Name: Alan Madewell, P.E.

Title: Manager, Environmental, Energy Supp

Company: Progress Energy Carolinas, 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

Progress Energy, Asheville Plant, 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 17, 2011 Page 1 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Facility Information:

Progress Energy, Asheville, Unit 1

200 CP&L Drive

Arden NC 28704-9781

Contact: Cynthia Winston

Phone: 919-546-5538

Fax: 919-546-5538

Email: Cynthia.Winston@pgnmail.com

Testing Company:

Grace Consulting, Inc.

510 Dickson Street

Wellington OH 44090

Contact:Carl Vineyard

Phone: 440-647-6672

Fax: 440-647-6673

Email: carlvineyard@gcitest.com

Air Permit Number:

11-628-05

Permitted Source ID/Name:

Asheville Unit 1

Permitted Maximum Process Rate:

2155 mmbtu/hr

Max. Normal Operation Process Rate:

1400 mmBtu

Target Process Test Rate

1400 mmBtu

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

 process flow diagram:

Flow diagram attached.

Industry/SCC/NAIS 22111

Sampling Location Information:

Test Parameter Information:

AFS #: 3702100628 FRS #: 110000587071

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

Unit 1 Stack 198 0 0 0 2052 708 4 4

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Unit 1 Stack Hydrogen Chloride Method 26A 3 180 0

Unit 1 Stack Hydrogen Fluoride Method 26A 3 180 0

Unit 1 Stack Cadmium Method 29 3 240 0

Unit 1 Stack Antimony Method 29 3 240 0

Unit 1 Stack Arsenic Method 29 3 240 0

Unit 1 Stack Beryllium Method 29 3 240 0

Unit 1 Stack Filterable Particulate Method 29 3 240 0

Thursday, February 17, 2011 Page 2 of 19
Progress Energy, Asheville Plant, Unit 1

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.

The HCN was sampled using CTM 033 with 6 Normal NaOH and an additional impinger for one hour per the 

clarification given by the USEPA.

Unit 1 Stack Chromium Method 29 3 240 0

Unit 1 Stack Cobalt Method 29 3 240 0

Unit 1 Stack Thallium Method 29 3 240 0

Unit 1 Stack Barium Method 29 3 240 0

Unit 1 Stack Zinc Method 29 3 240 0

Unit 1 Stack Copper Method 29 3 240 0

Unit 1 Stack Selenium Method 29 3 240 0

Unit 1 Stack Silver Method 29 3 240 0

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

Unit 1 Stack Lead Method 29 3 240 0

Unit 1 Stack Nickel Method 29 3 240 0

Unit 1 Stack Manganese Method 29 3 240 0

Unit 1 Stack Co2 Method 3A CO2 3 240 0

Unit 1 Stack O2 Method 3A O2 3 240 0

Organic Condensible 

Particulate

Unit 1 Stack Method 5/OTM-28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Unit 1 Stack Method 5/OTM-28 3 240 0

Unit 1 Stack Filterable Particulate Method 5/OTM-28 3 240 0

Unit 1 Stack Total Particulate Method 5/OTM-28 3 240 0

Unit 1 Stack Sulfur Dioxide Method 6C 3 240 0

Unit 1 Stack Nitrogen oxides (NOx) Method 7E 3 240 0

Thursday, February 17, 2011 Page 3 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Sampling / Stack Data Results Summary

Location Unit 1 Stack - Method 26A

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 12:00:00 

PM

6:30:00 AM

Run Finish Time 10:20:30 AM 3:20:30 PM 9:50:30 AM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 144.702 109.198 108.757 120.886

Moisture Content of Stack Gas, % 12.97 14.59 14.21 13.923

Moisture Saturation at Stack Gas Temperature, % 12.97 12.88 12.94 12.930

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Average Stack Gas Temperature, °F 123.00 122.75 122.88 122.877

Dry Volumetric Flow Rate, dry scfm 508,351.1 503,632.5 504,207.3 505,396.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 669,571.6 662,387.1 664,439.8 665,466.167

Percent Isokinetic of Sampling Rate, % 99.2 99.4 98.9 99.167

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 17, 2011 Page 4 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Location Unit 1 Stack - Method 29

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 12:00:00 

PM

6:30:00 AM

Run Finish Time 11:16:00 AM 4:17:00 PM 10:45:00 AM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 190.761 124.011 146.497 153.756

Moisture Content of Stack Gas, % 12.96 14.87 12.86 13.563

Moisture Saturation at Stack Gas Temperature, % 13.26 13.02 13.48 13.253

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Average Stack Gas Temperature, °F 123.81 123.13 124.35 123.763

Dry Volumetric Flow Rate, dry scfm 504,007.5 500,841.0 507,131.0 503,993.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 664,696.4 660,206.1 669,828.2 664,910.233

Percent Isokinetic of Sampling Rate, % 98.9 92.6 108.0 99.833

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 1 Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 1:00:00 PM 6:30:00 AM

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

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Dry Volumetric Flow Rate, dry scfm 586473 584462 582975 584,636.667

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Moisture, % 13.6 11 10.4 11.667

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 17, 2011 Page 5 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Location Unit 1 Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 1:00:00 PM 6:30:00 AM

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

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Dry Volumetric Flow Rate, dry scfm 586473 584462 582975 584,636.667

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Moisture, % 13.6 11 10.4 11.667

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 1 Stack - Method 5/OTM-28

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 12:00:00 

PM

6:30:00 AM

Run Finish Time 11:30:00 AM 4:30:00 PM 10:40:00 AM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 197.752 155.472 155.264 169.496

Moisture Content of Stack Gas, % 11.72 11.00 10.37 11.030

Moisture Saturation at Stack Gas Temperature, % 13.64 13.56 13.48 13.560

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Average Stack Gas Temperature, °F 124.83 124.63 124.35 124.603

Dry Volumetric Flow Rate, dry scfm 515,614.8 519,998.0 522,621.2 519,411.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 671,624.3 671,624.3 671,111.1 671,453.233

Percent Isokinetic of Sampling Rate, % 100.2 97.3 96.7 98.067

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 17, 2011 Page 6 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Location Unit 1 Stack - Method 6C

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 1:00:00 PM 6:30:00 AM

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

Carbon Dioxide, % 12.4 12.2 12.3 12.300

Oxygen, % 6.2 6.1 5.9 6.067

Dry Volumetric Flow Rate, dry scfm 586473 584462 582975 584,636.667

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Moisture, % 13.6 11 10.4 11.667

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 1 Stack - Method 7E

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 1:00:00 PM 6:30:00 AM

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

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Dry Volumetric Flow Rate, dry scfm 586473 584462 582975 584,636.667

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Moisture, % 13.6 11 10.4 11.667

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 17, 2011 Page 7 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Emissions Summary

Location: Unit 1 Stack - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 32.174 26.361 16.234 24.923

lb/mmBtuO2 6.76E-03 7.21E-03 4.43E-03 0.006

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.282 0.224 0.246 0.251

lb/mmBtuO2 5.92E-05 6.13E-05 6.72E-05 0.000

Location: Unit 1 Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000768 0.000258 0.000112 0.000

lb/mmBtuO2 1.22E-07 6.22E-08 2.27E-08 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0213 0.012 0.0053 0.013

lb/mmBtuO2 3.39E-06 2.89E-06 1.07E-06 0.000

Compound: Barium

Average

RunNumber 1 2 3

Mass_mg 0.0178 0.0084 0.0018 0.009

lb/mmBtuO2 2.84E-06 2.02E-06 3.65E-07 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000282 0.000035 0.000024 0.000

lb/mmBtuO2 4.49E-08 8.43E-09 4.87E-09 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.002017 0.000367 0.000142 0.001

lb/mmBtuO2 3.21E-07 8.84E-08 2.88E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.1629 0.028 0.0072 0.066

lb/mmBtuO2 2.60E-05 6.75E-06 1.46E-06 0.000

Thursday, February 17, 2011 Page 8 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.012314 0.002314 0.001684 0.005

lb/mmBtuO2 1.96E-06 5.58E-07 3.41E-07 0.000

Compound: Copper

Average

RunNumber 1 2 3

Mass_mg 0.0635 0.0147 0.0299 0.036

lb/mmBtuO2 1.01E-05 3.54E-06 6.06E-06 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 22.5 10.3 11.2 14.667

lb/mmBtuO2 3.59E-03 2.48E-03 2.27E-03 0.003

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.02902 0.00062 0.03607 0.022

lb/mmBtuO2 4.62E-06 1.49E-07 7.31E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.04794 0.01074 0.05754 0.039

lb/mmBtuO2 7.64E-06 2.59E-06 1.17E-05 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.2403 0.0274 2.2246 0.831

lb/mmBtuO2 3.83E-05 6.60E-06 4.51E-04 0.000

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 0.0533 0.0159 0.0107 0.027

lb/mmBtuO2 8.49E-06 3.83E-06 2.17E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.1212 0.0667 0.0623 0.083

lb/mmBtuO2 1.93E-05 1.61E-05 1.26E-05 0.000

Compound: Silver

Average

RunNumber 1 2 3

Mass_mg 0.003477 0.001497 0.000437 0.002

lb/mmBtuO2 5.54E-07 3.61E-07 8.86E-08 0.000

Thursday, February 17, 2011 Page 9 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Compound: Thallium

Average

RunNumber 1 2 3

Mass_mg 0.000137 0.000102 0.000102 0.000

lb/mmBtuO2 2.18E-08 2.46E-08 2.07E-08 0.000

Compound: Zinc

Average

RunNumber 1 2 3

Mass_mg 0.1793 0.0696 0.0581 0.102

lb/mmBtuO2 2.86E-05 1.68E-05 1.18E-05 0.000

Location: Unit 1 Stack - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 36.4 11.7 10.1 19.400

lb/mmBtuO2 5.59E-03 2.25E-03 1.93E-03 0.003

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 113.2 30 10 51.067

lb/mmBtuO2 1.74E-02 5.77E-03 1.91E-03 0.008

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 5.6 6.7 1.9 4.733

lb/mmBtuO2 8.61E-04 1.29E-03 3.64E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 155.2 48.4 22 75.200

lb/mmBtuO2 2.39E-02 9.30E-03 4.21E-03 0.012

Location: Unit 1 Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 5.34E-02 5.67E-02 4.48E-02 0.052

ppm 2.33E+01 2.52E+01 2.00E+01 22.833

ppm@7%O2 2.20E+01 2.37E+01 1.85E+01 21.400

Location: Unit 1 Stack - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 3.76E-02 3.79E-02 3.51E-02 0.037

ppm 2.29E+01 2.34E+01 2.18E+01 22.700

ppm@7%O2 2.17E+01 2.20E+01 2.02E+01 21.300

Thursday, February 17, 2011 Page 10 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Process Run Data

Thursday, February 17, 2011 Page 11 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 1422 mmBtu/hr 1400

1 Steam Flow 1365 klbs/hr 1350

1 Coal Burned 85.15 tons/hr 80

2 Heat Input 1422 mmBtu/hr 1400

2 Steam Flow 1373 klbs/hr 1350

2 Coal Burned 81.89 tons/hr 80

3 Heat Input 1422 mmBtu/hr 1400

3 Steam Flow 1388 klbs/hr 1350

3 Coal Burned 82.42 tons/hr 80

Run Name Value UOM Comments

Target

Value

1 Slurry Flow 60.79 GPM 60

2 Slurry Flow 60.25 GPM 60

3 Slurry Flow 61.57 GPM 60

Run Name Value UOM Comments

1 0

Thursday, February 17, 2011 Page 12 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Sampling / Stack Data Results Detail

Location Unit 1 Stack - Method 26A

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 12:00:00 PM 6:30:00 AM

Run Finish Time 10:20:30 AM 3:20:30 PM 9:50:30 AM

Net Traversing Points 24 24 24

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.25 0.218 0.218 0.229

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 28.86 28.86 28.82 28.847

Average Orifice Meter Differential, inches H2O 2.26 1.34 1.30 1.633

Dry Gas Meter Volume Sampled, cubic feet 151.512 116.699 114.215 127.475

Average Dry Gas Meter Temperature, °F 84.38 94.33 83.92 87.543

Dry Gas Meter Volume Sampled, dscf 144.702 109.198 108.757 120.886

Total Moisture Liquid collected, g 458.2 396.3 382.6 412.367

Volume of Water Vapor, standard cubic feet 21.57 18.65 18.01 19.410

Moisture Content of Stack Gas, % 12.97 14.59 14.21 13.923

Moisture Saturation at Stack Gas Temperature, % 12.97 12.88 12.94 12.930

Dry Mole Fraction 0.8703 0.8712 0.8706 0.871

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Carbon Monoxide & Nitrogen, % 81.7 81.7 81.8 81.733

Fuel Factor 1.21 1.21 1.22

Dry Molecular Weight, lb/lb-Mole 30.18 30.20 30.20 30.193

Wet Molecular weight, lb/lb-Mole 28.60 28.94 28.85 28.797

Flue Gas Static Pressure, inches of H2O -0.59 -0.49 -0.4 -0.493

Absolute Flue Gas Pressure, inches of Mercury 28.82 28.82 28.79 28.810

Average Stack Gas Temperature, °F 123.00 122.75 122.88 122.877

Average Velocity Head, inches of H2O 0.7468850291

47593

0.739699714

278986

0.741039846

745239

0.743

Average Stack Gas Velocity, feet/second 52.19 51.63 51.79 51.870

Stack Cross-Sectional Area, square feet 213.825 213.825 213.825 213.825

Dry Volumetric Flow Rate, dry scfm 508,351.1 503,632.5 504,207.3 505,396.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 669,571.6 662,387.1 664,439.8 665,466.167

Percent Isokinetic of Sampling Rate, % 99.2 99.4 98.9 99.167

Percent Excess Air, % 40.3 39.4 37.6 39.100

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Round Duct Diameter, inches 198 198 198

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 13 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Location Unit 1 Stack - Method 29

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 12:00:00 PM 6:30:00 AM

Run Finish Time 11:16:00 AM 4:17:00 PM 10:45:00 AM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.25 0.209 0.209 0.223

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.017 1.017 1.017 1.017

Barometric Pressure, inches of Mercury 28.86 28.86 28.82 28.847

Average Orifice Meter Differential, inches H2O 2.35 1.17 1.16 1.560

Dry Gas Meter Volume Sampled, cubic feet 201.161 132.680 154.710 162.850

Average Dry Gas Meter Temperature, °F 89.46 95.81 87.85 91.040

Dry Gas Meter Volume Sampled, dscf 190.761 124.011 146.497 153.756

Total Moisture Liquid collected, g 603.6 460.4 459.3 507.767

Volume of Water Vapor, standard cubic feet 28.41 21.67 21.62 23.900

Moisture Content of Stack Gas, % 12.96 14.87 12.86 13.563

Moisture Saturation at Stack Gas Temperature, % 13.26 13.02 13.48 13.253

Dry Mole Fraction 0.8704 0.8698 0.8714 0.871

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Carbon Monoxide & Nitrogen, % 81.7 81.7 81.8 81.733

Fuel Factor 1.21 1.21 1.22

Dry Molecular Weight, lb/lb-Mole 30.18 30.20 30.20 30.193

Wet Molecular weight, lb/lb-Mole 28.60 28.94 28.63 28.723

Flue Gas Static Pressure, inches of H2O -0.59 -0.54 -0.62 -0.583

Absolute Flue Gas Pressure, inches of Mercury 28.82 28.82 28.77 28.803

Average Stack Gas Temperature, °F 123.81 123.13 124.35 123.763

Average Velocity Head, inches of H2O 0.7347722814

75748

0.734477056

706402

0.745019341

554471

0.738

Average Stack Gas Velocity, feet/second 51.81 51.46 52.21 51.827

Stack Cross-Sectional Area, square feet 213.825 213.825 213.825 213.825

Dry Volumetric Flow Rate, dry scfm 504,007.5 500,841.0 507,131.0 503,993.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 664,696.4 660,206.1 669,828.2 664,910.233

Percent Isokinetic of Sampling Rate, % 98.9 92.6 108.0 99.833

Percent Excess Air, % 40.3 39.4 37.6 39.100

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Round Duct Diameter, inches 198 198 198

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 14 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Location Unit 1 Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 1:00:00 PM 6:30:00 AM

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

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Fuel Factor 1.21 1.21 1.22

Dry Volumetric Flow Rate, dry scfm 586473 584462 582975 584,636.667

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Moisture, % 13.6 11 10.4 11.667

Analyzer Make Calif 

Analytical

Calif 

Analytical

Calif 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 18.1 18.1 18.1 18.100

Operating Units % % %

No. Readings/Avg. 240 240 240 240.000

Calibration Set 5 5 6 5.333

Calibration Pre Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Pre Zero Cylinder Instrument Response 0.11 0.05 0.13 0.097

Calibration Pre Zero Cylinder Bias 0.5 0.17 0.22 0.297

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0002789_C

O2

EB0002789_

CO2

EB0002789_

CO2

Calibration Pre High Cylinder Instrument Response 9.06 9.03 9.16 9.083

Calibration Pre High Cylinder Bias 0.11 -0.06 0.28 0.110

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Post Zero Cylinder Instrument Response 0.05 0.04 0.06 0.050

Calibration Post Zero Cylinder Bias 0.17 0.11 -0.17 0.037

Calibration Post Zero Cylinder Drift 0.33 0.06 0.39 0.260

Calibration Post High Cylinder ID EB0002789_C

O2

EB0002789_

CO2

EB0002789_

CO2

Calibration Post High Cylinder Instrument Response 9.03 9.04 9.05 9.040

Calibration Post High Cylinder Bias -0.06 0 -0.33 -0.130

Calibration Post High Cylinder Drift 0.17 0.06 0.61 0.280

Cavg 12.16 12.23 12.43 12.273

Cavg Units ppmvd ppmvd ppmvd

Cgas 12.0867 12.1579 12.2802 12.175

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 17, 2011 Page 15 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Location Unit 1 Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 1:00:00 PM 6:30:00 AM

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

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Fuel Factor 1.21 1.21 1.22

Dry Volumetric Flow Rate, dry scfm 586473 584462 582975 584,636.667

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Moisture, % 13.6 11 10.4 11.667

Analyzer Make Calif 

Analytical

Calif 

Analytical

Calif 

Analytical

Analyzer Model 200 200 200 200.000

Analyzer Serial Number 1L05017 1L05017 1L05017

Operating Range 22.4 22.4 22.4 22.400

Operating Units % % %

No. Readings/Avg. 240 240 240 240.000

Calibration Set 7 7 8 7.333

Calibration Pre Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Pre Zero Cylinder Instrument Response 0.04 0.09 0.01 0.047

Calibration Pre Zero Cylinder Bias -0.13 0.09 -0.18 -0.073

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0002789 EB0002789 EB0002789

Calibration Pre High Cylinder Instrument Response 11.05 11.01 11.09 11.050

Calibration Pre High Cylinder Bias 0.09 -0.09 0.22 0.073

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Post Zero Cylinder Instrument Response 0.09 0.11 0.02 0.073

Calibration Post Zero Cylinder Bias 0.09 0.18 -0.13 0.047

Calibration Post Zero Cylinder Drift 0.22 0.09 0.05 0.120

Calibration Post High Cylinder ID EB0002789 EB0002789 EB0002789

Calibration Post High Cylinder Instrument Response 11.01 11.1 11.02 11.043

Calibration Post High Cylinder Bias -0.09 0.31 -0.09 0.043

Calibration Post High Cylinder Drift 0.18 0.4 0.31 0.297

Cavg 6.25 6.2 5.98 6.143

Cavg Units ppmvd ppmvd ppmvd

Cgas 6.2047 6.1251 5.9434 6.091

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 17, 2011 Page 16 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Location Unit 1 Stack - Method 5/OTM-28

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 12:00:00 PM 6:30:00 AM

Run Finish Time 11:30:00 AM 4:30:00 PM 10:40:00 AM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.25 0.224 0.224 0.233

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 28.86 28.86 28.82 28.847

Average Orifice Meter Differential, inches H2O 2.40 1.55 1.50 1.817

Dry Gas Meter Volume Sampled, cubic feet 207.733 164.579 161.719 178.010

Average Dry Gas Meter Temperature, °F 87.96 91.00 81.33 86.763

Dry Gas Meter Volume Sampled, dscf 197.752 155.472 155.264 169.496

Total Moisture Liquid collected, g 557.8 408.1 381.7 449.200

Volume of Water Vapor, standard cubic feet 26.26 19.21 17.97 21.147

Moisture Content of Stack Gas, % 11.72 11.00 10.37 11.030

Moisture Saturation at Stack Gas Temperature, % 13.64 13.56 13.48 13.560

Dry Mole Fraction 0.8828 0.89 0.8963 0.890

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Carbon Monoxide & Nitrogen, % 81.7 81.7 81.8 81.733

Fuel Factor 1.21 1.21 1.22

Dry Molecular Weight, lb/lb-Mole 30.18 30.20 30.20 30.193

Wet Molecular weight, lb/lb-Mole 28.75 28.86 28.93 28.847

Flue Gas Static Pressure, inches of H2O -0.59 -0.54 -0.62 -0.583

Absolute Flue Gas Pressure, inches of Mercury 28.82 28.82 28.77 28.803

Average Stack Gas Temperature, °F 124.83 124.63 124.35 124.603

Average Velocity Head, inches of H2O 0.7529115119

52957

0.756177505

14338

0.755735259

298353

0.755

Average Stack Gas Velocity, feet/second 52.35 52.35 52.31 52.337

Stack Cross-Sectional Area, square feet 213.825 213.825 213.825 213.825

Dry Volumetric Flow Rate, dry scfm 515,614.8 519,998.0 522,621.2 519,411.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 671,624.3 671,624.3 671,111.1 671,453.233

Percent Isokinetic of Sampling Rate, % 100.2 97.3 96.7 98.067

Percent Excess Air, % 40.3 39.4 37.6 39.100

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Round Duct Diameter, inches 198 198 198

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 17 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Location Unit 1 Stack - Method 6C

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 1:00:00 PM 6:30:00 AM

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

Carbon Dioxide, % 12.4 12.2 12.3 12.300

Oxygen, % 6.2 6.1 5.9 6.067

Fuel Factor 1.19 1.21 1.22

Dry Volumetric Flow Rate, dry scfm 586473 584462 582975 584,636.667

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Moisture, % 13.6 11 10.4 11.667

Analyzer Make Western 

Research

Western 

Research

Western 

Research

Analyzer Model 721M 721M 721M

Analyzer Serial Number 93-721M8062-693-721M8062-693-721M8062-6

Operating Range 50.1 50.1 50.1 50.100

Operating Units ppm ppm ppm

No. Readings/Avg. 240 240 240 240.000

Calibration Set 1 1 2 1.333

Calibration Pre Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Pre Zero Cylinder Instrument Response 0.06 0.01 0.17 0.080

Calibration Pre Zero Cylinder Bias -0.04 -0.14 0.24 0.020

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0012233 EB0012233 EB0012233

Calibration Pre High Cylinder Instrument Response 25.56 25.28 25.99 25.610

Calibration Pre High Cylinder Bias 1.4 0.84 2.12 1.453

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Post Zero Cylinder Instrument Response 0.01 0.09 0.06 0.053

Calibration Post Zero Cylinder Bias -0.14 0.02 0.02 -0.033

Calibration Post Zero Cylinder Drift 0.1 0.16 0.22 0.160

Calibration Post High Cylinder ID EB0012233 EB0012233 EB0012233

Calibration Post High Cylinder Instrument Response 25.28 25.12 25.16 25.187

Calibration Post High Cylinder Bias 0.84 0.52 0.46 0.607

Calibration Post High Cylinder Drift 0.56 0.32 1.66 0.847

Cavg 23.61 25.27 20.41 23.097

Cavg Units ppmvd ppmvd ppmvd

Cgas 23.3103 25.1699 20.008 22.829

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 17, 2011 Page 18 of 19
Progress Energy, Asheville Plant, Unit 1

9/3/2010

Location Unit 1 Stack - Method 7E

Average

Run Number 1 2 3

Test Date 4/13/2010 4/13/2010 4/14/2010

Run Start Time 7:00:00 AM 1:00:00 PM 6:30:00 AM

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

Carbon Dioxide, % 12.1 12.2 12.3 12.200

Oxygen, % 6.2 6.1 5.9 6.067

Fuel Factor 1.21 1.21 1.22

Dry Volumetric Flow Rate, dry scfm 586473 584462 582975 584,636.667

F-Factor, dscfm/MMBtu @ %O2 9697 9599 9671 9,655.667

Moisture, % 13.6 11 10.4 11.667

Analyzer Make Thermo Thermo Thermo

Analyzer Model 42C 42C 42C

Analyzer Serial Number 42chl_67507_

357

42chl_67507

_357

42chl_67507_

357

Operating Range 50.6 50.6 50.6 50.600

Operating Units ppm ppm ppm

No. Readings/Avg. 240 240 240 240.000

Calibration Set 3 3 4 3.333

Calibration Pre Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Pre Zero Cylinder Instrument Response 0.03 0.09 0.17 0.097

Calibration Pre Zero Cylinder Bias 0 0.12 0.18 0.100

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0021065 EB0021065 EB0021065

Calibration Pre High Cylinder Instrument Response 25.14 24.97 25.16 25.090

Calibration Pre High Cylinder Bias 0.06 -0.28 48.4 16.060

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Post Zero Cylinder Instrument Response 0.09 0.13 0.05 0.090

Calibration Post Zero Cylinder Bias 0.12 0.2 -0.06 0.087

Calibration Post Zero Cylinder Drift 0.12 0.08 0.24 0.147

Calibration Post High Cylinder ID EB0021065 EB0021065 EB0021065

Calibration Post High Cylinder Instrument Response 24.97 24.48 24.89 24.780

Calibration Post High Cylinder Bias -0.28 -1.25 47.87 15.447

Calibration Post High Cylinder Drift 0.34 0.97 0.530000000

000001

0.613

Cavg 23.38 23.66 22.32 23.120

Cavg Units ppmvd ppmvd ppmvd

Cgas 22.8582 23.44 21.8401 22.713

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 17, 2011 Page 19 of 19