.17 mg/kg

2 Fuel Manganese Content 0.4 mg/kg

2 Fuel Nickel Content 22.5 mg/kg

2 Fuel Selenium Content 0.03 mg/kg

2 Fuel Sulfur Content 10500 mg/kg

2 Fuel Proximate Analysis (Carbon) 87.72 %

2 Fuel Proximate Analysis (Hydrogen) 9.97 %

2 Fuel Proximate Analysis (Nitrogen) 0.59 %

2 Fuel Proximate Analysis (Oxygen) 0.5 %

2 Fuel Proximate Analysis (Sulfur) 1.2 %

3 Fuel Higher Heating Value 17900 Btu/lb

3 Fuel Moisture 0.22 %

3 Fuel Mercury Content 0.003 mg/kg

3 Fuel Chlorine Content 213 mg/kg

3 Fuel Fluorine Content 78 mg/kg

3 Fuel Antimony Content 1.2 mg/kg

3 Fuel Arsenic Content 0.056 mg/kg

3 Fuel Beryllium Content 0.008 mg/kg

3 Fuel Cadmium Content 0.009 mg/kg

Monday, February 14, 2011 Page 22 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

3 Fuel Chromium Content 0.1 mg/kg

3 Fuel Cobalt Content 0.94 mg/kg

3 Fuel Lead Content 0.19 mg/kg

3 Fuel Manganese Content 0.5 mg/kg

3 Fuel Nickel Content 22.3 mg/kg

3 Fuel Selenium Content 0.03 mg/kg

3 Fuel Sulfur Content 10000 mg/kg

3 Fuel Proximate Analysis (Carbon) 87.96 %

3 Fuel Proximate Analysis (Hydrogen) 10.57 %

3 Fuel Proximate Analysis (Nitrogen) 0.68 %

3 Fuel Proximate Analysis (Oxygen) 0.5 %

3 Fuel Proximate Analysis (Sulfur) 1.16 %

Monday, February 14, 2011 Page 23 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Sampling / Stack Data Results Detail

Location PMT1 - D/F - Method 23

Average

Run Number PMT1-23-1 PMT1-23-2 PMT1-23-3

Test Date 5/17/2010 5/18/2010 5/20/2010

Run Start Time 9:37:00 AM 11:05:00 AM 11:10:00 AM

Run Finish Time 5:37:00 PM 7:05:00 PM 7:10:00 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 30.01 30.01 29.9 29.973

Average Orifice Meter Differential, inches H2O 2.16 2.24 2.06 2.153

Dry Gas Meter Volume Sampled, cubic feet 376.740 379.760 366.460 374.320

Average Dry Gas Meter Temperature, °F 74.92 78.33 78.46 77.237

Dry Gas Meter Volume Sampled, dscf 370.084 370.760 356.228 365.691

Total Moisture Liquid collected, g 802.6 821.1 754.9 792.867

Volume of Water Vapor, standard cubic feet 37.78 38.65 35.53 37.320

Moisture Content of Stack Gas, % 9.26 9.44 9.07 9.257

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

Dry Mole Fraction 0.9074 0.9056 0.9093 0.907

Carbon Dioxide, % 12.79 12.66 12.86 12.770

Oxygen, % 5.26 5.36 5.28 5.300

Carbon Monoxide & Nitrogen, % 81.95 81.98 81.86 81.930

Fuel Factor 1.22 1.23 1.21

Dry Molecular Weight, lb/lb-Mole 30.26 30.24 30.27 30.257

Wet Molecular weight, lb/lb-Mole 29.12 29.08 29.16 29.120

Flue Gas Static Pressure, inches of H2O -1.4 -1.4 -1.4 -1.400

Absolute Flue Gas Pressure, inches of Mercury 29.91 29.91 29.80 29.873

Average Stack Gas Temperature, °F 323.33 328.50 329.38 327.070

Average Velocity Head, inches of H2O 0.8219652069

63952

0.850952866

417075

0.808911559

550721

0.827

Average Stack Gas Velocity, feet/second 61.74 63.07 61.56 62.123

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

Dry Volumetric Flow Rate, dry scfm 1,577,964.0 1,598,210.6 1,558,820.1 1,578,331.5

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,580,799.9 2,636,395.4 2,573,275.7 2,596,823.6

67

Percent Isokinetic of Sampling Rate, % 99.9 98.8 97.3 98.667

Percent Excess Air, % 32.1 32.9 32.3 32.433

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 24 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - 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 25 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - 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 26 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - Gases - Method 3A CO2

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 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - Gases - Method 3A O2

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 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - Gases - Method 6C

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 29 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - Gases - Method 7E

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 30 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - 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 31 of 32
Manatee Energy Center, Unit #1, Information Collection Request

8/23/2010

Location PMT1 - 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 32 of 32