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 Power Plant Unit 2

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 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Facility Information:

Progress Energy Florida, Inc. Suwannee Riv

4037 River Road

Live Oak FL 32060

Contact: Cary W. Hamilton

Phone:

Fax:

Email: cary.hamilton@pgnmail.com

Testing Company:

Kleinfleder Southeast Inc.

6200 Harris Technology Blvd.

Charlotte NC 28269

Contact:W. Quentin Best

Phone: 704-598-1049

Fax: 704-598-1050

Email: qbest@kleinfelder.com

Air Permit Number:

1210003-007-AV

Permitted Source ID/Name:

Suw Unit 2 Fossil Fuel Fired Steam Generator Unit No. 2

Permitted Maximum Process Rate: Max. Normal Operation Process Rate: Target Process Test Rate

Industry/SCC/NAIS 221121 AFS #: 1212100003 FRS #: 110000909214

SCC / Description 10100501 External Combustion Boilers - Electric Generation - Distillate Oil - Grades 1 and 2 

Oil 

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

Regulation Description Compound Limit Unit

ICR % H2O 0 percent(%)

ICR 1,2,3,4,6,7,8-HpCDD 0 ng/dscm corrected

ICR 1,2,3,4,6,7,8-HpCDD 0 lb/million BTU 

using O2

ICR 1,2,3,4,6,7,8-HpCDF 0 ng/dscm corrected

ICR 1,2,3,4,6,7,8-HpCDF 0 lb/million BTU 

using O2

ICR 1,2,3,4,7,8,9-HpCDF 0 ng/dscm corrected

ICR 1,2,3,4,7,8,9-HpCDF 0 lb/million BTU 

using O2

ICR 1,2,3,4,7,8-HxCDD 0 ng/dscm corrected

ICR 1,2,3,4,7,8-HxCDD 0 lb/million BTU 

using O2

ICR 1,2,3,4,7,8-HxCDF 0 ng/dscm corrected

ICR 1,2,3,4,7,8-HxCDF 0 lb/million BTU 

using O2

ICR 1,2,3,6,7,8-HxCDD 0 ng/dscm corrected

ICR 1,2,3,6,7,8-HxCDD 0 lb/million BTU 

using O2

ICR 1,2,3,6,7,8-HxCDF 0 ng/dscm corrected

ICR 1,2,3,6,7,8-HxCDF 0 lb/million BTU 

using O2

ICR 1,2,3,7,8,9-HxCDD 0 ng/dscm corrected

Thursday, February 17, 2011 Page 2 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

ICR 1,2,3,7,8,9-HxCDD 0 lb/million BTU 

using O2

ICR 1,2,3,4,6,7,8-HpCDF 0 ng/dscm corrected

ICR 1,2,3,7,8,9-HxCDF 0 lb/million BTU 

using O2

ICR 1,2,3,7,8-PeCDD 0 ng/dscm corrected

ICR 1,2,3,7,8-PeCDD 0 lb/million BTU 

using O2

ICR 1,2,3,7,8-PeCDF 0 ng/dscm corrected

ICR 1,2,3,7,8-PeCDF 0 lb/million BTU 

using O2

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

(PCB189)

0 ng/dscm corrected

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

(PCB189)

0 lb/million BTU 

using O2

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

HxCB (PCBs156/157)

0 ng/dscm corrected

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

HxCB (PCBs156/157)

0 lb/million BTU 

using O2

ICR 2,3,3',4,4'-PeCB (PCB105) 0 ng/dscm corrected

ICR 2,3,3',4,4'-PeCB (PCB105) 0 lb/million BTU 

using O2

ICR 2,3',4,4',5,5'-HxCB 

(PCB167)

0 ng/dscm corrected

ICR 2,3',4,4',5,5'-HxCB 

(PCB167)

0 lb/million BTU 

using O2

ICR 2,3,4,4',5-PeCB (PCB114) 0 ng/dscm corrected

ICR 2,3,4,4',5-PeCB (PCB114) 0 lb/million BTU 

using O2

ICR 2,3',4,4',5-PeCB (PCB118) 0 ng/dscm corrected

ICR 2,3',4,4',5-PeCB (PCB118) 0 lb/million BTU 

using O2

ICR 2',3,4,4',5-PeCB (PCB123) 0 ng/dscm corrected

ICR 2',3,4,4',5-PeCB (PCB123) 0 lb/million BTU 

using O2

ICR 2,3,4,6,7,8-HxCDF 0 ng/dscm corrected

ICR 2,3,4,6,7,8-HxCDF 0 lb/million BTU 

using O2

ICR 2,3,4,7,8-PeCDF 0 ng/dscm corrected

ICR 2,3,4,7,8-PeCDF 0 lb/million BTU 

using O2

ICR 2,3,7,8-TCDD 0 ng/dscm corrected

ICR 2,3,7,8-TCDD 0 lb/million BTU 

using O2

ICR 2,3,7,8-TCDF 0 ng/dscm corrected

ICR 2,3,7,8-TCDF 0 lb/million BTU 

using O2

ICR 2-Methylnaphthalene 0 ng/dscm corrected

ICR 2-Methylnaphthalene 0 lb/million BTU 

using O2

ICR 3,3',4,4',5,5'-HxCB 

(PCB169)

0 ng/dscm corrected

Thursday, February 17, 2011 Page 3 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

ICR 3,3',4,4',5,5'-HxCB 

(PCB169)

0 lb/million BTU 

using O2

ICR 3,3',4,4',5-PeCB (PCB126) 0 ng/dscm corrected

ICR 3,3',4,4',5-PeCB (PCB126) 0 lb/million BTU 

using O2

ICR 3,3',4,4'-TCB (PCB77) 0 ng/dscm corrected

ICR 3,3',4,4'-TCB (PCB77) 0 lb/million BTU 

using O2

ICR 3,4,4',5-TCB (PCB81) 0 ng/dscm corrected

ICR 3,4,4',5-TCB (PCB81) 0 lb/million BTU 

using O2

ICR Acenaphthene** 0 ug/dscm corrected

ICR Acenaphthene** 0 lb/million BTU 

using O2

ICR Acenaphthylene** 0 ug/dscm corrected

ICR Acenaphthylene** 0 lb/million BTU 

using O2

ICR Anthracene** 0 ug/dscm corrected

ICR Anthracene** 0 lb/million BTU 

using O2

ICR Antimony 0 lb/million BTU 

using O2

ICR Arsenic 0 lb/million BTU 

using O2

ICR Barium 0 lb/million BTU 

using O2

ICR Benzo(a)Anthracene* 0 ug/dscm corrected

ICR Benzo(a)Anthracene* 0 lb/million BTU 

using O2

ICR Benzo(a)Pyrene* 0 ug/dscm corrected

ICR Benzo(a)Pyrene* 0 lb/million BTU 

using O2

ICR Benzo(b)Fluoranthene* 0 ug/dscm corrected

ICR Benzo(b)Fluoranthene* 0 lb/million BTU 

using O2

ICR Benzo(e)Pyrene 0 ug/dscm corrected

ICR Benzo(e)Pyrene 0 lb/million BTU 

using O2

ICR Benzo(ghi)Perylene** 0 ug/dscm corrected

ICR Benzo(ghi)Perylene** 0 lb/million BTU 

using O2

ICR Benzo(k)Fluoranthene* 0 ug/dscm corrected

ICR Benzo(k)Fluoranthene* 0 lb/million BTU 

using O2

ICR Beryllium 0 lb/million BTU 

using O2

ICR Bromine 0 lb/million BTU 

using O2

ICR Cadmium 0 lb/million BTU 

using O2

ICR Carbon Monoxide 0 ppm corrected

ICR Carbon Monoxide 0 lb/million BTU 

using O2

Thursday, February 17, 2011 Page 4 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

ICR Chromium 0 lb/million BTU 

using O2

ICR Chrysene* 0 ug/dscm corrected

ICR Chrysene* 0 lb/million BTU 

using O2

ICR Co2 0 percent(%)

ICR Cobalt 0 lb/million BTU 

using O2

ICR Copper 0 lb/million BTU 

using O2

ICR Dibenzo(a,h)Anthracene* 0 ng/dscm corrected

ICR Dibenzo(a,h)Anthracene* 0 lb/million BTU 

using O2

ICR Filterable Particulate 0 lb/million BTU 

using O2

ICR Filterable PM2.5 0 lb/million BTU 

using O2

ICR Fluoranthene** 0 ug/dscm corrected

ICR Fluoranthene** 0 lb/million BTU 

using O2

ICR Fluorene** 0 ug/dscm corrected

ICR Fluorene** 0 lb/million BTU 

using O2

ICR Formaldehyde 0 ppm corrected

ICR Formaldehyde 0 lb/million BTU 

using O2

ICR Hydrogen Chloride 0 lb/million BTU 

using O2

ICR Hydrogen Fluoride 0 lb/million BTU 

using O2

ICR Indeno(1,2,3-cd)Pyrene* 0 ug/dscm corrected

ICR Indeno(1,2,3-cd)Pyrene* 0 lb/million BTU 

using O2

ICR Inorganic (Aqueous) 

Condensible Part.

0 lb/million BTU 

using O2

ICR Lead 0 lb/million BTU 

using O2

ICR Magnesium 0 lb/million BTU 

using O2

ICR Manganese 0 lb/million BTU 

using O2

ICR Mercury 0 lb/million BTU 

using O2

ICR Naphthalene** 0 ug/dscm corrected

ICR Naphthalene** 0 lb/million BTU 

using O2

ICR Nickel 0 lb/million BTU 

using O2

ICR Nitrogen oxides (NOx) 0 ppm corrected

ICR Nitrogen oxides (NOx) 0 lb/million BTU 

using O2

ICR O2 0 percent(%)

ICR OCDD 0 ng/dscm corrected

Thursday, February 17, 2011 Page 5 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

ICR OCDD 0 lb/million BTU 

using O2

ICR OCDF 0 ng/dscm corrected

ICR OCDF 0 lb/million BTU 

using O2

ICR Organic Condensible 

Particulate

0 lb/million BTU 

using O2

ICR Other Di-CBs 0 ng/dscm corrected

ICR Other Di-CBs 0 lb/million BTU 

using O2

ICR Other Hepta-CBs 0 ng/dscm corrected

ICR Other Hepta-CBs 0 lb/million BTU 

using O2

ICR Other Hexa-CBs 0 ng/dscm corrected

ICR Other Hexa-CBs 0 lb/million BTU 

using O2

ICR Other HpCDD 0 ng/dscm corrected

ICR Other HpCDD 0 lb/million BTU 

using O2

ICR Other HpCDF 0 ng/dscm corrected

ICR Other HpCDF 0 lb/million BTU 

using O2

ICR Other HxCDD 0 ng/dscm corrected

ICR Other HxCDD 0 lb/million BTU 

using O2

ICR Other HxCDF 0 ng/dscm corrected

ICR Other HxCDF 0 lb/million BTU 

using O2

ICR Other Mono-CBs 0 ug/dscm corrected

ICR Other Mono-CBs 0 lb/million BTU 

using O2

ICR Other Nona-CBs 0 ng/dscm corrected

ICR Other Nona-CBs 0 lb/million BTU 

using O2

ICR Other Octa-CBs 0 ng/dscm corrected

ICR Other Octa-CBs 0 lb/million BTU 

using O2

ICR Other PeCDD 0 ng/dscm corrected

ICR Other PeCDD 0 lb/million BTU 

using O2

ICR Other PeCDF 0 ng/dscm corrected

ICR Other PeCDF 0 lb/million BTU 

using O2

ICR Other Penta-CBs 0 ng/dscm corrected

ICR Other Penta-CBs 0 lb/million BTU 

using O2

ICR Other TCDD 0 ng/dscm corrected

ICR Other TCDD 0 lb/million BTU 

using O2

ICR Other TCDF 0 ng/dscm corrected

ICR Other TCDF 0 lb/million BTU 

using O2

Thursday, February 17, 2011 Page 6 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

ICR Other Tetra-CBs 0 ng/dscm corrected

ICR Other Tetra-CBs 0 lb/million BTU 

using O2

ICR Other Tri-CBs 0 ng/dscm corrected

ICR Other Tri-CBs 0 lb/million BTU 

using O2

ICR Perylene 0 ug/dscm corrected

ICR Perylene 0 lb/million BTU 

using O2

ICR Phenanthrene** 0 ug/dscm corrected

ICR Phenanthrene** 0 lb/million BTU 

using O2

ICR Phosphorus (yellow or 

white)

0 lb/million BTU 

using O2

ICR Pyrene** 0 ug/dscm corrected

ICR Pyrene** 0 lb/million BTU 

using O2

ICR Selenium 0 lb/million BTU 

using O2

ICR Silver 0 lb/million BTU 

using O2

ICR Sulfur Dioxide 0 ppm corrected

ICR Sulfur Dioxide 0 lb/million BTU 

using O2

ICR Thallium 0 lb/million BTU 

using O2

ICR Total 16*/**PAH 0 ug/dscm corrected

ICR Total 16*/**PAH 0 lb/million BTU 

using O2

ICR Total 7*PAH 0 ug/dscm corrected

ICR Total 7*PAH 0 lb/million BTU 

using O2

ICR Total Dioxins 0 ng/dscm corrected

ICR Total Dioxins 0 lb/million BTU 

using O2

ICR Total Furans 0 ng/dscm corrected

ICR Total Furans 0 lb/million BTU 

using O2

ICR Total organic compounds 

(TOC) as Propane

0 ppm corrected

ICR Total organic compounds 

(TOC) as Propane

0 lb/million BTU 

using O2

ICR Total PCBs 0 ng/dscm corrected

ICR Total PCBs 0 lb/million BTU 

using O2

ICR Total PM2.5 0 lb/million BTU 

using O2

ICR Total TEQ 0 ng/dscm corrected

ICR Total TEQ 0 lb/million BTU 

using O2

ICR Zinc 0 lb/million BTU 

using O2

ICR Methane 0 ppm corrected

Thursday, February 17, 2011 Page 7 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

Boiler No. 2 (E.U. ID No. -002) is a nominal 34.0 megawatt electric steam generator. The boiler 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. The “onspecification used oil is generally fired as blended fuel oil with either the No.2 fuel oil or No. 6 fuel oil. The boiler 

drives a turbine generator for electrical power and vents to its own stack. There is no air pollution equipment control 

devices associated with the boiler.

Sampling Location Information:

Test Parameter Information:

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 84 0 0 0 900 216 2 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit Formaldehyde Method 0011 3 120 0

Stack Exit 2,3,7,8-TCDD Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDD Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Stack Exit OCDD Method 23 3 480 0

Stack Exit 2,3,7,8-TCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDF Method 23 3 480 0

Stack Exit 2,3,4,7,8-PeCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8,9-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

Stack Exit OCDF Method 23 3 480 0

Stack Exit Other TCDD Method 23 3 480 0

Stack Exit Other PeCDD Method 23 3 480 0

Stack Exit Other HxCDD Method 23 3 480 0

Stack Exit Other HpCDD Method 23 3 480 0

Stack Exit Other TCDF Method 23 3 480 0

Stack Exit Other PeCDF Method 23 3 480 0

Stack Exit Other HxCDF Method 23 3 480 0

Stack Exit Other HpCDF Method 23 3 480 0

Stack Exit Total Dioxins Method 23 3 480 0

ICR Methane 0 lb/million BTU 

using O2

ICR Hydrogen Cyanide 0 lb/million BTU 

using O2

Thursday, February 17, 2011 Page 8 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

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.

Stack Exit Total Furans Method 23 3 480 0

Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0

Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

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

HxCB (PCBs156/157)

Stack Exit Method 23 3 480 0

Stack Exit 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

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

(PCB189)

Stack Exit Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 360 0

Stack Exit Total PM2.5 OTM - 27/28 3 360 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 360 0

Stack Exit Filterable Particulate OTM - 27/28 0

Stack Exit Total Particulate OTM - 27/28 0

Stack Exit Filterable PM2.5 OTM - 27/28 3 360 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Thallium Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Copper Method 29 3 240 0

Stack Exit Silver Method 29 3 240 0

Stack Exit Zinc Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Barium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit Mercury Method 30B 6 120 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 9 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Thursday, February 17, 2011 Page 10 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 2/27/2010 2/28/2010 2/28/2010

Run Start Time 12:55:00 PM 8:58:00 

AM

12:55:00 PM

Run Finish Time 3:13:00 PM 11:15:00 

AM

3:13:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 87.443 86.808 91.373 88.541

Moisture Content of Stack Gas, % 7.43 6.41 5.13 6.323

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

Carbon Dioxide, % 10.31 10.19 10.09 10.197

Oxygen, % 8.04 8.19 8.24 8.157

Average Stack Gas Temperature, °F 332.58 329.33 336.04 332.650

Dry Volumetric Flow Rate, dry scfm 104,043.1 104,141.1 109,696.9 105,960.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 169,280.1 166,070.5 174,036.9 169,795.833

Percent Isokinetic of Sampling Rate, % 99.4 98.6 98.5 98.833

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 11 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Location Stack Exit - Method 23

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 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

Thursday, February 17, 2011 Page 12 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

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

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

Thursday, February 17, 2011 Page 13 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

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

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

Thursday, February 17, 2011 Page 14 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

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 15 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.00414 0.00245 0.00248 0.003

Elb/hr 6.52E-04 3.89E-04 3.94E-04 0.000

gr/dscf 7.31E-07 4.36E-07 4.19E-07 0.000

lb/mmBtuO2 1.56E-06 9.40E-07 9.08E-07 0.000

mg/dscm 1.67E-03 9.97E-04 9.59E-04 0.001

ppm 1.34E-03 7.98E-04 7.68E-04 0.001

ppm@7%O2 1.45E-03 8.73E-04 8.43E-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

lb/mmBtuO2 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 23

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000552 0.00000000361 0.00000000474 0.000

Elb/hr 2.05E-10 1.31E-10 1.71E-10 0.000

lb/mmBtuO2 5.06E-13 3.22E-13 4.43E-13 0.000

ng/dscm 5.66E-04 3.53E-04 4.71E-04 0.000

ng/dscm@7%O2 5.87E-04 3.73E-04 5.13E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000325 0.0000000063 0.0000000129 0.000

Elb/hr 1.20E-10 2.28E-10 4.67E-10 0.000

lb/mmBtuO2 2.98E-13 5.61E-13 1.20E-12 0.000

ng/dscm 3.33E-04 6.16E-04 1.28E-03 0.001

ng/dscm@7%O2 3.45E-04 6.51E-04 1.39E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000479 0.00000000305 0.00000000353 0.000

Elb/hr 1.78E-10 1.10E-10 1.28E-10 0.000

lb/mmBtuO2 4.39E-13 2.72E-13 3.30E-13 0.000

ng/dscm 4.91E-04 2.98E-04 3.51E-04 0.000

ng/dscm@7%O2 5.09E-04 3.15E-04 3.82E-04 0.000

Thursday, February 17, 2011 Page 16 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000451 0.00000000256 0.00000000352 0.000

Elb/hr 1.67E-10 9.27E-11 1.27E-10 0.000

lb/mmBtuO2 4.13E-13 2.28E-13 3.29E-13 0.000

ng/dscm 4.62E-04 2.50E-04 3.50E-04 0.000

ng/dscm@7%O2 4.79E-04 2.64E-04 3.81E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000313 0.00000000228 0.00000000257 0.000

Elb/hr 1.16E-10 8.26E-11 9.30E-11 0.000

lb/mmBtuO2 2.87E-13 2.03E-13 2.40E-13 0.000

ng/dscm 3.21E-04 2.23E-04 2.55E-04 0.000

ng/dscm@7%O2 3.33E-04 2.36E-04 2.78E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000429 0.00000000265 0.00000000324 0.000

Elb/hr 1.59E-10 9.60E-11 1.17E-10 0.000

lb/mmBtuO2 3.93E-13 2.36E-13 3.03E-13 0.000

ng/dscm 4.40E-04 2.59E-04 3.22E-04 0.000

ng/dscm@7%O2 4.56E-04 2.74E-04 3.51E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000278 0.00000000197 0.00000000235 0.000

Elb/hr 1.03E-10 7.13E-11 8.50E-11 0.000

lb/mmBtuO2 2.55E-13 1.76E-13 2.20E-13 0.000

ng/dscm 2.85E-04 1.93E-04 2.34E-04 0.000

ng/dscm@7%O2 2.95E-04 2.04E-04 2.55E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000046 0.00000000322 0.000000004 0.000

Elb/hr 1.71E-10 1.17E-10 1.45E-10 0.000

lb/mmBtuO2 4.21E-13 2.87E-13 3.74E-13 0.000

ng/dscm 4.71E-04 3.15E-04 3.98E-04 0.000

ng/dscm@7%O2 4.88E-04 3.33E-04 4.34E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000367 0.00000000303 0.00000000355 0.000

Elb/hr 1.36E-10 1.10E-10 1.28E-10 0.000

lb/mmBtuO2 3.36E-13 2.70E-13 3.32E-13 0.000

ng/dscm 3.76E-04 2.96E-04 3.53E-04 0.000

ng/dscm@7%O2 3.90E-04 3.13E-04 3.85E-04 0.000

Thursday, February 17, 2011 Page 17 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000037 0.00000000204 0.00000000283 0.000

Elb/hr 1.37E-10 7.39E-11 1.02E-10 0.000

lb/mmBtuO2 3.39E-13 1.82E-13 2.64E-13 0.000

ng/dscm 3.79E-04 1.99E-04 2.81E-04 0.000

ng/dscm@7%O2 3.93E-04 2.10E-04 3.06E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000243 0.00000000185 0.00000000211 0.000

Elb/hr 9.01E-11 6.70E-11 7.63E-11 0.000

lb/mmBtuO2 2.23E-13 1.65E-13 1.97E-13 0.000

ng/dscm 2.49E-04 1.81E-04 2.10E-04 0.000

ng/dscm@7%O2 2.58E-04 1.91E-04 2.29E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000239 0.00000000487 0.00000000432 0.000

Elb/hr 8.86E-11 1.76E-10 1.56E-10 0.000

lb/mmBtuO2 2.19E-13 4.34E-13 4.04E-13 0.000

ng/dscm 2.45E-04 4.76E-04 4.29E-04 0.000

ng/dscm@7%O2 2.54E-04 5.03E-04 4.67E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000531 0.0000000327 0.0000000225 0.000

Elb/hr 1.97E-09 1.18E-09 8.14E-10 0.000

lb/mmBtuO2 4.86E-12 2.91E-12 2.10E-12 0.000

ng/dscm 5.44E-03 3.20E-03 2.24E-03 0.004

ng/dscm@7%O2 5.64E-03 3.38E-03 2.44E-03 0.004

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber 1 2 3

Mass_mg 0.000000187 0.000000126 0.0000000672 0.000

Elb/hr 6.93E-09 4.56E-09 2.43E-09 0.000

lb/mmBtuO2 1.71E-11 1.12E-11 6.28E-12 0.000

ng/dscm 1.92E-02 1.23E-02 6.68E-03 0.013

ng/dscm@7%O2 1.99E-02 1.30E-02 7.28E-03 0.013

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

Average

RunNumber 1 2 3

Mass_mg 0.00000002 0.0000000147 0.00000000812 0.000

Elb/hr 7.41E-10 5.32E-10 2.94E-10 0.000

lb/mmBtuO2 1.83E-12 1.31E-12 7.58E-13 0.000

ng/dscm 2.05E-03 1.44E-03 8.07E-04 0.001

ng/dscm@7%O2 2.12E-03 1.52E-03 8.79E-04 0.002

Thursday, February 17, 2011 Page 18 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000125 0.00000000851 0.00000000628 0.000

Elb/hr 4.63E-10 3.08E-10 2.27E-10 0.000

lb/mmBtuO2 1.15E-12 7.58E-13 5.87E-13 0.000

ng/dscm 1.28E-03 8.32E-04 6.24E-04 0.001

ng/dscm@7%O2 1.33E-03 8.79E-04 6.80E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000518 0.000000338 0.000000182 0.000

Elb/hr 1.92E-08 1.22E-08 6.58E-09 0.000

lb/mmBtuO2 4.74E-11 3.01E-11 1.70E-11 0.000

ng/dscm 5.31E-02 3.30E-02 1.81E-02 0.035

ng/dscm@7%O2 5.50E-02 3.49E-02 1.97E-02 0.037

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000976 0.00000000475 0.00000000413 0.000

Elb/hr 3.62E-10 1.72E-10 1.49E-10 0.000

lb/mmBtuO2 8.94E-13 4.23E-13 3.86E-13 0.000

ng/dscm 1.00E-03 4.64E-04 4.11E-04 0.001

ng/dscm@7%O2 1.04E-03 4.90E-04 4.48E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000274 0.00000000201 0.00000000229 0.000

Elb/hr 1.02E-10 7.28E-11 8.28E-11 0.000

lb/mmBtuO2 2.51E-13 1.79E-13 2.14E-13 0.000

ng/dscm 2.81E-04 1.96E-04 2.28E-04 0.000

ng/dscm@7%O2 2.91E-04 2.07E-04 2.48E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000238 0.00000000175 0.00000000193 0.000

Elb/hr 8.82E-11 6.34E-11 6.98E-11 0.000

lb/mmBtuO2 2.18E-13 1.56E-13 1.80E-13 0.000

ng/dscm 2.44E-04 1.71E-04 1.92E-04 0.000

ng/dscm@7%O2 2.53E-04 1.81E-04 2.09E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000347 0.00000000293 0.00000000304 0.000

Elb/hr 1.29E-10 1.06E-10 1.10E-10 0.000

lb/mmBtuO2 3.18E-13 2.61E-13 2.84E-13 0.000

ng/dscm 3.56E-04 2.86E-04 3.02E-04 0.000

ng/dscm@7%O2 3.69E-04 3.02E-04 3.29E-04 0.000

Thursday, February 17, 2011 Page 19 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000579 0.00000000484 0.00000000152 0.000

Elb/hr 2.15E-10 1.75E-10 5.50E-11 0.000

lb/mmBtuO2 5.30E-13 4.31E-13 1.42E-13 0.000

ng/dscm 5.93E-04 4.73E-04 1.51E-04 0.000

ng/dscm@7%O2 6.15E-04 5.00E-04 1.64E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000501 0.00000000458 0.00000000662 0.000

Elb/hr 1.86E-10 1.66E-10 2.39E-10 0.000

lb/mmBtuO2 4.59E-13 4.08E-13 6.18E-13 0.000

ng/dscm 5.13E-04 4.48E-04 6.58E-04 0.001

ng/dscm@7%O2 5.32E-04 4.74E-04 7.17E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000344 0.00000000629 0.00000000396 0.000

Elb/hr 1.28E-10 2.28E-10 1.43E-10 0.000

lb/mmBtuO2 3.15E-13 5.60E-13 3.70E-13 0.000

ng/dscm 3.52E-04 6.15E-04 3.94E-04 0.000

ng/dscm@7%O2 3.65E-04 6.50E-04 4.29E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000289 0.0000000323 0.0000000236 0.000

Elb/hr 1.07E-09 1.17E-09 8.54E-10 0.000

lb/mmBtuO2 2.65E-12 2.88E-12 2.20E-12 0.000

ng/dscm 2.96E-03 3.16E-03 2.35E-03 0.003

ng/dscm@7%O2 3.07E-03 3.34E-03 2.56E-03 0.003

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000555 0.00000000807 0.0000000082 0.000

Elb/hr 2.06E-10 2.92E-10 2.97E-10 0.000

lb/mmBtuO2 5.08E-13 7.19E-13 7.66E-13 0.000

ng/dscm 5.69E-04 7.89E-04 8.15E-04 0.001

ng/dscm@7%O2 5.90E-04 8.34E-04 8.88E-04 0.001

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000141 0.000000017 0.0000000139 0.000

Elb/hr 5.23E-10 6.16E-10 5.03E-10 0.000

lb/mmBtuO2 1.29E-12 1.51E-12 1.30E-12 0.000

ng/dscm 1.44E-03 1.66E-03 1.38E-03 0.001

ng/dscm@7%O2 1.49E-03 1.75E-03 1.50E-03 0.002

Thursday, February 17, 2011 Page 20 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000867 0.000000113 0.0000000771 0.000

Elb/hr 3.21E-10 4.09E-09 2.79E-09 0.000

lb/mmBtuO2 7.94E-13 1.01E-11 7.20E-12 0.000

ng/dscm 8.88E-04 1.10E-02 7.66E-03 0.007

ng/dscm@7%O2 9.20E-04 1.16E-02 8.34E-03 0.007

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000552 0.00000000361 0.00000000474 0.000

Elb/hr 2.05E-10 1.31E-10 1.71E-10 0.000

lb/mmBtuO2 5.06E-13 3.22E-13 4.43E-13 0.000

ng/dscm 5.66E-04 3.53E-04 4.71E-04 0.000

ng/dscm@7%O2 5.87E-04 3.73E-04 5.13E-04 0.000

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000393 0.0000000111 0.0000000129 0.000

Elb/hr 1.46E-10 4.02E-10 4.67E-10 0.000

lb/mmBtuO2 3.60E-13 9.89E-13 1.20E-12 0.000

ng/dscm 4.03E-04 1.08E-03 1.28E-03 0.001

ng/dscm@7%O2 4.18E-04 1.14E-03 1.39E-03 0.001

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000445 0.00000000279 0.00000000357 0.000

Elb/hr 1.65E-10 1.01E-10 1.29E-10 0.000

lb/mmBtuO2 4.08E-13 2.49E-13 3.33E-13 0.000

ng/dscm 4.56E-04 2.73E-04 3.55E-04 0.000

ng/dscm@7%O2 4.73E-04 2.89E-04 3.87E-04 0.000

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000304 0.00000000227 0.0000000026 0.000

Elb/hr 1.13E-10 8.22E-11 9.41E-11 0.000

lb/mmBtuO2 2.78E-13 2.02E-13 2.43E-13 0.000

ng/dscm 3.11E-04 2.22E-04 2.58E-04 0.000

ng/dscm@7%O2 3.22E-04 2.35E-04 2.81E-04 0.000

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.0000000037 0.00000000204 0.00000000283 0.000

Elb/hr 1.37E-10 7.39E-11 1.02E-10 0.000

lb/mmBtuO2 3.39E-13 1.82E-13 2.64E-13 0.000

ng/dscm 3.79E-04 1.99E-04 2.81E-04 0.000

ng/dscm@7%O2 3.93E-04 2.10E-04 3.06E-04 0.000

Thursday, February 17, 2011 Page 21 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000373 0.0000000084 0.00000000202 0.000

Elb/hr 1.38E-09 3.04E-10 7.31E-11 0.000

lb/mmBtuO2 3.42E-12 7.48E-13 1.89E-13 0.000

ng/dscm 3.82E-03 8.21E-04 2.01E-04 0.002

ng/dscm@7%O2 3.96E-03 8.68E-04 2.19E-04 0.002

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000533 0.00000000353 0.00000000423 0.000

Elb/hr 1.98E-10 1.28E-10 1.53E-10 0.000

lb/mmBtuO2 4.88E-13 3.15E-13 3.95E-13 0.000

ng/dscm 5.46E-04 3.45E-04 4.21E-04 0.000

ng/dscm@7%O2 5.66E-04 3.65E-04 4.59E-04 0.000

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.0000000201 0.0000000125 0.00000000122 0.000

Elb/hr 7.45E-10 4.53E-10 4.41E-11 0.000

lb/mmBtuO2 1.84E-12 1.11E-12 1.14E-13 0.000

ng/dscm 2.06E-03 1.22E-03 1.21E-04 0.001

ng/dscm@7%O2 2.14E-03 1.29E-03 1.32E-04 0.001

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.0000000591 0.00000004245 0.00000003527 0.000

Elb/hr 2.19E-09 1.54E-09 1.28E-09 0.000

lb/mmBtuO2 5.41E-12 3.78E-12 3.29E-12 0.000

ng/dscm 6.06E-03 4.15E-03 3.51E-03 0.005

ng/dscm@7%O2 6.28E-03 4.39E-03 3.82E-03 0.005

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.000000104 0.00000017435 0.00000012397 0.000

Elb/hr 3.86E-09 6.31E-09 4.48E-09 0.000

lb/mmBtuO2 9.53E-12 1.55E-11 1.16E-11 0.000

ng/dscm 1.07E-02 1.70E-02 1.23E-02 0.013

ng/dscm@7%O2 1.11E-02 1.80E-02 1.34E-02 0.014

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 3.12E-01 3.17E-01 2.98E-01 0.309

lb/mmBtuO2 7.85E-04 7.84E-04 7.28E-04 0.001

ppm 4.59E-01 4.53E-01 4.19E-01 0.444

ppm@7%O2 4.96E-01 4.95E-01 4.60E-01 0.484

Thursday, February 17, 2011 Page 22 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 2.82 2.85 2.76 2.810

lb/mmBtuO2 7.40E-04 7.36E-04 7.30E-04 0.001

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.368 0.388 0.318 0.358

lb/mmBtuO2 9.66E-05 1.00E-04 8.41E-05 0.000

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.16005 0.16803 0.183 0.170

lb/mmBtuO2 2.90E-05 2.99E-05 3.35E-05 0.000

Compound: Arsenic

Average

RunNumber 1 3 2

Mass_mg 0.0086 0.0087 0.00857 0.009

lb/mmBtuO2 1.56E-06 1.59E-06 1.52E-06 0.000

Compound: Barium

Average

RunNumber 1 3 2

Mass_mg 0.12922 0.15011 0.12807 0.136

lb/mmBtuO2 2.34E-05 2.75E-05 2.28E-05 0.000

Compound: Beryllium

Average

RunNumber 1 3 2

Mass_mg 0.00023 0.000243 0.000224 0.000

lb/mmBtuO2 4.17E-08 4.45E-08 3.98E-08 0.000

Compound: Cadmium

Average

RunNumber 3 1 2

Mass_mg 0.000859 0.00079 0.001009 0.001

lb/mmBtuO2 1.57E-07 1.43E-07 1.79E-07 0.000

Compound: Chromium

Average

RunNumber 1 3 2

Mass_mg 0.01321 0.01271 0.01431 0.013

lb/mmBtuO2 2.39E-06 2.33E-06 2.54E-06 0.000

Compound: Cobalt

Average

Thursday, February 17, 2011 Page 23 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

RunNumber 1 3 2

Mass_mg 0.0268 0.02789 0.02664 0.027

lb/mmBtuO2 4.85E-06 5.11E-06 4.74E-06 0.000

Compound: Copper

Average

RunNumber 1 3 2

Mass_mg 0.06393 0.07713 0.06563 0.069

lb/mmBtuO2 1.16E-05 1.41E-05 1.17E-05 0.000

Compound: Filterable Particulate

Average

RunNumber 1 3 2

Mass_mg 89.1 96.6 91 92.233

lb/mmBtuO2 1.61E-02 1.77E-02 1.62E-02 0.017

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.16391 0.16901 0.17061 0.168

lb/mmBtuO2 2.97E-05 3.01E-05 3.13E-05 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.16289 0.16488 0.1718 0.167

lb/mmBtuO2 2.95E-05 2.93E-05 3.15E-05 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.05119 0.52909 0.52449 0.368

lb/mmBtuO2 9.27E-06 9.41E-05 9.62E-05 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0067 0.0062 0.0071 0.007

lb/mmBtuO2 1.21E-06 1.10E-06 1.30E-06 0.000

Compound: Silver

Average

RunNumber 1 3 2

Mass_mg 0.0007 0.00047 0.001217 0.001

lb/mmBtuO2 1.27E-07 8.62E-08 2.16E-07 0.000

Compound: Thallium

Average

RunNumber 3 1 2

Mass_mg 0.00026 0.00024 0.000249 0.000

lb/mmBtuO2 4.77E-08 4.35E-08 4.43E-08 0.000

Compound: Zinc

Average

Thursday, February 17, 2011 Page 24 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

RunNumber 1 3 2

Mass_mg 0.9302 1.0489 0.9573 0.979

lb/mmBtuO2 1.68E-04 1.92E-04 1.70E-04 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 3.88E+02 3.99E+02 3.86E+02 391.000

lb/mmBtuO2 9.90E-01 9.94E-01 9.73E-01 0.986

ppm 3.96E+02 3.93E+02 3.81E+02 390.000

ppm@7%O2 4.31E+02 4.33E+02 4.23E+02 429.000

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 1.07E+02 1.11E+02 1.10E+02 109.333

lb/mmBtuO2 2.74E-01 2.77E-01 2.76E-01 0.276

ppm 1.53E+02 1.53E+02 1.51E+02 152.333

ppm@7%O2 1.67E+02 1.69E+02 1.68E+02 168.000

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 82.6 49.2 149.2 93.667

lb/mmBtuO2 2.26E-02 1.22E-02 3.66E-02 0.024

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 74 40.2 124.8 79.667

lb/mmBtuO2 2.03E-02 1.00E-02 3.06E-02 0.020

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 31.3 19.6 47.5 32.800

lb/mmBtuO2 8.58E-03 4.87E-03 1.17E-02 0.008

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 32.7 6 3.7 14.133

lb/mmBtuO2 8.96E-03 1.49E-03 9.09E-04 0.004

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 146.6 74.8 200.4 140.600

lb/mmBtuO2 4.02E-02 1.86E-02 4.92E-02 0.036

Thursday, February 17, 2011 Page 25 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Process Run Data

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 138 65.8 176 126.600

lb/mmBtuO2 3.78E-02 1.64E-02 4.32E-02 0.032

Thursday, February 17, 2011 Page 26 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Distillate Oil (No. 1 & 2) Burned 0 1000 Gallons 0

1 Average Heat Inpt 0 Million Btu/hr 0

1 Average Steam Output 0 1000 lb steam/hr 0

Run Name Value UOM Comments

Target

Value

1 NA 0 0

Run Name Value UOM Comments

1 Ash Content 0 Percent

1 Sulfur Content 0 Percent

1 BTU Content 0 BTU

1 Carbon Content 0 Percent

1 Hyrdrogen Content 0 Precent

1 Nitrogen Content 0 Present

Thursday, February 17, 2011 Page 27 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 2/27/2010 2/28/2010 2/28/2010

Run Start Time 12:55:00 PM 8:58:00 AM 12:55:00 PM

Run Finish Time 3:13:00 PM 11:15:00 AM 3:13:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.223 0.223 0.223 0.223

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.006 1.006 1.006 1.006

Barometric Pressure, inches of Mercury 29.74 29.88 29.88 29.833

Average Orifice Meter Differential, inches H2O 2.01 1.93 2.13 2.023

Dry Gas Meter Volume Sampled, cubic feet 88.114 87.097 92.110 89.107

Average Dry Gas Meter Temperature, °F 74.67 74.75 77.54 75.653

Dry Gas Meter Volume Sampled, dscf 87.443 86.808 91.373 88.541

Total Moisture Liquid collected, g 149.2 126.4 105 126.867

Volume of Water Vapor, standard cubic feet 7.02 5.95 4.94 5.970

Moisture Content of Stack Gas, % 7.43 6.41 5.13 6.323

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

Dry Mole Fraction 0.9257 0.9359 0.9487 0.937

Carbon Dioxide, % 10.31 10.19 10.09 10.197

Oxygen, % 8.04 8.19 8.24 8.157

Carbon Monoxide & Nitrogen, % 81.65 81.62 81.67 81.647

Fuel Factor 1.25 1.25 1.25

Dry Molecular Weight, lb/lb-Mole 29.97 29.96 29.94 29.957

Wet Molecular weight, lb/lb-Mole 29.08 29.19 29.33 29.200

Flue Gas Static Pressure, inches of H2O 1.1 1.2 1.2 1.167

Absolute Flue Gas Pressure, inches of Mercury 29.82 29.97 29.97 29.920

Average Stack Gas Temperature, °F 332.58 329.33 336.04 332.650

Average Velocity Head, inches of H2O 1.1400944386

824

1.111590864

48537

1.216356144

536

1.156

Average Stack Gas Velocity, feet/second 73.31 71.92 75.37 73.533

Stack Cross-Sectional Area, square feet 38.485 38.485 38.485 38.485

Dry Volumetric Flow Rate, dry scfm 104,043.1 104,141.1 109,696.9 105,960.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 169,280.1 166,070.5 174,036.9 169,795.833

Percent Isokinetic of Sampling Rate, % 99.4 98.6 98.5 98.833

Percent Excess Air, % 59.5 61.3 61.9 60.900

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

Round Duct Diameter, inches 84 84 84

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 28 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

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 29 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

9/3/2010

Location Stack Exit - Method 23

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 30 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

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 31 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

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 32 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

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 33 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

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 34 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

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 35 of 36
Progress Energy Florida Suwannee River Power Plant Unit 2

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 36 of 36