Name:

Title:

Company:

Sign Date:

Name:

Title:

Company:

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Big Bend Unit 2 ICR 26A HCl, HF

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.

Wednesday, February 09, 2011 Page 1 of 7
Big Bend Unit 2 ICR 26A HCl, HF

Facility Information:

Big Bend Station - Unit #2

P.O. Box 111

Tampa FL 33601-0111

Contact: Julie M.Ward

Phone:

Fax:

Email: jmward@tecoenergy.com

Testing Company:

Tampa Electric Company - Air Services Group

P.O. Box 111

Tampa FL 33601-0111

Contact: David A. Smith

Phone:

Fax:

Email: dasmith@tecoenergy.com

Air Permit Number:

0570039-039-AV

Permitted Source ID/Name:

Permitted Maximum Process Rate:

3996 mmBtu/hr

Max. Normal Operation Process Rate: Target Process Test Rate

90 - 100%

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

 process flow diagram:

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.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 0570039 FRS #:

SCC / Description 10100211 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Wet Bottom (Tangential) (Bituminous Coal) 

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

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

Stack 359.004 0 0 0 870 3138 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Hydrogen Fluoride Method 26A 3 180 0

Stack Hydrogen Chloride Method 26A 3 180 0

Regulation Description Compound Limit Unit

Hydrogen Chloride 0 lb/hr

Hydrogen Fluoride 0 lb/hr

Wednesday, February 09, 2011 Page 2 of 7
Big Bend Unit 2 ICR 26A HCl, HF

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.

Wednesday, February 09, 2011 Page 3 of 7
Big Bend Unit 2 ICR 26A HCl, HF

Sampling / Stack Data Results Summary

Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 3/10/2010 3/10/2010 3/11/2010

Run Start Time 9:00:00 AM 1:28:00 PM 9:28:00 AM

Run Finish Time 12:42:00 PM 5:00:00 PM 1:19:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 104.176 109.291 114.918 109.462

Moisture Content of Stack Gas, % 14.84 14.46 15.51 14.937

Moisture Saturation at Stack Gas Temperature, % 14.93 14.60 15.00 14.843

Carbon Dioxide, % 10 10 12 10.667

Oxygen, % 9 9 7 8.333

Average Stack Gas Temperature, °F 129.17 128.33 129.08 128.860

Dry Volumetric Flow Rate, dry scfm 907,583.2 946,237.1 981,959.3 945,259.867

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,202,469.7 1,246,333.9 1,312,130.2 1,253,644.60

0

Percent Isokinetic of Sampling Rate, % 99.8 100.4 101.7 100.633

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

Wednesday, February 09, 2011 Page 4 of 7
Big Bend Unit 2 ICR 26A HCl, HF

Emissions Summary

Process Run Data

Location: Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 16.878 21.815 18.867 19.187

Elb/hr 1.95E+01 2.50E+01 2.13E+01 21.933

mg/dscm 5.72E+00 7.05E+00 5.80E+00 6.190

ppm 3.77E+00 4.65E+00 3.83E+00 4.083

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.1886 0.2908 0.375 0.285

Elb/hr 2.17E-01 3.33E-01 4.24E-01 0.325

mg/dscm 6.39E-02 9.40E-02 1.15E-01 0.091

ppm 7.69E-02 1.13E-01 1.39E-01 0.110

Wednesday, February 09, 2011 Page 5 of 7
Big Bend Unit 2 ICR 26A HCl, HF

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Bituminous Coal Burned 0 Tons/hr 0

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR 0 0

1 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

1 WET SCRUBBER 0 0

Wednesday, February 09, 2011 Page 6 of 7
Big Bend Unit 2 ICR 26A HCl, HF

Sampling / Stack Data Results Detail

Location Stack - Method 26A

Average

Run Number 1 2 3

Test Date 3/10/2010 3/10/2010 3/11/2010

Run Start Time 9:00:00 AM 1:28:00 PM 9:28:00 AM

Run Finish Time 12:42:00 PM 5:00:00 PM 1:19:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.287 0.287 0.287 0.287

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1 1 1 1.000

Barometric Pressure, inches of Mercury 29.6 29.6 29.4 29.533

Average Orifice Meter Differential, inches H2O 1.20 1.31 1.42 1.310

Dry Gas Meter Volume Sampled, cubic feet 107.375 113.138 117.678 112.730

Average Dry Gas Meter Temperature, °F 80.00 82.50 73.17 78.557

Dry Gas Meter Volume Sampled, dscf 104.176 109.291 114.918 109.462

Total Moisture Liquid collected, g 385.9 392.6 448.3 408.933

Volume of Water Vapor, standard cubic feet 18.16 18.48 21.10 19.247

Moisture Content of Stack Gas, % 14.84 14.46 15.51 14.937

Moisture Saturation at Stack Gas Temperature, % 14.93 14.60 15.00 14.843

Dry Mole Fraction 0.8516 0.8554 0.85 0.852

Carbon Dioxide, % 10 10 12 10.667

Oxygen, % 9 9 7 8.333

Carbon Monoxide & Nitrogen, % 81 81 81 81.000

Fuel Factor 1.19 1.19 1.16

Dry Molecular Weight, lb/lb-Mole 29.96 29.96 30.20 30.040

Wet Molecular weight, lb/lb-Mole 28.19 28.23 28.46 28.293

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 29.59 29.59 29.39 29.523

Average Stack Gas Temperature, °F 129.17 128.33 129.08 128.860

Average Velocity Head, inches of H2O 0.2232130324

48807

0.240477776

74911

0.266552680

117907

0.243

Average Stack Gas Velocity, feet/second 28.51 29.55 31.11 29.723

Stack Cross-Sectional Area, square feet 702.952 702.952 702.952 702.952

Dry Volumetric Flow Rate, dry scfm 907,583.2 946,237.1 981,959.3 945,259.867

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,202,469.7 1,246,333.9 1,312,130.2 1,253,644.6

00

Percent Isokinetic of Sampling Rate, % 99.8 100.4 101.7 100.633

Percent Excess Air, % 72.7 72.7 48.7 64.700

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

Round Duct Diameter, inches 359.004 359.004 359.004

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

Wednesday, February 09, 2011 Page 7 of 7