### Name: Paul Plotkin

Title: General Manager Company: Florida Power & Light Manatee Plant Sign Date: 7/14/2010 Name: Thomas K. Graham Title: Director of Operations Company: Air Hygiene International, Inc. Sign Date: 7/10/2010 Permitted Facility Representative / Date Testing Company Representative / Date



## Manatee Energy Center, Unit #2, Information Collection Request Final Test Report for

/ / Based on information and belief formed after reasonable inquiry, I certify that the statements and information in this test report are true, accurate, and complete. I have reviewed all testing details and results in this test report and hereby certify that the test report is authentic and accurate.

Monday, February 14, 2011 Page 1 of 34

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 Facility Information: Manatee Energy Center
19050 State Road 62

Parrish FL 34219 Contact: Augie De La Vega Phone: (305) 242-3896 Fax: Email: augie.de.la.vega@fpl.com Testing Company: Air Hygiene International, Inc. 5634 S. 122nd East Ave, Suite F

Tulsa OK 74146 Contact: Thomas Graham Phone: (918) 307-8865 Fax: (918) 307-9131 Email: tom@airhygiene.com

Air Permit Number: 0810010-014-AV Permitted Source ID/Name: Foster Wheeler, Wall Fired Boiler PMT2 Permitted Maximum Process Rate: 863.3 MW Max. Normal Operation Process Rate: 800 MW Target Process Test Rate 800 MW

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: Florida Power and Light Company (FPL) operates two oil fired electric utility steam generating units of Foster Wheeler design, designated as Units PMT1 and PMT2. The facility is located at 19050 State Road 62 in Parrish, Florida. Unit PMT1 and PMT2 are of identical design and consists of two wall fired boilers and ancillary equipment designed to generate 863.3 megawatts (MW) of electricity each with rated heat inputs of 8,650 million British thermal units per hour (MMBtu/hr) based on high heating value (HHV). Fuel oil consumption is rated at 600,000 pounds per hour. Unit PMT1 and PMT2 utilize low nitrogen oxide (NOx) burner technology to control NOx emissions and cyclone separators to control particulate matter (PM) emissions. Emission testing will be conducted from platforms on the independent stacks of each unit. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 0810010 FRS #: 110000496776

SCC / Description 10100401 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: Normal Firing

The following state and federal regulations that apply to the proposed testing:

Location Round

Duct Diam. Distance from upstream dist. Distance from

downstream dist. Number of

Traverse Ports Equiv. Diam Min.Travers Points Rect. Duct Length /Width PMT2 - D/F 357.4 4524 876 4 0 24 0 0 PMT2 - Gases 357.4 4524 876 4 0 1 0 0 PMT2 - Metals 357.4 4524 876 4 0 24 0 0 PMT2 - PM 357.4 4524 876 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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location % H2O Method 1 - 4 3 480 24 PMT2 - D/F 2,3,7,8-TCDD Method 23 3 480 24 PMT2 - D/F 1,2,3,7,8-PeCDD Method 23 3 480 24 PMT2 - D/F 1,2,3,4,7,8-HxCDD Method 23 3 480 24 PMT2 - D/F 1,2,3,6,7,8-HxCDD Method 23 3 480 24 PMT2 - D/F 1,2,3,7,8,9-HxCDD Method 23 3 480 24 PMT2 - D/F 1,2,3,4,6,7,8-HpCDD Method 23 3 480 24 PMT2 - D/F OCDD Method 23 3 480 24 PMT2 - D/F 2,3,7,8-TCDF Method 23 3 480 24 PMT2 - D/F 1,2,3,7,8-PeCDF Method 23 3 480 24 PMT2 - D/F 2,3,4,7,8-PeCDF Method 23 3 480 24 PMT2 - D/F 1,2,3,4,7,8-HxCDF Method 23 3 480 24 PMT2 - D/F 1,2,3,6,7,8-HxCDF Method 23 3 480 24 PMT2 - D/F 2,3,4,6,7,8-HxCDF Method 23 3 480 24 PMT2 - D/F 1,2,3,7,8,9-HxCDF Method 23 3 480 24 PMT2 - D/F 1,2,3,4,6,7,8-HpCDF Method 23 3 480 24 PMT2 - D/F 1,2,3,4,7,8,9-HpCDF Method 23 3 480 24 PMT2 - D/F OCDF Method 23 3 480 24 PMT2 - D/F Total Dioxins Method 23 3 480 24 PMT2 - D/F Total Furans Method 23 3 480 24 PMT2 - D/F 3,3',4,4'-TCB (PCB77) Method 23 3 480 24 PMT2 - D/F 3,4,4',5-TCB (PCB81) Method 23 3 480 24 PMT2 - D/F 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 24 PMT2 - D/F 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 24 PMT2 - D/F 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 24 PMT2 - D/F 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 24 PMT2 - D/F 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 24 PMT2 - D/F 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) Method 23 3 480 24 PMT2 - D/F

2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 24 PMT2 - D/F 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 24 PMT2 - D/F 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 24 PMT2 - D/F

O2 Method 3A O2 3 480 24 PMT2 - D/F Co2 Method 3A CO2 3 480 24 PMT2 - D/F % H2O Method 1 - 4 3 120 1 Determined after initial stratification test PMT2 - Gases

Carbon Monoxide Method 10 3 120 1 Determined after initial stratification test PMT2 - Gases
Total organic compounds

(TOC) as Propane Method 25A 3 120 1 Determined after initial stratification test PMT2 - Gases

O2 Method 3A O2 3 120 1 Determined after initial stratification test PMT2 - Gases

Co2 Method 3A CO2 3 120 1 Determined after initial stratification test PMT2 - Gases

Sulfur Dioxide Method 6C 3 120 1 Determined after initial stratification test PMT2 - Gases
Nitrogen oxides (NOx) Method 7E 3 120 1 Determined after initial stratification test PMT2 - Gases

% H2O Method 1 - 4 3 240 24 PMT2 - Metals Selenium Method 29 3 240 24 PMT2 - Metals Manganese Method 29 3 240 24 PMT2 - Metals


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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010

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

Lead Method 29 3 240 24 PMT2 - Metals Filterable Particulate Method 29 3 240 24 PMT2 - Metals Cobalt Method 29 3 240 24 PMT2 - Metals Cadmium Method 29 3 240 24 PMT2 - Metals Chromium Method 29 3 240 24 PMT2 - Metals Nickel Method 29 3 240 24 PMT2 - Metals Co2 Method 3A CO2 3 240 24 PMT2 - Metals O2 Method 3A O2 3 240 24 PMT2 - Metals % H2O Method 1 - 4 3 120 12 Run times vary based on method calculations PMT2 - PM

Filterable Particulate OTM - 27/28 3 120 12 Run times vary based on method calculations PMT2 - PM

Filterable PM2.5 OTM - 27/28 3 120 12 Run times vary based on method calculations PMT2 - PM
Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 120 12 Run times vary based on method calculations PMT2 - PM
Organic Condensible

Particulate OTM - 27/28 3 120 12 Run times vary based on method calculations PMT2 - PM

Total PM2.5 OTM - 27/28 3 120 12 Run times vary based on method calculations PMT2 - PM

Total Particulate OTM - 27/28 3 120 12 Run times vary based on method calculations PMT2 - PM

O2 Method 3A O2 3 120 12 Run times vary based on method calculations PMT2 - PM

Co2 Method 3A CO2 3 120 12 Run times vary based on method calculations PMT2 - PM



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 Sampling / Stack Data Results Summary



### Location PMT2 - D/F - Method 23 Average Run Number PMT2-23-1 PMT2-23-2 PMT2-23-3
Test Date 5/11/2010 5/12/2010 5/13/2010 Run Start Time 12:58:00 PM 12:00:00 PM 8:06:00 AM

Run Finish Time 8:58:00 PM 8:00:00 PM 4:06:00 PM Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 365.205 374.736 379.425 373.122 Moisture Content of Stack Gas, % 9.20 9.09 8.71 9.000 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 12.59 12.9 12.7 12.730 Oxygen, % 4.99 5.04 5.11 5.047 Average Stack Gas Temperature, °F 320.08 321.71 321.63 321.140 Dry Volumetric Flow Rate, dry scfm 1,584,973.2 1,601,200.3 1,624,125.4 1,603,432.96 7 Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,570,349.6 2,593,758.3 2,619,674.9 2,594,594.26 7 Percent Isokinetic of Sampling Rate, % 98.1 99.6 99.5 99.067 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Location PMT2 - Gases - Method 10 Average Run Number
Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Gases - Method 25A Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Location PMT2 - Gases - Method 3A CO2 Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc PMT2 - Gases PMT2 -

Gases PMT2 -

Gases



### Monday, February 14, 2011 Page 6 of 34

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Gases - Method 3A O2 Average Run Number 2-O2-1 2-O2-2 2-O2-3
Test Date 5/11/2010 5/11/2010 5/11/2010 Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM
Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM Carbon Dioxide, % 12.59 12.9 12.7 12.730 Oxygen, % 4.99 5.04 5.11 5.047 Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.00 0 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 9.22 9.22 9.22 9.220 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Location PMT2 - Gases - Method 6C Average Run Number 2-SO2-1 2-SO2-2 2-SO2-3
Test Date 5/11/2010 5/11/2010 5/11/2010 Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM Carbon Dioxide, % 12.59 12.9 12.7 12.730 Oxygen, % 4.99 5.04 5.11 5.047 Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.00 0 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 9.22 9.22 9.22 9.220 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Monday, February 14, 2011 Page 7 of 34

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Gases - Method 7E Average Run Number 2-NOx-1 2-NOx-2 2-NOx-3
Test Date 5/11/2010 5/11/2010 5/11/2010 Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM
Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM Carbon Dioxide, % 12.59 12.9 12.7 12.730 Oxygen, % 4.99 5.04 5.11 5.047 Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.00 0 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 9.22 9.22 9.22 9.220 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Location PMT2 - Metals - Method 29 Average Run Number
Test Date Run Start Time Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - PM - OTM - 27/28 Average Run Number
Test Date Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 Emissions Summary



### Location: PMT2 - D/F - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000077 0.0000000037 0.0000000089 0.000 lb/mmBtuO2 5.61E-13 2.64E-13 6.29E-13 0.000 ng/dscm 7.45E-04 3.49E-04 8.28E-04 0.001 ng/dscm@7%O2 6.51E-04 3.06E-04 7.29E-04 0.001 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000042 0.000000003 0.0000000083 0.000 lb/mmBtuO2 3.06E-13 2.14E-13 5.87E-13 0.000 ng/dscm 4.06E-04 2.83E-04 7.73E-04 0.000 ng/dscm@7%O2 3.55E-04 2.48E-04 6.80E-04 0.000 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000058 0.0000000041 0.000000006 0.000 lb/mmBtuO2 4.23E-13 2.92E-13 4.24E-13 0.000 ng/dscm 5.61E-04 3.86E-04 5.59E-04 0.001 ng/dscm@7%O2 4.90E-04 3.38E-04 4.92E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000069 0.0000000032 0.0000000049 0.000 lb/mmBtuO2 5.03E-13 2.28E-13 3.46E-13 0.000 ng/dscm 6.67E-04 3.02E-04 4.56E-04 0.000 ng/dscm@7%O2 5.83E-04 2.65E-04 4.01E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDF Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000047 0.0000000032 0.0000000029 0.000 lb/mmBtuO2 3.43E-13 2.28E-13 2.05E-13 0.000 ng/dscm 4.55E-04 3.02E-04 2.70E-04 0.000 ng/dscm@7%O2 3.98E-04 2.65E-04 2.38E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000057 0.0000000027 0.0000000041 0.000 lb/mmBtuO2 4.15E-13 1.92E-13 2.90E-13 0.000 ng/dscm 5.51E-04 2.54E-04 3.82E-04 0.000 ng/dscm@7%O2 4.81E-04 2.23E-04 3.36E-04 0.000 

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



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000042 0.0000000028 0.0000000026 0.000 lb/mmBtuO2 3.06E-13 1.99E-13 1.84E-13 0.000 ng/dscm 4.06E-04 2.64E-04 2.42E-04 0.000 ng/dscm@7%O2 3.55E-04 2.31E-04 2.13E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.000000006 0.0000000028 0.0000000043 0.000 lb/mmBtuO2 4.37E-13 1.99E-13 3.04E-13 0.000 ng/dscm 5.80E-04 2.64E-04 4.00E-04 0.000 ng/dscm@7%O2 5.07E-04 2.31E-04 3.52E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000053 0.0000000036 0.0000000033 0.000 lb/mmBtuO2 3.86E-13 2.56E-13 2.33E-13 0.000 ng/dscm 5.13E-04 3.39E-04 3.07E-04 0.000 ng/dscm@7%O2 4.48E-04 2.97E-04 2.70E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000054 0.0000000043 0.0000000052 0.000 lb/mmBtuO2 3.94E-13 3.06E-13 3.68E-13 0.000 ng/dscm 5.22E-04 4.05E-04 4.84E-04 0.000 ng/dscm@7%O2 4.56E-04 3.55E-04 4.26E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000053 0.000000008 0.0000000045 0.000 lb/mmBtuO2 3.86E-13 5.70E-13 3.18E-13 0.000 ng/dscm 5.13E-04 7.54E-04 4.19E-04 0.001 ng/dscm@7%O2 4.48E-04 6.61E-04 3.69E-04 0.000 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.000000016 0.0000000023 0.0000000817 0.000 lb/mmBtuO2 1.17E-12 1.64E-13 5.77E-12 0.000 ng/dscm 1.55E-03 2.17E-04 7.61E-03 0.003 ng/dscm@7%O2 1.35E-03 1.90E-04 6.70E-03 0.003 

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000659 0.0000000043 0.000000216 0.000 lb/mmBtuO2 4.80E-12 3.06E-13 1.53E-11 0.000 ng/dscm 6.37E-03 4.05E-04 2.01E-02 0.009 ng/dscm@7%O2 5.57E-03 3.55E-04 1.77E-02 0.008



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.000000395 0.0000000996 0.00000137 0.000 lb/mmBtuO2 2.88E-11 7.10E-12 9.68E-11 0.000 ng/dscm 3.82E-02 9.39E-03 1.28E-01 0.059 ng/dscm@7%O2 3.34E-02 8.23E-03 1.13E-01 0.052 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000772 0.0000000023 0.00000031 0.000 lb/mmBtuO2 5.63E-12 1.64E-13 2.19E-11 0.000 ng/dscm 7.47E-03 2.17E-04 2.89E-02 0.012 ng/dscm@7%O2 6.53E-03 1.90E-04 2.54E-02 0.011 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.000000018 0.000000013 0.000000098 0.000 lb/mmBtuO2 1.31E-12 9.26E-13 6.93E-12 0.000 ng/dscm 1.74E-03 1.23E-03 9.12E-03 0.004 ng/dscm@7%O2 1.52E-03 1.08E-03 8.03E-03 0.004 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.00000105 0.00000027 0.00000301 0.000 lb/mmBtuO2 7.65E-11 1.92E-11 2.13E-10 0.000 ng/dscm 1.02E-01 2.54E-02 2.80E-01 0.136 ng/dscm@7%O2 8.91E-02 2.23E-02 2.46E-01 0.119 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.000000043 0.000000013 0.000000097 0.000 lb/mmBtuO2 3.13E-12 9.26E-13 6.86E-12 0.000 ng/dscm 4.16E-03 1.23E-03 9.03E-03 0.005 ng/dscm@7%O2 3.63E-03 1.08E-03 7.95E-03 0.004 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000045 0.000000003 0.0000000028 0.000 lb/mmBtuO2 3.28E-13 2.14E-13 1.98E-13 0.000 ng/dscm 4.35E-04 2.83E-04 2.61E-04 0.000 ng/dscm@7%O2 3.80E-04 2.48E-04 2.30E-04 0.000 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.000000005 0.0000000077 0.0000000043 0.000 lb/mmBtuO2 3.64E-13 5.49E-13 3.04E-13 0.000



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 ng/dscm 4.84E-04 7.26E-04 4.00E-04 0.001 ng/dscm@7%O2 4.23E-04 6.36E-04 3.52E-04 0.000 

### Compound: 2,3,7,8-TCDD Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000069 0.0000000082 0.0000000042 0.000 lb/mmBtuO2 5.03E-13 5.84E-13 2.97E-13 0.000 ng/dscm 6.67E-04 7.73E-04 3.91E-04 0.001 ng/dscm@7%O2 5.83E-04 6.77E-04 3.44E-04 0.001 

### Compound: 2,3,7,8-TCDF Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000068 0.0000000057 0.0000000042 0.000 lb/mmBtuO2 4.96E-13 4.06E-13 2.97E-13 0.000 ng/dscm 6.58E-04 5.37E-04 3.91E-04 0.001 ng/dscm@7%O2 5.75E-04 4.71E-04 3.44E-04 0.000 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000039 0.0000000022 0.000000012 0.000 lb/mmBtuO2 2.84E-13 1.57E-13 8.48E-13 0.000 ng/dscm 3.77E-04 2.07E-04 1.12E-03 0.001 ng/dscm@7%O2 3.29E-04 1.81E-04 9.86E-04 0.000 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.000000023 0.000000016 0.0000000587 0.000 lb/mmBtuO2 1.68E-12 1.14E-12 4.15E-12 0.000 ng/dscm 2.22E-03 1.51E-03 5.46E-03 0.003 ng/dscm@7%O2 1.94E-03 1.32E-03 4.81E-03 0.003 

### Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000974 0.00000003 0.000000292 0.000 lb/mmBtuO2 7.10E-12 2.14E-12 2.06E-11 0.000 ng/dscm 9.42E-03 2.83E-03 2.72E-02 0.013 ng/dscm@7%O2 8.23E-03 2.48E-03 2.39E-02 0.012 

### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000082 0.0000000078 0.0000000184 0.000 lb/mmBtuO2 5.98E-13 5.56E-13 1.30E-12 0.000 ng/dscm 7.93E-04 7.35E-04 1.71E-03 0.001 ng/dscm@7%O2 6.93E-04 6.44E-04 1.51E-03 0.001 

### Compound: OCDD Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3


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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 Mass_mg 0.000000024 0.000000006 0.0000000514 0.000 lb/mmBtuO2 1.75E-12 4.27E-13 3.63E-12 0.000 ng/dscm 2.32E-03 5.66E-04 4.78E-03 0.003 ng/dscm@7%O2 2.03E-03 4.96E-04 4.21E-03 0.002 

### Compound: OCDF Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000059 0.0000000031 0.000000011 0.000 lb/mmBtuO2 4.30E-13 2.21E-13 7.77E-13 0.000 ng/dscm 5.71E-04 2.92E-04 1.02E-03 0.001 ng/dscm@7%O2 4.99E-04 2.56E-04 8.98E-04 0.001 

### Compound: Total Dioxins Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000626 0.0000000309 0.000000083 0.000 lb/mmBtuO2 4.56E-12 2.20E-12 5.87E-12 0.000 ng/dscm 6.05E-03 2.91E-03 7.73E-03 0.006 ng/dscm@7%O2 5.29E-03 2.55E-03 6.80E-03 0.005 

### Compound: Total Furans Average RunNumber PMT2-23-1 PMT2-23-2 PMT2-23-3 Mass_mg 0.0000000517 0.0000000442 0.0000000499 0.000 lb/mmBtuO2 3.77E-12 3.15E-12 3.53E-12 0.000 ng/dscm 5.00E-03 4.17E-03 4.65E-03 0.005 ng/dscm@7%O2 4.37E-03 3.65E-03 4.09E-03 0.004



### Location: PMT2 - Gases - Method 10 Compound: Carbon Monoxide Average Run 2-CO-1 2-CO-2 2-CO-3 lb/mmBtuO2 1.73E-01 1.62E-01 1.85E-01 0.173 ppm 1.97E+02 1.84E+02 2.09E+02 196.667 ppm@7%O2 1.72E+02 1.61E+02 1.84E+02 172.333



### Location: PMT2 - Gases - Method 25A Compound: Total organic compounds (TOC) as Average Run 2-THC-1 2-THC-2 2-THC-3 lb/mmBtuO2 0.00E+00 3.68E-04 0.00E+00 0.000 ppm 0.00E+00 2.65E-01 0.00E+00 0.088 ppm@7%O2 0.00E+00 2.32E-01 0.00E+00 0.077



### Location: PMT2 - Gases - Method 6C Compound: Sulfur Dioxide Average Run 2-SO2-1 2-SO2-2 2-SO2-3 lb/mmBtuO2 9.19E-01 9.03E-01 9.37E-01 0.920 ppm 4.58E+02 4.49E+02 4.63E+02 456.667 ppm@7%O2 4.00E+02 3.94E+02 4.08E+02 400.667



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010

Location: PMT2 - Gases - Method 7E 

### Compound: Nitrogen oxides (NOx) Average Run 2-NOx-1 2-NOx-2 2-NOx-3 lb/mmBtuO2 2.38E-01 2.42E-01 2.39E-01 0.240 ppm 1.65E+02 1.67E+02 1.65E+02 165.667 ppm@7%O2 1.44E+02 1.46E+02 1.45E+02 145.000



### Location: PMT2 - Metals - Method 29 

### Compound: Antimony Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 0.159 0.167 0.0584 0.128 Elb/hr 1.85E-01 1.93E-01 6.66E-02 0.148 lb/mmBtuO2 2.35E-05 2.46E-05 8.34E-06 0.000 mg/dscm 3.12E-02 3.25E-02 1.10E-02 0.025 mg/dscm@7%O2 2.73E-02 2.85E-02 9.64E-03 0.022 

### Compound: Arsenic Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 0.0125 0.0157 0.00538 0.011 Elb/hr 1.45E-02 1.82E-02 6.13E-03 0.013 lb/mmBtuO2 1.85E-06 2.31E-06 7.68E-07 0.000 mg/dscm 2.45E-03 3.05E-03 1.02E-03 0.002 mg/dscm@7%O2 2.14E-03 2.67E-03 8.94E-04 0.002 

### Compound: Beryllium Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 0.0003 0.000344 0.000227 0.000 Elb/hr 3.49E-04 3.98E-04 2.59E-04 0.000 lb/mmBtuO2 4.44E-08 5.06E-08 3.24E-08 0.000 mg/dscm 5.89E-05 6.69E-05 4.29E-05 0.000 mg/dscm@7%O2 5.15E-05 5.86E-05 3.76E-05 0.000 

### Compound: Cadmium Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 0.000346 0.000466 0.000166 0.000 Elb/hr 4.02E-04 5.39E-04 1.89E-04 0.000 lb/mmBtuO2 5.12E-08 6.85E-08 2.37E-08 0.000 mg/dscm 6.79E-05 9.07E-05 3.13E-05 0.000 mg/dscm@7%O2 5.93E-05 7.95E-05 2.74E-05 0.000 

### Compound: Chromium Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 0.0301 0.0356 0.0147 0.027 Elb/hr 3.50E-02 4.12E-02 1.68E-02 0.031 lb/mmBtuO2 4.45E-06 5.24E-06 2.10E-06 0.000 mg/dscm 5.91E-03 6.93E-03 2.78E-03 0.005



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 mg/dscm@7%O2 5.16E-03 6.07E-03 2.44E-03 0.005 

### Compound: Cobalt Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 0.185 0.222 0.0846 0.164 Elb/hr 2.15E-01 2.57E-01 9.65E-02 0.190 lb/mmBtuO2 2.74E-05 3.26E-05 1.21E-05 0.000 mg/dscm 3.63E-02 4.32E-02 1.60E-02 0.032 mg/dscm@7%O2 3.17E-02 3.79E-02 1.40E-02 0.028 

### Compound: Filterable Particulate Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 165.1 185.3 60.6 137.000 Elb/hr 1.92E+02 2.14E+02 6.91E+01 158.367 lb/mmBtuO2 2.44E-02 2.73E-02 8.65E-03 0.020 mg/dscm 3.24E+01 3.61E+01 1.14E+01 26.633 mg/dscm@7%O2 2.83E+01 3.16E+01 9.99E+00 23.297 

### Compound: Lead Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 0.0359 0.0436 0.0161 0.032 Elb/hr 4.18E-02 5.04E-02 1.84E-02 0.037 lb/mmBtuO2 5.31E-06 6.41E-06 2.30E-06 0.000 mg/dscm 7.05E-03 8.48E-03 3.04E-03 0.006 mg/dscm@7%O2 6.16E-03 7.43E-03 2.66E-03 0.005 

### Compound: Manganese Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 0.0712 0.0844 0.036 0.064 Elb/hr 8.28E-02 9.76E-02 4.11E-02 0.074 lb/mmBtuO2 1.05E-05 1.24E-05 5.14E-06 0.000 mg/dscm 1.40E-02 1.64E-02 6.80E-03 0.012 mg/dscm@7%O2 1.22E-02 1.44E-02 5.96E-03 0.011 

### Compound: Nickel Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 4.06 4.41 1.52 3.330 Elb/hr 4.72E+00 5.10E+00 1.73E+00 3.850 lb/mmBtuO2 6.00E-04 6.49E-04 2.17E-04 0.000 mg/dscm 7.97E-01 8.58E-01 2.87E-01 0.647 mg/dscm@7%O2 6.96E-01 7.52E-01 2.52E-01 0.567 

### Compound: Selenium Average RunNumber PMT2-29-1 PMT2-29-2 PMT2-29-3 Mass_mg 0.00416 0.002 0.002 0.003 Elb/hr 4.84E-03 2.31E-03 2.28E-03 0.003 lb/mmBtuO2 6.15E-07 2.94E-07 2.85E-07 0.000 mg/dscm 8.16E-04 3.89E-04 3.78E-04 0.001


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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010

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



### Location: PMT2 - PM - OTM - 27/28 Compound: Filterable Particulate Average RunNumber PMT2-27/28-2 PMT2-27/28-3 PMT2-27/28-1 Mass_mg 12.597 43.997 70.747 42.447 lb/mmBtuO2 7.37E-03 2.66E-02 4.35E-02 0.026 

### Compound: Filterable PM2.5 Average RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3 Mass_mg 43.314 8.672 31.772 27.919 lb/mmBtuO2 2.67E-02 5.08E-03 1.92E-02 0.017 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3 Mass_mg 0.254 1.309 7.771 3.111 lb/mmBtuO2 1.56E-04 7.66E-04 4.70E-03 0.002 

### Compound: Organic Condensible Particulate Average RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3 Mass_mg 1.725 0.54 274.91 92.392 lb/mmBtuO2 1.06E-03 3.16E-04 1.66E-01 0.056 

### Compound: Total Particulate Average RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3 Mass_mg 75.49 15.393 327.274 139.386 lb/mmBtuO2 4.65E-02 9.01E-03 1.98E-01 0.085 

### Compound: Total PM2.5 Average RunNumber PMT2-27/28-1 PMT2-27/28-2 PMT2-27/28-3 Mass_mg 45.293 10.521 314.452 123.422 lb/mmBtuO2 2.79E-02 6.16E-03 1.90E-01 0.075



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 Process Run Data



### Run Name Value UOM Comments Target Value 1 Residual Oil (No. 6) Burned 60065 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 5/11/2010; Start - 12:47; End - 14:47 0



### 10 Residual Oil (No. 6) Burned 59941 gal/hr Method 027/028; Run PM-1; Date - 5/11/2010; Start - 08:49; End - 12:36 0

11 Residual Oil (No. 6) Burned 60117 gal/hr Method 027/028; Run PM-2; Date - 5/11/2010; Start - 18:33; End - 21:33 0

12 Residual Oil (No. 6) Burned 60000 gal/hr Method 027/028; Run PM-3; Date - 5/12/2010; Start - 08:23; End - 11:32 0

2 Residual Oil (No. 6) Burned 60080 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 5/11/2010; Start - 15:09; End - 17:09 0

3 Residual Oil (No. 6) Burned 60124 gal/hr Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 5/11/2010; Start - 17:33; End - 19:33 0



### 4 Residual Oil (No. 6) Burned 60088 gal/hr Method 23; Run D/F-1; Date - 5/11/2010; Start - 12:58; End - 22:36 0

5 Residual Oil (No. 6) Burned 60059 gal/hr Method 23; Run D/F-2; Date - 5/12/2010; Start - 12:00; End - 21:05 0

6 Residual Oil (No. 6) Burned 60161 gal/hr Method 23; Run D/F-3; Date - 5/13/2010; Start - 08:06; End - 17:07 0

7 Residual Oil (No. 6) Burned 60073 gal/hr Method 29; Run M-1; Date - 5/11/2010; Start - 13:18; End - 18:11 0



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 8 Residual Oil (No. 6) Burned 59985 gal/hr Method 29; Run M-2; Date - 5/12/2010; Start - 08:22; End - 13:04 0

9 Residual Oil (No. 6) Burned 60088 gal/hr Method 29; Run M-3; Date - 5/12/2010; Start - 13:32; End - 18:13 0

1 Average Heat Input 7506 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 5/11/2010; Start - 12:47; End - 14:47 0



### 10 Average Heat Input 7492 MMBtu/hr Method 027/028; Run PM-1; Date - 5/11/2010; Start - 08:49; End - 12:36 0

11 Average Heat Input 7514 MMBtu/hr Method 027/028; Run PM-2; Date - 5/11/2010; Start - 18:33; End - 21:33 0

12 Average Heat Input 7499 MMBtu/hr Method 027/028; Run PM-3; Date - 5/12/2010; Start - 08:23; End - 11:32 0

2 Average Heat Input 7508 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 5/11/2010; Start - 15:09; End - 17:09 0

3 Average Heat Input 7514 MMBtu/hr Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 5/11/2010; Start - 17:33; End - 19:33 0



### 4 Average Heat Input 7511 MMBtu/hr Method 23; Run D/F-1; Date - 5/11/2010; Start - 12:58; End - 22:36 0

5 Average Heat Input 7507 MMBtu/hr Method 23; Run D/F-2; Date - 5/12/2010; Start - 12:00; End - 21:05 0

6 Average Heat Input 7520 MMBtu/hr Method 23; Run D/F-3; Date - 5/13/2010; Start - 08:06; End - 17:07 0



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
7 Average Heat Input 7509 MMBtu/hr Method 29; Run M-1; Date - 5/11/2010; Start - 13:18; End - 18:11 0

8 Average Heat Input 7498 MMBtu/hr Method 29; Run M-2; Date - 5/12/2010; Start - 08:22; End - 13:04 0

9 Average Heat Input 7510 MMBtu/hr Method 29; Run M-3; Date - 5/12/2010; Start - 13:32; End - 18:13 0

1 Steam Output 5327 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 5/11/2010; Start - 12:47; End - 14:47 0



### 10 Steam Output 5319 1000 lb Method 027/028; Run PM-1; Date - 5/11/2010; Start - 08:49; End - 12:36 0

11 Steam Output 5330 1000 lb Method 027/028; Run PM-2; Date - 5/11/2010; Start - 18:33; End - 21:33 0

12 Steam Output 5316 1000 lb Method 027/028; Run PM-3; Date - 5/12/2010; Start - 08:23; End - 11:32 0

2 Steam Output 5325 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 5/11/2010; Start - 15:09; End - 17:09 0

3 Steam Output 5329 1000 lb Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 5/11/2010; Start - 17:33; End - 19:33 0

4 Steam Output 5328 1000 lb Method 23; Run D/F-1; Date - 5/11/2010; Start - 12:58; End - 22:36 0

5 Steam Output 5325 1000 lb Method 23; Run D/F-2; Date - 5/12/2010; Start - 12:00; End - 21:05 0



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
6 Steam Output 5324 1000 lb Method 23; Run D/F-3; Date - 5/13/2010; Start - 08:06; End - 17:07 0

7 Steam Output 5327 1000 lb Method 29; Run M-1; Date - 5/11/2010; Start - 13:18; End - 18:11 0

8 Steam Output 5317 1000 lb Method 29; Run M-2; Date - 5/12/2010; Start - 08:22; End - 13:04 0

9 Steam Output 5326 1000 lb Method 29; Run M-3; Date - 5/12/2010; Start - 13:32; End - 18:13 0

1 Unit Gross Electrical Output 798 MWg Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 5/11/2010; Start - 12:47; End - 14:47 0



### 10 Unit Gross Electrical Output 798 MWg Method 027/028; Run PM-1; Date - 5/11/2010; Start - 08:49; End - 12:36 0

11 Unit Gross Electrical Output 798 MWg Method 027/028; Run PM-2; Date - 5/11/2010; Start - 18:33; End - 21:33 0

12 Unit Gross Electrical Output 798 MWg Method 027/028; Run PM-3; Date - 5/12/2010; Start - 08:23; End - 11:32 0

2 Unit Gross Electrical Output 798 MWg Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 5/11/2010; Start - 15:09; End - 17:09 0

3 Unit Gross Electrical Output 798 MWg Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 5/11/2010; Start - 17:33; End - 19:33 0

4 Unit Gross Electrical Output 798 MWg Method 23; Run D/F-1; Date - 5/11/2010; Start - 12:58; End - 22:36 0



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 5 Unit Gross Electrical Output 798 MWg Method 23; Run D/F-2; Date - 5/12/2010; Start - 12:00; End - 21:05 0

6 Unit Gross Electrical Output 798 MWg Method 23; Run D/F-3; Date - 5/13/2010; Start - 08:06; End - 17:07 0

7 Unit Gross Electrical Output 798 MWg Method 29; Run M-1; Date - 5/11/2010; Start - 13:18; End - 18:11 0

8 Unit Gross Electrical Output 798 MWg Method 29; Run M-2; Date - 5/12/2010; Start - 08:22; End - 13:04 0

9 Unit Gross Electrical Output 798 MWg Method 29; Run M-3; Date - 5/12/2010; Start - 13:32; End - 18:13 0

1 Unit Net Electric Generation 766 MWn Methods 6c, 7e, 10, and 25a; Run RM-1 and FTIR-1; Date - 5/11/2010; Start - 12:47; End - 14:47 0



### 10 Unit Net Electric Generation 766 MWn Method 027/028; Run PM-1; Date - 5/11/2010; Start - 08:49; End - 12:36 0

11 Unit Net Electric Generation 766 MWn Method 027/028; Run PM-2; Date - 5/11/2010; Start - 18:33; End - 21:33 0

12 Unit Net Electric Generation 767 MWn Method 027/028; Run PM-3; Date - 5/12/2010; Start - 08:23; End - 11:32 0

2 Unit Net Electric Generation 766 MWn Methods 6c, 7e, 10, and 25a; Run RM-2 and FTIR-2; Date - 5/11/2010; Start - 15:09; End - 17:09 0

3 Unit Net Electric Generation 766 MWn Methods 6c, 7e, 10, and 25a; Run RM-3 and FTIR-3; Date - 5/11/2010; Start - 17:33; End - 19:33 0



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010

APCD Run Data

Process Lab Run Data 4 Unit Net Electric Generation 766 MWn Method 23; Run D/F-1; Date - 5/11/2010; Start - 12:58; End - 22:36 0

5 Unit Net Electric Generation 766 MWn Method 23; Run D/F-2; Date - 5/12/2010; Start - 12:00; End - 21:05 0

6 Unit Net Electric Generation 766 MWn Method 23; Run D/F-3; Date - 5/13/2010; Start - 08:06; End - 17:07 0

7 Unit Net Electric Generation 766 MWn Method 29; Run M-1; Date - 5/11/2010; Start - 13:18; End - 18:11 0

8 Unit Net Electric Generation 767 MWn Method 29; Run M-2; Date - 5/12/2010; Start - 08:22; End - 13:04 0

9 Unit Net Electric Generation 766 MWn Method 29; Run M-3; Date - 5/12/2010; Start - 13:32; End - 18:13 0



### Run Name Value UOM Comments Target Value 1 LOW NOX BURNERS 164 NOx Emissions 0


### 2 LOW NOX BURNERS 166 NOx Emissions 0
3 LOW NOX BURNERS 165 NOx Emissions 0
1 CYCLONE SEPARATORS 14.8 Opacity 0


### 2 CYCLONE SEPARATORS 16 Opacity 0
3 CYCLONE SEPARATORS 15.4 Opacity 0

Run Name Value UOM Comments 

### 1 Fuel Higher Heating Value 17800 Btu/lb 1 Fuel Moisture 0.096 % 1 Fuel Mercury Content 0.002 mg/kg 1 Fuel Chlorine Content 145 mg/kg 

### 1 Fuel Fluorine Content 76 mg/kg 1 Fuel Antimony Content 0.8 mg/kg 1 Fuel Arsenic Content 0.067 mg/kg 

### 1 Fuel Beryllium Content 0.008 mg/kg
Monday, February 14, 2011 Page 23 of 34

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 1 Fuel Cadmium Content 0.009 mg/kg 

### 1 Fuel Chromium Content 0.088 mg/kg 1 Fuel Cobalt Content 1.1 mg/kg 1 Fuel Lead Content 0.15 mg/kg 1 Fuel Manganese Content 0.3 mg/kg 

### 1 Fuel Nickel Content 22.8 mg/kg 1 Fuel Selenium Content 0.03 mg/kg 1 Fuel Sulfur Content 11800 mg/kg 

### 1 Fuel Proximate Analysis (Carbon) 88.31 % 1 Fuel Proximate Analysis (Hydrogen) 10.02 % 1 Fuel Proximate Analysis (Nitrogen) 0.67 % 1 Fuel Proximate Analysis (Oxygen) 0.5 % 

### 1 Fuel Proximate Analysis (Sulfur) 1.13 % 2 Fuel Higher Heating Value 17700 Btu/lb 2 Fuel Moisture 0.114 % 

### 2 Fuel Mercury Content 0.002 mg/kg 2 Fuel Chlorine Content 261 mg/kg 2 Fuel Fluorine Content 76 mg/kg 2 Fuel Antimony Content 0.8 mg/kg 

### 2 Fuel Arsenic Content 0.06 mg/kg 2 Fuel Beryllium Content 0.008 mg/kg 2 Fuel Cadmium Content 0.008 mg/kg 

### 2 Fuel Chromium Content 0.078 mg/kg 2 Fuel Cobalt Content 1.1 mg/kg 2 Fuel Lead Content 0.14 mg/kg 2 Fuel Manganese Content 0.3 mg/kg 

### 2 Fuel Nickel Content 22.3 mg/kg 2 Fuel Selenium Content 0.03 mg/kg 2 Fuel Sulfur Content 10100 mg/kg 

### 2 Fuel Proximate Analysis (Carbon) 88.27 % 2 Fuel Proximate Analysis (Hydrogen) 10.1 % 2 Fuel Proximate Analysis (Nitrogen) 0.66 % 2 Fuel Proximate Analysis (Oxygen) 0.5 % 

### 2 Fuel Proximate Analysis (Sulfur) 1.09 % 3 Fuel Higher Heating Value 17900 Btu/lb 3 Fuel Moisture 0.111 % 

### 3 Fuel Mercury Content 0.001 mg/kg 3 Fuel Chlorine Content 255 mg/kg 3 Fuel Fluorine Content 72 mg/kg 3 Fuel Antimony Content 0.7 mg/kg 

### 3 Fuel Arsenic Content 0.049 mg/kg 3 Fuel Beryllium Content 0.008 mg/kg 3 Fuel Cadmium Content 0.009 mg/kg



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 3 Fuel Chromium Content 0.1 mg/kg 

### 3 Fuel Cobalt Content 1.1 mg/kg 3 Fuel Lead Content 0.14 mg/kg 3 Fuel Manganese Content 0.3 mg/kg 3 Fuel Nickel Content 22.1 mg/kg 

### 3 Fuel Selenium Content 0.03 mg/kg 3 Fuel Sulfur Content 10500 mg/kg 3 Fuel Proximate Analysis (Carbon) 87.97 % 

### 3 Fuel Proximate Analysis (Hydrogen) 9.95 % 3 Fuel Proximate Analysis (Nitrogen) 0.72 % 3 Fuel Proximate Analysis (Oxygen) 0.5 % 3 Fuel Proximate Analysis (Sulfur) 1.12 %



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010 Sampling / Stack Data Results Detail



### Location PMT2 - D/F - Method 23 Average Run Number PMT2-23-1 PMT2-23-2 PMT2-23-3 Test Date 5/11/2010 5/12/2010 5/13/2010 Run Start Time 12:58:00 PM 12:00:00 PM 8:06:00 AM Run Finish Time 8:58:00 PM 8:00:00 PM 4:06:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.25 0.25 0.25 0.250 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.987 0.987 0.987 0.987 Barometric Pressure, inches of Mercury 30.14 30.2 30.2 30.180 Average Orifice Meter Differential, inches H2O 2.16 2.20 2.25 2.203 Dry Gas Meter Volume Sampled, cubic feet 373.520 381.680 385.720 380.307 Average Dry Gas Meter Temperature, °F 79.75 78.63 77.67 78.683 Dry Gas Meter Volume Sampled, dscf 365.205 374.736 379.425 373.122 Total Moisture Liquid collected, g 786.3 796.1 769.1 783.833 Volume of Water Vapor, standard cubic feet 37.01 37.47 36.20 36.893 Moisture Content of Stack Gas, % 9.20 9.09 8.71 9.000 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.908 0.9091 0.9129 0.910 Carbon Dioxide, % 12.59 12.9 12.7 12.730 Oxygen, % 4.99 5.04 5.11 5.047 Carbon Monoxide & Nitrogen, % 82.42 82.06 82.19 82.223 Fuel Factor 1.26 1.23 1.24 Dry Molecular Weight, lb/lb-Mole 30.21 30.27 30.24 30.240 Wet Molecular weight, lb/lb-Mole 29.09 29.15 29.17 29.137 Flue Gas Static Pressure, inches of H2O -1.6 -1.6 -1.6 -1.600 Absolute Flue Gas Pressure, inches of Mercury 30.02 30.08 30.08 30.060 Average Stack Gas Temperature, °F 320.08 321.71 321.63 321.140 Average Velocity Head, inches of H2O 0.8208445492 94092 0.837588525

270098 0.854896842

115147 0.838
Average Stack Gas Velocity, feet/second 61.49 62.05 62.67 62.070 Stack Cross-Sectional Area, square feet 696.685 696.685 696.685 696.685 Dry Volumetric Flow Rate, dry scfm 1,584,973.2 1,601,200.3 1,624,125.4 1,603,432.9 67 Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,570,349.6 2,593,758.3 2,619,674.9 2,594,594.2 67 Percent Isokinetic of Sampling Rate, % 98.1 99.6 99.5 99.067 Percent Excess Air, % 29.8 30.3 30.8 30.300 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Round Duct Diameter, inches 357.4 357.4 357.4 Rectangular Duct Width, inches 0 0 0 Rectangular Duct Length, inches 0 0 0 Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000



### Monday, February 14, 2011 Page 26 of 34

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Gases - Method 10 Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Gases - Method 25A Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Gases - Method 3A CO2 Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Method 3A CO2 Method 3A

CO2 Method 3A

CO2 Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc PMT2 - Gases PMT2 - Gases PMT2 - Gases
Cgasw 2-CO2-1 2-CO2-2 2-CO2-3 Cgasw Units 5/11/2010 5/11/2010 5/11/2010



### Monday, February 14, 2011 Page 29 of 34

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Gases - Method 3A O2 Average Run Number 2-O2-1 2-O2-2 2-O2-3 Test Date 5/11/2010 5/11/2010 5/11/2010 Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM Carbon Dioxide, % 12.59 12.9 12.7 12.730 Oxygen, % 4.99 5.04 5.11 5.047 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.0 00 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 9.22 9.22 9.22 9.220 Analyzer Make THERMO THERMO THERMO Analyzer Model 42i-HL 42i-HL 42i-HL Analyzer Serial Number INST-N2-0002 INST-N2- 0002 INST-N2-

0002 Operating Range 21.1 21.1 21.1 21.100 Operating Units % % % No. Readings/Avg. 240 240 240 240.000 Calibration Set 1 1 1 1.000 Calibration Pre Zero Cylinder ID ALM031337 ALM031337 ALM031337 Calibration Pre Zero Cylinder Instrument Response 0.37 0.37 0.37 0.370 Calibration Pre Zero Cylinder Bias 1.47 1.47 1.47 1.470 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID AAL12025-O2 AAL12025- O2 AAL12025-

O2 Calibration Pre High Cylinder Instrument Response 12.02 11.91 11.9 11.943 Calibration Pre High Cylinder Bias 0.05 -0.47 -0.52 -0.313 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337 Calibration Post Zero Cylinder Instrument Response 0.37 0.37 0.36 0.367 Calibration Post Zero Cylinder Bias 1.47 1.47 1.42 1.453 Calibration Post Zero Cylinder Drift 0 0 0.05 0.017 Calibration Post High Cylinder ID AAL12025-O2 AAL12025- O2 AAL12025-

O2 Calibration Post High Cylinder Instrument Response 11.91 11.9 11.88 11.897 Calibration Post High Cylinder Bias -0.47 -0.52 -0.62 -0.537 Calibration Post High Cylinder Drift 0.52 0.05 0.1 0.223 Cavg 5.15 5.18 5.23 5.187 Cavg Units %vd %vd %vd Cgas 4.9882 5.0456 5.1077 5.047 Cgas Units %vd %vd %vd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units %vw %vw %vw



### Monday, February 14, 2011 Page 30 of 34

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Gases - Method 6C Average Run Number 2-SO2-1 2-SO2-2 2-SO2-3 Test Date 5/11/2010 5/11/2010 5/11/2010 Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM Carbon Dioxide, % 12.59 12.9 12.7 12.730 Oxygen, % 4.99 5.04 5.11 5.047 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.0 00 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 9.22 9.22 9.22 9.220 Analyzer Make THERMO THERMO THERMO Analyzer Model 43i-HL 43i-HL 43i-HL Analyzer Serial Number INST-S2-0005 INST-S2- 0005 INST-S2-

0005 Operating Range 959 959 959 959.000 Operating Units ppm ppm ppm No. Readings/Avg. 240 240 240 240.000 Calibration Set 3 3 3 3.000 Calibration Pre Zero Cylinder ID ALM031337 ALM031337 ALM031337 Calibration Pre Zero Cylinder Instrument Response 2.05 3.71 2.96 2.907 Calibration Pre Zero Cylinder Bias 0.17 0.34 0.26 0.257 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID CC66246 CC66246 CC66246 Calibration Pre High Cylinder Instrument Response 406.28 402.58 406.32 405.060 Calibration Pre High Cylinder Bias -1.48 -1.87 -1.48 -1.610 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337 Calibration Post Zero Cylinder Instrument Response 3.71 2.96 3.18 3.283 Calibration Post Zero Cylinder Bias 0.34 0.26 0.28 0.293 Calibration Post Zero Cylinder Drift 0.17 0.08 0.02 0.090 Calibration Post High Cylinder ID CC66246 CC66246 CC66246 Calibration Post High Cylinder Instrument Response 402.58 406.32 405.99 404.963 Calibration Post High Cylinder Bias -1.87 -1.48 -1.51 -1.620 Calibration Post High Cylinder Drift 0.39 0.39 0.03 0.270 Cavg 432.44 423.73 439.23 431.800 Cavg Units ppmvd ppmvd ppmvd Cgas 457.855 448.5723 463.1194 456.516 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units ppmvw ppmvw ppmvw



### Monday, February 14, 2011 Page 31 of 34

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Gases - Method 7E Average Run Number 2-NOx-1 2-NOx-2 2-NOx-3 Test Date 5/11/2010 5/11/2010 5/11/2010 Run Start Time 12:47:59 PM 3:09:59 PM 5:33:59 PM Run Finish Time 2:47:29 PM 5:09:29 PM 7:33:29 PM Carbon Dioxide, % 12.59 12.9 12.7 12.730 Oxygen, % 4.99 5.04 5.11 5.047 Fuel Factor 1.32 1.32 1.32 Dry Volumetric Flow Rate, dry scfm 1584637 1584637 1584637 1,584,637.0 00 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 9.22 9.22 9.22 9.220 Analyzer Make THERMO THERMO THERMO Analyzer Model 42i-HL 42i-HL 42i-HL Analyzer Serial Number INST-N2-0002 INST-N2- 0002 INST-N2-

0002 Operating Range 1110 1110 1110 1,110.000 Operating Units ppm ppm ppm No. Readings/Avg. 240 240 240 240.000 Calibration Set 4 4 4 4.000 Calibration Pre Zero Cylinder ID ALM031337 ALM031337 ALM031337 Calibration Pre Zero Cylinder Instrument Response 1.19 2.24 1.91 1.780 Calibration Pre Zero Cylinder Bias 0.02 0.11 0.08 0.070 Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID ALM042523- NOx ALM042523

-NOx ALM042523-

NOx Calibration Pre High Cylinder Instrument Response 536.28 531.09 531.7 533.023 Calibration Pre High Cylinder Bias -1.81 -2.27 -2.22 -2.100 Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID ALM031337 ALM031337 ALM031337 Calibration Post Zero Cylinder Instrument Response 2.24 1.91 1.93 2.027 Calibration Post Zero Cylinder Bias 0.11 0.08 0.09 0.093 Calibration Post Zero Cylinder Drift 0.09 0.03 0.01 0.043 Calibration Post High Cylinder ID ALM042523- NOx ALM042523

-NOx ALM042523-

NOx Calibration Post High Cylinder Instrument Response 531.09 531.7 530.29 531.027 Calibration Post High Cylinder Bias -2.27 -2.22 -2.35 -2.280 Calibration Post High Cylinder Drift 0.46 4.999999999 99998E-02 0.13 0.213
Cavg 162.64 164.16 161.36 162.720 Cavg Units ppmvd ppmvd ppmvd Cgas 165.4717 167.4989 164.8418 165.937 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 10320 10,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units ppmvw ppmvw ppmvw



### Monday, February 14, 2011 Page 32 of 34

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - Metals - Method 29 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



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

### Manatee Energy Center, Unit #2, Information Collection Request
7/14/2010
Location PMT2 - PM - OTM - 27/28 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



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