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 2

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 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Facility Information:

Progress Energy, Asheville, Unit 2

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 2

Permitted Maximum Process Rate:

2155 mmbtu/hr

Max. Normal Operation Process Rate:

1500

Target Process Test Rate

1500

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

 process flow diagram:

Flow diagram attached.

Industry/SCC/NAIS 221112

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 2 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 2 Stack Chromium Method 29 3 240 0

Unit 2 Stack Antimony Method 29 3 240 0

Unit 2 Stack Arsenic Method 29 3 240 0

Unit 2 Stack Barium Method 29 3 240 0

Unit 2 Stack Cadmium Method 29 3 240 0

Unit 2 Stack Filterable Particulate Method 29 3 240 0

Unit 2 Stack Cobalt Method 29 3 240 0

Thursday, February 17, 2011 Page 2 of 16
Progress Energy, Asheville Plant, Unit 2

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.

No modification or deviations

Unit 2 Stack Copper Method 29 3 240 0

Unit 2 Stack Thallium Method 29 3 240 0

Unit 2 Stack Beryllium Method 29 3 240 0

Unit 2 Stack Zinc Method 29 3 240 0

Unit 2 Stack Lead Method 29 3 240 0

Unit 2 Stack Silver Method 29 3 240 0

Unit 2 Stack Selenium Method 29 3 240 0

Unit 2 Stack Phosphorus (yellow or white) Method 29 3 240 0

Unit 2 Stack Nickel Method 29 3 240 0

Unit 2 Stack Manganese Method 29 3 240 0

Unit 2 Stack Co2 Method 3A CO2 3 240 0

Unit 2 Stack O2 Method 3A O2 3 240 0

Organic Condensible 

Particulate

Unit 2 Stack Method 5/OTM-28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Unit 2 Stack Method 5/OTM-28 3 240 0

Unit 2 Stack Filterable Particulate Method 5/OTM-28 3 240 0

Unit 2 Stack Total Particulate Method 5/OTM-28 3 240 0

Unit 2 Stack Sulfur Dioxide Method 6C 3 240 0

Unit 2 Stack Nitrogen oxides (NOx) Method 7E 3 240 0

Thursday, February 17, 2011 Page 3 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Sampling / Stack Data Results Summary

Location Unit 2 Stack - Method 29

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

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

AM

11:20:00 AM

Run Finish Time 4:15:00 PM 10:45:00 

AM

3:35:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 146.475 148.108 147.467 147.350

Moisture Content of Stack Gas, % 12.59 13.53 12.82 12.980

Moisture Saturation at Stack Gas Temperature, % 13.93 14.14 14.13 14.067

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Average Stack Gas Temperature, °F 125.54 125.35 125.35 125.413

Dry Volumetric Flow Rate, dry scfm 510,391.1 501,001.6 504,628.5 505,340.400

Actual Wet Volumetric Flue Gas Flow Rate, acfm 673,420.5 681,503.0 680,605.0 678,509.500

Percent Isokinetic of Sampling Rate, % 98.6 101.6 100.4 100.200

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 2 Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 12:45:00 PM 6:30:00 

AM

11:20:00 AM

Run Finish Time 4:45:00 PM 10:30:00 

AM

3:20:00 PM

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Dry Volumetric Flow Rate, dry scfm 591028 590136 584846 588,670.000

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Moisture, % 13.3 14.4 11.2 12.967

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 17, 2011 Page 4 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Location Unit 2 Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 12:45:00 PM 6:30:00 

AM

11:20:00 AM

Run Finish Time 4:45:00 PM 10:30:00 

AM

3:20:00 PM

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Dry Volumetric Flow Rate, dry scfm 591028 590136 584846 588,670.000

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Moisture, % 13.3 14.4 11.2 12.967

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 2 Stack - Method 5/OTM-28

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 11:45:00 AM 6:30:00 

AM

11:20:00 AM

Run Finish Time 4:00:00 PM 10:50:00 

AM

3:41:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 200.091 158.688 158.246 172.342

Moisture Content of Stack Gas, % 13.25 14.57 11.21 13.010

Moisture Saturation at Stack Gas Temperature, % 14.29 14.36 14.84 14.497

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Average Stack Gas Temperature, °F 126.48 125.92 127.17 126.523

Dry Volumetric Flow Rate, dry scfm 512,373.4 505,228.4 519,018.7 512,206.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 682,272.8 694,589.1 689,457.3 688,773.067

Percent Isokinetic of Sampling Rate, % 102.1 102.3 99.3 101.233

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 17, 2011 Page 5 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Location Unit 2 Stack - Method 6C

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 12:45:00 PM 6:30:00 

AM

11:20:00 AM

Run Finish Time 4:45:00 PM 10:30:00 

AM

3:20:00 PM

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Dry Volumetric Flow Rate, dry scfm 591028 590136 584846 588,670.000

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Moisture, % 13.3 14.4 11.2 12.967

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Unit 2 Stack - Method 7E

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 12:45:00 PM 6:30:00 

AM

11:20:00 AM

Run Finish Time 4:45:00 PM 10:30:00 

AM

3:20:00 PM

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Dry Volumetric Flow Rate, dry scfm 591028 590136 584846 588,670.000

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Moisture, % 13.3 14.4 11.2 12.967

Fuel Type Override Override Override

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Thursday, February 17, 2011 Page 6 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Emissions Summary

Location: Unit 2 Stack - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000558 0.000898 0.001031 0.001

lb/mmBtuO2 1.10E-07 1.76E-07 2.03E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.0142 0.0168 0.0172 0.016

lb/mmBtuO2 2.79E-06 3.29E-06 3.38E-06 0.000

Compound: Barium

Average

RunNumber 1 2 3

Mass_mg 0.0293 0.0436 0.0436 0.039

lb/mmBtuO2 5.75E-06 8.55E-06 8.56E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000122 0.000162 0.000162 0.000

lb/mmBtuO2 2.40E-08 3.18E-08 3.18E-08 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000427 0.000267 0.000105 0.000

lb/mmBtuO2 8.39E-08 5.23E-08 2.06E-08 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0086 0.0079 0.0049 0.007

lb/mmBtuO2 1.69E-06 1.55E-06 9.63E-07 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.001984 0.00147 0.00105 0.002

lb/mmBtuO2 3.90E-07 2.88E-07 2.06E-07 0.000

Compound: Copper

Average

RunNumber 1 2 3

Mass_mg 0.023 0.0085 0.0093 0.014

lb/mmBtuO2 4.52E-06 1.67E-06 1.83E-06 0.000

Compound: Filterable Particulate

Average

Thursday, February 17, 2011 Page 7 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

RunNumber 1 2 3

Mass_mg 24.3 23.1 13.8 20.400

lb/mmBtuO2 4.77E-03 4.53E-03 2.71E-03 0.004

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00102 0.00122 0.00112 0.001

lb/mmBtuO2 2.00E-07 2.39E-07 2.20E-07 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.01924 0.01044 0.00664 0.012

lb/mmBtuO2 3.78E-06 2.05E-06 1.30E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.40213 0.09943 0.04793 0.183

lb/mmBtuO2 7.90E-05 1.95E-05 9.42E-06 0.000

Compound: Phosphorus (yellow or white)

Average

RunNumber 1 2 3

Mass_mg 0.0182 0.0244 0.0221 0.022

lb/mmBtuO2 3.57E-06 4.78E-06 4.34E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.1103 0.0908 0.0945 0.099

lb/mmBtuO2 2.17E-05 1.78E-05 1.86E-05 0.000

Compound: Silver

Average

RunNumber 1 2 3

Mass_mg 0.000192 0.000037 0.0001045 0.000

lb/mmBtuO2 3.77E-08 7.25E-09 2.05E-08 0.000

Compound: Thallium

Average

RunNumber 1 2 3

Mass_mg 0.000201 0.000241 0.000271 0.000

lb/mmBtuO2 3.95E-08 4.72E-08 5.32E-08 0.000

Compound: Zinc

Average

RunNumber 1 2 3

Mass_mg 0.0561 0.0301 0.026 0.037

lb/mmBtuO2 1.10E-05 5.90E-06 5.11E-06 0.000

Location: Unit 2 Stack - Method 5/OTM-28

Thursday, February 17, 2011 Page 8 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Process Run Data

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 24.3 23.1 9.7 19.033

lb/mmBtuO2 3.49E-03 4.23E-03 1.78E-03 0.003

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 58.2 21.9 24.6 34.900

lb/mmBtuO2 8.37E-03 4.01E-03 4.50E-03 0.006

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 1.9 4.2 5.4 3.833

lb/mmBtuO2 2.73E-04 7.68E-04 9.89E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 84.4 49.2 39.7 57.767

lb/mmBtuO2 1.21E-02 9.00E-03 7.27E-03 0.009

Location: Unit 2 Stack - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 4.20E-02 5.23E-02 4.48E-02 0.046

ppm 1.94E+01 2.39E+01 2.05E+01 21.267

ppm@7%O2 1.74E+01 2.17E+01 1.85E+01 19.200

Location: Unit 2 Stack - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 1.64E-01 1.71E-01 1.68E-01 0.168

ppm 1.05E+02 1.09E+02 1.07E+02 107.000

ppm@7%O2 9.42E+01 9.90E+01 9.66E+01 96.600

Thursday, February 17, 2011 Page 9 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 1566 mmBtu/hr 1500

2 Heat Input 1656 mmBtu/hr 1500

3 Heat Input 1748 mmBtu/hr 1500

1 Steam Flow 1410 klbs/hr 1350

2 Steam Flow 1388 klbs/hr 1350

3 Steam Flow 1413 klbs/hr 1350

1 Coal Burned 85 tons/hr 80

2 Coal Burned 86 tons/hr 80

3 Coal Burned 81 tons/hr 80

Run Name Value UOM Comments

Target

Value

1 0

Run Name Value UOM Comments

1 0

Thursday, February 17, 2011 Page 10 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Sampling / Stack Data Results Detail

Location Unit 2 Stack - Method 29

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 12:00:00 PM 6:30:00 AM 11:20:00 AM

Run Finish Time 4:15:00 PM 10:45:00 AM 3:35:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

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 1.017 1.017 1.017 1.017

Barometric Pressure, inches of Mercury 28.81 28.25 28.25 28.437

Average Orifice Meter Differential, inches H2O 1.38 1.39 1.43 1.400

Dry Gas Meter Volume Sampled, cubic feet 157.415 158.421 159.730 158.522

Average Dry Gas Meter Temperature, °F 97.63 84.27 91.21 91.037

Dry Gas Meter Volume Sampled, dscf 146.475 148.108 147.467 147.350

Total Moisture Liquid collected, g 448.1 492.4 460.6 467.033

Volume of Water Vapor, standard cubic feet 21.09 23.18 21.68 21.983

Moisture Content of Stack Gas, % 12.59 13.53 12.82 12.980

Moisture Saturation at Stack Gas Temperature, % 13.93 14.14 14.13 14.067

Dry Mole Fraction 0.8741 0.8647 0.8718 0.870

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Carbon Monoxide & Nitrogen, % 81.8 81.8 81.7 81.767

Fuel Factor 1.21 1.21 1.20

Dry Molecular Weight, lb/lb-Mole 30.26 30.24 30.27 30.257

Wet Molecular weight, lb/lb-Mole 28.72 28.58 28.70 28.667

Flue Gas Static Pressure, inches of H2O -0.55 -0.63 -0.53 -0.570

Absolute Flue Gas Pressure, inches of Mercury 28.77 28.20 28.21 28.393

Average Stack Gas Temperature, °F 125.54 125.35 125.35 125.413

Average Velocity Head, inches of H2O 0.7540312966

59673

0.753355142

947822

0.754717264

38445

0.754

Average Stack Gas Velocity, feet/second 52.49 53.12 53.05 52.887

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

Dry Volumetric Flow Rate, dry scfm 510,391.1 501,001.6 504,628.5 505,340.400

Actual Wet Volumetric Flue Gas Flow Rate, acfm 673,420.5 681,503.0 680,605.0 678,509.500

Percent Isokinetic of Sampling Rate, % 98.6 101.6 100.4 100.200

Percent Excess Air, % 33.3 35.0 34.2 34.167

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

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 11 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Location Unit 2 Stack - Method 3A CO2

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 12:45:00 PM 6:30:00 AM 11:20:00 AM

Run Finish Time 4:45:00 PM 10:30:00 AM 3:20:00 PM

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Fuel Factor 1.21 1.21 1.2

Dry Volumetric Flow Rate, dry scfm 591028 590136 584846 588,670.000

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Moisture, % 13.3 14.4 11.2 12.967

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 13 14 14 13.667

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.11 0.03 0.09 0.077

Calibration Pre Zero Cylinder Bias 0.28 -0.5 -0.17 -0.130

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 9.08 9.01 9.09 9.060

Calibration Pre High Cylinder Bias -0.06 -0.83 -0.39 -0.427

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.04 0.09 0.07 0.067

Calibration Post Zero Cylinder Bias -0.11 -0.17 -0.28 -0.187

Calibration Post Zero Cylinder Drift 0.39 0.33 0.11 0.277

Calibration Post High Cylinder ID EB0002789_C

O2

EB0002789_

CO2

EB0002789_

CO2

Calibration Post High Cylinder Instrument Response 9.03 9.09 9.06 9.060

Calibration Post High Cylinder Bias -0.33 -0.39 -0.55 -0.423

Calibration Post High Cylinder Drift 0.27 0.44 0.16 0.290

Cavg 12.91 12.67 12.9 12.827

Cavg Units ppmvd ppmvd ppmvd

Cgas 12.8207 12.5819 12.7844 12.729

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 12 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Location Unit 2 Stack - Method 3A O2

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 12:45:00 PM 6:30:00 AM 11:20:00 AM

Run Finish Time 4:45:00 PM 10:30:00 AM 3:20:00 PM

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Fuel Factor 1.21 1.21 1.2

Dry Volumetric Flow Rate, dry scfm 591028 590136 584846 588,670.000

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Moisture, % 13.3 14.4 11.2 12.967

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 15 16 16 15.667

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.07 0.12 0.03 0.073

Calibration Pre Zero Cylinder Bias 0.09 0.36 -0.04 0.137

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0002789 EB0002789 EB0002789

Calibration Pre High Cylinder Instrument Response 11.01 10.87 11.03 10.970

Calibration Pre High Cylinder Bias -0.13 -0.85 -0.13 -0.370

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.04 0.03 0.01 0.027

Calibration Post Zero Cylinder Bias -0.04 -0.04 -0.13 -0.070

Calibration Post Zero Cylinder Drift 0.13 0.4 0.09 0.207

Calibration Post High Cylinder ID EB0002789 EB0002789 EB0002789

Calibration Post High Cylinder Instrument Response 11.03 11.03 11.03 11.030

Calibration Post High Cylinder Bias -0.04 -0.13 -0.13 -0.100

Calibration Post High Cylinder Drift 0.09 0.72 0 0.270

Cavg 5.44 5.63 5.53 5.533

Cavg Units ppmvd ppmvd ppmvd

Cgas 5.4022 5.6189 5.505 5.509

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 13 of 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Location Unit 2 Stack - Method 5/OTM-28

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 11:45:00 AM 6:30:00 AM 11:20:00 AM

Run Finish Time 4:00:00 PM 10:50:00 AM 3:41:00 PM

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 28.81 28.25 28.25 28.437

Average Orifice Meter Differential, inches H2O 2.44 1.57 1.61 1.873

Dry Gas Meter Volume Sampled, cubic feet 211.603 168.259 170.679 183.514

Average Dry Gas Meter Temperature, °F 90.75 80.31 89.67 86.910

Dry Gas Meter Volume Sampled, dscf 200.091 158.688 158.246 172.342

Total Moisture Liquid collected, g 649.1 575 424.3 549.467

Volume of Water Vapor, standard cubic feet 30.55 27.07 19.97 25.863

Moisture Content of Stack Gas, % 13.25 14.57 11.21 13.010

Moisture Saturation at Stack Gas Temperature, % 14.29 14.36 14.84 14.497

Dry Mole Fraction 0.8675 0.8564 0.8879 0.871

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Carbon Monoxide & Nitrogen, % 81.8 81.8 81.7 81.767

Fuel Factor 1.21 1.21 1.20

Dry Molecular Weight, lb/lb-Mole 30.26 30.24 30.27 30.257

Wet Molecular weight, lb/lb-Mole 28.64 28.52 28.89 28.683

Flue Gas Static Pressure, inches of H2O -0.55 -0.63 -0.53 -0.570

Absolute Flue Gas Pressure, inches of Mercury 28.77 28.20 28.21 28.393

Average Stack Gas Temperature, °F 126.48 125.92 127.17 126.523

Average Velocity Head, inches of H2O 0.7704130584

99981

0.780196840

67038

0.777223358

203542

0.776

Average Stack Gas Velocity, feet/second 53.18 54.14 53.74 53.687

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

Dry Volumetric Flow Rate, dry scfm 512,373.4 505,228.4 519,018.7 512,206.833

Actual Wet Volumetric Flue Gas Flow Rate, acfm 682,272.8 694,589.1 689,457.3 688,773.067

Percent Isokinetic of Sampling Rate, % 102.1 102.3 99.3 101.233

Percent Excess Air, % 33.3 35.0 34.2 34.167

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

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 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Location Unit 2 Stack - Method 6C

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 12:45:00 PM 6:30:00 AM 11:20:00 AM

Run Finish Time 4:45:00 PM 10:30:00 AM 3:20:00 PM

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Fuel Factor 1.21 1.21 1.2

Dry Volumetric Flow Rate, dry scfm 591028 590136 584846 588,670.000

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Moisture, % 13.3 14.4 11.2 12.967

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 11 12 12 11.667

Calibration Pre Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Pre Zero Cylinder Instrument Response 0.23 0.34 0.04 0.203

Calibration Pre Zero Cylinder Bias 0.24 0.04 -0.56 -0.093

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID EB0012233 EB0012233 EB0012233

Calibration Pre High Cylinder Instrument Response 25.17 24.98 24.32 24.823

Calibration Pre High Cylinder Bias -1.6 0.44 -0.88 -0.680

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB00020795 EB00020795 EB00020795

Calibration Post Zero Cylinder Instrument Response 0.11 0.04 0.05 0.067

Calibration Post Zero Cylinder Bias 0 -0.56 -0.54 -0.367

Calibration Post Zero Cylinder Drift 0.24 0.6 0.02 0.287

Calibration Post High Cylinder ID EB0012233 EB0012233 EB0012233

Calibration Post High Cylinder Instrument Response 24.97 24.32 25.01 24.767

Calibration Post High Cylinder Bias -2 -0.88 0.5 -0.793

Calibration Post High Cylinder Drift 0.4 1.32 1.38 1.033

Cavg 19.37 23.48 20.18 21.010

Cavg Units ppmvd ppmvd ppmvd

Cgas 19.3542 23.8994 20.5276 21.260

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 16
Progress Energy, Asheville Plant, Unit 2

9/3/2010

Location Unit 2 Stack - Method 7E

Average

Run Number 1 2 3

Test Date 4/14/2010 4/15/2010 4/15/2010

Run Start Time 12:45:00 PM 6:30:00 AM 11:20:00 AM

Run Finish Time 4:45:00 PM 10:30:00 AM 3:20:00 PM

Carbon Dioxide, % 12.8 12.6 12.8 12.733

Oxygen, % 5.4 5.6 5.5 5.500

Fuel Factor 1.21 1.21 1.2

Dry Volumetric Flow Rate, dry scfm 591028 590136 584846 588,670.000

F-Factor, dscfm/MMBtu @ %O2 9677 9641 9682 9,666.667

Moisture, % 13.3 14.4 11.2 12.967

Analyzer Make Thermo Thermo Thermo

Analyzer Model 42C 42C 42C

Analyzer Serial Number 42chl_6750_3

57

42chi_67507

_357

42chi_67507_

357

Operating Range 125 125 125 125.000

Operating Units ppm ppm ppm

No. Readings/Avg. 240 240 240 240.000

Calibration Set 9 10 10 9.667

Calibration Pre Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Pre Zero Cylinder Instrument Response 0.06 0.38 0.17 0.203

Calibration Pre Zero Cylinder Bias -0.74 -0.05 -0.22 -0.337

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC316274 CC316274 CC316274

Calibration Pre High Cylinder Instrument Response 85.12 86.13 84.76 85.337

Calibration Pre High Cylinder Bias -0.24 0.62 -0.47 -0.030

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID EB0020795 EB0020795 EB0020795

Calibration Post Zero Cylinder Instrument Response 0.03 0.17 0.09 0.097

Calibration Post Zero Cylinder Bias -0.76 -0.22 -0.28 -0.420

Calibration Post Zero Cylinder Drift 0.02 0.17 0.06 0.083

Calibration Post High Cylinder ID CC316274 CC316274 CC316274

Calibration Post High Cylinder Instrument Response 85.45 84.76 85.05 85.087

Calibration Post High Cylinder Bias 0.02 -0.47 -0.24 -0.230

Calibration Post High Cylinder Drift 0.26 1.09 0.23 0.527

Cavg 106.83 110.36 108.13 108.440

Cavg Units ppmvd ppmvd ppmvd

Cgas 105.3569 108.702 107.1401 107.066

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 16