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:

Unit 1 Fossil Fuel Fired Steam Generator Unit No. 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 0 0 0 240 240 2 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 180 0

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit Formaldehyde Method 0011 3 120 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

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.

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

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

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

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

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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

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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

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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

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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

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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

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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

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Process Run Data

APCD Run Data

Run Name Value UOM Comments

Target

Value

1 Residual Oil (No. 6) Burned 2302.5 1000 Gallons 0 Run 1 M26 & 0011

2 Residual Oil (No. 6) Burned 2305 1000 Gallons 0 Run 2 M26 & 0011

3 Residual Oil (No. 6) Burned 2292 1000 Gallons 0 Run 3 M26 & 0011

1 Average Heat Input 377.9 MMBtu/hr 0 Run 1 M26 & 0011

2 Average Heat Input 377 MMBtu/hr 0 Run 2 M26 & 0011

3 Average Heat Input 372.2 MMBtu/hr 0 Run 3 M26 & 0011

1 Steam Output 313 1000 lb steam/hr 0 Run 1 M26 & 0011

2 Steam Output 313 1000 lb steam/hr 0 Run 2 M26 & 0011

3 Steam Output 313 1000 lb steam/hr 0 Run 3 M26 & 0011

4 Residual Oil (No. 6) Burned 2263.6 1000 Gallons 0 Run1 M29 & 30B

4 Average Heat Input 419.9 MMBtu/hr 0 Run1 M29 & 30B

4 Steam Output 313.2 1000 lb steam/hr 0 Run1 M29 & 30B

5 Residual Oil (No. 6) Burned 2266.8 1000 Gallons 0 Run 2 M29 & 30B

5 Average Heat Input 378.5 MMBtu/hr 0 Run 2 M29 & 30B

5 Steam Output 313 1000 lb steam/hr 0 Run 2 M29 & 30B

6 Residual Oil (No. 6) Burned 2277.6 1000 Gallons 0 Run 3 M29 & 30B

6 Average Heat Input 375.2 MMBtu/hr 0 Run 3 M29 & 30B

6 Steam Output 313 1000 lb steam/hr 0 Run 3 M29 & 30B

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