### Name: Patricia Q. West

Title: Manager, Environmental, Energy Supp Company: Progress Energy Florida, Inc. Sign Date: 9/3/2010 Name: Michael Sussman, P.E. Title: Project Manager Company: Kleinfelder Southeast, Inc. Sign Date: 9/3/2010 Permitted Facility Representative / Date Testing Company Representative / Date



## Progress Energy Florida Suwannee River Unit 1

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.

Thursday, February 17, 2011 Page 1 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010 Facility Information: Progress Energy Florida Suwannee Unit 1
4037 River Road

Live Oak FL 32060 Contact: Cary W. Hamilton
Phone: Of above person
Fax: Of above person
Email: cary.hamilton@pgnmail Testing Company: Kleinfelder Southeast, Inc. 6200 Harris Technology Blvd.

Charlotte NC 28269 Contact: W. Quentin Best
Phone: 704-598-1049
Fax: 704-598-1050
Email: qbest@klienfelder.com

Air Permit Number: 1210003-007-AV Permitted Source ID/Name: Fossil Fuel Fired Steam Generator Unit No. 1 Unit 1
Permitted Maximum Process Rate: 450 million Btu/hr Max. Normal Operation Process Rate: N/A Target Process Test Rate N/A

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: . Boiler No. 1 (E.U. ID No. -001) is a nominal 35.0 megawatt electric steam generator. The permitted capacity for Unit No. 1 on fuel oil is 450 MMBtu/hr heat input. The Unit is allowed to fire No. 2 fuel oil, No. 6 fuel oil, “on specification” used oil, natural gas and a blend of fuel oil and natural gas. Unit No. 1 drives a turbine generator for electrical power and vents to its own stack. There are no air pollution equipment control devices associated with Unit No. 1. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 1212100003 FRS #: 110000909214

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
Stack Exit 83.063 240 240 2 0 24 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location % H2O Method 1 - 4 3 180 0 Stack Exit Carbon Monoxide Method 10 3 120 0 Stack Exit Formaldehyde Method 0011 3 120 0 Stack Exit Total organic compounds

(TOC) as Propane Method 25A 3 120 0 Stack Exit

Hydrogen Chloride Method 26A 3 180 0 Stack Exit



### Thursday, February 17, 2011 Page 2 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010

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. Followed test protocol.

Hydrogen Fluoride Method 26A 3 180 0 Stack Exit Total Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Organic Condensible

Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Cobalt Method 29 0 Stack Exit Antimony Method 29 3 240 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit Beryllium Method 29 3 240 0 Stack Exit Cadmium Method 29 3 240 0 Stack Exit Chromium Method 29 3 240 0 Stack Exit Lead Method 29 3 240 0 Stack Exit Manganese Method 29 3 240 0 Stack Exit Nickel Method 29 3 240 0 Stack Exit Filterable Particulate Method 29 3 240 0 Stack Exit Filterable Particulate Method 29 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit O2 Method 3A O2 3 240 0 Stack Exit Co2 Method 3A CO2 3 240 0 Stack Exit Co2 Method 3A CO2 3 120 0 Stack Exit O2 Method 3A O2 3 120 0 Stack Exit O2 Method 3A O2 3 480 0 Stack Exit Co2 Method 3A CO2 3 480 0 Stack Exit Sulfur Dioxide Method 6C 3 180 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### Thursday, February 17, 2011 Page 3 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010 Sampling / Stack Data Results Summary



### Location Stack Exit - Method 0011 Average
Run Number 1 2 3
Test Date 6/20/2010 6/20/2010 6/21/2010
Run Start Time 10:57:00 AM 10:13:00 AM
Run Finish Time 1:18:00 PM 12:30:00 PM Net Run Time, minutes 120 120 120 Dry Gas Meter Volume Sampled, dscf 82.906 80.655 83.287 82.283 Moisture Content of Stack Gas, % 7.77 7.81 7.75 7.777 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 9.838 9.873 9.894 9.868 Oxygen, % 8.942 8.841 8.852 8.878 Average Stack Gas Temperature, °F 322.54 324.83 321.38 322.917 Dry Volumetric Flow Rate, dry scfm 100,024.9 96,898.4 100,612.7 99,178.667 Actual Wet Volumetric Flue Gas Flow Rate, acfm 160,466.1 155,973.0 161,188.6 159,209.233 Percent Isokinetic of Sampling Rate, % 100.3 100.7 100.1 100.367 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 Stack Exit - 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



### Thursday, February 17, 2011 Page 4 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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 Stack Exit - Method 26A 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



### Thursday, February 17, 2011 Page 5 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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



### Location Stack Exit - 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



### Thursday, February 17, 2011 Page 6 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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 Stack Exit - 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



### Thursday, February 17, 2011 Page 7 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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 Stack Exit - 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



### Thursday, February 17, 2011 Page 8 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010 Emissions Summary



### Location: Stack Exit - Method 0011 Compound: Formaldehyde Average RunNumber 1 2 3 Mass_mg 0.00397 0.00346 0.00229 0.003 Elb/hr 6.34E-04 5.50E-04 3.66E-04 0.001 gr/dscf 7.39E-07 6.62E-07 4.24E-07 0.000 lb/mmBtuO2 1.70E-06 1.51E-06 9.66E-07 0.000 mg/dscm 1.69E-03 1.52E-03 9.71E-04 0.001 ppm 1.35E-03 1.21E-03 7.78E-04 0.001 ppm@7%O2 1.57E-03 1.39E-03 8.98E-04 0.001



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 gr/dscf 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000 mg/dscm 0.00E+00 0.00E+00 0.00E+00 0.000 mg/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000 ppm 0.00E+00 0.00E+00 0.00E+00 0.000 ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average Run 1 2 3 Elb/hr 6.88E-02 9.08E-02 2.05E+00 0.737 gr/dscf 8.07E-05 1.14E-04 2.44E-03 0.001 lb/mmBtuO2 1.85E-04 2.61E-04 5.55E-03 0.002 mg/dscm 1.85E-01 2.61E-01 5.58E+00 2.009 ppm 1.01E-01 1.43E-01 3.04E+00 1.095 ppm@7%O2 1.17E-01 1.65E-01 3.51E+00 1.264



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 1.171 1.121 1.176 1.156 Elb/hr 1.19E-01 1.19E-01 1.20E-01 0.119 lb/mmBtuO2 3.15E-04 3.17E-04 3.23E-04 0.000 mg/dscm 3.08E-01 3.11E-01 3.15E-01 0.311 mg/dscm@7%O2 3.65E-01 3.67E-01 3.74E-01 0.369


### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 0.169 0.153 0.169 0.164 Elb/hr 1.72E-02 1.63E-02 1.73E-02 0.017


### Thursday, February 17, 2011 Page 9 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
lb/mmBtuO2 4.55E-05 4.32E-05 4.64E-05 0.000 mg/dscm 4.44E-02 4.25E-02 4.53E-02 0.044 mg/dscm@7%O2 5.27E-02 5.01E-02 5.37E-02 0.052



### Location: Stack Exit - Method 29 

### Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.08856 0.08465 0.0838 0.086 Elb/hr 6.70E-03 6.44E-03 6.44E-03 0.007 gr/dscf 6.94E-06 7.42E-06 7.52E-06 0.000 lb/mmBtuO2 1.60E-05 1.70E-05 1.72E-05 0.000 mg/dscm 1.59E-02 1.70E-02 1.72E-02 0.017 mg/dscm@7%O2 1.85E-02 1.98E-02 1.99E-02 0.019


### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.00216 0.00253 0.00324 0.003 Elb/hr 1.63E-04 1.92E-04 2.49E-04 0.000 gr/dscf 1.69E-07 2.22E-07 2.91E-07 0.000 lb/mmBtuO2 3.89E-07 5.09E-07 6.64E-07 0.000 mg/dscm 3.88E-04 5.07E-04 6.65E-04 0.001 mg/dscm@7%O2 4.52E-04 5.89E-04 7.70E-04 0.001


### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.000248 0.000223 0.000221 0.000 Elb/hr 1.88E-05 1.70E-05 1.70E-05 0.000 gr/dscf 1.94E-08 1.95E-08 1.98E-08 0.000 lb/mmBtuO2 4.47E-08 4.48E-08 4.53E-08 0.000 mg/dscm 4.45E-05 4.47E-05 4.54E-05 0.000 mg/dscm@7%O2 5.18E-05 5.19E-05 5.25E-05 0.000


### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.00022 0.000322 0.00167 0.001 Elb/hr 1.66E-05 2.45E-05 1.28E-04 0.000 gr/dscf 1.72E-08 2.82E-08 1.50E-07 0.000 lb/mmBtuO2 3.96E-08 6.47E-08 3.42E-07 0.000 mg/dscm 3.95E-05 6.46E-05 3.43E-04 0.000 mg/dscm@7%O2 4.60E-05 7.51E-05 3.97E-04 0.000


### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.01215 0.00885 0.00985 0.010 Elb/hr 9.19E-04 6.73E-04 7.57E-04 0.001 gr/dscf 9.53E-07 7.76E-07 8.83E-07 0.000 lb/mmBtuO2 2.19E-06 1.78E-06 2.02E-06 0.000 mg/dscm 2.18E-03 1.77E-03 2.02E-03 0.002



### Thursday, February 17, 2011 Page 10 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010 mg/dscm@7%O2 2.54E-03 2.06E-03 2.34E-03 0.002


### Compound: Cobalt Average RunNumber 1 2 3 Mass_mg 0.00999 0.010648 0.01085 0.010 Elb/hr 7.56E-04 8.10E-04 8.34E-04 0.001 gr/dscf 7.83E-07 9.33E-07 9.73E-07 0.000 lb/mmBtuO2 1.80E-06 2.14E-06 2.22E-06 0.000 mg/dscm 1.79E-03 2.14E-03 2.23E-03 0.002 mg/dscm@7%O2 2.08E-03 2.49E-03 2.58E-03 0.002


### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 164.3 103.5 106 124.600 Elb/hr 1.24E+01 7.87E+00 8.15E+00 9.473 gr/dscf 1.29E-02 9.07E-03 9.51E-03 0.010 lb/mmBtuO2 2.96E-02 2.08E-02 2.17E-02 0.024 mg/dscm 2.95E+01 2.08E+01 2.18E+01 24.033 mg/dscm@7%O2 3.43E+01 2.42E+01 2.52E+01 27.900


### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.09334 0.07414 0.08074 0.083 Elb/hr 7.06E-03 5.64E-03 6.21E-03 0.006 gr/dscf 7.32E-06 6.50E-06 7.24E-06 0.000 lb/mmBtuO2 1.68E-05 1.49E-05 1.65E-05 0.000 mg/dscm 1.67E-02 1.49E-02 1.66E-02 0.016 mg/dscm@7%O2 1.94E-02 1.73E-02 1.92E-02 0.019


### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.07987 0.07227 0.10467 0.086 Elb/hr 6.04E-03 5.50E-03 8.04E-03 0.007 gr/dscf 6.26E-06 6.33E-06 9.39E-06 0.000 lb/mmBtuO2 1.44E-05 1.45E-05 2.14E-05 0.000 mg/dscm 1.43E-02 1.45E-02 2.15E-02 0.017 mg/dscm@7%O2 1.66E-02 1.68E-02 2.49E-02 0.019


### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 0.16586 0.17256 0.21986 0.186 Elb/hr 1.25E-02 1.31E-02 1.69E-02 0.014 gr/dscf 1.30E-05 1.51E-05 1.97E-05 0.000 lb/mmBtuO2 2.99E-05 3.47E-05 4.51E-05 0.000 mg/dscm 2.98E-02 3.46E-02 4.51E-02 0.037 mg/dscm@7%O2 3.47E-02 4.02E-02 5.22E-02 0.042


### Compound: Selenium Average



### Thursday, February 17, 2011 Page 11 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
RunNumber 1 2 3 Mass_mg 0.00255 0.0049 0.0069 0.005 Elb/hr 1.93E-04 3.73E-04 5.30E-04 0.000 gr/dscf 2.00E-07 4.29E-07 6.19E-07 0.000 lb/mmBtuO2 4.59E-07 9.85E-07 1.41E-06 0.000 mg/dscm 4.58E-04 9.83E-04 1.42E-03 0.001 mg/dscm@7%O2 5.33E-04 1.14E-03 1.64E-03 0.001



### Location: Stack Exit - Method 6C Compound: Sulfur Dioxide Average Run 1 2 3 Elb/hr 3.69E+02 3.70E+02 3.66E+02 368.333 lb/mmBtuO2 9.77E-01 9.82E-01 9.83E-01 0.981 mg/dscm 9.55E+02 9.65E+02 9.61E+02 960.333 mg/dscm@7%O2 1.13E+03 1.14E+03 1.14E+03 1,136.667 ppm 3.59E+02 3.62E+02 3.61E+02 360.667 ppm@7%O2 4.26E+02 4.27E+02 4.28E+02 427.000



### Location: Stack Exit - Method 7E Compound: Nitrogen oxides (NOx) Average Run 1 2 3 Elb/hr 1.15E+02 1.17E+02 1.17E+02 116.333 lb/mmBtuO2 3.04E-01 3.10E-01 3.15E-01 0.310 mg/dscm 2.97E+02 3.05E+02 3.08E+02 303.333 mg/dscm@7%O2 3.52E+02 3.60E+02 3.65E+02 359.000 ppm 1.55E+02 1.59E+02 1.61E+02 158.333 ppm@7%O2 1.84E+02 1.87E+02 1.91E+02 187.333



### Location: Stack Exit - OTM - 27/28 

### Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 74.6 73.9 63.3 70.600 Elb/hr 8.31E+00 8.39E+00 7.25E+00 7.983 gr/dscf 9.29E-03 9.42E-03 8.25E-03 0.009 lb/mmBtuO2 2.13E-02 2.15E-02 1.89E-02 0.021 mg/dscm 2.13E+01 2.16E+01 1.89E+01 20.600


### Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 52.5 53.2 50.2 51.967 Elb/hr 5.85E+00 6.04E+00 5.75E+00 5.880 gr/dscf 6.54E-03 6.78E-03 6.54E-03 0.007 lb/mmBtuO2 1.50E-02 1.55E-02 1.50E-02 0.015 mg/dscm 1.50E+01 1.55E+01 1.50E+01 15.167


### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3



### Thursday, February 17, 2011 Page 12 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010

Process Run Data Mass_mg 24.1 46.3 20.9 30.433 Elb/hr 2.68E+00 5.26E+00 2.39E+00 3.443 gr/dscf 3.00E-03 5.90E-03 2.72E-03 0.004 lb/mmBtuO2 6.89E-03 1.35E-02 6.23E-03 0.009 mg/dscm 6.87E+00 1.35E+01 6.23E+00 8.867


### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 40.8 13 15.4 23.067 Elb/hr 4.54E+00 1.48E+00 1.76E+00 2.593 gr/dscf 5.08E-03 1.66E-03 2.01E-03 0.003 lb/mmBtuO2 1.17E-02 3.79E-03 4.59E-03 0.007 mg/dscm 1.16E+01 3.79E+00 4.59E+00 6.660


### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 139.5 133.2 99.6 124.100 Elb/hr 1.55E+01 1.51E+01 1.14E+01 14.000 gr/dscf 1.74E-02 1.70E-02 1.30E-02 0.016 lb/mmBtuO2 3.99E-02 3.88E-02 2.97E-02 0.036 mg/dscm 3.98E+01 3.89E+01 2.97E+01 36.133


### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 117.4 112.5 86.5 105.467 Elb/hr 1.31E+01 1.28E+01 9.91E+00 11.937 gr/dscf 1.46E-02 1.43E-02 1.13E-02 0.013 lb/mmBtuO2 3.36E-02 3.28E-02 2.58E-02 0.031 mg/dscm 3.35E+01 3.28E+01 2.58E+01 30.700



### Thursday, February 17, 2011 Page 13 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010 Process Run Data

APCD Run Data 

### Run Name Value UOM Comments Target Value 1 Residual Oil (No. 6) Burned 2302.5 1000 Gallons Run 1 M26 & 0011 0


### 2 Residual Oil (No. 6) Burned 2305 1000 Gallons Run 2 M26 & 0011 0
3 Residual Oil (No. 6) Burned 2292 1000 Gallons Run 3 M26 & 0011 0
1 Average Heat Input 377.9 MMBtu/hr Run 1 M26 & 0011 0


### 2 Average Heat Input 377 MMBtu/hr Run 2 M26 & 0011 0
3 Average Heat Input 372.2 MMBtu/hr Run 3 M26 & 0011 0
1 Steam Output 313 1000 lb steam/hr Run 1 M26 & 0011 0


### 2 Steam Output 313 1000 lb steam/hr Run 2 M26 & 0011 0
3 Steam Output 313 1000 lb steam/hr Run 3 M26 & 0011 0
4 Residual Oil (No. 6) Burned 2263.6 1000 Gallons Run1 M29 & 30B 0


### 4 Average Heat Input 419.9 MMBtu/hr Run1 M29 & 30B 0
4 Steam Output 313.2 1000 lb steam/hr Run1 M29 & 30B 0
5 Residual Oil (No. 6) Burned 2266.8 1000 Gallons Run 2 M29 & 30B 0


### 5 Average Heat Input 378.5 MMBtu/hr Run 2 M29 & 30B 0
5 Steam Output 313 1000 lb steam/hr Run 2 M29 & 30B 0
6 Residual Oil (No. 6) Burned 2277.6 1000 Gallons Run 3 M29 & 30B 0


### 6 Average Heat Input 375.2 MMBtu/hr Run 3 M29 & 30B 0
6 Steam Output 313 1000 lb steam/hr Run 3 M29 & 30B 0
7 Residual Oil (No. 6) Burned 2194 1000 Gallons Run 1 M30B & OTM 27/28 0

7 Average Heat Input 389.3 MMBtu/hr Run 1 M30B & OTM 27/28 0



### 7 Steam Output 313 1000 lb steam/hr Run 1 M30B & OTM 27/28 0

8 Residual Oil (No. 6) Burned 2263 1000 Gallons Run 2 M30B & OTM 27/28 0



### 8 Average Heat Input 389.8 MMBtu/hr Run 2 M30B & OTM 27/28 0

8 Steam Output 310.9 1000 lb steam/hr Run 2 M30B & OTM 27/28 0



### 9 Residual Oil (No. 6) Burned 2275.4 1000 Gallons Run 3 M30B & OTM 27/28 0

9 Average Heat Input 384.4 MMBtu/hr Run 3 M30B & OTM 27/28 0



### 9 Steam Output 312.9 1000 lb steam/hr Run 3 M30B & OTM 27/28 0

Thursday, February 17, 2011 Page 14 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010

Process Lab Run Data Run Name Value UOM Comments Target Value 1 UNCONTROLLED 0 0



### Run Name Value UOM Comments 1 Fuel Higher Heating Value 0 Btu/lb 

### 1 Fuel Moisture 0 % 1 Fuel Mercury Content 0 ppm 1 Fuel Cadmium Content 0 ppm 

### 1 Ultimate/Proximate Analysis 0 1 Fuel Nickel Content 0 ppm 1 Fuel Arsenic Content 0 ppm 1 Fuel Chromium Content 0 ppm 

### 1 Fuel Beryllium Content 0 ppm 1 Fuel Lead Content 0 ppm 1 Fuel Manganese Content 0 ppm 1 Fuel Chlorine Content 0 ppm 

### 1 Fuel Fluorine Content 0 ppm

Thursday, February 17, 2011 Page 15 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010 Sampling / Stack Data Results Detail



### Location Stack Exit - Method 0011 Average Run Number 1 2 3 Test Date 6/20/2010 6/20/2010 6/21/2010 Run Start Time 10:57:00 AM 10:13:00 AM Run Finish Time 1:18:00 PM 12:30:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 120 120 120 Nozzle Diameter, inches 0.218 0.218 0.218 0.218 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 1.015 1.015 1.015 1.015 Barometric Pressure, inches of Mercury 29.94 29.94 29.93 29.937 Average Orifice Meter Differential, inches H2O 1.74 1.65 1.74 1.710 Dry Gas Meter Volume Sampled, cubic feet 87.155 85.044 85.734 85.978 Average Dry Gas Meter Temperature, °F 106.17 107.75 94.21 102.710 Dry Gas Meter Volume Sampled, dscf 82.906 80.655 83.287 82.283 Total Moisture Liquid collected, g 148.3 145.2 148.8 147.433 Volume of Water Vapor, standard cubic feet 6.98 6.83 7.00 6.937 Moisture Content of Stack Gas, % 7.77 7.81 7.75 7.777 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9223 0.9219 0.9225 0.922 Carbon Dioxide, % 9.838 9.873 9.894 9.868 Oxygen, % 8.942 8.841 8.852 8.878 Carbon Monoxide & Nitrogen, % 81.22 81.286 81.254 81.253 Fuel Factor 1.22 1.22 1.22 Dry Molecular Weight, lb/lb-Mole 29.93 29.93 29.94 29.933 Wet Molecular weight, lb/lb-Mole 29.00 29.00 29.01 29.003 Flue Gas Static Pressure, inches of H2O 0.44 0.44 0.47 0.450 Absolute Flue Gas Pressure, inches of Mercury 29.97 29.97 29.96 29.967 Average Stack Gas Temperature, °F 322.54 324.83 321.38 322.917 Average Velocity Head, inches of H2O 1.0878864115 8817 1.024795672

04965 1.099403240

9173 1.071

Average Stack Gas Velocity, feet/second 71.07 69.08 71.39 70.513 Stack Cross-Sectional Area, square feet 37.631 37.631 37.631 37.631 Dry Volumetric Flow Rate, dry scfm 100,024.9 96,898.4 100,612.7 99,178.667 Actual Wet Volumetric Flue Gas Flow Rate, acfm 160,466.1 155,973.0 161,188.6 159,209.233 Percent Isokinetic of Sampling Rate, % 100.3 100.7 100.1 100.367 Percent Excess Air, % 71.5 70.1 70.3 70.633 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Round Duct Diameter, inches 83.063 83.063 83.063 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



### Thursday, February 17, 2011 Page 16 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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



### Thursday, February 17, 2011 Page 17 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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



### Thursday, February 17, 2011 Page 18 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - Method 26A 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



### Thursday, February 17, 2011 Page 19 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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



### Thursday, February 17, 2011 Page 20 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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



### Thursday, February 17, 2011 Page 21 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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



### Thursday, February 17, 2011 Page 22 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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



### Thursday, February 17, 2011 Page 23 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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



### Thursday, February 17, 2011 Page 24 of 25

### Progress Energy Florida Suwannee River Unit 1

9/3/2010
Location Stack Exit - 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



### Thursday, February 17, 2011 Page 25 of 25