Name: Patricia Q. West

Title: Manager, Environmental, Energy Supp

Company: Progress Energy Florida, Inc.

Sign Date: 9/3/2010

Name: Carl Vineyard, P.E.

Title: Project Manager

Company: Grace Consulting, Inc.

Sign Date: 9/3/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Crystal River 5

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 14
Crystal River 5

9/3/2010

Facility Information:

Crystal River Power Plant Unit 5

15760 West Power Line Road

Crystal River FL 344286708

Contact: Dave Meyer

Phone: 727-820-5229

Fax: 727-820-5229

Email: Dave.Meyer@pgnmail.com

Testing Company:

Grace Consulting, Inc.

PO Box 58

510 Dickson St.

Wellington OH 44090

Contact: Hal Stiles

Phone: 440-647-6672

Fax: 440-647-6673

Email: halstiles@gcitest.com

Air Permit Number:

0170004-024-AV

Permitted Source ID/Name:

0170004 Crystal River North Plant

Permitted Maximum Process Rate:

7200 mmBtu/hr

Max. Normal Operation Process Rate:

7200 mmBtu/hr

Target Process Test Rate

6480 mmBtu/hr

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

 process flow diagram:

diagram attached

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 #: FRS #: 110017431215

SCC / Description 10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (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 Unit 5 372 0 0 0 1248 3744 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Unit 5 Hydrogen Fluoride Method 26A 3 180 0

Stack Unit 5 Hydrogen Chloride Method 26A 3 180 0

Stack Unit 5 O2 Method 3A O2 3 180 0

Stack Unit 5 Co2 Method 3A CO2 3 180 0 3 points

Stack Unit 5 Sulfur Dioxide Method 6C 3 180 0

Stack Unit 5 Nitrogen oxides (NOx) Method 7E 3 180 0

Thursday, February 17, 2011 Page 2 of 14
Crystal River 5

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.

HCN will be collected using CTM-033 with 2 N NaOH to help keep the pH of the impingers above 12. The sample 

time for CTM-033 will be 60 minutes with a target sample volume of 30 cubic ft.

Thursday, February 17, 2011 Page 3 of 14
Crystal River 5

9/3/2010

Sampling / Stack Data Results Summary

Location Stack Unit 5 - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 3/29/2010 3/29/2010 3/29/2010

Run Start Time 8:22:30 AM 8:07:30 

AM

3:22:30 PM

Run Finish Time 11:30:00 AM 11:15:00 

AM

6:30:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 113.625 113.706 112.937 113.423

Moisture Content of Stack Gas, % 14.51 12.72 14.07 13.767

Moisture Saturation at Stack Gas Temperature, % 13.41 13.43 13.15 13.330

Carbon Dioxide, % 12.5 12.4 12.3 12.400

Oxygen, % 6.6 6.8 6.9 6.767

Average Stack Gas Temperature, °F 124.75 124.83 124.04 124.540

Dry Volumetric Flow Rate, dry scfm 1,834,924.7 1,854,113.4 1,825,986.5 1,838,341.53

3

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,400,615.1 2,406,049.4 2,378,877.8 2,395,180.76

7

Percent Isokinetic of Sampling Rate, % 100.2 99.2 100.1 99.833

F-Factor, dscfm/MMBtu @ %O2 9690 9563 9436 9,563.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Unit 5 - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Thursday, February 17, 2011 Page 4 of 14
Crystal River 5

9/3/2010

Location Stack Unit 5 - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Unit 5 - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Thursday, February 17, 2011 Page 5 of 14
Crystal River 5

9/3/2010

Location Stack Unit 5 - 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 6 of 14
Crystal River 5

9/3/2010

Emissions Summary

Process Run Data

Location: Stack Unit 5 - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0.79 1.602 0.597 0.996

lb/mmBtuO2 2.17E-04 4.40E-04 1.64E-04 0.000

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 1.933 0.5272 0.335 0.932

lb/mmBtuO2 5.31E-04 1.45E-04 9.21E-05 0.000

Location: Stack Unit 5 - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 6.52E-02 6.66E-02 6.39E-02 0.065

ppm 2.77E+01 2.82E+01 2.73E+01 27.733

ppm@7%O2 2.69E+01 2.78E+01 2.71E+01 27.267

Location: Stack Unit 5 - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 4.49E-02 4.49E-02 4.70E-02 0.046

ppm 2.65E+01 2.65E+01 2.80E+01 27.000

ppm@7%O2 2.58E+01 2.61E+01 2.78E+01 26.567

Thursday, February 17, 2011 Page 7 of 14
Crystal River 5

9/3/2010

Process Run Data

APCD Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Burned 288 Tons/hr 280

1 Steam Output 5290 1000 lb steam/hr 5240

1 Flue Gas Carbon Dioxide Content 9.6 % 10.1

1 Flue Gas Sampling Point Temperature 129 Deg F 128

1 Flue Gas Sampling Point Pressure 29.2 in. Hg 29.2

1 Unit Gross Electrical Output 770 Mwe 750

1 Unit Net Electric Generation 718 MWh 715

1 Scrubber Liquor pH 5.92 pH 5.45

1 Scrubber Liquor Flow Rate 166 gpm 150

1 Heat Input 6690 mmBtu/hr 6500

2 Coal Burned 289 Tons/hr 280

2 Steam Output 5300 1000 lb steam/hr 5240

2 Flue Gas Carbon Dioxide Content 10.9 % 10.1

2 Flue Gas Sampling Point Temperature 128 Deg F 128

2 Flue Gas Sampling Point Pressure 29.2 in. Hg 29.2

2 Unit Gross Electrical Output 770 Mwe 750

2 Unit Net Electric Generation 718 MWh 715

2 Scrubber Liquor pH 5.8 pH 5.45

2 Scrubber Liquor Flow Rate 166 gpm 150

2 Heat Input 6723 mmBtu/hr 6500

3 Coal Burned 290 Tons/hr 280

3 Steam Output 5305 1000 lb steam/hr 5240

3 Flue Gas Carbon Dioxide Content 10.9 % 10.1

3 Flue Gas Sampling Point Temperature 128 Deg F 128

3 Flue Gas Sampling Point Pressure 29.2 in. Hg 29.2

3 Unit Gross Electrical Output 772 Mwe 750

3 Unit Net Electric Generation 720 MWh 715

3 Scrubber Liquor pH 5.9 pH 5.45

3 Scrubber Liquor Flow Rate 676 gpm 150

3 Heat Input 6742 mmBtu/hr 6500

Run Name Value UOM Comments

Target

Value

1 Precipitator 0

Thursday, February 17, 2011 Page 8 of 14
Crystal River 5

9/3/2010

Process Lab Run Data

1 0

1 0

Thursday, February 17, 2011 Page 9 of 14
Crystal River 5

9/3/2010

Sampling / Stack Data Results Detail

Location Stack Unit 5 - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 3/29/2010 3/29/2010 3/29/2010

Run Start Time 8:22:30 AM 8:07:30 AM 3:22:30 PM

Run Finish Time 11:30:00 AM 11:15:00 AM 6:30:00 PM

Net Traversing Points 25 25 25

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.218 0.218 0.218 0.218

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.016 1.016 1.016 1.016

Barometric Pressure, inches of Mercury 29.3 29.3 29.3 29.300

Average Orifice Meter Differential, inches H2O 1.49 1.49 1.48 1.487

Dry Gas Meter Volume Sampled, cubic feet 118.132 118.485 118.088 118.235

Average Dry Gas Meter Temperature, °F 88.21 89.46 91.33 89.667

Dry Gas Meter Volume Sampled, dscf 113.625 113.706 112.937 113.423

Total Moisture Liquid collected, g 409.5 352.1 392.9 384.833

Volume of Water Vapor, standard cubic feet 19.28 16.57 18.49 18.113

Moisture Content of Stack Gas, % 14.51 12.72 14.07 13.767

Moisture Saturation at Stack Gas Temperature, % 13.41 13.43 13.15 13.330

Dry Mole Fraction 0.8659 0.8728 0.8685 0.869

Carbon Dioxide, % 12.5 12.4 12.3 12.400

Oxygen, % 6.6 6.8 6.9 6.767

Carbon Monoxide & Nitrogen, % 80.9 80.8 80.8 80.833

Fuel Factor 1.14 1.14 1.14

Dry Molecular Weight, lb/lb-Mole 30.26 30.26 30.24 30.253

Wet Molecular weight, lb/lb-Mole 28.81 28.70 28.80 28.770

Flue Gas Static Pressure, inches of H2O -0.68 -0.55 -0.66 -0.630

Absolute Flue Gas Pressure, inches of Mercury 29.25 29.26 29.25 29.253

Average Stack Gas Temperature, °F 124.75 124.83 124.04 124.540

Average Velocity Head, inches of H2O 0.7853431111

7961

0.786119188

212873

0.771784683

297989

0.781

Average Stack Gas Velocity, feet/second 53.01 53.13 52.53 52.890

Stack Cross-Sectional Area, square feet 754.768 754.768 754.768 754.768

Dry Volumetric Flow Rate, dry scfm 1,834,924.7 1,854,113.4 1,825,986.5 1,838,341.5

33

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,400,615.1 2,406,049.4 2,378,877.8 2,395,180.7

67

Percent Isokinetic of Sampling Rate, % 100.2 99.2 100.1 99.833

Percent Excess Air, % 44.7 46.8 47.8 46.433

F-Factor, dscfm/MMBtu @ %O2 9690 9563 9436 9,563.000

Round Duct Diameter, inches 372 372 372

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 17, 2011 Page 10 of 14
Crystal River 5

9/3/2010

Location Stack Unit 5 - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, February 17, 2011 Page 11 of 14
Crystal River 5

9/3/2010

Location Stack Unit 5 - Method 3A O2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, February 17, 2011 Page 12 of 14
Crystal River 5

9/3/2010

Location Stack Unit 5 - 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 13 of 14
Crystal River 5

9/3/2010

Location Stack Unit 5 - 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 14 of 14