Name: Rudy Sanchez

Title: Plant General Manager

Company: Florida Power & Light Co

Sign Date: 6/22/2010

Name: Thomas K. Graham

Title: Director of Operations

Company: Air Hygiene International, Inc.

Sign Date: 5/17/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Turkey Point 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 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Facility Information:

Turkey Point Energy Center

9760 SW 344th Street

Homestead FL 33035

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:

0250003-011-AV

Permitted Source ID/Name:

PTP1 Foster Wheeler, Wall Fired Boiler

Permitted Maximum Process Rate:

440 MW

Max. Normal Operation Process Rate:

400 MW

Target Process Test Rate

380 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 PTP1 and PTP2. The facility is located at 9760 SW 344th Street in Homestead, 

Florida. Unit PTP1 and PTP2 are of identical design and consists of two wall fired boilers and ancillary equipment 

designed to generate 440 megawatts (MW) of electricity each with rated heat inputs of 4,000 million British thermal 

units per hour (MMBtu/hr) based on high heating value (HHV). Fuel oil consumption is rated at 228,000 pounds per 

hour. Unit PTP1 and PTP2 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 #: 0250003 FRS #: 110000914832

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

PTP1 - D/F 242.3 0 0 0 2202 2002 4 12

PTP1 - Gases 242.3 0 0 0 2202 2002 4 1

PTP1 - Metals 242.3 0 0 0 2202 2002 4 12

PTP1 - PM 242.3 0 0 0 2202 2002 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
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

PTP1 - D/F % H2O Method 1 - 4 3 480 12

PTP1 - D/F 2,3,7,8-TCDD Method 23 3 480 12

PTP1 - D/F 1,2,3,7,8-PeCDD Method 23 3 480 12

PTP1 - D/F 1,2,3,4,7,8-HxCDD Method 23 3 480 12

PTP1 - D/F 1,2,3,6,7,8-HxCDD Method 23 3 480 12

PTP1 - D/F 1,2,3,7,8,9-HxCDD Method 23 3 480 12

PTP1 - D/F 1,2,3,4,6,7,8-HpCDD Method 23 3 480 12

PTP1 - D/F OCDD Method 23 3 480 12

PTP1 - D/F 2,3,7,8-TCDF Method 23 3 480 12

PTP1 - D/F 1,2,3,7,8-PeCDF Method 23 3 480 12

PTP1 - D/F 2,3,4,7,8-PeCDF Method 23 3 480 12

PTP1 - D/F 1,2,3,4,7,8-HxCDF Method 23 3 480 12

PTP1 - D/F 1,2,3,6,7,8-HxCDF Method 23 3 480 12

PTP1 - D/F 2,3,4,6,7,8-HxCDF Method 23 3 480 12

PTP1 - D/F 1,2,3,7,8,9-HxCDF Method 23 3 480 12

PTP1 - D/F 1,2,3,4,6,7,8-HpCDF Method 23 3 480 12

PTP1 - D/F 1,2,3,4,7,8,9-HpCDF Method 23 3 480 12

PTP1 - D/F OCDF Method 23 3 480 12

PTP1 - D/F Total Dioxins Method 23 3 480 12

PTP1 - D/F Total Furans Method 23 3 480 12

PTP1 - D/F 3,3',4,4'-TCB (PCB77) Method 23 3 480 12

PTP1 - D/F 3,4,4',5-TCB (PCB81) Method 23 3 480 12

PTP1 - D/F 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 12

PTP1 - D/F 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 12

PTP1 - D/F 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 12

PTP1 - D/F 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 12

PTP1 - D/F 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 12

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

HxCB (PCBs156/157)

PTP1 - D/F Method 23 3 480 12

PTP1 - D/F 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 12

PTP1 - D/F 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 12

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

(PCB189)

PTP1 - D/F Method 23 3 480 12

PTP1 - D/F O2 Method 3A O2 3 480 12

PTP1 - D/F Co2 Method 3A CO2 3 480 12

% H2O Method 1 - 4 3 120 1 Determined after 

initial stratification test

PTP1 - Gases

Carbon Monoxide Method 10 3 120 1 Determined after 

initial stratification test

PTP1 - Gases

Total organic compounds 

(TOC) as Propane

Method 25A 3 120 1 Determined after 

initial stratification test

PTP1 - Gases

O2 Method 3A O2 3 120 1 Determined after 

initial stratification test

PTP1 - Gases

Co2 Method 3A CO2 3 120 1 Determined after 

initial stratification test

PTP1 - Gases

Sulfur Dioxide Method 6C 3 120 1 Determined after 

initial stratification test

PTP1 - Gases

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

initial stratification test

PTP1 - Gases

PTP1 - Metals % H2O Method 1 - 4 3 240 12

PTP1 - Metals Selenium Method 29 3 240 12

PTP1 - Metals Manganese Method 29 3 240 12

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

PTP1 - Metals Lead Method 29 3 240 12

PTP1 - Metals Filterable Particulate Method 29 3 240 12

PTP1 - Metals Cobalt Method 29 3 240 12

PTP1 - Metals Cadmium Method 29 3 240 12

PTP1 - Metals Chromium Method 29 3 240 12

PTP1 - Metals Nickel Method 29 3 240 12

PTP1 - Metals Co2 Method 3A CO2 3 240 12

PTP1 - Metals O2 Method 3A O2 3 240 12

% H2O Method 1 - 4 3 130 12 Run times vary based 

on method calculations

PTP1 - PM

Filterable Particulate OTM - 27/28 3 130 12 Run times vary based 

on method calculations

PTP1 - PM

Filterable PM2.5 OTM - 27/28 3 130 12 Run times vary based 

on method calculations

PTP1 - PM

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 130 12 Run times vary based 

on method calculations

PTP1 - PM

Organic Condensible 

Particulate

OTM - 27/28 3 130 12 Run times vary based 

on method calculations

PTP1 - PM

Total PM2.5 OTM - 27/28 3 130 12 Run times vary based 

on method calculations

PTP1 - PM

Total Particulate OTM - 27/28 3 130 12 Run times vary based 

on method calculations

PTP1 - PM

O2 Method 3A O2 3 130 12 Run times vary based 

on method calculations

PTP1 - PM

Co2 Method 3A CO2 3 130 12 Run times vary based 

on method calculations

PTP1 - PM

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

Location PTP1 - D/F - Method 23

Average

Run Number PTP1-23-1 PTP1-23-2 PTP1-23-3

Test Date 4/1/2010 4/2/2010 4/3/2010

Run Start Time 8:38:00 AM 8:02:00 

AM

9:39:00 AM

Run Finish Time 6:44:00 PM 5:17:00 PM 6:13:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 405.087 404.203 395.239 401.510

Moisture Content of Stack Gas, % 10.00 10.33 10.06 10.130

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

Carbon Dioxide, % 14.57 14.8 14.77 14.713

Oxygen, % 2.79 2.93 2.88 2.867

Average Stack Gas Temperature, °F 278.92 290.00 303.67 290.863

Dry Volumetric Flow Rate, dry scfm 794,677.3 782,009.0 773,897.8 783,528.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,236,522.9 1,242,094.6 1,247,858.4 1,242,158.63

3

Percent Isokinetic of Sampling Rate, % 99.8 101.2 99.9 100.300

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 PTP1 - Gases - Method 10

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 14, 2011 Page 5 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

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Location PTP1 - Gases - Method 25A

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location PTP1 - Gases - Method 3A CO2

Average

Run Number 1-CO2-1 1-CO2-2 1-CO2-3

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Monday, February 14, 2011 Page 6 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

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Location PTP1 - Gases - Method 3A O2

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location PTP1 - Gases - Method 6C

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

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
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Location PTP1 - Gases - Method 7E

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

Fuel Type Oil Oil Oil

Fw 10320 10320 10320 10,320.000

Fc 1420 1420 1420 1,420.000

Location PTP1 - Metals - Method 29

Average

Run Number PTP1-29-1 PTP1-29-2 PTP1-29-3

Test Date 4/1/2010 4/2/2010 4/3/2010

Run Start Time 2:32:00 PM 2:34:00 PM 1:40:00 PM

Run Finish Time 7:06:00 PM 7:06:00 PM 6:05:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 192.039 195.812 200.612 196.154

Moisture Content of Stack Gas, % 10.12 10.30 9.59 10.003

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

Carbon Dioxide, % 14.57 14.8 14.77 14.713

Oxygen, % 2.79 2.93 2.88 2.867

Average Stack Gas Temperature, °F 280.75 287.17 305.83 291.250

Dry Volumetric Flow Rate, dry scfm 776,840.4 775,881.2 797,928.5 783,550.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,211,354.4 1,227,300.9 1,282,248.9 1,240,301.40

0

Percent Isokinetic of Sampling Rate, % 96.8 98.8 98.4 98.000

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

Monday, February 14, 2011 Page 8 of 34
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Location PTP1 - PM - OTM - 27/28

Average

Run Number PTP1-27/28-

1

PTP1-

27/28-2

PTP1-27/28-

3

Test Date 4/1/2010 4/2/2010 4/3/2010

Run Start Time 11:28:00 AM 11:18:00 

AM

10:47:00 AM

Run Finish Time 2:07:00 PM 2:01:00 PM 1:17:00 PM

Net Run Time, minutes 131 130 131

Dry Gas Meter Volume Sampled, dscf 45.753 45.949 41.855 44.519

Moisture Content of Stack Gas, % 11.30 9.92 9.88 10.367

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

Carbon Dioxide, % 14.57 14.8 14.77 14.713

Oxygen, % 2.79 2.93 2.88 2.867

Average Stack Gas Temperature, °F 281.92 292.92 303.08 292.640

Dry Volumetric Flow Rate, dry scfm 740,867.8 763,760.8 752,507.9 752,378.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,175,619.0 1,209,048.9 1,210,009.5 1,198,225.80

0

Percent Isokinetic of Sampling Rate, % 113.7 111.6 102.4 109.233

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

Monday, February 14, 2011 Page 9 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

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Emissions Summary

Location: PTP1 - D/F - Method 23

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000043 0.0000000058 0.00000000598 0.000

lb/mmBtuO2 2.48E-13 3.38E-13 3.56E-13 0.000

ng/dscm 3.75E-04 5.07E-04 5.34E-04 0.000

ng/dscm@7%O2 2.88E-04 3.92E-04 4.12E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000024 0.0000000045 0.0000000023 0.000

lb/mmBtuO2 1.39E-13 2.62E-13 1.37E-13 0.000

ng/dscm 2.09E-04 3.93E-04 2.06E-04 0.000

ng/dscm@7%O2 1.60E-04 3.04E-04 1.59E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000031 0.0000000022 0.0000000029 0.000

lb/mmBtuO2 1.79E-13 1.28E-13 1.72E-13 0.000

ng/dscm 2.70E-04 1.92E-04 2.59E-04 0.000

ng/dscm@7%O2 2.07E-04 1.49E-04 2.00E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000032 0.0000000026 0.0000000026 0.000

lb/mmBtuO2 1.85E-13 1.52E-13 1.55E-13 0.000

ng/dscm 2.79E-04 2.27E-04 2.32E-04 0.000

ng/dscm@7%O2 2.14E-04 1.76E-04 1.79E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000016 0.00000000094 0.0000000014 0.000

lb/mmBtuO2 9.24E-14 5.48E-14 8.32E-14 0.000

ng/dscm 1.40E-04 8.21E-05 1.25E-04 0.000

ng/dscm@7%O2 1.07E-04 6.35E-05 9.64E-05 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000031 0.0000000026 0.0000000025 0.000

lb/mmBtuO2 1.79E-13 1.52E-13 1.49E-13 0.000

ng/dscm 2.70E-04 2.27E-04 2.23E-04 0.000

ng/dscm@7%O2 2.07E-04 1.76E-04 1.72E-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 PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000015 0.00000000087 0.0000000022 0.000

lb/mmBtuO2 8.66E-14 5.07E-14 1.31E-13 0.000

ng/dscm 1.31E-04 7.60E-05 1.97E-04 0.000

ng/dscm@7%O2 1.01E-04 5.88E-05 1.52E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000032 0.0000000026 0.0000000026 0.000

lb/mmBtuO2 1.85E-13 1.52E-13 1.55E-13 0.000

ng/dscm 2.79E-04 2.27E-04 2.32E-04 0.000

ng/dscm@7%O2 2.14E-04 1.76E-04 1.79E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000025 0.000000001 0.0000000015 0.000

lb/mmBtuO2 1.44E-13 5.83E-14 8.92E-14 0.000

ng/dscm 2.18E-04 8.74E-05 1.34E-04 0.000

ng/dscm@7%O2 1.67E-04 6.76E-05 1.03E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000025 0.0000000021 0.0000000022 0.000

lb/mmBtuO2 1.44E-13 1.22E-13 1.31E-13 0.000

ng/dscm 2.18E-04 1.84E-04 1.97E-04 0.000

ng/dscm@7%O2 1.67E-04 1.42E-04 1.52E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000014 0.0000000014 0.0000000013 0.000

lb/mmBtuO2 8.08E-14 8.16E-14 7.73E-14 0.000

ng/dscm 1.22E-04 1.22E-04 1.16E-04 0.000

ng/dscm@7%O2 9.36E-05 9.44E-05 8.95E-05 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000051 0.000000002 0.000000006 0.000

lb/mmBtuO2 2.94E-13 1.17E-13 3.57E-13 0.000

ng/dscm 4.45E-04 1.75E-04 5.36E-04 0.000

ng/dscm@7%O2 3.42E-04 1.35E-04 4.13E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000201 0.000000015 0.0000000175 0.000

lb/mmBtuO2 1.16E-12 8.74E-13 1.04E-12 0.000

ng/dscm 1.75E-03 1.31E-03 1.56E-03 0.002

ng/dscm@7%O2 1.34E-03 1.01E-03 1.20E-03 0.001

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.000000472 0.000000468 0.000000421 0.000

lb/mmBtuO2 2.72E-11 2.73E-11 2.50E-11 0.000

ng/dscm 4.12E-02 4.09E-02 3.76E-02 0.040

ng/dscm@7%O2 3.16E-02 3.16E-02 2.90E-02 0.031

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000428 0.000000034 0.0000000337 0.000

lb/mmBtuO2 2.47E-12 1.98E-12 2.00E-12 0.000

ng/dscm 3.73E-03 2.97E-03 3.01E-03 0.003

ng/dscm@7%O2 2.86E-03 2.30E-03 2.32E-03 0.002

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000437 0.000000035 0.0000000452 0.000

lb/mmBtuO2 2.52E-12 2.04E-12 2.69E-12 0.000

ng/dscm 3.81E-03 3.06E-03 4.04E-03 0.004

ng/dscm@7%O2 2.92E-03 2.37E-03 3.12E-03 0.003

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.00000122 0.00000133 0.00000112 0.000

lb/mmBtuO2 7.04E-11 7.75E-11 6.66E-11 0.000

ng/dscm 1.06E-01 1.16E-01 1.00E-01 0.107

ng/dscm@7%O2 8.14E-02 8.97E-02 7.71E-02 0.083

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.000000023 0.0000000234 0.000000019 0.000

lb/mmBtuO2 1.33E-12 1.36E-12 1.13E-12 0.000

ng/dscm 2.01E-03 2.04E-03 1.70E-03 0.002

ng/dscm@7%O2 1.54E-03 1.58E-03 1.31E-03 0.001

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000041 0.00000000092 0.0000000014 0.000

lb/mmBtuO2 2.37E-13 5.36E-14 8.32E-14 0.000

ng/dscm 3.57E-04 8.04E-05 1.25E-04 0.000

ng/dscm@7%O2 2.74E-04 6.22E-05 9.64E-05 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000013 0.0000000013 0.0000000012 0.000

lb/mmBtuO2 7.50E-14 7.58E-14 7.13E-14 0.000

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ng/dscm 1.13E-04 1.14E-04 1.07E-04 0.000

ng/dscm@7%O2 8.67E-05 8.82E-05 8.25E-05 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000047 0.0000000022 0.000000003 0.000

lb/mmBtuO2 2.71E-13 1.28E-13 1.78E-13 0.000

ng/dscm 4.10E-04 1.92E-04 2.68E-04 0.000

ng/dscm@7%O2 3.15E-04 1.49E-04 2.07E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000021 0.0000000016 0.000000002 0.000

lb/mmBtuO2 1.21E-13 9.33E-14 1.19E-13 0.000

ng/dscm 1.83E-04 1.40E-04 1.79E-04 0.000

ng/dscm@7%O2 1.40E-04 1.08E-04 1.38E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.00000000041 0.0000000011 0.00000000017 0.000

lb/mmBtuO2 2.37E-14 6.41E-14 1.01E-14 0.000

ng/dscm 3.57E-05 9.61E-05 1.52E-05 0.000

ng/dscm@7%O2 2.74E-05 7.43E-05 1.17E-05 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000042 0.0000000032 0.0000000067 0.000

lb/mmBtuO2 2.42E-13 1.87E-13 3.98E-13 0.000

ng/dscm 3.66E-04 2.80E-04 5.99E-04 0.000

ng/dscm@7%O2 2.81E-04 2.17E-04 4.62E-04 0.000

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.000000151 0.000000152 0.000000163 0.000

lb/mmBtuO2 8.72E-12 8.86E-12 9.69E-12 0.000

ng/dscm 1.32E-02 1.33E-02 1.46E-02 0.014

ng/dscm@7%O2 1.01E-02 1.03E-02 1.13E-02 0.011

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

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.00000000852 0.00000000761 0.00000000821 0.000

lb/mmBtuO2 4.92E-13 4.44E-13 4.88E-13 0.000

ng/dscm 7.43E-04 6.65E-04 7.34E-04 0.001

ng/dscm@7%O2 5.70E-04 5.14E-04 5.66E-04 0.001

Compound: OCDD

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Monday, February 14, 2011 Page 13 of 34
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Mass_mg 0.000000008 0.0000000065 0.0000000084 0.000

lb/mmBtuO2 4.62E-13 3.79E-13 4.99E-13 0.000

ng/dscm 6.98E-04 5.68E-04 7.51E-04 0.001

ng/dscm@7%O2 5.36E-04 4.39E-04 5.79E-04 0.001

Compound: OCDF

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000132 0.000000009 0.000000011 0.000

lb/mmBtuO2 7.62E-13 5.25E-13 6.54E-13 0.000

ng/dscm 1.15E-03 7.86E-04 9.83E-04 0.001

ng/dscm@7%O2 8.83E-04 6.08E-04 7.58E-04 0.001

Compound: Total Dioxins

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.000000029 0.0000000244 0.00000002728 0.000

lb/mmBtuO2 1.67E-12 1.42E-12 1.62E-12 0.000

ng/dscm 2.53E-03 2.13E-03 2.44E-03 0.002

ng/dscm@7%O2 1.94E-03 1.65E-03 1.88E-03 0.002

Compound: Total Furans

Average

RunNumber PTP1-23-1 PTP1-23-2 PTP1-23-3

Mass_mg 0.0000000332 0.00000002373 0.0000000272 0.000

lb/mmBtuO2 1.92E-12 1.38E-12 1.62E-12 0.000

ng/dscm 2.89E-03 2.07E-03 2.43E-03 0.002

ng/dscm@7%O2 2.22E-03 1.60E-03 1.87E-03 0.002

Location: PTP1 - Gases - Method 10

Compound: Carbon Monoxide

Average

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

lb/mmBtuO2 1.40E-01 8.70E-02 3.04E-02 0.086

ppm 1.82E+02 1.12E+02 3.90E+01 111.000

ppm@7%O2 1.40E+02 8.64E+01 3.02E+01 85.533

Location: PTP1 - Gases - Method 25A

Compound: Total organic compounds (TOC) as 

Average

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

lb/mmBtuO2 9.49E-04 1.54E-03 2.31E-04 0.001

ppm 7.82E-01 1.26E+00 1.89E-01 0.744

ppm@7%O2 6.00E-01 9.72E-01 1.47E-01 0.573

Location: PTP1 - Gases - Method 6C

Compound: Sulfur Dioxide

Average

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

lb/mmBtuO2 9.76E-01 9.94E-01 1.01E+00 0.993

ppm 5.54E+02 5.61E+02 5.67E+02 560.667

ppm@7%O2 4.25E+02 4.33E+02 4.40E+02 432.667

Monday, February 14, 2011 Page 14 of 34
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Location: PTP1 - Gases - Method 7E

Compound: Nitrogen oxides (NOx)

Average

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

lb/mmBtuO2 5.54E-01 5.82E-01 5.94E-01 0.577

ppm 4.37E+02 4.57E+02 4.64E+02 452.667

ppm@7%O2 3.35E+02 3.53E+02 3.60E+02 349.333

Location: PTP1 - Metals - Method 29

Compound: Antimony

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 0.396 0.404 0.29 0.363

Elb/hr 2.12E-01 2.12E-01 1.53E-01 0.192

lb/mmBtuO2 4.82E-05 4.86E-05 3.40E-05 0.000

mg/dscm 7.28E-02 7.29E-02 5.11E-02 0.066

mg/dscm@7%O2 5.59E-02 5.64E-02 3.94E-02 0.051

Compound: Arsenic

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 0.0231 0.0247 0.023 0.024

Elb/hr 1.24E-02 1.29E-02 1.21E-02 0.012

lb/mmBtuO2 2.81E-06 2.97E-06 2.69E-06 0.000

mg/dscm 4.25E-03 4.46E-03 4.05E-03 0.004

mg/dscm@7%O2 3.26E-03 3.45E-03 3.12E-03 0.003

Compound: Beryllium

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 0.00119 0.00134 0.00167 0.001

Elb/hr 6.37E-04 7.02E-04 8.79E-04 0.001

lb/mmBtuO2 1.45E-07 1.61E-07 1.96E-07 0.000

mg/dscm 2.19E-04 2.42E-04 2.94E-04 0.000

mg/dscm@7%O2 1.68E-04 1.87E-04 2.27E-04 0.000

Compound: Cadmium

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 0.000754 0.000779 0.000584 0.001

Elb/hr 4.03E-04 4.08E-04 3.07E-04 0.000

lb/mmBtuO2 9.18E-08 9.37E-08 6.84E-08 0.000

mg/dscm 1.39E-04 1.41E-04 1.03E-04 0.000

mg/dscm@7%O2 1.07E-04 1.09E-04 7.95E-05 0.000

Compound: Chromium

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 0.041 0.0453 0.0314 0.039

Elb/hr 2.19E-02 2.37E-02 1.65E-02 0.021

lb/mmBtuO2 4.99E-06 5.45E-06 3.68E-06 0.000

mg/dscm 7.54E-03 8.17E-03 5.53E-03 0.007

Monday, February 14, 2011 Page 15 of 34
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mg/dscm@7%O2 5.79E-03 6.32E-03 4.27E-03 0.005

Compound: Cobalt

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 0.212 0.224 0.192 0.209

Elb/hr 1.13E-01 1.17E-01 1.01E-01 0.110

lb/mmBtuO2 2.58E-05 2.70E-05 2.25E-05 0.000

mg/dscm 3.90E-02 4.04E-02 3.38E-02 0.038

mg/dscm@7%O2 2.99E-02 3.12E-02 2.61E-02 0.029

Compound: Filterable Particulate

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 191.2 244.3 219.2 218.233

Elb/hr 1.02E+02 1.28E+02 1.15E+02 115.000

lb/mmBtuO2 2.33E-02 2.94E-02 2.57E-02 0.026

mg/dscm 3.52E+01 4.41E+01 3.86E+01 39.300

mg/dscm@7%O2 2.70E+01 3.41E+01 2.98E+01 30.300

Compound: Lead

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 0.0535 0.0546 0.0393 0.049

Elb/hr 2.86E-02 2.86E-02 2.07E-02 0.026

lb/mmBtuO2 6.51E-06 6.57E-06 4.60E-06 0.000

mg/dscm 9.84E-03 9.85E-03 6.92E-03 0.009

mg/dscm@7%O2 7.55E-03 7.62E-03 5.34E-03 0.007

Compound: Manganese

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 0.207 0.251 0.303 0.254

Elb/hr 1.11E-01 1.32E-01 1.59E-01 0.134

lb/mmBtuO2 2.52E-05 3.02E-05 3.55E-05 0.000

mg/dscm 3.81E-02 4.53E-02 5.33E-02 0.046

mg/dscm@7%O2 2.92E-02 3.50E-02 4.11E-02 0.035

Compound: Nickel

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 4.75 5.05 4.01 4.603

Elb/hr 2.54E+00 2.65E+00 2.11E+00 2.433

lb/mmBtuO2 5.78E-04 6.08E-04 4.70E-04 0.001

mg/dscm 8.74E-01 9.11E-01 7.06E-01 0.830

mg/dscm@7%O2 6.71E-01 7.05E-01 5.45E-01 0.640

Compound: Selenium

Average

RunNumber PTP1-29-1 PTP1-29-2 PTP1-29-3

Mass_mg 0.0287 0.036 0.0268 0.031

Elb/hr 1.54E-02 1.89E-02 1.41E-02 0.016

lb/mmBtuO2 3.49E-06 4.33E-06 3.14E-06 0.000

mg/dscm 5.28E-03 6.49E-03 4.72E-03 0.005

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

mg/dscm@7%O2 4.05E-03 5.02E-03 3.64E-03 0.004

Location: PTP1 - PM - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber PTP1-27/28-2 PTP1-27/28-3 PTP1-27/28-1

Mass_mg 51.642 45.542 45.117 47.434

lb/mmBtuO2 2.65E-02 2.56E-02 2.31E-02 0.025

Compound: Filterable PM2.5

Average

RunNumber PTP1-27/28-1 PTP1-27/28-2 PTP1-27/28-3

Mass_mg 38.633 42.358 39.583 40.191

lb/mmBtuO2 1.97E-02 2.17E-02 2.22E-02 0.021

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber PTP1-27/28-1 PTP1-27/28-2 PTP1-27/28-3

Mass_mg 0.118 1.476 0 0.531

lb/mmBtuO2 6.03E-05 7.57E-04 0.00E+00 0.000

Compound: Organic Condensible Particulate

Average

RunNumber PTP1-27/28-1 PTP1-27/28-2 PTP1-27/28-3

Mass_mg 1.992 1.475 1.175 1.547

lb/mmBtuO2 1.02E-03 7.56E-04 6.60E-04 0.001

Compound: Total Particulate

Average

RunNumber PTP1-27/28-1 PTP1-27/28-2 PTP1-27/28-3

Mass_mg 47.226 54.593 46.717 49.512

lb/mmBtuO2 2.41E-02 2.80E-02 2.62E-02 0.026

Compound: Total PM2.5

Average

RunNumber PTP1-27/28-1 PTP1-27/28-2 PTP1-27/28-3

Mass_mg 40.743 45.31 40.758 42.270

lb/mmBtuO2 2.08E-02 2.32E-02 2.29E-02 0.022

Monday, February 14, 2011 Page 17 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Residual Oil (No. 6) Burned 28568 gal/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 4/1/2010; 

Start - 16:08; 

End - 18:08

0

10 Residual Oil (No. 6) Burned 28565 gal/hr Method 027/028; 

Run PM-1; Date - 

4/1/2010; Start - 

11:28; End - 14:07

0

11 Residual Oil (No. 6) Burned 28521 gal/hr Method 027/028; 

Run PM-2; Date - 

4/2/2010; Start - 

11:18; End - 14:01

0

12 Residual Oil (No. 6) Burned 28653 gal/hr Method 027/028; 

Run PM-3; Date - 

4/3/2010; Start - 

10:47; End - 13:17

0

2 Residual Oil (No. 6) Burned 28524 gal/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 4/2/2010; 

Start - 15:03; 

End - 17:02

0

3 Residual Oil (No. 6) Burned 28524 gal/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 4/2/2010; 

Start - 17:18; 

End - 19:18

0

4 Residual Oil (No. 6) Burned 28565 gal/hr Method 23; Run 

D/F-1; Date - 

4/1/2010; Start - 

08:38; End - 18:44

0

5 Residual Oil (No. 6) Burned 28521 gal/hr Method 23; Run 

D/F-2; Date - 

4/2/2010; Start - 

08:02; End - 17:17

0

6 Residual Oil (No. 6) Burned 28653 gal/hr Method 23; Run 

D/F-3; Date - 

4/3/2010; Start - 

09:39; End - 18:13

0

7 Residual Oil (No. 6) Burned 28565 gal/hr Method 29; Run 

M-1; Date - 

4/1/2010; Start - 

14:32; End - 19:06

0

Monday, February 14, 2011 Page 18 of 34
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8 Residual Oil (No. 6) Burned 28521 gal/hr Method 29; Run 

M-2; Date - 

4/2/2010; Start - 

14:34; End - 19:06

0

9 Residual Oil (No. 6) Burned 28653 gal/hr Method 29; Run 

M-3; Date - 

4/3/2010; Start - 

13:40; End - 18:05

0

1 Average Heat Input 3524 MMBtu/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 4/1/2010; 

Start - 16:08; 

End - 18:08

0

10 Average Heat Input 3524 MMBtu/hr Method 027/028; 

Run PM-1; Date - 

4/1/2010; Start - 

11:28; End - 14:07

0

11 Average Heat Input 3519 MMBtu/hr Method 027/028; 

Run PM-2; Date - 

4/2/2010; Start - 

11:18; End - 14:01

0

12 Average Heat Input 3535 MMBtu/hr Method 027/028; 

Run PM-3; Date - 

4/3/2010; Start - 

10:47; End - 13:17

0

2 Average Heat Input 3519 MMBtu/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 4/2/2010; 

Start - 15:03; 

End - 17:02

0

3 Average Heat Input 3519 MMBtu/hr Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 4/2/2010; 

Start - 17:18; 

End - 19:18

0

4 Average Heat Input 3524 MMBtu/hr Method 23; Run 

D/F-1; Date - 

4/1/2010; Start - 

08:38; End - 18:44

0

5 Average Heat Input 3519 MMBtu/hr Method 23; Run 

D/F-2; Date - 

4/2/2010; Start - 

08:02; End - 17:17

0

6 Average Heat Input 3535 MMBtu/hr Method 23; Run 

D/F-3; Date - 

4/3/2010; Start - 

09:39; End - 18:13

0

Monday, February 14, 2011 Page 19 of 34
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6/22/2010

7 Average Heat Input 3524 MMBtu/hr Method 29; Run 

M-1; Date - 

4/1/2010; Start - 

14:32; End - 19:06

0

8 Average Heat Input 3519 MMBtu/hr Method 29; Run 

M-2; Date - 

4/2/2010; Start - 

14:34; End - 19:06

0

9 Average Heat Input 3535 MMBtu/hr Method 29; Run 

M-3; Date - 

4/3/2010; Start - 

13:40; End - 18:05

0

1 Steam Output 2678 1000 lb Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 4/1/2010; 

Start - 16:08; 

End - 18:08

0

10 Steam Output 2672 1000 lb Method 027/028; 

Run PM-1; Date - 

4/1/2010; Start - 

11:28; End - 14:07

0

11 Steam Output 2663 1000 lb Method 027/028; 

Run PM-2; Date - 

4/2/2010; Start - 

11:18; End - 14:01

0

12 Steam Output 2689 1000 lb Method 027/028; 

Run PM-3; Date - 

4/3/2010; Start - 

10:47; End - 13:17

0

2 Steam Output 2657 1000 lb Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 4/2/2010; 

Start - 15:03; 

End - 17:02

0

3 Steam Output 2654 1000 lb Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 4/2/2010; 

Start - 17:18; 

End - 19:18

0

4 Steam Output 2675 1000 lb Method 23; Run 

D/F-1; Date - 

4/1/2010; Start - 

08:38; End - 18:44

0

5 Steam Output 2663 1000 lb Method 23; Run 

D/F-2; Date - 

4/2/2010; Start - 

08:02; End - 17:17

0

Monday, February 14, 2011 Page 20 of 34
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6/22/2010

6 Steam Output 2686 1000 lb Method 23; Run 

D/F-3; Date - 

4/3/2010; Start - 

09:39; End - 18:13

0

7 Steam Output 2678 1000 lb Method 29; Run 

M-1; Date - 

4/1/2010; Start - 

14:32; End - 19:06

0

8 Steam Output 2656 1000 lb Method 29; Run 

M-2; Date - 

4/2/2010; Start - 

14:34; End - 19:06

0

9 Steam Output 2684 1000 lb Method 29; Run 

M-3; Date - 

4/3/2010; Start - 

13:40; End - 18:05

0

1 Unit Gross Electrical Output 400 MWg Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 4/1/2010; 

Start - 16:08; 

End - 18:08

0

10 Unit Gross Electrical Output 400 MWg Method 027/028; 

Run PM-1; Date - 

4/1/2010; Start - 

11:28; End - 14:07

0

11 Unit Gross Electrical Output 400 MWg Method 027/028; 

Run PM-2; Date - 

4/2/2010; Start - 

11:18; End - 14:01

0

12 Unit Gross Electrical Output 402 MWg Method 027/028; 

Run PM-3; Date - 

4/3/2010; Start - 

10:47; End - 13:17

0

2 Unit Gross Electrical Output 400 MWg Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 4/2/2010; 

Start - 15:03; 

End - 17:02

0

3 Unit Gross Electrical Output 400 MWg Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 4/2/2010; 

Start - 17:18; 

End - 19:18

0

4 Unit Gross Electrical Output 400 MWg Method 23; Run 

D/F-1; Date - 

4/1/2010; Start - 

08:38; End - 18:44

0

Monday, February 14, 2011 Page 21 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

5 Unit Gross Electrical Output 400 MWg Method 23; Run 

D/F-2; Date - 

4/2/2010; Start - 

08:02; End - 17:17

0

6 Unit Gross Electrical Output 402 MWg Method 23; Run 

D/F-3; Date - 

4/3/2010; Start - 

09:39; End - 18:13

0

7 Unit Gross Electrical Output 400 MWg Method 29; Run 

M-1; Date - 

4/1/2010; Start - 

14:32; End - 19:06

0

8 Unit Gross Electrical Output 400 MWg Method 29; Run 

M-2; Date - 

4/2/2010; Start - 

14:34; End - 19:06

0

9 Unit Gross Electrical Output 402 MWg Method 29; Run 

M-3; Date - 

4/3/2010; Start - 

13:40; End - 18:05

0

1 Unit Net Electric Generation 381 MWn Methods 6c, 7e, 

10, and 25a; Run 

RM-1 and FTIR-1; 

Date - 4/1/2010; 

Start - 16:08; 

End - 18:08

0

10 Unit Net Electric Generation 381 MWn Method 027/028; 

Run PM-1; Date - 

4/1/2010; Start - 

11:28; End - 14:07

0

11 Unit Net Electric Generation 381 MWn Method 027/028; 

Run PM-2; Date - 

4/2/2010; Start - 

11:18; End - 14:01

0

12 Unit Net Electric Generation 382 MWn Method 027/028; 

Run PM-3; Date - 

4/3/2010; Start - 

10:47; End - 13:17

0

2 Unit Net Electric Generation 381 MWn Methods 6c, 7e, 

10, and 25a; Run 

RM-2 and FTIR-2; 

Date - 4/2/2010; 

Start - 15:03; 

End - 17:02

0

3 Unit Net Electric Generation 381 MWn Methods 6c, 7e, 

10, and 25a; Run 

RM-3 and FTIR-3; 

Date - 4/2/2010; 

Start - 17:18; 

End - 19:18

0

Monday, February 14, 2011 Page 22 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

APCD Run Data

Process Lab Run Data

4 Unit Net Electric Generation 381 MWn Method 23; Run 

D/F-1; Date - 

4/1/2010; Start - 

08:38; End - 18:44

0

5 Unit Net Electric Generation 381 MWn Method 23; Run 

D/F-2; Date - 

4/2/2010; Start - 

08:02; End - 17:17

0

6 Unit Net Electric Generation 382 MWn Method 23; Run 

D/F-3; Date - 

4/3/2010; Start - 

09:39; End - 18:13

0

7 Unit Net Electric Generation 381 MWn Method 29; Run 

M-1; Date - 

4/1/2010; Start - 

14:32; End - 19:06

0

8 Unit Net Electric Generation 381 MWn Method 29; Run 

M-2; Date - 

4/2/2010; Start - 

14:34; End - 19:06

0

9 Unit Net Electric Generation 382 MWn Method 29; Run 

M-3; Date - 

4/3/2010; Start - 

13:40; End - 18:05

0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 370 NOx Emissions 0

2 LOW NOX BURNERS 381 NOx Emissions 0

3 LOW NOX BURNERS 382 NOx Emissions 0

1 CYCLONE SEPARATORS 6.6 Opacity 0

2 CYCLONE SEPARATORS 7.6 Opacity 0

3 CYCLONE SEPARATORS 7.3 Opacity 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 18500 Btu/lb

1 Fuel Moisture 0.646 %

1 Fuel Mercury Content 0.011 mg/kg

1 Fuel Chlorine Content 97 mg/kg

1 Fuel Fluorine Content 64 mg/kg

1 Fuel Antimony Content 4.8 mg/kg

1 Fuel Arsenic Content 0.11 mg/kg

1 Fuel Beryllium Content 0.008 mg/kg

Monday, February 14, 2011 Page 23 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

1 Fuel Cadmium Content 0.012 mg/kg

1 Fuel Chromium Content 0.19 mg/kg

1 Fuel Cobalt Content 0.83 mg/kg

1 Fuel Lead Content 0.41 mg/kg

1 Fuel Manganese Content 0.8 mg/kg

1 Fuel Nickel Content 20.1 mg/kg

1 Fuel Selenium Content 0.03 mg/kg

1 Fuel Sulfur Content 9370 mg/kg

1 Fuel Proximate Analysis (Carbon) 87.85 %

1 Fuel Proximate Analysis (Hydrogen) 10.16 %

1 Fuel Proximate Analysis (Nitrogen) 0.5 %

1 Fuel Proximate Analysis (Oxygen) 0.5 %

1 Fuel Proximate Analysis (Sulfur) 0.979 %

2 Fuel Higher Heating Value 18400 Btu/lb

2 Fuel Moisture 0.72 %

2 Fuel Mercury Content 0.011 mg/kg

2 Fuel Chlorine Content 110 mg/kg

2 Fuel Fluorine Content 72 mg/kg

2 Fuel Antimony Content 1.8 mg/kg

2 Fuel Arsenic Content 0.074 mg/kg

2 Fuel Beryllium Content 0.008 mg/kg

2 Fuel Cadmium Content 0.011 mg/kg

2 Fuel Chromium Content 0.21 mg/kg

2 Fuel Cobalt Content 0.83 mg/kg

2 Fuel Lead Content 0.4 mg/kg

2 Fuel Manganese Content 0.9 mg/kg

2 Fuel Nickel Content 20.1 mg/kg

2 Fuel Selenium Content 0.03 mg/kg

2 Fuel Sulfur Content 9140 mg/kg

2 Fuel Proximate Analysis (Carbon) 87.9 %

2 Fuel Proximate Analysis (Hydrogen) 10.15 %

2 Fuel Proximate Analysis (Nitrogen) 0.5 %

2 Fuel Proximate Analysis (Oxygen) 0.5 %

2 Fuel Proximate Analysis (Sulfur) 0.982 %

3 Fuel Higher Heating Value 18400 Btu/lb

3 Fuel Moisture 0.706 %

3 Fuel Mercury Content 0.011 mg/kg

3 Fuel Chlorine Content 100 mg/kg

3 Fuel Fluorine Content 69 mg/kg

3 Fuel Antimony Content 1.4 mg/kg

3 Fuel Arsenic Content 0.083 mg/kg

3 Fuel Beryllium Content 0.008 mg/kg

3 Fuel Cadmium Content 0.01 mg/kg

Monday, February 14, 2011 Page 24 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

3 Fuel Chromium Content 0.15 mg/kg

3 Fuel Cobalt Content 0.72 mg/kg

3 Fuel Lead Content 0.31 mg/kg

3 Fuel Manganese Content 1.1 mg/kg

3 Fuel Nickel Content 18.3 mg/kg

3 Fuel Selenium Content 0.03 mg/kg

3 Fuel Sulfur Content 9280 mg/kg

3 Fuel Proximate Analysis (Carbon) 87.18 %

3 Fuel Proximate Analysis (Hydrogen) 10.38 %

3 Fuel Proximate Analysis (Nitrogen) 0.59 %

3 Fuel Proximate Analysis (Oxygen) 0.54 %

3 Fuel Proximate Analysis (Sulfur) 1.01 %

Monday, February 14, 2011 Page 25 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Sampling / Stack Data Results Detail

Location PTP1 - D/F - Method 23

Average

Run Number PTP1-23-1 PTP1-23-2 PTP1-23-3

Test Date 4/1/2010 4/2/2010 4/3/2010

Run Start Time 8:38:00 AM 8:02:00 AM 9:39:00 AM

Run Finish Time 6:44:00 PM 5:17:00 PM 6:13:00 PM

Net Traversing Points 12 12 12

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 29.83 29.77 29.77 29.790

Average Orifice Meter Differential, inches H2O 2.56 2.52 2.48 2.520

Dry Gas Meter Volume Sampled, cubic feet 412.310 415.180 407.240 411.577

Average Dry Gas Meter Temperature, °F 72.17 75.92 77.54 75.210

Dry Gas Meter Volume Sampled, dscf 405.087 404.203 395.239 401.510

Total Moisture Liquid collected, g 956.3 988.7 939.4 961.467

Volume of Water Vapor, standard cubic feet 45.01 46.54 44.22 45.257

Moisture Content of Stack Gas, % 10.00 10.33 10.06 10.130

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

Dry Mole Fraction 0.9 0.8967 0.8994 0.899

Carbon Dioxide, % 14.57 14.8 14.77 14.713

Oxygen, % 2.79 2.93 2.88 2.867

Carbon Monoxide & Nitrogen, % 82.64 82.27 82.35 82.420

Fuel Factor 1.24 1.21 1.22

Dry Molecular Weight, lb/lb-Mole 30.44 30.49 30.48 30.470

Wet Molecular weight, lb/lb-Mole 29.20 29.20 29.22 29.207

Flue Gas Static Pressure, inches of H2O 1 1 1 1.000

Absolute Flue Gas Pressure, inches of Mercury 29.90 29.84 29.84 29.860

Average Stack Gas Temperature, °F 278.92 290.00 303.67 290.863

Average Velocity Head, inches of H2O 0.9491081224

70964

0.941552327

692749

0.934042909

798599

0.942

Average Stack Gas Velocity, feet/second 64.36 64.65 64.95 64.653

Stack Cross-Sectional Area, square feet 320.210 320.210 320.210 320.210

Dry Volumetric Flow Rate, dry scfm 794,677.3 782,009.0 773,897.8 783,528.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,236,522.9 1,242,094.6 1,247,858.4 1,242,158.6

33

Percent Isokinetic of Sampling Rate, % 99.8 101.2 99.9 100.300

Percent Excess Air, % 14.7 15.6 15.3 15.200

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

Round Duct Diameter, inches 242.3 242.3 242.3

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
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Location PTP1 - Gases - Method 10

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Fuel Factor 1.32 1.32 1.32

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

Analyzer Make THERMO THERMO THERMO

Analyzer Model 48i 48i 48i

Analyzer Serial Number INST-CO0017INST-CO0017INST-CO0017

Operating Range 1109 1109 1109 1,109.000

Operating Units ppm ppm ppm

No. Readings/Avg. 240 240 240 240.000

Calibration Set 5 11 11 9.000

Calibration Pre Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Pre Zero Cylinder Instrument Response 2.18 3.1 3.15 2.810

Calibration Pre Zero Cylinder Bias 0.19 0.32 0.32 0.277

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID ALM042523-

CO

ALM042523

-CO

ALM042523-

CO

Calibration Pre High Cylinder Instrument Response 554.2 531.32 534.96 540.160

Calibration Pre High Cylinder Bias 0.08 -1.62 -1.3 -0.947

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Post Zero Cylinder Instrument Response 3.34 3.15 3.01 3.167

Calibration Post Zero Cylinder Bias 0.3 0.32 0.31 0.310

Calibration Post Zero Cylinder Drift 0.11 0 0.01 0.040

Calibration Post High Cylinder ID ALM042523-

CO

ALM042523

-CO

ALM042523-

CO

Calibration Post High Cylinder Instrument Response 555.29 534.96 538.6 542.950

Calibration Post High Cylinder Bias 0.18 -1.3 -0.97 -0.697

Calibration Post High Cylinder Drift 0.1 0.32 0.33 0.250

Cavg 185.89 111.5 41.02 112.803

Cavg Units ppmvd ppmvd ppmvd

Cgas 182.1397 112.257 39.0277 111.141

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 27 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Location PTP1 - Gases - Method 25A

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Fuel Factor 1.32 1.32 1.32

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

Analyzer Make VIG VIG VIG

Analyzer Model 20 20 20 20.000

Analyzer Serial Number INST-TH0007INST-TH0007INST-TH0007

Operating Range 50 50 50 50.000

Operating Units ppm ppm ppm

No. Readings/Avg. 240 240 240 240.000

Calibration Set 6 12 12 10.000

Calibration Pre Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Pre Zero Cylinder Instrument Response -0.09 -0.18 0.02 -0.083

Calibration Pre Zero Cylinder Bias 0 -0.58 -0.18 -0.253

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID CC115743 CC115743 CC115743

Calibration Pre High Cylinder Instrument Response 14.01 14.01 14.04 14.020

Calibration Pre High Cylinder Bias 0 -0.34 -0.28 -0.207

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Post Zero Cylinder Instrument Response -0.11 0.02 0.11 0.007

Calibration Post Zero Cylinder Bias -0.04 -0.18 0 -0.073

Calibration Post Zero Cylinder Drift 0.04 0.4 0.18 0.207

Calibration Post High Cylinder ID CC115743 CC115743 CC115743

Calibration Post High Cylinder Instrument Response 14.04 14.04 14.2 14.093

Calibration Post High Cylinder Bias 0.06 -0.28 0.04 -0.060

Calibration Post High Cylinder Drift 0.06 0.06 0.32 0.147

Cavg 0.59 1.03 0.23 0.617

Cavg Units ppmvw ppmvw ppmvw

Cgas 0.7818 1.2639 0.1885 0.745

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 0.7034336283

18584

1.133215171

92485

0.169050160

085379

0.669

Cgasw Units ppmvw ppmvw ppmvw

Monday, February 14, 2011 Page 28 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Location PTP1 - Gases - Method 3A CO2

Average

Run Number 1-CO2-1 1-CO2-2 1-CO2-3

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Fuel Factor 1.32 1.32 1.32

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

Analyzer Make THERMO THERMO THERMO

Analyzer Model 410i 410i 410i

Analyzer Serial Number INST-C2-0010 INST-C2-

0010

INST-C2-

0010

Operating Range 19.3 19.3 19.3 19.300

Operating Units % % %

No. Readings/Avg. 240 240 240 240.000

Calibration Set 2 8 8 6.000

Calibration Pre Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Pre Zero Cylinder Instrument Response 0.08 0.05 0.09 0.073

Calibration Pre Zero Cylinder Bias 0.21 0.1 0.31 0.207

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID AAL12025-

CO2

AAL12025-

CO2

AAL12025-

CO2

Calibration Pre High Cylinder Instrument Response 8.72 8.43 8.54 8.563

Calibration Pre High Cylinder Bias -0.83 -2.44 -1.87 -1.713

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Post Zero Cylinder Instrument Response 0.05 0.09 0.11 0.083

Calibration Post Zero Cylinder Bias 0.05 0.31 0.41 0.257

Calibration Post Zero Cylinder Drift 0.16 0.21 0.1 0.157

Calibration Post High Cylinder ID AAL12025-

CO2

AAL12025-

CO2

AAL12025-

CO2

Calibration Post High Cylinder Instrument Response 8.79 8.54 8.53 8.620

Calibration Post High Cylinder Bias -0.47 -1.87 -1.92 -1.420

Calibration Post High Cylinder Drift 0.36 0.57 4.999999999

99998E-02

0.327

Cavg 14.3 14.12 14.11 14.177

Cavg Units %vd %vd %vd

Cgas 14.5626 14.8431 14.7657 14.724

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 29 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Location PTP1 - Gases - Method 3A O2

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Fuel Factor 1.32 1.32 1.32

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

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 7 7 5.000

Calibration Pre Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Pre Zero Cylinder Instrument Response 0.49 0.41 0.24 0.380

Calibration Pre Zero Cylinder Bias 2.18 2.09 1.28 1.850

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID AAL12025-O2 AAL12025-

O2

AAL12025-

O2

Calibration Pre High Cylinder Instrument Response 12.2 11.93 11.8 11.977

Calibration Pre High Cylinder Bias 0.62 -0.57 -1.18 -0.377

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Post Zero Cylinder Instrument Response 0.27 0.24 0.09 0.200

Calibration Post Zero Cylinder Bias 1.14 1.28 0.57 0.997

Calibration Post Zero Cylinder Drift 1.04 0.81 0.71 0.853

Calibration Post High Cylinder ID AAL12025-O2 AAL12025-

O2

AAL12025-

O2

Calibration Post High Cylinder Instrument Response 11.84 11.8 11.8 11.813

Calibration Post High Cylinder Bias -1.09 -1.18 -1.18 -1.150

Calibration Post High Cylinder Drift 1.71 0.61 0 0.773

Cavg 3.07 3.08 3.02 3.057

Cavg Units %vd %vd %vd

Cgas 2.7963 2.8887 2.9691 2.885

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
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Location PTP1 - Gases - Method 6C

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Fuel Factor 1.32 1.32 1.32

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

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 9 9 7.000

Calibration Pre Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Pre Zero Cylinder Instrument Response 4.45 6.04 7.48 5.990

Calibration Pre Zero Cylinder Bias 0.43 0.6 0.75 0.593

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID CC66246 CC66246 CC66246

Calibration Pre High Cylinder Instrument Response 441.32 424.96 420.53 428.937

Calibration Pre High Cylinder Bias 0.06 -1 -1.46 -0.800

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Post Zero Cylinder Instrument Response 7.34 7.48 11.1 8.640

Calibration Post Zero Cylinder Bias 0.74 0.75 1.13 0.873

Calibration Post Zero Cylinder Drift 0.31 0.15 0.38 0.280

Calibration Post High Cylinder ID CC66246 CC66246 CC66246

Calibration Post High Cylinder Instrument Response 433.36 420.53 421.72 425.203

Calibration Post High Cylinder Bias -0.77 -1.46 -1.34 -1.190

Calibration Post High Cylinder Drift 0.83 0.46 0.12 0.470

Cavg 564.09 551.62 554.75 556.820

Cavg Units ppmvd ppmvd ppmvd

Cgas 553.7379 560.5973 566.8699 560.402

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
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Location PTP1 - Gases - Method 7E

Average

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

Test Date 4/1/2010 4/2/2010 4/2/2010

Run Start Time 4:08:50 PM 3:03:20 PM 5:18:50 PM

Run Finish Time 6:08:20 PM 5:02:50 PM 7:18:20 PM

Carbon Dioxide, % 14.57 14.84 14.76 14.723

Oxygen, % 2.79 2.89 2.97 2.883

Fuel Factor 1.32 1.32 1.32

Dry Volumetric Flow Rate, dry scfm 794574 781958 781958 786,163.333

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

Moisture, % 10.02 10.34 10.34 10.233

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 10 10 8.000

Calibration Pre Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Pre Zero Cylinder Instrument Response 1.62 1.84 1.96 1.807

Calibration Pre Zero Cylinder Bias 0.12 0.14 0.15 0.137

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID ALM042523-

NOx

ALM042523

-NOx

ALM042523-

NOx

Calibration Pre High Cylinder Instrument Response 563.68 531.31 529.76 541.583

Calibration Pre High Cylinder Bias -0.16 -1.93 -2.07 -1.387

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337

Calibration Post Zero Cylinder Instrument Response 1.39 1.96 1.89 1.747

Calibration Post Zero Cylinder Bias 0.1 0.15 0.15 0.133

Calibration Post Zero Cylinder Drift 0.02 9.999999999

99998E-03

0 0.010

Calibration Post High Cylinder ID ALM042523-

NOx

ALM042523

-NOx

ALM042523-

NOx

Calibration Post High Cylinder Instrument Response 552.64 529.76 531.51 537.970

Calibration Post High Cylinder Bias -1.15 -2.07 -1.91 -1.710

Calibration Post High Cylinder Drift 0.99 0.14 0.16 0.430

Cavg 446.51 443.41 450.57 446.830

Cavg Units ppmvd ppmvd ppmvd

Cgas 437.2865 456.8482 464.1653 452.767

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
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Location PTP1 - Metals - Method 29

Average

Run Number PTP1-29-1 PTP1-29-2 PTP1-29-3

Test Date 4/1/2010 4/2/2010 4/3/2010

Run Start Time 2:32:00 PM 2:34:00 PM 1:40:00 PM

Run Finish Time 7:06:00 PM 7:06:00 PM 6:05:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 240 240 240

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 0.979 0.979 0.979 0.979

Barometric Pressure, inches of Mercury 29.88 29.77 29.8 29.817

Average Orifice Meter Differential, inches H2O 2.28 2.32 2.45 2.350

Dry Gas Meter Volume Sampled, cubic feet 198.640 205.000 209.330 204.323

Average Dry Gas Meter Temperature, °F 76.96 81.54 80.46 79.653

Dry Gas Meter Volume Sampled, dscf 192.039 195.812 200.612 196.154

Total Moisture Liquid collected, g 459.3 477.5 451.8 462.867

Volume of Water Vapor, standard cubic feet 21.62 22.48 21.27 21.790

Moisture Content of Stack Gas, % 10.12 10.30 9.59 10.003

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

Dry Mole Fraction 0.8988 0.897 0.9041 0.900

Carbon Dioxide, % 14.57 14.8 14.77 14.713

Oxygen, % 2.79 2.93 2.88 2.867

Carbon Monoxide & Nitrogen, % 82.64 82.27 82.35 82.420

Fuel Factor 1.24 1.21 1.22

Dry Molecular Weight, lb/lb-Mole 30.44 30.49 30.48 30.470

Wet Molecular weight, lb/lb-Mole 29.18 29.20 29.28 29.220

Flue Gas Static Pressure, inches of H2O 1 1 1 1.000

Absolute Flue Gas Pressure, inches of Mercury 29.95 29.84 29.87 29.887

Average Stack Gas Temperature, °F 280.75 287.17 305.83 291.250

Average Velocity Head, inches of H2O 0.9094438747

67445

0.922651781

47092

0.986549073

441848

0.940

Average Stack Gas Velocity, feet/second 63.05 63.88 66.74 64.557

Stack Cross-Sectional Area, square feet 320.210 320.210 320.210 320.210

Dry Volumetric Flow Rate, dry scfm 776,840.4 775,881.2 797,928.5 783,550.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,211,354.4 1,227,300.9 1,282,248.9 1,240,301.4

00

Percent Isokinetic of Sampling Rate, % 96.8 98.8 98.4 98.000

Percent Excess Air, % 14.7 15.6 15.3 15.200

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

Round Duct Diameter, inches 242.3 242.3 242.3

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 33 of 34
Turkey Point Energy Center, Unit #1, Information Collection Request

6/22/2010

Location PTP1 - PM - OTM - 27/28

Average

Run Number PTP1-27/28-1 PTP1-27/28-

2

PTP1-27/28-3

Test Date 4/1/2010 4/2/2010 4/3/2010

Run Start Time 11:28:00 AM 11:18:00 AM 10:47:00 AM

Run Finish Time 2:07:00 PM 2:01:00 PM 1:17:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 131 130 131

Nozzle Diameter, inches 0.156 0.156 0.156 0.156

Pitot Tube Coefficient 0.8 0.8 0.8 0.800

Dry Gas Meter Calibration Factor 0.979 0.979 0.979 0.979

Barometric Pressure, inches of Mercury 29.8 29.85 29.77 29.807

Average Orifice Meter Differential, inches H2O 0.40 0.40 0.40 0.400

Dry Gas Meter Volume Sampled, cubic feet 47.390 47.900 43.620 46.303

Average Dry Gas Meter Temperature, °F 73.79 78.13 76.54 76.153

Dry Gas Meter Volume Sampled, dscf 45.753 45.949 41.855 44.519

Total Moisture Liquid collected, g 123.9 107.6 97.5 109.667

Volume of Water Vapor, standard cubic feet 5.83 5.06 4.59 5.160

Moisture Content of Stack Gas, % 11.30 9.92 9.88 10.367

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

Dry Mole Fraction 0.887 0.9008 0.9012 0.896

Carbon Dioxide, % 14.57 14.8 14.77 14.713

Oxygen, % 2.79 2.93 2.88 2.867

Carbon Monoxide & Nitrogen, % 82.64 82.27 82.35 82.420

Fuel Factor 1.24 1.21 1.22

Dry Molecular Weight, lb/lb-Mole 30.44 30.49 30.48 30.470

Wet Molecular weight, lb/lb-Mole 29.03 29.25 29.25 29.177

Flue Gas Static Pressure, inches of H2O 1 1 1 1.000

Absolute Flue Gas Pressure, inches of Mercury 29.87 29.92 29.84 29.877

Average Stack Gas Temperature, °F 281.92 292.92 303.08 292.640

Average Velocity Head, inches of H2O 0.9355257028

80071

0.984100902

654807

0.969883457

527265

0.963

Average Stack Gas Velocity, feet/second 61.19 62.93 62.98 62.367

Stack Cross-Sectional Area, square feet 320.210 320.210 320.210 320.210

Dry Volumetric Flow Rate, dry scfm 740,867.8 763,760.8 752,507.9 752,378.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,175,619.0 1,209,048.9 1,210,009.5 1,198,225.8

00

Percent Isokinetic of Sampling Rate, % 113.7 111.6 102.4 109.233

Percent Excess Air, % 14.7 15.6 15.3 15.200

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

Round Duct Diameter, inches 242.3 242.3 242.3

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 34 of 34