Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Tampa Electric Company - Polk Power Station - 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 10, 2011 Page 1 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Facility Information:

Tampa Electric Power Company, Polk Powe

9995 State Route 37 South

Mulberry FL 32060

Contact:

Phone:

Fax:

Email:

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:

1050233-026-AV

Permitted Source ID/Name:

IGCC Unit No. 1

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

Industry/SCC/NAIS 221121 AFS #: 121050233 FRS #: 110000365113

SCC / Description 10101901 External Combustion Boilers - Electric Generation - Coal-based Synfuel - 

All 

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 10, 2011 Page 2 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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 10, 2011 Page 3 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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 10, 2011 Page 4 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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 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

ICR OCDD 0 lb/million BTU 

using O2

Thursday, February 10, 2011 Page 5 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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

ICR Other Tetra-CBs 0 ng/dscm corrected

Thursday, February 10, 2011 Page 6 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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

 process flow diagram:

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 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 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 Methane 0 ppm corrected

ICR Methane 0 lb/million BTU 

using O2

ICR Hydrogen Cyanide 0 lb/million BTU 

using O2

Thursday, February 10, 2011 Page 7 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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

 process flow diagram:

Unit 1 is an integrated coal gasification combined cycle combustion turbine (IGCC), nominal 260 megawatt 

(electric) unit capable of firing coal gasification synthetic gas (syngas) or a limited amount of No. 2 fuel oil. The 

original design maximum heat input at 59 degrees F is 1,755 million Btu per hour when firing syngas and 1,765 

million Btu per hour when firing No. 2 fuel oil. The combustion turbine uses nitrogen diluent injection and syngas 

moisture saturation when firing syngas and water injection when firing No. 2 fuel oil to control NOx (nitrogen oxide) 

emissions. The air separation unit produces nitrogen for use in the IGCC, and oxygen for use in the solid fuel 

gasification system. The nitrogen diluent injection system and syngas moisture saturation controls NOx emissions by 

reducing the flame temperature in the combustion turbine. It also serves a secondary purpose of increasing the fuel 

mass flow of the relatively low heat content syngas in order to increase the power output of the IGCC. The flue gases 

passed from the IGCC through ductwork, heat recovery steam generator (HRSG) and stack to the atmosphere.

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 228 0 0 0 168 456 4 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

Stack Exit Total Furans Method 23 3 480 0

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

Thursday, February 10, 2011 Page 8 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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 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

Stack Exit Other Mono-CBs Method 23 3 480 0

Stack Exit Other Di-CBs Method 23 3 480 0

Stack Exit Other Tri-CBs Method 23 3 480 0

Stack Exit Other Tetra-CBs Method 23 3 480 0

Stack Exit Other Penta-CBs Method 23 3 480 0

Stack Exit Other Hexa-CBs Method 23 3 480 0

Stack Exit Other Hepta-CBs Method 23 3 480 0

Stack Exit Other Octa-CBs Method 23 3 480 0

Stack Exit Other Nona-CBs Method 23 3 480 0

Stack Exit DeCB Method 23 3 480 0

Stack Exit Total PCBs Method 23 3 480 0

Stack Exit Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Stack Exit Hydrogen Fluoride 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

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

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 360 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Antimony 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 Sulfur Dioxide Method 6C 3 180 0

Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0

Thursday, February 10, 2011 Page 9 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Thursday, February 10, 2011 Page 10 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 10:14:00 AM 1:25:00 PM 4:39:00 PM

Run Finish Time 12:39:00 PM 3:50:00 PM 7:00:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 85.425 89.175 88.764 87.788

Moisture Content of Stack Gas, % 6.08 5.59 5.25 5.640

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

Carbon Dioxide, % 8.43 8.42 8.67 8.507

Oxygen, % 11.742 11.823 11.804 11.790

Average Stack Gas Temperature, °F 320.42 323.33 320.29 321.347

Dry Volumetric Flow Rate, dry scfm 848,044.5 851,793.6 857,536.9 852,458.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,333,720.4 1,337,633.1 1,336,612.4 1,335,988.63

3

Percent Isokinetic of Sampling Rate, % 96.2 97.2 98.8 97.400

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 10:14:00 AM 1:24:00 PM 4:39:00 PM

Run Finish Time 12:14:00 PM 3:24:00 PM 6:39:00 PM

Carbon Dioxide, % 8.43 8.42 8.67 8.507

Oxygen, % 11.74 11.82 11.8 11.787

Dry Volumetric Flow Rate, dry scfm 811852 827229 815701 818,260.667

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 5.7 5.6 5 5.433

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 10, 2011 Page 11 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 4/8/2010 4/9/2010 4/12/2010

Run Start Time 1:37:00 AM 2:46:00 PM 3:10:00 PM

Run Finish Time 5:10:00 PM 11:11:00 

PM

11:30:00 PM

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 358.453 361.381 353.939 357.924

Moisture Content of Stack Gas, % 5.94 5.52 5.37 5.610

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

Carbon Dioxide, % 8.74 8.74 8.92 8.800

Oxygen, % 11.82 11.83 11.81 11.820

Average Stack Gas Temperature, °F 321.98 322.56 325.56 323.367

Dry Volumetric Flow Rate, dry scfm 846,456.5 851,337.4 853,386.5 850,393.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,339,504.4 1,337,292.9 1,338,143.5 1,338,313.60

0

Percent Isokinetic of Sampling Rate, % 101.1 97.6 98.1 98.933

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 10:14:00 AM 1:24:00 PM 4:39:00 PM

Run Finish Time 12:14:00 PM 3:24:00 PM 6:39:00 PM

Carbon Dioxide, % 8.43 8.42 8.67 8.507

Oxygen, % 11.74 11.82 11.8 11.787

Dry Volumetric Flow Rate, dry scfm 811852 827229 815701 818,260.667

F-Factor, dscfm/MMBtu @ %O2 0 9780 9780 6,520.000

Moisture, % 5.7 5.6 5 5.433

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Fw 0 10640 10640 7,093.333

Fc 0 1800 1800 1,200.000

Thursday, February 10, 2011 Page 12 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/13/2010

Run Start Time 8:21:00 AM 12:23:00 

PM

4:10:00 PM

Run Finish Time 11:46:00 AM 3:48:00 PM 7:27:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 131.244 135.155 133.904 133.434

Moisture Content of Stack Gas, % 6.08 7.35 6.05 6.493

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

Carbon Dioxide, % 8.99 8.83 8.95 8.923

Oxygen, % 11.82 11.85 11.84 11.837

Average Stack Gas Temperature, °F 325.00 324.83 320.63 323.487

Dry Volumetric Flow Rate, dry scfm 836,812.5 819,796.6 827,209.5 827,939.533

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,321,131.7 1,310,414.3 1,300,887.8 1,310,811.26

7

Percent Isokinetic of Sampling Rate, % 98.9 100.2 98.4 99.167

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 10, 2011 Page 13 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 4/8/2010 4/9/2010 4/12/2010

Run Start Time 9:21:00 AM 9:08:00 

AM

9:11:00 AM

Run Finish Time 1:45:00 PM 1:22:00 PM 1:38:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 171.797 174.691 175.059 173.849

Moisture Content of Stack Gas, % 6.12 6.29 5.96 6.123

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

Carbon Dioxide, % 8.72 8.8 8.92 8.813

Oxygen, % 11.84 11.74 11.76 11.780

Average Stack Gas Temperature, °F 319.54 323.13 329.04 323.903

Dry Volumetric Flow Rate, dry scfm 835,189.3 845,416.5 842,930.0 841,178.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,316,538.6 1,343,927.5 1,335,931.9 1,332,132.66

7

Percent Isokinetic of Sampling Rate, % 98.2 98.7 99.1 98.667

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 10, 2011 Page 14 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - OTM - 27/28

Average

Run Number 1 2 3

Test Date 4/8/2010 4/9/2010 4/14/2010

Run Start Time 9:08:00 

AM

Run Finish Time 3:22:00 PM

Net Run Time, minutes 377.4 360.47 357.46

Dry Gas Meter Volume Sampled, dscf 141.317 135.634 136.169 137.707

Moisture Content of Stack Gas, % 5.90 5.90 5.46 5.753

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

Carbon Dioxide, % 8.73 8.8 8.84 8.790

Oxygen, % 11.86 11.78 11.83 11.823

Average Stack Gas Temperature, °F 324.92 324.25 323.52 324.230

Dry Volumetric Flow Rate, dry scfm 841,184.8 844,610.7 845,260.5 843,685.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,332,019.2 1,338,994.1 1,319,260.4 1,330,091.23

3

Percent Isokinetic of Sampling Rate, % 95.1 95.2 96.3 95.533

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 10, 2011 Page 15 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.0868 0.0587 0.0612 0.069

Elb/hr 1.14E-01 7.42E-02 7.82E-02 0.089

gr/dscf 1.57E-05 1.02E-05 1.06E-05 0.000

lb/mmBtuO2 5.00E-05 3.27E-05 3.42E-05 0.000

mg/dscm 3.59E-02 2.32E-02 2.44E-02 0.028

ppm 2.87E-02 1.86E-02 1.95E-02 0.022

ppm@7%O2 4.36E-02 2.85E-02 2.98E-02 0.034

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 2.97E+01 2.76E+01 2.73E+01 28.200

lb/mmBtuO2 1.36E-02 1.25E-02 1.25E-02 0.013

ppm 8.40E+00 7.66E+00 7.66E+00 7.907

ppm@7%O2 1.27E+01 1.17E+01 1.17E+01 12.033

Location: Stack Exit - Method 23

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000293 0.00000000373 0.00000000329 0.000

Elb/hr 9.15E-10 1.16E-09 1.05E-09 0.000

lb/mmBtuO2 4.06E-13 5.13E-13 4.61E-13 0.000

ng/dscm 2.89E-04 3.65E-04 3.28E-04 0.000

ng/dscm@7%O2 4.42E-04 5.59E-04 5.02E-04 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000179 0.00000000263 0.00000000162 0.000

Elb/hr 5.59E-10 8.20E-10 5.17E-10 0.000

lb/mmBtuO2 2.48E-13 3.62E-13 2.27E-13 0.000

ng/dscm 1.76E-04 2.57E-04 1.62E-04 0.000

ng/dscm@7%O2 2.69E-04 3.94E-04 2.48E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000285 0.00000000335 0.00000000279 0.000

Elb/hr 8.90E-10 1.04E-09 8.90E-10 0.000

lb/mmBtuO2 3.95E-13 4.61E-13 3.91E-13 0.000

ng/dscm 2.81E-04 3.27E-04 2.78E-04 0.000

ng/dscm@7%O2 4.30E-04 5.01E-04 4.25E-04 0.000

Thursday, February 10, 2011 Page 16 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000269 0.00000000237 0.00000000255 0.000

Elb/hr 8.40E-10 7.39E-10 8.13E-10 0.000

lb/mmBtuO2 3.72E-13 3.26E-13 3.57E-13 0.000

ng/dscm 2.65E-04 2.32E-04 2.54E-04 0.000

ng/dscm@7%O2 4.06E-04 3.56E-04 3.88E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000019 0.00000000175 0.00000000159 0.000

Elb/hr 5.93E-10 5.45E-10 5.07E-10 0.000

lb/mmBtuO2 2.63E-13 2.41E-13 2.23E-13 0.000

ng/dscm 1.87E-04 1.71E-04 1.59E-04 0.000

ng/dscm@7%O2 2.86E-04 2.62E-04 2.43E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000269 0.0000000028 0.00000000274 0.000

Elb/hr 8.40E-10 8.73E-10 8.74E-10 0.000

lb/mmBtuO2 3.72E-13 3.85E-13 3.84E-13 0.000

ng/dscm 2.65E-04 2.74E-04 2.73E-04 0.000

ng/dscm@7%O2 4.06E-04 4.20E-04 4.17E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000156 0.0000000014 0.00000000136 0.000

Elb/hr 4.87E-10 4.36E-10 4.34E-10 0.000

lb/mmBtuO2 2.16E-13 1.92E-13 1.90E-13 0.000

ng/dscm 1.54E-04 1.37E-04 1.36E-04 0.000

ng/dscm@7%O2 2.36E-04 2.10E-04 2.08E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000297 0.00000000289 0.00000000296 0.000

Elb/hr 9.28E-10 9.01E-10 9.44E-10 0.000

lb/mmBtuO2 4.11E-13 3.97E-13 4.15E-13 0.000

ng/dscm 2.93E-04 2.82E-04 2.95E-04 0.000

ng/dscm@7%O2 4.49E-04 4.32E-04 4.51E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000236 0.00000000215 0.00000000192 0.000

Elb/hr 7.37E-10 6.70E-10 6.12E-10 0.000

lb/mmBtuO2 3.27E-13 2.96E-13 2.69E-13 0.000

ng/dscm 2.33E-04 2.10E-04 1.92E-04 0.000

ng/dscm@7%O2 3.57E-04 3.22E-04 2.94E-04 0.000

Thursday, February 10, 2011 Page 17 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000333 0.00000000307 0.00000000316 0.000

Elb/hr 1.04E-09 9.57E-10 1.01E-09 0.000

lb/mmBtuO2 4.61E-13 4.22E-13 4.43E-13 0.000

ng/dscm 3.28E-04 3.00E-04 3.15E-04 0.000

ng/dscm@7%O2 5.02E-04 4.60E-04 4.82E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000155 0.00000000186 0.00000000153 0.000

Elb/hr 4.84E-10 5.80E-10 4.88E-10 0.000

lb/mmBtuO2 2.15E-13 2.56E-13 2.14E-13 0.000

ng/dscm 1.53E-04 1.82E-04 1.53E-04 0.000

ng/dscm@7%O2 2.34E-04 2.79E-04 2.34E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000327 0.00000000155 0.00000000285 0.000

Elb/hr 1.02E-09 4.83E-10 9.09E-10 0.000

lb/mmBtuO2 4.53E-13 2.13E-13 3.99E-13 0.000

ng/dscm 3.22E-04 1.51E-04 2.84E-04 0.000

ng/dscm@7%O2 4.93E-04 2.31E-04 4.34E-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 0.00000000565 0.0000000194 0.0000000551 0.000

Elb/hr 1.76E-09 6.05E-09 1.76E-08 0.000

lb/mmBtuO2 7.82E-13 2.67E-12 7.72E-12 0.000

ng/dscm 5.57E-04 1.90E-03 5.50E-03 0.003

ng/dscm@7%O2 8.53E-04 2.91E-03 8.41E-03 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000416 0.0000000608 0.000000174 0.000

Elb/hr 1.30E-08 1.89E-08 5.55E-08 0.000

lb/mmBtuO2 5.76E-12 8.36E-12 2.44E-11 0.000

ng/dscm 4.10E-03 5.94E-03 1.74E-02 0.009

ng/dscm@7%O2 6.28E-03 9.10E-03 2.66E-02 0.014

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000368 0.00000000633 0.0000000174 0.000

Elb/hr 1.15E-09 1.97E-09 5.55E-09 0.000

lb/mmBtuO2 5.10E-13 8.70E-13 2.44E-12 0.000

ng/dscm 3.63E-04 6.19E-04 1.74E-03 0.001

ng/dscm@7%O2 5.56E-04 9.49E-04 2.66E-03 0.001

Thursday, February 10, 2011 Page 18 of 35
Tampa Electric Company - Polk Power Station - Unit #1

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000412 0.00000000414 0.0000000129 0.000

Elb/hr 1.29E-09 1.29E-09 4.11E-09 0.000

lb/mmBtuO2 5.70E-13 5.69E-13 1.81E-12 0.000

ng/dscm 4.06E-04 4.05E-04 1.29E-03 0.001

ng/dscm@7%O2 6.22E-04 6.21E-04 1.97E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.000000107 0.000000147 0.000000633 0.000

Elb/hr 3.34E-08 4.58E-08 2.02E-07 0.000

lb/mmBtuO2 1.48E-11 2.02E-11 8.87E-11 0.000

ng/dscm 1.05E-02 1.44E-02 6.32E-02 0.029

ng/dscm@7%O2 1.61E-02 2.21E-02 9.66E-02 0.045

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000429 0.0000000023 0.00000000911 0.000

Elb/hr 1.34E-09 7.17E-10 2.91E-09 0.000

lb/mmBtuO2 5.94E-13 3.16E-13 1.28E-12 0.000

ng/dscm 4.23E-04 2.25E-04 9.09E-04 0.001

ng/dscm@7%O2 6.48E-04 3.45E-04 1.39E-03 0.001

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000203 0.00000000213 0.00000000192 0.000

Elb/hr 6.34E-10 6.64E-10 6.12E-10 0.000

lb/mmBtuO2 2.81E-13 2.93E-13 2.69E-13 0.000

ng/dscm 2.00E-04 2.08E-04 1.92E-04 0.000

ng/dscm@7%O2 3.06E-04 3.19E-04 2.94E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.0000000015 0.00000000192 0.0000000016 0.000

Elb/hr 4.69E-10 5.98E-10 5.10E-10 0.000

lb/mmBtuO2 2.08E-13 2.64E-13 2.24E-13 0.000

ng/dscm 1.48E-04 1.88E-04 1.60E-04 0.000

ng/dscm@7%O2 2.27E-04 2.88E-04 2.45E-04 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 2 1 3

Mass_mg 0.0000000033 0.00000000287 0.0000000033 0.000

Elb/hr 1.03E-09 8.96E-10 1.05E-09 0.000

lb/mmBtuO2 4.54E-13 3.97E-13 4.62E-13 0.000

ng/dscm 3.23E-04 2.83E-04 3.29E-04 0.000

ng/dscm@7%O2 4.95E-04 4.33E-04 5.03E-04 0.000

Thursday, February 10, 2011 Page 19 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Compound: 2,3,7,8-TCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000151 0.00000000132 0.00000000267 0.000

Elb/hr 4.72E-10 4.11E-10 8.52E-10 0.000

lb/mmBtuO2 2.09E-13 1.81E-13 3.74E-13 0.000

ng/dscm 1.49E-04 1.29E-04 2.66E-04 0.000

ng/dscm@7%O2 2.28E-04 1.98E-04 4.07E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000452 0.0000000018 0.00000000311 0.000

Elb/hr 1.41E-09 5.61E-10 9.92E-10 0.000

lb/mmBtuO2 6.26E-13 2.47E-13 4.36E-13 0.000

ng/dscm 4.45E-04 1.76E-04 3.10E-04 0.000

ng/dscm@7%O2 6.81E-04 2.70E-04 4.74E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000411 0.00000000189 0.00000000247 0.000

Elb/hr 1.28E-09 5.89E-10 7.88E-10 0.000

lb/mmBtuO2 5.69E-13 2.60E-13 3.46E-13 0.000

ng/dscm 4.05E-04 1.85E-04 2.46E-04 0.000

ng/dscm@7%O2 6.20E-04 2.84E-04 3.76E-04 0.000

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

Average

RunNumber 1 2 3

Mass_mg 0.00000002 0.0000000165 0.0000000345 0.000

Elb/hr 6.25E-09 5.14E-09 1.10E-08 0.000

lb/mmBtuO2 2.77E-12 2.27E-12 4.83E-12 0.000

ng/dscm 1.97E-03 1.61E-03 3.44E-03 0.002

ng/dscm@7%O2 3.02E-03 2.47E-03 5.26E-03 0.004

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

Average

RunNumber 1 2 3

Mass_mg 0.00000000435 0.00000000194 0.00000000334 0.000

Elb/hr 1.36E-09 6.05E-10 1.07E-09 0.000

lb/mmBtuO2 6.02E-13 2.67E-13 4.68E-13 0.000

ng/dscm 4.29E-04 1.90E-04 3.33E-04 0.000

ng/dscm@7%O2 6.57E-04 2.91E-04 5.09E-04 0.000

Compound: DeCB

Average

RunNumber 1 2 3

Mass_mg 0.000000004 0.00000000934 0.00000000328 0.000

Elb/hr 1.25E-09 2.91E-09 1.05E-09 0.000

lb/mmBtuO2 5.54E-13 1.28E-12 4.59E-13 0.000

ng/dscm 3.94E-04 9.13E-04 3.27E-04 0.001

ng/dscm@7%O2 6.03E-04 1.40E-03 5.00E-04 0.001

Thursday, February 10, 2011 Page 20 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Compound: OCDD

Average

RunNumber 1 2 3

Mass_mg 0.000000011 0.0000000189 0.0000000209 0.000

Elb/hr 3.44E-09 5.89E-09 6.67E-09 0.000

lb/mmBtuO2 1.52E-12 2.60E-12 2.93E-12 0.000

ng/dscm 1.08E-03 1.85E-03 2.09E-03 0.002

ng/dscm@7%O2 1.65E-03 2.84E-03 3.20E-03 0.003

Compound: OCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000425 0.00000000551 0.00000000416 0.000

Elb/hr 1.33E-09 1.72E-09 1.33E-09 0.000

lb/mmBtuO2 5.88E-13 7.58E-13 5.83E-13 0.000

ng/dscm 4.19E-04 5.39E-04 4.15E-04 0.000

ng/dscm@7%O2 6.41E-04 8.26E-04 6.35E-04 0.001

Compound: Other Di-CBs

Average

RunNumber 1 2 3

Mass_mg 0.0000197 0.00000246 0.0000047 0.000

Elb/hr 6.15E-06 7.67E-07 1.50E-06 0.000

lb/mmBtuO2 2.73E-09 3.38E-10 6.58E-10 0.000

ng/dscm 1.94E+00 2.40E-01 4.69E-01 0.883

ng/dscm@7%O2 2.97E+00 3.68E-01 7.17E-01 1.352

Compound: Other Hepta-CBs

Average

RunNumber 1 2 3

Mass_mg 0.000000106 0.000000247 0.000000294 0.000

Elb/hr 3.31E-08 7.70E-08 9.38E-08 0.000

lb/mmBtuO2 1.47E-11 3.40E-11 4.12E-11 0.000

ng/dscm 1.04E-02 2.41E-02 2.93E-02 0.021

ng/dscm@7%O2 1.59E-02 3.69E-02 4.48E-02 0.033

Compound: Other Hexa-CBs

Average

RunNumber 1 2 3

Mass_mg 0.000000304 0.000000584 0.00000121 0.000

Elb/hr 9.50E-08 1.82E-07 3.86E-07 0.000

lb/mmBtuO2 4.21E-11 8.03E-11 1.69E-10 0.000

ng/dscm 3.00E-02 5.71E-02 1.21E-01 0.069

ng/dscm@7%O2 4.59E-02 8.75E-02 1.85E-01 0.106

Compound: Other HpCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000293 0.00000000373 0.00000000329 0.000

Elb/hr 9.15E-10 1.16E-09 1.05E-09 0.000

lb/mmBtuO2 4.06E-13 5.13E-13 4.61E-13 0.000

ng/dscm 2.89E-04 3.65E-04 3.28E-04 0.000

ng/dscm@7%O2 4.42E-04 5.59E-04 5.02E-04 0.001

Thursday, February 10, 2011 Page 21 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Compound: Other HpCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000227 0.00000000263 0.0000000021 0.000

Elb/hr 7.09E-10 8.20E-10 6.70E-10 0.000

lb/mmBtuO2 3.14E-13 3.62E-13 2.94E-13 0.000

ng/dscm 2.24E-04 2.57E-04 2.10E-04 0.000

ng/dscm@7%O2 3.43E-04 3.94E-04 3.21E-04 0.000

Compound: Other HxCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000278 0.00000000268 0.00000000274 0.000

Elb/hr 8.68E-10 8.35E-10 8.74E-10 0.000

lb/mmBtuO2 3.85E-13 3.68E-13 3.84E-13 0.000

ng/dscm 2.74E-04 2.62E-04 2.73E-04 0.000

ng/dscm@7%O2 4.19E-04 4.02E-04 4.17E-04 0.000

Compound: Other HxCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000193 0.00000000182 0.00000000167 0.000

Elb/hr 6.03E-10 5.67E-10 5.33E-10 0.000

lb/mmBtuO2 2.67E-13 2.50E-13 2.34E-13 0.000

ng/dscm 1.90E-04 1.78E-04 1.67E-04 0.000

ng/dscm@7%O2 2.91E-04 2.73E-04 2.55E-04 0.000

Compound: Other Mono-CBs

Average

RunNumber 1 2 3

Mass_mg 0.00000138 0.00000114 0.000000496 0.000

Elb/hr 4.31E-07 3.55E-07 1.58E-07 0.000

lb/mmBtuO2 1.91E-10 1.57E-10 6.95E-11 0.000

ng/dscm 1.36E-01 1.11E-01 4.95E-02 0.099

ng/dscm@7%O2 2.08E-01 1.70E-01 7.57E-02 0.151

Compound: Other Nona-CBs

Average

RunNumber 1 2 3

Mass_mg 0.00000000569 0.00000000795 0.00000000508 0.000

Elb/hr 1.78E-09 2.48E-09 1.62E-09 0.000

lb/mmBtuO2 7.88E-13 1.09E-12 7.12E-13 0.000

ng/dscm 5.61E-04 7.77E-04 5.07E-04 0.001

ng/dscm@7%O2 8.59E-04 1.19E-03 7.75E-04 0.001

Compound: Other Octa-CBs

Average

RunNumber 1 2 3

Mass_mg 0.00000000352 0.0000000536 0.0000000438 0.000

Elb/hr 1.10E-09 1.67E-08 1.40E-08 0.000

lb/mmBtuO2 4.87E-13 7.37E-12 6.13E-12 0.000

ng/dscm 3.47E-04 5.24E-03 4.37E-03 0.003

ng/dscm@7%O2 5.31E-04 8.03E-03 6.68E-03 0.005

Thursday, February 10, 2011 Page 22 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Compound: Other PeCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000333 0.00000000307 0.00000000316 0.000

Elb/hr 1.04E-09 9.57E-10 1.01E-09 0.000

lb/mmBtuO2 4.61E-13 4.22E-13 4.43E-13 0.000

ng/dscm 3.28E-04 3.00E-04 3.15E-04 0.000

ng/dscm@7%O2 5.02E-04 4.60E-04 4.82E-04 0.000

Compound: Other PeCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000153 0.00000000189 0.00000000156 0.000

Elb/hr 4.78E-10 5.89E-10 4.98E-10 0.000

lb/mmBtuO2 2.12E-13 2.60E-13 2.19E-13 0.000

ng/dscm 1.51E-04 1.85E-04 1.56E-04 0.000

ng/dscm@7%O2 2.31E-04 2.84E-04 2.39E-04 0.000

Compound: Other Penta-CBs

Average

RunNumber 1 2 3

Mass_mg 0.000000872 0.000000962 0.00000267 0.000

Elb/hr 2.72E-07 3.00E-07 8.52E-07 0.000

lb/mmBtuO2 1.21E-10 1.32E-10 3.74E-10 0.000

ng/dscm 8.59E-02 9.40E-02 2.66E-01 0.149

ng/dscm@7%O2 1.31E-01 1.44E-01 4.07E-01 0.227

Compound: Other TCDD

Average

RunNumber 1 2 3

Mass_mg 0.00000000287 0.0000000033 0.0000000033 0.000

Elb/hr 8.96E-10 1.03E-09 1.05E-09 0.000

lb/mmBtuO2 3.97E-13 4.54E-13 4.62E-13 0.000

ng/dscm 2.83E-04 3.23E-04 3.29E-04 0.000

ng/dscm@7%O2 4.33E-04 4.95E-04 5.03E-04 0.000

Compound: Other TCDF

Average

RunNumber 1 2 3

Mass_mg 0.00000000151 0.00000000132 0.00000000968 0.000

Elb/hr 4.72E-10 4.11E-10 3.09E-09 0.000

lb/mmBtuO2 2.09E-13 1.81E-13 1.36E-12 0.000

ng/dscm 1.49E-04 1.29E-04 9.66E-04 0.000

ng/dscm@7%O2 2.28E-04 1.98E-04 1.48E-03 0.001

Compound: Other Tetra-CBs

Average

RunNumber 1 2 3

Mass_mg 0.00000238 0.00000191 0.00000266 0.000

Elb/hr 7.43E-07 5.95E-07 8.48E-07 0.000

lb/mmBtuO2 3.30E-10 2.63E-10 3.73E-10 0.000

ng/dscm 2.35E-01 1.87E-01 2.65E-01 0.229

ng/dscm@7%O2 3.60E-01 2.87E-01 4.05E-01 0.351

Thursday, February 10, 2011 Page 23 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Compound: Other Tri-CBs

Average

RunNumber 1 2 3

Mass_mg 0.00000343 0.00000197 0.00000256 0.000

Elb/hr 1.07E-06 6.14E-07 8.16E-07 0.000

lb/mmBtuO2 4.75E-10 2.71E-10 3.59E-10 0.000

ng/dscm 3.38E-01 1.93E-01 2.55E-01 0.262

ng/dscm@7%O2 5.17E-01 2.96E-01 3.90E-01 0.401

Compound: Total Dioxins

Average

RunNumber 1 2 3

Mass_mg 0.00000002848 0.00000003706 0.0000000389 0.000

Elb/hr 8.90E-09 1.15E-08 1.24E-08 0.000

lb/mmBtuO2 3.94E-12 5.10E-12 5.45E-12 0.000

ng/dscm 2.81E-03 3.62E-03 3.88E-03 0.003

ng/dscm@7%O2 4.30E-03 5.55E-03 5.93E-03 0.005

Compound: Total Furans

Average

RunNumber 1 2 3

Mass_mg 0.0000000213 0.00000002402 0.00000002116 0.000

Elb/hr 6.65E-09 7.49E-09 6.75E-09 0.000

lb/mmBtuO2 2.95E-12 3.30E-12 2.96E-12 0.000

ng/dscm 2.10E-03 2.35E-03 2.11E-03 0.002

ng/dscm@7%O2 3.21E-03 3.60E-03 3.23E-03 0.003

Compound: Total PCBs

Average

RunNumber 1 2 3

Mass_mg 0.0000282 0.00000934 0.0000146 0.000

Elb/hr 8.81E-06 2.91E-06 4.66E-06 0.000

lb/mmBtuO2 3.90E-09 1.28E-09 2.04E-09 0.000

ng/dscm 2.78E+00 9.13E-01 1.46E+00 1.718

ng/dscm@7%O2 4.26E+00 1.40E+00 2.23E+00 2.630

Compound: Total TEQ

Average

RunNumber 1 2 3

Mass_mg 0.00000000723 0.00000000769 0.00000000763 0.000

Elb/hr 2.26E-09 2.40E-09 2.43E-09 0.000

lb/mmBtuO2 1.00E-12 1.06E-12 1.07E-12 0.000

ng/dscm 7.12E-04 7.52E-04 7.61E-04 0.001

ng/dscm@7%O2 1.09E-03 1.15E-03 1.16E-03 0.001

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 0.00E+00 2.84E-03 5.94E-01 0.199

lb/mmBtuO2 0.00E+00 1.29E-06 2.73E-04 0.000

ppm 0.00E+00 5.00E-04 1.06E-01 0.036

ppm@7%O2 0.00E+00 7.65E-04 1.62E-01 0.054

Thursday, February 10, 2011 Page 24 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.21 0.217 0.227 0.218

lb/mmBtuO2 7.94E-05 7.99E-05 8.43E-05 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.215 0.223 0.232 0.223

lb/mmBtuO2 8.13E-05 8.22E-05 8.62E-05 0.000

Location: Stack Exit - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000917 0.000254 0.000235 0.000

Elb/hr 5.90E-04 1.63E-04 1.50E-04 0.000

gr/dscf 8.24E-08 2.24E-08 2.07E-08 0.000

lb/mmBtuO2 2.65E-07 7.15E-08 6.62E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.002719 0.00326 0.00223 0.003

Elb/hr 1.75E-03 2.09E-03 1.42E-03 0.002

gr/dscf 2.44E-07 2.88E-07 1.97E-07 0.000

lb/mmBtuO2 7.87E-07 9.18E-07 6.28E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00005 0.00005 0.00005 0.000

Elb/hr 3.22E-05 3.20E-05 3.18E-05 0.000

gr/dscf 4.49E-09 4.42E-09 4.41E-09 0.000

lb/mmBtuO2 1.45E-08 1.41E-08 1.41E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000364 0.0002 0.0002 0.000

Elb/hr 2.34E-04 1.28E-04 1.27E-04 0.000

gr/dscf 3.27E-08 1.77E-08 1.76E-08 0.000

lb/mmBtuO2 1.05E-07 5.63E-08 5.63E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.003014 0.002574 0.000588 0.002

Elb/hr 1.94E-03 1.65E-03 3.75E-04 0.001

gr/dscf 2.71E-07 2.27E-07 5.18E-08 0.000

Thursday, February 10, 2011 Page 25 of 35
Tampa Electric Company - Polk Power Station - Unit #1

lb/mmBtuO2 8.73E-07 7.25E-07 1.66E-07 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.000406 0.000214 0.0002 0.000

Elb/hr 2.61E-04 1.37E-04 1.27E-04 0.000

gr/dscf 3.65E-08 1.89E-08 1.76E-08 0.000

lb/mmBtuO2 1.18E-07 6.03E-08 5.63E-08 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 5.8 7.1 1.1 4.667

Elb/hr 3.73E+00 4.55E+00 7.01E-01 2.994

gr/dscf 5.21E-04 6.27E-04 9.70E-05 0.000

lb/mmBtuO2 1.68E-03 2.00E-03 3.10E-04 0.001

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.085389 0.013689 0.006049 0.035

Elb/hr 5.49E-02 8.76E-03 3.85E-03 0.023

gr/dscf 7.67E-06 1.21E-06 5.33E-07 0.000

lb/mmBtuO2 2.47E-05 3.86E-06 1.70E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.002136 0.000797 0.00154 0.001

Elb/hr 1.37E-03 5.10E-04 9.81E-04 0.001

gr/dscf 1.92E-07 7.04E-08 1.36E-07 0.000

lb/mmBtuO2 6.18E-07 2.24E-07 4.34E-07 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.011324 0.010054 0.002784 0.008

Elb/hr 7.28E-03 6.44E-03 1.77E-03 0.005

gr/dscf 1.02E-06 8.88E-07 2.45E-07 0.000

lb/mmBtuO2 3.28E-06 2.83E-06 7.84E-07 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0271 0.0426 0.02225 0.031

Elb/hr 1.74E-02 2.73E-02 1.42E-02 0.020

gr/dscf 2.43E-06 3.76E-06 1.96E-06 0.000

lb/mmBtuO2 7.85E-06 1.20E-05 6.27E-06 0.000

Location: Stack Exit - OTM - 27/28

Compound: Filterable PM2.5

Average

Thursday, February 10, 2011 Page 26 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Process Run Data

RunNumber 1 2 3

Mass_mg 10.7 9.75 10.9 10.450

lb/mmBtuO2 3.77E-03 3.55E-03 3.98E-03 0.004

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 24 30 36.5 30.167

lb/mmBtuO2 8.47E-03 1.09E-02 1.33E-02 0.011

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 4.2 1.8 9.6 5.200

lb/mmBtuO2 1.48E-03 6.56E-04 3.50E-03 0.002

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 38.9 41.55 57 45.817

lb/mmBtuO2 1.37E-02 1.51E-02 2.08E-02 0.017

Thursday, February 10, 2011 Page 27 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Average Heat Inpt 0 Million Btu/hr 0

1 Average Steam Output 0 1000 lb steam/hr 0

1 0/million BTU using O2 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 10, 2011 Page 28 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 10:14:00 AM 1:25:00 PM 4:39:00 PM

Run Finish Time 12:39:00 PM 3:50:00 PM 7:00:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.213 0.216 0.213 0.214

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 30 30 30 30.000

Average Orifice Meter Differential, inches H2O 1.78 1.95 1.94 1.890

Dry Gas Meter Volume Sampled, cubic feet 85.467 90.970 92.595 89.677

Average Dry Gas Meter Temperature, °F 79.96 90.79 103.21 91.320

Dry Gas Meter Volume Sampled, dscf 85.425 89.175 88.764 87.788

Total Moisture Liquid collected, g 117.5 112.2 104.5 111.400

Volume of Water Vapor, standard cubic feet 5.53 5.28 4.92 5.243

Moisture Content of Stack Gas, % 6.08 5.59 5.25 5.640

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

Dry Mole Fraction 0.9392 0.9441 0.9475 0.944

Carbon Dioxide, % 8.43 8.42 8.67 8.507

Oxygen, % 11.742 11.823 11.804 11.790

Carbon Monoxide & Nitrogen, % 79.828 79.757 79.526 79.704

Fuel Factor 1.09 1.08 1.05

Dry Molecular Weight, lb/lb-Mole 29.82 29.82 29.86 29.833

Wet Molecular weight, lb/lb-Mole 29.10 29.16 29.24 29.167

Flue Gas Static Pressure, inches of H2O -0.84 -0.84 -0.84 -0.840

Absolute Flue Gas Pressure, inches of Mercury 29.94 29.94 29.94 29.940

Average Stack Gas Temperature, °F 320.42 323.33 320.29 321.347

Average Velocity Head, inches of H2O 1.3307550131

3712

1.336380274

66606

1.343147919

78855

1.337

Average Stack Gas Velocity, feet/second 78.40 78.63 78.57 78.533

Stack Cross-Sectional Area, square feet 283.529 283.529 283.529 283.529

Dry Volumetric Flow Rate, dry scfm 848,044.5 851,793.6 857,536.9 852,458.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,333,720.4 1,337,633.1 1,336,612.4 1,335,988.6

33

Percent Isokinetic of Sampling Rate, % 96.2 97.2 98.8 97.400

Percent Excess Air, % 125.8 128.1 128.4 127.433

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 228 228 228

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 10, 2011 Page 29 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 10:14:00 AM 1:24:00 PM 4:39:00 PM

Run Finish Time 12:14:00 PM 3:24:00 PM 6:39:00 PM

Carbon Dioxide, % 8.43 8.42 8.67 8.507

Oxygen, % 11.74 11.82 11.8 11.787

Fuel Factor 1.09 1.08 1.05

Dry Volumetric Flow Rate, dry scfm 811852 827229 815701 818,260.667

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 5.7 5.6 5 5.433

Analyzer Make Teledyne Teledyne Teledyne

Analyzer Model 300E 300E 300E

Analyzer Serial Number 2369 2369 2369 2,369.000

Operating Range 28.9 28.9 28.9 28.900

Operating Units ppm ppm ppm

No. Readings/Avg. 0 0 0 0.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID CC201341 CC201341 CC201341

Calibration Pre Zero Cylinder Instrument Response 0.26 0.416 0.333 0.336

Calibration Pre Zero Cylinder Bias 0.89 1.43 1.14 1.153

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC42990 CC42990 CC42990

Calibration Pre High Cylinder Instrument Response 15.936 15.868 15.859 15.888

Calibration Pre High Cylinder Bias 0.44 0.21 0.18 0.277

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC201341 CC201341 CC201341

Calibration Post Zero Cylinder Instrument Response 0.416 0.333 0.22 0.323

Calibration Post Zero Cylinder Bias 1.43 1.14 0.75 1.107

Calibration Post Zero Cylinder Drift 0.54 1.15 0.39 0.693

Calibration Post High Cylinder ID CC42990 CC42990 CC42990

Calibration Post High Cylinder Instrument Response 15.868 15.859 15.818 15.848

Calibration Post High Cylinder Bias 0.21 0.18 0.03 0.140

Calibration Post High Cylinder Drift 0.23 0.18 0.15 0.187

Cavg 8.507 7.788 7.727 8.007

Cavg Units ppmvd ppmvd ppmvd

Cgas 8.3978 7.6581 7.6602 7.905

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 10, 2011 Page 30 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - Method 23

Average

Run Number 1 2 3

Test Date 4/8/2010 4/9/2010 4/12/2010

Run Start Time 1:37:00 AM 2:46:00 PM 3:10:00 PM

Run Finish Time 5:10:00 PM 11:11:00 PM 11:30:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.213 0.217 0.214 0.215

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 29.83 29.94 30.06 29.943

Average Orifice Meter Differential, inches H2O 1.88 2.00 1.92 1.933

Dry Gas Meter Volume Sampled, cubic feet 362.036 368.870 357.075 362.660

Average Dry Gas Meter Temperature, °F 82.15 90.08 85.75 85.993

Dry Gas Meter Volume Sampled, dscf 358.453 361.381 353.939 357.924

Total Moisture Liquid collected, g 481 448.9 427.1 452.333

Volume of Water Vapor, standard cubic feet 22.64 21.13 20.10 21.290

Moisture Content of Stack Gas, % 5.94 5.52 5.37 5.610

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

Dry Mole Fraction 0.9406 0.9448 0.9463 0.944

Carbon Dioxide, % 8.74 8.74 8.92 8.800

Oxygen, % 11.82 11.83 11.81 11.820

Carbon Monoxide & Nitrogen, % 79.44 79.43 79.27 79.380

Fuel Factor 1.04 1.04 1.02

Dry Molecular Weight, lb/lb-Mole 29.87 29.87 29.90 29.880

Wet Molecular weight, lb/lb-Mole 29.16 29.21 29.26 29.210

Flue Gas Static Pressure, inches of H2O -0.84 -0.82 -0.84 -0.833

Absolute Flue Gas Pressure, inches of Mercury 29.77 29.88 30.00 29.883

Average Stack Gas Temperature, °F 321.98 322.56 325.56 323.367

Average Velocity Head, inches of H2O 1.3347307475

2372

1.336560367

63432

1.340819795

11873

1.337

Average Stack Gas Velocity, feet/second 78.74 78.61 78.66 78.670

Stack Cross-Sectional Area, square feet 283.529 283.529 283.529 283.529

Dry Volumetric Flow Rate, dry scfm 846,456.5 851,337.4 853,386.5 850,393.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,339,504.4 1,337,292.9 1,338,143.5 1,338,313.6

00

Percent Isokinetic of Sampling Rate, % 101.1 97.6 98.1 98.933

Percent Excess Air, % 129.1 129.4 129.5 129.333

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 228 228 228

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 10, 2011 Page 31 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 4/7/2010 4/7/2010 4/7/2010

Run Start Time 10:14:00 AM 1:24:00 PM 4:39:00 PM

Run Finish Time 12:14:00 PM 3:24:00 PM 6:39:00 PM

Carbon Dioxide, % 8.43 8.42 8.67 8.507

Oxygen, % 11.74 11.82 11.8 11.787

Fuel Factor 1.09 1.08 1.05

Dry Volumetric Flow Rate, dry scfm 811852 827229 815701 818,260.667

F-Factor, dscfm/MMBtu @ %O2 0 9780 9780 6,520.000

Moisture, % 5.7 5.6 5 5.433

Analyzer Make California California California

Analyzer Model 300-HFID CE 300-FFID 

CE

300-HFID-CE

Analyzer Serial Number 4M08005 4M08005 4M08005

Operating Range 0 30 30 20.000

Operating Units ppm ppm ppm

No. Readings/Avg. 0 0 0 0.000

Calibration Set 3 3 3 3.000

Calibration Pre Zero Cylinder ID SX19928 SX19928 SX19928

Calibration Pre Zero Cylinder Instrument Response 0.008 0.004 0.008 0.007

Calibration Pre Zero Cylinder Bias 0.01 -0.01 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC51105 CC51105 CC51105

Calibration Pre High Cylinder Instrument Response 14.394 15.808 14.394 14.865

Calibration Pre High Cylinder Bias 0 4.71 0 1.570

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID SX19928 SX19928 SX19928

Calibration Post Zero Cylinder Instrument Response -0.007 0.155 0.016 0.055

Calibration Post Zero Cylinder Bias -0.05 0.49 0.03 0.157

Calibration Post Zero Cylinder Drift 0.06 0.5 0.03 0.197

Calibration Post High Cylinder ID CC51105 CC51105 CC51105

Calibration Post High Cylinder Instrument Response 14.568 14.762 14.552 14.627

Calibration Post High Cylinder Bias 0.58 1.23 0.53 0.780

Calibration Post High Cylinder Drift 0.58 3.48 0.53 1.530

Cavg -0.069 0.08 0.112 0.041

Cavg Units ppmvw ppmvw ppmvw

Cgas 0 0.0005 0.106 0.036

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Fw 0 10640 10640 7,093.333

Fc 0 1800 1800 1,200.000

Cgasw 0 4.787741277

82711E-04

0.100684599

958509

0.034

Cgasw Units ppmvw ppmvw ppmvw

Thursday, February 10, 2011 Page 32 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/13/2010

Run Start Time 8:21:00 AM 12:23:00 PM 4:10:00 PM

Run Finish Time 11:46:00 AM 3:48:00 PM 7:27:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.214 0.218 0.218 0.217

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 30.06 30.09 30 30.050

Average Orifice Meter Differential, inches H2O 1.82 1.97 1.96 1.917

Dry Gas Meter Volume Sampled, cubic feet 131.146 137.563 137.682 135.464

Average Dry Gas Meter Temperature, °F 80.42 91.21 95.17 88.933

Dry Gas Meter Volume Sampled, dscf 131.244 135.155 133.904 133.434

Total Moisture Liquid collected, g 180.3 227.8 183.1 197.067

Volume of Water Vapor, standard cubic feet 8.49 10.72 8.62 9.277

Moisture Content of Stack Gas, % 6.08 7.35 6.05 6.493

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

Dry Mole Fraction 0.9392 0.9265 0.9395 0.935

Carbon Dioxide, % 8.99 8.83 8.95 8.923

Oxygen, % 11.82 11.85 11.84 11.837

Carbon Monoxide & Nitrogen, % 79.19 79.32 79.21 79.240

Fuel Factor 1.01 1.02 1.01

Dry Molecular Weight, lb/lb-Mole 29.91 29.89 29.91 29.903

Wet Molecular weight, lb/lb-Mole 29.19 29.02 29.19 29.133

Flue Gas Static Pressure, inches of H2O -0.79 -0.79 -0.81 -0.797

Absolute Flue Gas Pressure, inches of Mercury 30.00 30.03 29.94 29.990

Average Stack Gas Temperature, °F 325.00 324.83 320.63 323.487

Average Velocity Head, inches of H2O 1.3045818059

6539

1.277479523

12302

1.269544125

55052

1.284

Average Stack Gas Velocity, feet/second 77.66 77.03 76.47 77.053

Stack Cross-Sectional Area, square feet 283.529 283.529 283.529 283.529

Dry Volumetric Flow Rate, dry scfm 836,812.5 819,796.6 827,209.5 827,939.533

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,321,131.7 1,310,414.3 1,300,887.8 1,310,811.2

67

Percent Isokinetic of Sampling Rate, % 98.9 100.2 98.4 99.167

Percent Excess Air, % 130.1 130.4 130.5 130.333

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 228 228 228

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 10, 2011 Page 33 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - Method 29

Average

Run Number 1 2 3

Test Date 4/8/2010 4/9/2010 4/12/2010

Run Start Time 9:21:00 AM 9:08:00 AM 9:11:00 AM

Run Finish Time 1:45:00 PM 1:22:00 PM 1:38:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.213 0.213 0.213 0.213

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 29.91 29.85 30.06 29.940

Average Orifice Meter Differential, inches H2O 1.80 1.87 1.83 1.833

Dry Gas Meter Volume Sampled, cubic feet 172.825 175.761 175.801 174.796

Average Dry Gas Meter Temperature, °F 81.33 80.42 83.13 81.627

Dry Gas Meter Volume Sampled, dscf 171.797 174.691 175.059 173.849

Total Moisture Liquid collected, g 237.8 248.9 235.7 240.800

Volume of Water Vapor, standard cubic feet 11.19 11.72 11.09 11.333

Moisture Content of Stack Gas, % 6.12 6.29 5.96 6.123

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

Dry Mole Fraction 0.9388 0.9371 0.9404 0.939

Carbon Dioxide, % 8.72 8.8 8.92 8.813

Oxygen, % 11.84 11.74 11.76 11.780

Carbon Monoxide & Nitrogen, % 79.44 79.46 79.32 79.407

Fuel Factor 1.04 1.04 1.02

Dry Molecular Weight, lb/lb-Mole 29.87 29.88 29.90 29.883

Wet Molecular weight, lb/lb-Mole 29.14 29.13 29.19 29.153

Flue Gas Static Pressure, inches of H2O -0.8 -0.82 -0.8 -0.807

Absolute Flue Gas Pressure, inches of Mercury 29.85 29.79 30.00 29.880

Average Stack Gas Temperature, °F 319.54 323.13 329.04 323.903

Average Velocity Head, inches of H2O 1.2958152054

4926

1.341102678

88126

1.327205726

79136

1.321

Average Stack Gas Velocity, feet/second 77.39 79.00 78.53 78.307

Stack Cross-Sectional Area, square feet 283.529 283.529 283.529 283.529

Dry Volumetric Flow Rate, dry scfm 835,189.3 845,416.5 842,930.0 841,178.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,316,538.6 1,343,927.5 1,335,931.9 1,332,132.6

67

Percent Isokinetic of Sampling Rate, % 98.2 98.7 99.1 98.667

Percent Excess Air, % 129.7 127.1 128.1 128.300

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 228 228 228

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 10, 2011 Page 34 of 35
Tampa Electric Company - Polk Power Station - Unit #1

Location Stack Exit - OTM - 27/28

Average

Run Number 1 2 3

Test Date 4/8/2010 4/9/2010 4/14/2010

Run Start Time 9:08:00 AM

Run Finish Time 3:22:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 377.4 360.47 357.46

Nozzle Diameter, inches 0.156 0.156 0.156 0.156

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 29.91 29.85 30.15 29.970

Average Orifice Meter Differential, inches H2O 0.48 0.49 0.49 0.487

Dry Gas Meter Volume Sampled, cubic feet 142.101 136.462 136.185 138.249

Average Dry Gas Meter Temperature, °F 79.35 78.58 80.75 79.560

Dry Gas Meter Volume Sampled, dscf 141.317 135.634 136.169 137.707

Total Moisture Liquid collected, g 188.3 180.5 167.2 178.667

Volume of Water Vapor, standard cubic feet 8.86 8.50 7.87 8.410

Moisture Content of Stack Gas, % 5.90 5.90 5.46 5.753

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

Dry Mole Fraction 0.941 0.941 0.9454 0.942

Carbon Dioxide, % 8.73 8.8 8.84 8.790

Oxygen, % 11.86 11.78 11.83 11.823

Carbon Monoxide & Nitrogen, % 79.41 79.42 79.33 79.387

Fuel Factor 1.04 1.04 1.03

Dry Molecular Weight, lb/lb-Mole 29.87 29.88 29.89 29.880

Wet Molecular weight, lb/lb-Mole 29.17 29.18 29.24 29.197

Flue Gas Static Pressure, inches of H2O -0.8 -0.82 -0.82 -0.813

Absolute Flue Gas Pressure, inches of Mercury 29.85 29.79 30.09 29.910

Average Stack Gas Temperature, °F 324.92 324.25 323.52 324.230

Average Velocity Head, inches of H2O 1.3187122117

0551

1.331672793

76901

1.309518567

91747

1.320

Average Stack Gas Velocity, feet/second 78.30 78.71 77.55 78.187

Stack Cross-Sectional Area, square feet 283.529 283.529 283.529 283.529

Dry Volumetric Flow Rate, dry scfm 841,184.8 844,610.7 845,260.5 843,685.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,332,019.2 1,338,994.1 1,319,260.4 1,330,091.2

33

Percent Isokinetic of Sampling Rate, % 95.1 95.2 96.3 95.533

Percent Excess Air, % 130.3 128.2 129.8 129.433

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 228 228 228

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 10, 2011 Page 35 of 35