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 1

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Thursday, February 17, 2011 Page 1 of 29
Crystal River 1

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Facility Information:

Crystal River Power Plant Unit 1

15760 West Power Line Road

Crystal River FL 344286708

Contact: Dave Meyer

Phone: 727-820-5295

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 Power Plant

Permitted Maximum Process Rate:

3750 mmBtu/hr

Max. Normal Operation Process Rate:

3750 mmBtu/hr

Target Process Test Rate

3375 mmBtu/hr

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

 process flow diagram:

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 1 182 0 0 0 1440 1560 4 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Unit 1 Carbon Monoxide Method 10 3 180 0 3 points

Stack Unit 1 Formaldehyde Method 0011 3 120 0 12 points

Total organic compounds 

(TOC) as Propane

Stack Unit 1 Method 25A 3 120 0 3 points

Stack Unit 1 Hydrogen Chloride Method 26A 3 180 0 12 points

Stack Unit 1 Hydrogen Fluoride Method 26A 3 180 0 12 points

Stack Unit 1 Filterable Particulate OTM - 27/28 3 360 0 12 points

Stack Unit 1 Filterable PM2.5 OTM - 27/28 3 360 0 12 points

Thursday, February 17, 2011 Page 2 of 29
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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.

Inorganic (Aqueous) 

Condensible Part.

Stack Unit 1 OTM - 27/28 3 360 0 12 points

Organic Condensible 

Particulate

Stack Unit 1 OTM - 27/28 3 360 0 12 points

Stack Unit 1 Total Particulate OTM - 27/28 3 360 0 12 points

Stack Unit 1 Total PM2.5 OTM - 27/28 3 360 0 12 points

Stack Unit 1 Beryllium Method 29 3 240 0 12 points

Stack Unit 1 Arsenic Method 29 3 240 0 12 points

Stack Unit 1 Zinc Method 29 3 240 0

Stack Unit 1 Phosphorus (yellow or white) Method 29 3 240 0 12 points

Stack Unit 1 Chromium Method 29 3 240 0 12 points

Stack Unit 1 Cobalt Method 29 3 240 0 12 points

Stack Unit 1 Lead Method 29 3 240 0 12 points

Stack Unit 1 Manganese Method 29 3 240 0 12 points

Stack Unit 1 Nickel Method 29 3 240 0 12 points

Stack Unit 1 Cadmium Method 29 3 240 0 12 points

Stack Unit 1 Antimony Method 29 3 240 0 12 points

Stack Unit 1 Selenium Method 29 3 240 0 12 points

Stack Unit 1 Copper Method 29 3 240 0

Stack Unit 1 Barium Method 29 3 240 0

Stack Unit 1 Silver Method 29 3 240 0

Stack Unit 1 Thallium Method 29 3 240 0

Stack Unit 1 Co2 Method 3A CO2 9 240 0 3 points

Stack Unit 1 O2 Method 3A O2 9 240 0 3 Points

Stack Unit 1 Sulfur Dioxide Method 6C 3 180 0 3 points

Stack Unit 1 Nitrogen oxides (NOx) Method 7E 3 180 0 3 points

Thursday, February 17, 2011 Page 3 of 29
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9/3/2010

Sampling / Stack Data Results Summary

Location Stack Unit 1 - Method 0011

Average

Run Number 1 2 3

Test Date 3/26/2010 3/26/2010 3/26/2010

Run Start Time 1:55:00 PM 4:25:00 PM 6:55:00 PM

Run Finish Time 4:00:00 PM 6:30:00 PM 9:00:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 92.829 93.318 93.185 93.111

Moisture Content of Stack Gas, % 6.29 4.87 4.82 5.327

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

Carbon Dioxide, % 12.7 12.7 12.9 12.767

Oxygen, % 6.4 6.3 6.2 6.300

Average Stack Gas Temperature, °F 341.83 343.33 343.08 342.747

Dry Volumetric Flow Rate, dry scfm 834,868.8 847,333.0 845,738.6 842,646.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,363,427.5 1,366,137.5 1,362,885.5 1,364,150.16

7

Percent Isokinetic of Sampling Rate, % 100.2 99.3 99.3 99.600

F-Factor, dscfm/MMBtu @ %O2 9599 9481 9512 9,530.667

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Stack Unit 1 - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Thursday, February 17, 2011 Page 4 of 29
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Location Stack Unit 1 - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Unit 1 - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Thursday, February 17, 2011 Page 5 of 29
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Location Stack Unit 1 - Method 29

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Stack Unit 1 - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Thursday, February 17, 2011 Page 6 of 29
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Location Stack Unit 1 - Method 3A CO2 3

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 1 - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Thursday, February 17, 2011 Page 7 of 29
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Location Stack Unit 1 - 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 1 - Method 3A O2 3

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 8 of 29
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Location Stack Unit 1 - Method 3A O2 3 6

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 1 - 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 9 of 29
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9/3/2010

Location Stack Unit 1 - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Unit 1 - 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 10 of 29
Crystal River 1

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Emissions Summary

Location: Stack Unit 1 - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.0049 0.00228 0.00075 0.003

lb/mmBtuO2 1.61E-06 7.31E-07 2.40E-07 0.000

ppm 1.49E-03 6.91E-04 2.28E-04 0.001

ppm@7%O2 1.43E-03 6.58E-04 2.16E-04 0.001

Location: Stack Unit 1 - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 3.44E-03 1.18E-03 2.90E-03 0.003

ppm 3.42E+00 1.19E+00 2.95E+00 2.520

ppm@7%O2 3.28E+00 1.13E+00 2.79E+00 2.400

Location: Stack Unit 1 - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 1.61E-03 2.83E-03 1.79E-03 0.002

ppm 1.02E+00 1.82E+00 1.16E+00 1.333

ppm@7%O2 9.78E-01 1.73E+00 1.10E+00 1.269

Location: Stack Unit 1 - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 241.147 416.811 409.396 355.785

lb/mmBtuO2 5.05E-02 8.74E-02 8.52E-02 0.074

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 38.432 37.938 30.828 35.733

lb/mmBtuO2 8.04E-03 7.95E-03 6.42E-03 0.007

Location: Stack Unit 1 - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00449 0.01074 0.00908 0.008

lb/mmBtuO2 6.13E-07 1.46E-06 1.24E-06 0.000

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.05607 0.09097 0.08137 0.076

Thursday, February 17, 2011 Page 11 of 29
Crystal River 1

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lb/mmBtuO2 7.66E-06 1.24E-05 1.12E-05 0.000

Compound: Barium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.3265 0.5887 1.1892 0.701

lb/mmBtuO2 4.46E-05 8.01E-05 1.63E-04 0.000

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.005329 0.010042 0.010326 0.009

lb/mmBtuO2 7.28E-07 1.37E-06 1.42E-06 0.000

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.000767 0.00322 0.00493 0.003

lb/mmBtuO2 1.05E-07 4.38E-07 6.76E-07 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.3253 0.1103 0.0834 0.173

lb/mmBtuO2 4.44E-05 1.50E-05 1.14E-05 0.000

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.02639 0.03791 0.04061 0.035

lb/mmBtuO2 3.60E-06 5.16E-06 5.57E-06 0.000

Compound: Copper

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.11733 0.16133 0.15093 0.143

lb/mmBtuO2 1.60E-05 2.20E-05 2.07E-05 0.000

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.0479 0.0825 0.0812 0.071

lb/mmBtuO2 6.54E-06 1.12E-05 1.11E-05 0.000

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.08464 0.09114 0.08874 0.088

lb/mmBtuO2 1.16E-05 1.24E-05 1.22E-05 0.000

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 1.46133 0.12263 0.09153 0.558

Thursday, February 17, 2011 Page 12 of 29
Crystal River 1

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lb/mmBtuO2 2.00E-04 1.67E-05 1.25E-05 0.000

Compound: Phosphorus (yellow or white)

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.3688 0.9372 0.8631 0.723

lb/mmBtuO2 5.04E-05 1.28E-04 1.18E-04 0.000

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.535 0.956 1.102 0.864

lb/mmBtuO2 7.31E-05 1.30E-04 1.51E-04 0.000

Compound: Silver

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.000829 0.001139 0.000919 0.001

lb/mmBtuO2 1.13E-07 1.55E-07 1.26E-07 0.000

Compound: Thallium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.002151 0.003251 0.003251 0.003

lb/mmBtuO2 2.94E-07 4.43E-07 4.46E-07 0.000

Compound: Zinc

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.1148 0.177 0.1117 0.135

lb/mmBtuO2 1.57E-05 2.41E-05 1.53E-05 0.000

Location: Stack Unit 1 - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 1.31E+00 1.36E+00 1.43E+00 1.367

ppm 5.58E+02 5.82E+02 6.08E+02 582.667

ppm@7%O2 5.50E+02 5.70E+02 5.95E+02 571.667

Location: Stack Unit 1 - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 3.12E-01 3.09E-01 3.21E-01 0.314

ppm 1.85E+02 1.84E+02 1.91E+02 186.667

ppm@7%O2 1.82E+02 1.80E+02 1.87E+02 183.000

Location: Stack Unit 1 - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber M027-1 m027-2 M027-3

Thursday, February 17, 2011 Page 13 of 29
Crystal River 1

9/3/2010

Process Run Data

Mass_mg 1573.9 199.6 89.7 621.067

lb/mmBtuO2 3.48E-01 6.35E-02 2.98E-02 0.147

Compound: Filterable PM2.5

Average

RunNumber M027-1 m027-2 M027-3

Mass_mg 225.4 63.1 35.1 107.867

lb/mmBtuO2 4.98E-02 2.01E-02 1.17E-02 0.027

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber M027-1 m027-2 M027-3

Mass_mg 57.4 57.8 48 54.400

lb/mmBtuO2 1.27E-02 1.84E-02 1.59E-02 0.016

Compound: Organic Condensible Particulate

Average

RunNumber M027-1 m027-2 M027-3

Mass_mg 39.7 34.7 18.1 30.833

lb/mmBtuO2 8.77E-03 1.10E-02 6.01E-03 0.009

Compound: Total Particulate

Average

RunNumber M027-1 m027-2 M027-3

Mass_mg 1671 292.1 155.8 706.300

lb/mmBtuO2 3.69E-01 9.29E-02 5.17E-02 0.171

Compound: Total PM2.5

Average

RunNumber M027-1 m027-2 M027-3

Mass_mg 322.5 155.6 101.2 193.100

lb/mmBtuO2 7.13E-02 4.95E-02 3.36E-02 0.051

Thursday, February 17, 2011 Page 14 of 29
Crystal River 1

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Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Burned 148 tons/hr 140

1 Average Heat Input 3619 lbs/mmBtu 3500

1 Steam Output 2010 1000 lbs/hr 2010

1 Flue Gas Sampling Point Temperature 330 Deg F 280

1 Unit Gross Electrical Output 386 Mwe 375

1 Unit Net Electric Generation 360 MW 360

2 Coal Burned 144 tons/hr 140

2 Average Heat Input 3515 lbs/mmBtu 3500

2 Steam Output 2009 1000 lbs/hr 2010

2 Flue Gas Sampling Point Temperature 335 Deg F 280

2 Unit Gross Electrical Output 386 Mwe 375

2 Unit Net Electric Generation 361 MW 360

3 Coal Burned 149 tons/hr 140

3 Average Heat Input 3701 lbs/mmBtu 3500

3 Steam Output 2050 1000 lbs/hr 2010

3 Flue Gas Sampling Point Temperature 335 Deg F 280

3 Unit Gross Electrical Output 390 Mwe 375

3 Unit Net Electric Generation 370 MW 360

1 Heat Input Million Btus/million BTU using O2 0 0

Run Name Value UOM Comments

Target

Value

ELECTROSTATIC PRECIPITATOR 0

Run Name Value UOM Comments

1 Acid Gas HAP , Chlorine, Fluroine sulfur, HHV, 

Proximate & Ultimate

0

1 NON-Dioxin/furan Organic HAP analysis 0

1 Mercury & Non Mercury Metallic Hap (metals analysis) 0

Thursday, February 17, 2011 Page 15 of 29
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Sampling / Stack Data Results Detail

Location Stack Unit 1 - Method 0011

Average

Run Number 1 2 3

Test Date 3/26/2010 3/26/2010 3/26/2010

Run Start Time 1:55:00 PM 4:25:00 PM 6:55:00 PM

Run Finish Time 4:00:00 PM 6:30:00 PM 9:00:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.175 0.175 0.175 0.175

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.018 1.018 1.018 1.018

Barometric Pressure, inches of Mercury 29.85 29.85 29.85 29.850

Average Orifice Meter Differential, inches H2O 2.10 2.10 2.10 2.100

Dry Gas Meter Volume Sampled, cubic feet 91.348 91.727 91.582 91.552

Average Dry Gas Meter Temperature, °F 70.42 69.83 69.75 70.000

Dry Gas Meter Volume Sampled, dscf 92.829 93.318 93.185 93.111

Total Moisture Liquid collected, g 132.4 101.5 100.3 111.400

Volume of Water Vapor, standard cubic feet 6.23 4.78 4.72 5.243

Moisture Content of Stack Gas, % 6.29 4.87 4.82 5.327

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

Dry Mole Fraction 0.9371 0.9513 0.9518 0.947

Carbon Dioxide, % 12.7 12.7 12.9 12.767

Oxygen, % 6.4 6.3 6.2 6.300

Carbon Monoxide & Nitrogen, % 80.9 81 80.9 80.933

Fuel Factor 1.14 1.15 1.14

Dry Molecular Weight, lb/lb-Mole 30.29 30.28 30.31 30.293

Wet Molecular weight, lb/lb-Mole 29.52 29.68 29.72 29.640

Flue Gas Static Pressure, inches of H2O -2.2 -2.3 -2.5 -2.333

Absolute Flue Gas Pressure, inches of Mercury 29.69 29.68 29.67 29.680

Average Stack Gas Temperature, °F 341.83 343.33 343.08 342.747

Average Velocity Head, inches of H2O 3.3535234384

2617

3.377354937

2345

3.365924828

19975

3.366

Average Stack Gas Velocity, feet/second 125.78 126.03 125.73 125.847

Stack Cross-Sectional Area, square feet 180.663 180.663 180.663 180.663

Dry Volumetric Flow Rate, dry scfm 834,868.8 847,333.0 845,738.6 842,646.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,363,427.5 1,366,137.5 1,362,885.5 1,364,150.1

67

Percent Isokinetic of Sampling Rate, % 100.2 99.3 99.3 99.600

Percent Excess Air, % 42.8 41.8 40.9 41.833

F-Factor, dscfm/MMBtu @ %O2 9599 9481 9512 9,530.667

Round Duct Diameter, inches 182 182 182

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 16 of 29
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Location Stack Unit 1 - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, February 17, 2011 Page 17 of 29
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Location Stack Unit 1 - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, February 17, 2011 Page 18 of 29
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Location Stack Unit 1 - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Thursday, February 17, 2011 Page 19 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - Method 29

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Thursday, February 17, 2011 Page 20 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - Method 3A CO2

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, February 17, 2011 Page 21 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - Method 3A CO2 3

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, February 17, 2011 Page 22 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - Method 3A CO2 3 6

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Thursday, February 17, 2011 Page 23 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - 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 24 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - Method 3A O2 3

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 25 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - Method 3A O2 3 6

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 26 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - 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 27 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - 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 28 of 29
Crystal River 1

9/3/2010

Location Stack Unit 1 - 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 29 of 29