### Name: Jeffrey A. Smith

Title: PGD Regional Plant General Manager Company: Florida Power & Light Sign Date: 6/10/2010 Name: Thomas K. Graham Title: Director of Operations Company: Air Hygiene International, Inc. Sign Date: 6/2/2010 Permitted Facility Representative / Date Testing Company Representative / Date



## Port Everglades Energy Center, Unit #3, 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

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 Facility Information: Port Everglades Energy Center
8100 Eisenhower Blvd

Fort Lauderdale FL 33316 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: 0110036-009-AV Permitted Source ID/Name: Foster Wheeler, Wall Fired Boiler PPE3 Permitted Maximum Process Rate: 400 MW Max. Normal Operation Process Rate: 380 MW Target Process Test Rate 375 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 PPE3 and PPE4. The facility is located at 8100 Eisenhower Blvd in Fort Lauderdale, Florida. Unit PPE3 and PPE4 are of identical design and consists of two dry bottom, wall fired boilers and ancillary equipment designed to generate 400 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 230,000 pounds per hour. Unit PPE3 and PPE4 utilize low nitrogen oxide (NOx) burner technology to control NOx emissions and electrostatic precipitators (ESPs) 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 #: 110036 FRS #: 110000363847

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 PPE3 - D/F 251 2592 1016 4 0 24 0 0 PPE3 - Gases 251 2592 1016 4 0 1 0 0 PPE3 - Metals 251 2592 1016 4 0 24 0 0 PPE3 - PM 251 2592 1016 4 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location Regulation Description Compound Limit Unit Not applicable.



### Monday, February 14, 2011 Page 2 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location % H2O Method 1 - 4 3 480 24 PPE3 - D/F 2,3,7,8-TCDD Method 23 3 480 24 PPE3 - D/F 1,2,3,7,8-PeCDD Method 23 3 480 24 PPE3 - D/F 1,2,3,4,7,8-HxCDD Method 23 3 480 24 PPE3 - D/F 1,2,3,6,7,8-HxCDD Method 23 3 480 24 PPE3 - D/F 1,2,3,7,8,9-HxCDD Method 23 3 480 24 PPE3 - D/F 1,2,3,4,6,7,8-HpCDD Method 23 3 480 24 PPE3 - D/F OCDD Method 23 3 480 24 PPE3 - D/F 2,3,7,8-TCDF Method 23 3 480 24 PPE3 - D/F 1,2,3,7,8-PeCDF Method 23 3 480 24 PPE3 - D/F 2,3,4,7,8-PeCDF Method 23 3 480 24 PPE3 - D/F 1,2,3,4,7,8-HxCDF Method 23 3 480 24 PPE3 - D/F 1,2,3,6,7,8-HxCDF Method 23 3 480 24 PPE3 - D/F 2,3,4,6,7,8-HxCDF Method 23 3 480 24 PPE3 - D/F 1,2,3,7,8,9-HxCDF Method 23 3 480 24 PPE3 - D/F 1,2,3,4,6,7,8-HpCDF Method 23 3 480 24 PPE3 - D/F 1,2,3,4,7,8,9-HpCDF Method 23 3 480 24 PPE3 - D/F OCDF Method 23 3 480 24 PPE3 - D/F Total Dioxins Method 23 3 480 24 PPE3 - D/F Total Furans Method 23 3 480 24 PPE3 - D/F 3,3',4,4'-TCB (PCB77) Method 23 3 480 24 PPE3 - D/F 3,4,4',5-TCB (PCB81) Method 23 3 480 24 PPE3 - D/F 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 24 PPE3 - D/F 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 24 PPE3 - D/F 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 24 PPE3 - D/F 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 24 PPE3 - D/F 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 24 PPE3 - D/F 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 480 24 PPE3 - D/F

2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 24 PPE3 - D/F 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 24 PPE3 - D/F 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 24 PPE3 - D/F

O2 Method 3A O2 3 480 24 PPE3 - D/F Co2 Method 3A CO2 3 480 24 PPE3 - D/F % H2O Method 1 - 4 3 120 1 Determined after initial stratification test PPE3 - Gases

Carbon Monoxide Method 10 3 120 1 Determined after initial stratification test PPE3 - Gases
Total organic compounds

(TOC) as Propane Method 25A 3 120 1 Determined after initial stratification test PPE3 - Gases

O2 Method 3A O2 3 120 1 Determined after initial stratification test PPE3 - Gases

Co2 Method 3A CO2 3 120 1 Determined after initial stratification test PPE3 - Gases

Sulfur Dioxide Method 6C 3 120 1 Determined after initial stratification test PPE3 - Gases
Nitrogen oxides (NOx) Method 7E 3 120 1 Determined after initial stratification test PPE3 - Gases

% H2O Method 1 - 4 3 240 24 PPE3 - Metals Selenium Method 29 3 240 24 PPE3 - Metals Manganese Method 29 3 240 24 PPE3 - Metals


### Monday, February 14, 2011 Page 3 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010

The following describes any modifications and/or deviations to the applicable test methods. If alternative methods were requested, see the attachments for documentation of request AND approval, including dates. PM Run 2 - vaccuum maximized before end of run, did not pull required volume.
PM All - oily substance on all filters Lead Method 29 3 240 24 PPE3 - Metals Filterable Particulate Method 29 3 240 24 PPE3 - Metals Cobalt Method 29 3 240 24 PPE3 - Metals Cadmium Method 29 3 240 24 PPE3 - Metals Chromium Method 29 3 240 24 PPE3 - Metals Nickel Method 29 3 240 24 PPE3 - Metals Co2 Method 3A CO2 3 240 24 PPE3 - Metals O2 Method 3A O2 3 240 24 PPE3 - Metals % H2O Method 1 - 4 3 120 12 Run times vary based on method calculations PPE3 - PM

Filterable Particulate OTM - 27/28 3 120 12 Run times vary based on method calculations PPE3 - PM

Filterable PM2.5 OTM - 27/28 3 120 12 Run times vary based on method calculations PPE3 - PM
Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 120 12 Run times vary based on method calculations PPE3 - PM
Organic Condensible

Particulate OTM - 27/28 3 120 12 Run times vary based on method calculations PPE3 - PM

Total PM2.5 OTM - 27/28 3 120 12 Run times vary based on method calculations PPE3 - PM

Total Particulate OTM - 27/28 3 120 12 Run times vary based on method calculations PPE3 - PM

O2 Method 3A O2 3 120 12 Run times vary based on method calculations PPE3 - PM

Co2 Method 3A CO2 3 120 12 Run times vary based on method calculations PPE3 - PM



### Monday, February 14, 2011 Page 4 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 Sampling / Stack Data Results Summary



### Location PPE3 - D/F - Method 23 Average Run Number PPE3-23-1 PPE3-23-2 PPE3-23-3
Test Date 3/9/2010 3/10/2010 3/11/2010 Run Start Time 9:28:00 AM 8:40:00 AM 12:14:00 PM

Run Finish Time 5:28:00 PM 4:40:00 PM 8:14:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 362.078 351.716 356.983 356.926 Moisture Content of Stack Gas, % 8.57 9.36 9.79 9.240 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 13.96 13.95 13.88 13.930 Oxygen, % 4.1 4.18 4.21 4.163 Average Stack Gas Temperature, °F 322.21 324.25 324.13 323.530 Dry Volumetric Flow Rate, dry scfm 766,594.2 758,219.3 757,350.0 760,721.167 Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,246,711.2 1,249,597.6 1,261,555.5 1,252,621.43 3 Percent Isokinetic of Sampling Rate, % 99.2 97.4 99.0 98.533 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 PPE3 - Gases - Method 10 Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Monday, February 14, 2011 Page 5 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - 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 PPE3 - 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 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - 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 PPE3 - 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 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - 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 PPE3 - Metals - Method 29 Average Run Number
Test Date Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Monday, February 14, 2011 Page 8 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - PM - OTM - 27/28 Average Run Number
Test Date Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Monday, February 14, 2011 Page 9 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 Emissions Summary



### Location: PPE3 - D/F - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000054 0.00000000794 0.00000000971 0.000 lb/mmBtuO2 3.76E-13 5.72E-13 6.90E-13 0.000 ng/dscm 5.27E-04 7.97E-04 9.61E-04 0.001 ng/dscm@7%O2 4.36E-04 6.63E-04 8.00E-04 0.001 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000016 0.0000000063 0.0000000057 0.000 lb/mmBtuO2 1.11E-13 4.54E-13 4.05E-13 0.000 ng/dscm 1.56E-04 6.33E-04 5.64E-04 0.000 ng/dscm@7%O2 1.29E-04 5.26E-04 4.70E-04 0.000 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.000000002 0.0000000044 0.0000000027 0.000 lb/mmBtuO2 1.39E-13 3.17E-13 1.92E-13 0.000 ng/dscm 1.95E-04 4.42E-04 2.67E-04 0.000 ng/dscm@7%O2 1.61E-04 3.67E-04 2.22E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000018 0.0000000016 0.0000000023 0.000 lb/mmBtuO2 1.25E-13 1.15E-13 1.63E-13 0.000 ng/dscm 1.76E-04 1.61E-04 2.28E-04 0.000 ng/dscm@7%O2 1.46E-04 1.34E-04 1.90E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.00000000086 0.0000000019 0.0000000018 0.000 lb/mmBtuO2 5.99E-14 1.37E-13 1.28E-13 0.000 ng/dscm 8.39E-05 1.91E-04 1.78E-04 0.000 ng/dscm@7%O2 6.94E-05 1.59E-04 1.48E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000018 0.0000000016 0.0000000023 0.000 lb/mmBtuO2 1.25E-13 1.15E-13 1.63E-13 0.000 ng/dscm 1.76E-04 1.61E-04 2.28E-04 0.000 ng/dscm@7%O2 1.46E-04 1.34E-04 1.90E-04 0.000 

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



### Monday, February 14, 2011 Page 10 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000008 0.0000000018 0.0000000017 0.000 lb/mmBtuO2 5.57E-14 1.30E-13 1.21E-13 0.000 ng/dscm 7.80E-05 1.81E-04 1.68E-04 0.000 ng/dscm@7%O2 6.45E-05 1.50E-04 1.40E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000018 0.0000000019 0.0000000023 0.000 lb/mmBtuO2 1.25E-13 1.37E-13 1.63E-13 0.000 ng/dscm 1.76E-04 1.91E-04 2.28E-04 0.000 ng/dscm@7%O2 1.46E-04 1.59E-04 1.90E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000016 0.000000001 0.0000000019 0.000 lb/mmBtuO2 1.11E-13 7.20E-14 1.35E-13 0.000 ng/dscm 1.56E-04 1.00E-04 1.88E-04 0.000 ng/dscm@7%O2 1.29E-04 8.31E-05 1.57E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000021 0.0000000013 0.0000000015 0.000 lb/mmBtuO2 1.46E-13 9.36E-14 1.07E-13 0.000 ng/dscm 2.05E-04 1.31E-04 1.48E-04 0.000 ng/dscm@7%O2 1.70E-04 1.09E-04 1.23E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000015 0.0000000015 0.000000002 0.000 lb/mmBtuO2 1.04E-13 1.08E-13 1.42E-13 0.000 ng/dscm 1.46E-04 1.51E-04 1.98E-04 0.000 ng/dscm@7%O2 1.21E-04 1.26E-04 1.65E-04 0.000 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000043 0.0000000028 0.0000000029 0.000 lb/mmBtuO2 2.99E-13 2.02E-13 2.06E-13 0.000 ng/dscm 4.19E-04 2.81E-04 2.87E-04 0.000 ng/dscm@7%O2 3.47E-04 2.34E-04 2.39E-04 0.000 

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000137 0.0000000103 0.000000011 0.000 lb/mmBtuO2 9.54E-13 7.42E-13 7.82E-13 0.000 ng/dscm 1.34E-03 1.03E-03 1.09E-03 0.001 ng/dscm@7%O2 1.11E-03 8.56E-04 9.08E-04 0.001



### Monday, February 14, 2011 Page 11 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000004 0.000000411 0.000000406 0.000 lb/mmBtuO2 2.78E-11 2.96E-11 2.89E-11 0.000 ng/dscm 3.90E-02 4.13E-02 4.02E-02 0.040 ng/dscm@7%O2 3.23E-02 3.43E-02 3.35E-02 0.033 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.000000027 0.000000016 0.00000003 0.000 lb/mmBtuO2 1.88E-12 1.15E-12 2.13E-12 0.000 ng/dscm 2.63E-03 1.61E-03 2.97E-03 0.002 ng/dscm@7%O2 2.18E-03 1.34E-03 2.47E-03 0.002 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000302 0.0000000438 0.0000000446 0.000 lb/mmBtuO2 2.10E-12 3.15E-12 3.17E-12 0.000 ng/dscm 2.95E-03 4.40E-03 4.41E-03 0.004 ng/dscm@7%O2 2.44E-03 3.66E-03 3.67E-03 0.003 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.00000104 0.00000104 0.00000107 0.000 lb/mmBtuO2 7.24E-11 7.49E-11 7.60E-11 0.000 ng/dscm 1.01E-01 1.04E-01 1.06E-01 0.104 ng/dscm@7%O2 8.36E-02 8.65E-02 8.83E-02 0.086 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000239 0.0000000229 0.000000017 0.000 lb/mmBtuO2 1.66E-12 1.65E-12 1.21E-12 0.000 ng/dscm 2.33E-03 2.30E-03 1.68E-03 0.002 ng/dscm@7%O2 1.93E-03 1.91E-03 1.40E-03 0.002 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000021 0.0000000033 0.0000000017 0.000 lb/mmBtuO2 1.46E-13 2.38E-13 1.21E-13 0.000 ng/dscm 2.05E-04 3.31E-04 1.68E-04 0.000 ng/dscm@7%O2 1.70E-04 2.75E-04 1.40E-04 0.000 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000014 0.0000000022 0.0000000019 0.000 lb/mmBtuO2 9.75E-14 1.58E-13 1.35E-13 0.000



### Monday, February 14, 2011 Page 12 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 ng/dscm 1.37E-04 2.21E-04 1.88E-04 0.000 ng/dscm@7%O2 1.13E-04 1.84E-04 1.57E-04 0.000 

### Compound: 2,3,7,8-TCDD Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000028 0.0000000021 0.0000000021 0.000 lb/mmBtuO2 1.95E-13 1.51E-13 1.49E-13 0.000 ng/dscm 2.73E-04 2.11E-04 2.08E-04 0.000 ng/dscm@7%O2 2.26E-04 1.75E-04 1.73E-04 0.000 

### Compound: 2,3,7,8-TCDF Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000019 0.000000002 0.000000003 0.000 lb/mmBtuO2 1.32E-13 1.44E-13 2.13E-13 0.000 ng/dscm 1.85E-04 2.01E-04 2.97E-04 0.000 ng/dscm@7%O2 1.53E-04 1.67E-04 2.47E-04 0.000 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.00000000088 0.00000000058 0.00000000071 0.000 lb/mmBtuO2 6.13E-14 4.18E-14 5.05E-14 0.000 ng/dscm 8.58E-05 5.82E-05 7.02E-05 0.000 ng/dscm@7%O2 7.10E-05 4.84E-05 5.85E-05 0.000 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000026 0.0000000031 0.0000000035 0.000 lb/mmBtuO2 1.81E-13 2.23E-13 2.49E-13 0.000 ng/dscm 2.54E-04 3.11E-04 3.46E-04 0.000 ng/dscm@7%O2 2.10E-04 2.59E-04 2.88E-04 0.000 

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.000000234 0.000000279 0.000000264 0.000 lb/mmBtuO2 1.63E-11 2.01E-11 1.88E-11 0.000 ng/dscm 2.28E-02 2.80E-02 2.61E-02 0.026 ng/dscm@7%O2 1.89E-02 2.33E-02 2.17E-02 0.021 

### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000118 0.0000000151 0.0000000142 0.000 lb/mmBtuO2 8.21E-13 1.09E-12 1.01E-12 0.000 ng/dscm 1.15E-03 1.52E-03 1.40E-03 0.001 ng/dscm@7%O2 9.51E-04 1.26E-03 1.17E-03 0.001 

### Compound: OCDD Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3


### Monday, February 14, 2011 Page 13 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 Mass_mg 0.0000000055 0.0000000239 0.000000018 0.000 lb/mmBtuO2 3.83E-13 1.72E-12 1.28E-12 0.000 ng/dscm 5.37E-04 2.40E-03 1.78E-03 0.002 ng/dscm@7%O2 4.44E-04 2.00E-03 1.48E-03 0.001 

### Compound: OCDF Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000034 0.0000000295 0.0000000065 0.000 lb/mmBtuO2 2.37E-13 2.12E-12 4.62E-13 0.000 ng/dscm 3.32E-04 2.96E-03 6.43E-04 0.001 ng/dscm@7%O2 2.75E-04 2.46E-03 5.36E-04 0.001 

### Compound: Total Dioxins Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.0000000212 0.00000004034 0.00000003821 0.000 lb/mmBtuO2 1.48E-12 2.90E-12 2.72E-12 0.000 ng/dscm 2.07E-03 4.05E-03 3.78E-03 0.003 ng/dscm@7%O2 1.71E-03 3.37E-03 3.15E-03 0.003 

### Compound: Total Furans Average RunNumber PPE3-23-1 PPE3-23-2 PPE3-23-3 Mass_mg 0.00000001716 0.0000000539 0.0000000289 0.000 lb/mmBtuO2 1.19E-12 3.88E-12 2.05E-12 0.000 ng/dscm 1.67E-03 5.41E-03 2.86E-03 0.003 ng/dscm@7%O2 1.38E-03 4.50E-03 2.38E-03 0.003



### Location: PPE3 - Gases - Method 10 Compound: Carbon Monoxide Average Run 3-CO-1 3-CO-2 3-CO-3 lb/mmBtuO2 3.53E-03 7.56E-03 6.84E-03 0.006 ppm 4.27E+00 9.08E+00 8.20E+00 7.183 ppm@7%O2 3.52E+00 7.52E+00 6.81E+00 5.950



### Location: PPE3 - Gases - Method 25A Compound: Total organic compounds (TOC) as Average Run 3-THC-1 3-THC-2 3-THC-3 lb/mmBtuO2 8.40E-05 1.28E-04 3.99E-05 0.000 ppm 6.45E-02 9.79E-02 3.04E-02 0.064 ppm@7%O2 5.31E-02 8.11E-02 2.52E-02 0.053



### Location: PPE3 - Gases - Method 6C Compound: Sulfur Dioxide Average Run 3-SO2-1 3-SO2-2 3-SO2-3 lb/mmBtuO2 1.05E+00 1.03E+00 1.04E+00 1.040 ppm 5.53E+02 5.40E+02 5.47E+02 546.667 ppm@7%O2 4.55E+02 4.47E+02 4.54E+02 452.000



### Monday, February 14, 2011 Page 14 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010

Location: PPE3 - Gases - Method 7E 

### Compound: Nitrogen oxides (NOx) Average Run 3-NOx-1 3-NOx-2 3-NOx-3 lb/mmBtuO2 6.39E-01 6.45E-01 6.53E-01 0.646 ppm 4.70E+02 4.72E+02 4.77E+02 473.000 ppm@7%O2 3.87E+02 3.91E+02 3.96E+02 391.333



### Location: PPE3 - Metals - Method 29 

### Compound: Antimony Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.00311 0.00169 0.00228 0.002 Elb/hr 1.72E-03 9.28E-04 1.26E-03 0.001 lb/mmBtuO2 4.40E-07 2.39E-07 3.27E-07 0.000 mg/dscm 6.17E-04 3.33E-04 4.55E-04 0.000 mg/dscm@7%O2 5.10E-04 2.77E-04 3.79E-04 0.000 

### Compound: Arsenic Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.00116 0.00115 0.00115 0.001 Elb/hr 6.42E-04 6.31E-04 6.33E-04 0.001 lb/mmBtuO2 1.64E-07 1.63E-07 1.65E-07 0.000 mg/dscm 2.30E-04 2.27E-04 2.29E-04 0.000 mg/dscm@7%O2 1.90E-04 1.89E-04 1.91E-04 0.000 

### Compound: Beryllium Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.0002 0.0002 0.0002 0.000 Elb/hr 1.11E-04 1.10E-04 1.10E-04 0.000 lb/mmBtuO2 2.83E-08 2.83E-08 2.86E-08 0.000 mg/dscm 3.97E-05 3.95E-05 3.99E-05 0.000 mg/dscm@7%O2 3.28E-05 3.28E-05 3.32E-05 0.000 

### Compound: Cadmium Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.0001 0.0001 0.0001 0.000 Elb/hr 5.54E-05 5.49E-05 5.51E-05 0.000 lb/mmBtuO2 1.41E-08 1.41E-08 1.43E-08 0.000 mg/dscm 1.98E-05 1.97E-05 1.99E-05 0.000 mg/dscm@7%O2 1.64E-05 1.64E-05 1.66E-05 0.000 

### Compound: Chromium Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.00621 0.00791 0.00425 0.006 Elb/hr 3.44E-03 4.34E-03 2.34E-03 0.003 lb/mmBtuO2 8.79E-07 1.12E-06 6.09E-07 0.000 mg/dscm 1.23E-03 1.56E-03 8.47E-04 0.001



### Monday, February 14, 2011 Page 15 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 mg/dscm@7%O2 1.02E-03 1.30E-03 7.05E-04 0.001 

### Compound: Cobalt Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.00109 0.00488 0.00122 0.002 Elb/hr 6.04E-04 2.68E-03 6.72E-04 0.001 lb/mmBtuO2 1.54E-07 6.90E-07 1.75E-07 0.000 mg/dscm 2.16E-04 9.63E-04 2.43E-04 0.000 mg/dscm@7%O2 1.79E-04 8.01E-04 2.02E-04 0.000 

### Compound: Filterable Particulate Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 10.6 7.1 8.1 8.600 Elb/hr 5.87E+00 3.90E+00 4.46E+00 4.743 lb/mmBtuO2 1.50E-03 1.00E-03 1.16E-03 0.001 mg/dscm 2.10E+00 1.40E+00 1.61E+00 1.703 mg/dscm@7%O2 1.74E+00 1.16E+00 1.34E+00 1.413 

### Compound: Lead Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.00232 0.00169 0.000973 0.002 Elb/hr 1.28E-03 9.28E-04 5.36E-04 0.001 lb/mmBtuO2 3.28E-07 2.39E-07 1.39E-07 0.000 mg/dscm 4.60E-04 3.33E-04 1.94E-04 0.000 mg/dscm@7%O2 3.81E-04 2.77E-04 1.62E-04 0.000 

### Compound: Manganese Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.00523 0.00635 0.00602 0.006 Elb/hr 2.90E-03 3.49E-03 3.31E-03 0.003 lb/mmBtuO2 7.40E-07 8.98E-07 8.62E-07 0.000 mg/dscm 1.04E-03 1.25E-03 1.20E-03 0.001 mg/dscm@7%O2 8.60E-04 1.04E-03 9.99E-04 0.001 

### Compound: Nickel Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.0303 0.0334 0.0389 0.034 Elb/hr 1.68E-02 1.83E-02 2.14E-02 0.019 lb/mmBtuO2 4.29E-06 4.72E-06 5.57E-06 0.000 mg/dscm 6.01E-03 6.59E-03 7.76E-03 0.007 mg/dscm@7%O2 4.97E-03 5.48E-03 6.46E-03 0.006 

### Compound: Selenium Average RunNumber PPE3-29-1 PPE3-29-2 PPE3-29-3 Mass_mg 0.023 0.0231 0.0225 0.023 Elb/hr 1.27E-02 1.27E-02 1.24E-02 0.013 lb/mmBtuO2 3.25E-06 3.27E-06 3.22E-06 0.000 mg/dscm 4.56E-03 4.56E-03 4.49E-03 0.005



### Monday, February 14, 2011 Page 16 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010

Process Run Data mg/dscm@7%O2 3.77E-03 3.79E-03 3.74E-03 0.004



### Location: PPE3 - PM - OTM - 27/28 Compound: Filterable Particulate Average RunNumber PPE3-27/28-1 PPE3-27/28-2 PPE3-27/28-3 Mass_mg 17.55 15.925 14.375 15.950 lb/mmBtuO2 3.29E-03 3.73E-03 2.88E-03 0.003 

### Compound: Filterable PM2.5 Average RunNumber PPE3-27/28-1 PPE3-27/28-2 PPE3-27/28-3 Mass_mg 13.375 13.05 11.9 12.775 lb/mmBtuO2 2.51E-03 3.06E-03 2.38E-03 0.003 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber PPE3-27/28-1 PPE3-27/28-2 PPE3-27/28-3 Mass_mg 5.023 15.571 4.259 8.284 lb/mmBtuO2 9.42E-04 3.65E-03 8.52E-04 0.002 

### Compound: Organic Condensible Particulate Average RunNumber PPE3-27/28-1 PPE3-27/28-2 PPE3-27/28-3 Mass_mg 12.237 21.8 2.112 12.050 lb/mmBtuO2 2.30E-03 5.11E-03 4.22E-04 0.003 

### Compound: Total Particulate Average RunNumber PPE3-27/28-1 PPE3-27/28-2 PPE3-27/28-3 Mass_mg 34.81 53.296 20.747 36.284 lb/mmBtuO2 6.53E-03 1.25E-02 4.15E-03 0.008 

### Compound: Total PM2.5 Average RunNumber PPE3-27/28-1 PPE3-27/28-2 PPE3-27/28-3 Mass_mg 30.635 50.421 18.272 33.109 lb/mmBtuO2 5.75E-03 1.18E-02 3.65E-03 0.007



### Monday, February 14, 2011 Page 17 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 Process Run Data



### Run Name Value UOM Comments Target Value 1 Residual Oil (No. 6) Burned 27485 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 3/9/2010; Start - 08:49; End - 10:48 0



### 10 Residual Oil (No. 6) Burned 27321 gal/hr Method 027/028; Run PM-1; Date - 3/9/2010; Start - 08:51; End - 14:44 0

11 Residual Oil (No. 6) Burned 26955 gal/hr Method 027/028; Run PM-2; Date - 3/10/2010; Start - 10:45; End - 15:57 0

12 Residual Oil (No. 6) Burned 26999 gal/hr Method 027/028; Run PM-3; Date - 3/11/2010; Start - 08:46; End - 14:12 0

2 Residual Oil (No. 6) Burned 27251 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 3/9/2010; Start - 11:38; End - 13:37 0

3 Residual Oil (No. 6) Burned 27251 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 3/9/2010; Start - 14:03; End - 16:02 0



### 4 Residual Oil (No. 6) Burned 27262 gal/hr Method 23; Run D/F-1; Date - 3/9/2010; Start - 09:28; End - 17:19 0

5 Residual Oil (No. 6) Burned 26955 gal/hr Method 23; Run D/F-2; Date - 3/10/2010; Start - 08:40; End - 16:07 0

6 Residual Oil (No. 6) Burned 26984 gal/hr Method 23; Run D/F-3; Date - 3/11/2010; Start - 12:14; End - 20:40 0

7 Residual Oil (No. 6) Burned 27247 gal/hr Method 29; Run M-1; Date - 3/9/2010; Start - 16:44; End - 20:18 0



### Monday, February 14, 2011 Page 18 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 8 Residual Oil (No. 6) Burned 26940 gal/hr Method 29; Run M-2; Date - 3/10/2010; Start - 17:29; End - 21:45 0

9 Residual Oil (No. 6) Burned 27042 gal/hr Method 29; Run M-3; Date - 3/11/2010; Start - 15:37; End - 20:18 0

1 Average Heat Input 3486 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 3/9/2010; Start - 08:49; End - 10:48 0



### 10 Average Heat Input 3467 MMBtu/hr Method 027/028; Run PM-1; Date - 3/9/2010; Start - 08:51; End - 14:44 0

11 Average Heat Input 3420 MMBtu/hr Method 027/028; Run PM-2; Date - 3/10/2010; Start - 10:45; End - 15:57 0

12 Average Heat Input 3425 MMBtu/hr Method 027/028; Run PM-3; Date - 3/11/2010; Start - 08:46; End - 14:12 0

2 Average Heat Input 3458 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 3/9/2010; Start - 11:38; End - 13:37 0

3 Average Heat Input 3457 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 3/9/2010; Start - 14:03; End - 16:02 0



### 4 Average Heat Input 3459 MMBtu/hr Method 23; Run D/F-1; Date - 3/9/2010; Start - 09:28; End - 17:19 0

5 Average Heat Input 3420 MMBtu/hr Method 23; Run D/F-2; Date - 3/10/2010; Start - 08:40; End - 16:07 0

6 Average Heat Input 3424 MMBtu/hr Method 23; Run D/F-3; Date - 3/11/2010; Start - 12:14; End - 20:40 0



### Monday, February 14, 2011 Page 19 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
7 Average Heat Input 3457 MMBtu/hr Method 29; Run M-1; Date - 3/9/2010; Start - 16:44; End - 20:18 0

8 Average Heat Input 3418 MMBtu/hr Method 29; Run M-2; Date - 3/10/2010; Start - 17:29; End - 21:45 0

9 Average Heat Input 3431 MMBtu/hr Method 29; Run M-3; Date - 3/11/2010; Start - 15:37; End - 20:18 0

1 Steam Output 2676 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 3/9/2010; Start - 08:49; End - 10:48 0



### 10 Steam Output 2661 1000 lb Method 027/028; Run PM-1; Date - 3/9/2010; Start - 08:51; End - 14:44 0

11 Steam Output 2650 1000 lb Method 027/028; Run PM-2; Date - 3/10/2010; Start - 10:45; End - 15:57 0

12 Steam Output 2663 1000 lb Method 027/028; Run PM-3; Date - 3/11/2010; Start - 08:46; End - 14:12 0

2 Steam Output 2654 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 3/9/2010; Start - 11:38; End - 13:37 0

3 Steam Output 2653 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 3/9/2010; Start - 14:03; End - 16:02 0

4 Steam Output 2655 1000 lb Method 23; Run D/F-1; Date - 3/9/2010; Start - 09:28; End - 17:19 0

5 Steam Output 2651 1000 lb Method 23; Run D/F-2; Date - 3/10/2010; Start - 08:40; End - 16:07 0



### Monday, February 14, 2011 Page 20 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
6 Steam Output 2662 1000 lb Method 23; Run D/F-3; Date - 3/11/2010; Start - 12:14; End - 20:40 0

7 Steam Output 2648 1000 lb Method 29; Run M-1; Date - 3/9/2010; Start - 16:44; End - 20:18 0

8 Steam Output 2645 1000 lb Method 29; Run M-2; Date - 3/10/2010; Start - 17:29; End - 21:45 0

9 Steam Output 2667 1000 lb Method 29; Run M-3; Date - 3/11/2010; Start - 15:37; End - 20:18 0

1 Unit Gross Electrical Output 376 MWg Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 3/9/2010; Start - 08:49; End - 10:48 0



### 10 Unit Gross Electrical Output 375 MWg Method 027/028; Run PM-1; Date - 3/9/2010; Start - 08:51; End - 14:44 0

11 Unit Gross Electrical Output 375 MWg Method 027/028; Run PM-2; Date - 3/10/2010; Start - 10:45; End - 15:57 0

12 Unit Gross Electrical Output 376 MWg Method 027/028; Run PM-3; Date - 3/11/2010; Start - 08:46; End - 14:12 0

2 Unit Gross Electrical Output 375 MWg Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 3/9/2010; Start - 11:38; End - 13:37 0

3 Unit Gross Electrical Output 375 MWg Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 3/9/2010; Start - 14:03; End - 16:02 0

4 Unit Gross Electrical Output 375 MWg Method 23; Run D/F-1; Date - 3/9/2010; Start - 09:28; End - 17:19 0



### Monday, February 14, 2011 Page 21 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 5 Unit Gross Electrical Output 375 MWg Method 23; Run D/F-2; Date - 3/10/2010; Start - 08:40; End - 16:07 0

6 Unit Gross Electrical Output 376 MWg Method 23; Run D/F-3; Date - 3/11/2010; Start - 12:14; End - 20:40 0

7 Unit Gross Electrical Output 375 MWg Method 29; Run M-1; Date - 3/9/2010; Start - 16:44; End - 20:18 0

8 Unit Gross Electrical Output 375 MWg Method 29; Run M-2; Date - 3/10/2010; Start - 17:29; End - 21:45 0

9 Unit Gross Electrical Output 377 MWg Method 29; Run M-3; Date - 3/11/2010; Start - 15:37; End - 20:18 0

1 Unit Net Electric Generation 365 MWn Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 3/9/2010; Start - 08:49; End - 10:48 0



### 10 Unit Net Electric Generation 365 MWn Method 027/028; Run PM-1; Date - 3/9/2010; Start - 08:51; End - 14:44 0

11 Unit Net Electric Generation 364 MWn Method 027/028; Run PM-2; Date - 3/10/2010; Start - 10:45; End - 15:57 0

12 Unit Net Electric Generation 365 MWn Method 027/028; Run PM-3; Date - 3/11/2010; Start - 08:46; End - 14:12 0

2 Unit Net Electric Generation 364 MWn Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 3/9/2010; Start - 11:38; End - 13:37 0

3 Unit Net Electric Generation 364 MWn Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 3/9/2010; Start - 14:03; End - 16:02 0



### Monday, February 14, 2011 Page 22 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010

APCD Run Data

Process Lab Run Data 4 Unit Net Electric Generation 364 MWn Method 23; Run D/F-1; Date - 3/9/2010; Start - 09:28; End - 17:19 0

5 Unit Net Electric Generation 364 MWn Method 23; Run D/F-2; Date - 3/10/2010; Start - 08:40; End - 16:07 0

6 Unit Net Electric Generation 365 MWn Method 23; Run D/F-3; Date - 3/11/2010; Start - 12:14; End - 20:40 0

7 Unit Net Electric Generation 364 MWn Method 29; Run M-1; Date - 3/9/2010; Start - 16:44; End - 20:18 0

8 Unit Net Electric Generation 364 MWn Method 29; Run M-2; Date - 3/10/2010; Start - 17:29; End - 21:45 0

9 Unit Net Electric Generation 366 MWn Method 29; Run M-3; Date - 3/11/2010; Start - 15:37; End - 20:18 0



### Run Name Value UOM Comments Target Value 1 LOW NOX BURNERS 454 NOx Emissions 0


### 2 LOW NOX BURNERS 453 NOx Emissions 0
3 LOW NOX BURNERS 449 NOx Emissions 0
1 ELECTROSTATIC PRECIPITATORS 1.6 Opacity 0


### 2 ELECTROSTATIC PRECIPITATORS 1.5 Opacity 0
3 ELECTROSTATIC PRECIPITATORS 1.6 Opacity 0

Run Name Value UOM Comments 

### 1 Fuel Higher Heating Value 18000 Btu/lb 1 Fuel Moisture 1.5 % 1 Fuel Mercury Content 0.002 mg/kg 1 Fuel Chlorine Content 244 mg/kg 

### 1 Fuel Fluorine Content 76 mg/kg 1 Fuel Antimony Content 1.4 mg/kg 1 Fuel Arsenic Content 0.075 mg/kg 

### 1 Fuel Beryllium Content 0.006 mg/kg
Monday, February 14, 2011 Page 23 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 1 Fuel Cadmium Content 0.008 mg/kg 

### 1 Fuel Chromium Content 0.14 mg/kg 1 Fuel Cobalt Content 0.58 mg/kg 1 Fuel Lead Content 0.21 mg/kg 1 Fuel Manganese Content 1.2 mg/kg 

### 1 Fuel Nickel Content 21 mg/kg 1 Fuel Selenium Content 0.017 mg/kg 1 Fuel Sulfur Content 9630 mg/kg 

### 1 Fuel Proximate Analysis (Carbon) 87.67 % 1 Fuel Proximate Analysis (Hydrogen) 9.73 % 1 Fuel Proximate Analysis (Nitrogen) 0.5 % 1 Fuel Proximate Analysis (Oxygen) 0.58 % 

### 1 Fuel Proximate Analysis (Sulfur) 1.06 % 2 Fuel Higher Heating Value 18100 Btu/lb 2 Fuel Moisture 1.35 % 

### 2 Fuel Mercury Content 0.002 mg/kg 2 Fuel Chlorine Content 110 mg/kg 2 Fuel Fluorine Content 75 mg/kg 2 Fuel Antimony Content 1.4 mg/kg 

### 2 Fuel Arsenic Content 0.09 mg/kg 2 Fuel Beryllium Content 0.008 mg/kg 2 Fuel Cadmium Content 0.008 mg/kg 

### 2 Fuel Chromium Content 0.15 mg/kg 2 Fuel Cobalt Content 0.58 mg/kg 2 Fuel Lead Content 0.21 mg/kg 2 Fuel Manganese Content 1.2 mg/kg 

### 2 Fuel Nickel Content 21.1 mg/kg 2 Fuel Selenium Content 0.022 mg/kg 2 Fuel Sulfur Content 9290 mg/kg 

### 2 Fuel Proximate Analysis (Carbon) 88.15 % 2 Fuel Proximate Analysis (Hydrogen) 9.9 % 2 Fuel Proximate Analysis (Nitrogen) 0.5 % 2 Fuel Proximate Analysis (Oxygen) 0.5 % 

### 2 Fuel Proximate Analysis (Sulfur) 1.07 % 3 Fuel Higher Heating Value 18200 Btu/lb 3 Fuel Moisture 0.98 % 

### 3 Fuel Mercury Content 0.002 mg/kg 3 Fuel Chlorine Content 133 mg/kg 3 Fuel Fluorine Content 78 mg/kg 3 Fuel Antimony Content 1.4 mg/kg 

### 3 Fuel Arsenic Content 0.078 mg/kg 3 Fuel Beryllium Content 0.008 mg/kg 3 Fuel Cadmium Content 0.007 mg/kg



### Monday, February 14, 2011 Page 24 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 3 Fuel Chromium Content 0.14 mg/kg 

### 3 Fuel Cobalt Content 0.57 mg/kg 3 Fuel Lead Content 0.21 mg/kg 3 Fuel Manganese Content 1.2 mg/kg 3 Fuel Nickel Content 20.7 mg/kg 

### 3 Fuel Selenium Content 0.022 mg/kg 3 Fuel Sulfur Content 9610 mg/kg 3 Fuel Proximate Analysis (Carbon) 87.25 % 

### 3 Fuel Proximate Analysis (Hydrogen) 9.99 % 3 Fuel Proximate Analysis (Nitrogen) 0.5 % 3 Fuel Proximate Analysis (Oxygen) 0.67 % 3 Fuel Proximate Analysis (Sulfur) 1.06 %



### Monday, February 14, 2011 Page 25 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010 Sampling / Stack Data Results Detail



### Location PPE3 - D/F - Method 23 Average Run Number PPE3-23-1 PPE3-23-2 PPE3-23-3 Test Date 3/9/2010 3/10/2010 3/11/2010 Run Start Time 9:28:00 AM 8:40:00 AM 12:14:00 PM Run Finish Time 5:28:00 PM 4:40:00 PM 8:14:00 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 0.979 0.979 0.979 0.979 Barometric Pressure, inches of Mercury 29.74 29.68 29.5 29.640 Average Orifice Meter Differential, inches H2O 1.92 1.87 1.90 1.897 Dry Gas Meter Volume Sampled, cubic feet 377.220 365.800 373.610 372.210 Average Dry Gas Meter Temperature, °F 77.83 75.77 75.92 76.507 Dry Gas Meter Volume Sampled, dscf 362.078 351.716 356.983 356.926 Total Moisture Liquid collected, g 720.7 771.8 823.1 771.867 Volume of Water Vapor, standard cubic feet 33.92 36.33 38.74 36.330 Moisture Content of Stack Gas, % 8.57 9.36 9.79 9.240 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9143 0.9064 0.9021 0.908 Carbon Dioxide, % 13.96 13.95 13.88 13.930 Oxygen, % 4.1 4.18 4.21 4.163 Carbon Monoxide & Nitrogen, % 81.94 81.87 81.91 81.907 Fuel Factor 1.20 1.20 1.20 Dry Molecular Weight, lb/lb-Mole 30.40 30.40 30.39 30.397 Wet Molecular weight, lb/lb-Mole 29.34 29.24 29.18 29.253 Flue Gas Static Pressure, inches of H2O 1 1 1 1.000 Absolute Flue Gas Pressure, inches of Mercury 29.81 29.75 29.57 29.710 Average Stack Gas Temperature, °F 322.21 324.25 324.13 323.530 Average Velocity Head, inches of H2O 0.7928921801 24829 0.790137554

06079 0.798927431

392487 0.794
Average Stack Gas Velocity, feet/second 60.47 60.61 61.19 60.757 Stack Cross-Sectional Area, square feet 343.617 343.617 343.617 343.617 Dry Volumetric Flow Rate, dry scfm 766,594.2 758,219.3 757,350.0 760,721.167 Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,246,711.2 1,249,597.6 1,261,555.5 1,252,621.4 33 Percent Isokinetic of Sampling Rate, % 99.2 97.4 99.0 98.533 Percent Excess Air, % 23.4 24.0 24.2 23.867 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Round Duct Diameter, inches 251 251 251 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

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - Gases - Method 10 Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



### Monday, February 14, 2011 Page 27 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - Gases - Method 25A Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



### Monday, February 14, 2011 Page 28 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - 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 29 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - 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 30 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - 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 31 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - 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 32 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - Metals - Method 29 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 14, 2011 Page 33 of 34

### Port Everglades Energy Center, Unit #3, Information Collection Request

6/10/2010
Location PPE3 - PM - OTM - 27/28 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Monday, February 14, 2011 Page 34 of 34