Name: Jesse Locklar

Title: Plant Director

Company: Dominion Generation

Sign Date: 8/24/2010

Name: Athur B. Nunn

Title: President

Company: The Air Compliance Group, LLC

Sign Date: 7/14/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Morgantown Energy Facility ICR Testing

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.

Monday, January 17, 2011 Page 1 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Facility Information:

Morgantown Energy Facility

555 Beechurst Avenue

Morgantown W 26505

Contact: David Nuckols

Phone: 804-796-6021

Fax:

Email: david.nuckols@dom.com

Testing Company:

The Air Compliance Group, LLC

5075 Hollins Road

Roanoke VA 24019

Contact: Arthur B. Nunn, III - President

Phone: 540-265-1987, Ext. 201

Fax: 540-265-0082

Email: art.nunn@aircompgroup.com

Air Permit Number: Permitted Source ID/Name:

1 and 2 Boilers 1 and 2 Combined in Common Stack

Permitted Maximum Process Rate:

Two 280,000 lb/Hr Boilers

Max. Normal Operation Process Rate: Target Process Test Rate

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

 process flow diagram:

The Morgantown Energy Facility consists of two pulverized coal boilers, each with a fabric filter baghouse, and a 

turbine generator. The flue gases from the two boilers are exhausted through a common stack. Each boiler produces 

280,000 lb/hr of steam at a coal feed rate of 22.73 tons/hr. Steam from the boilers is fed to a condensing turbine 

generator. The rated generator output is approximately 58 MW.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 5406100027 FRS #: 110000344903

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 Exit 118 0 0 0 1389 2358 2 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit Carbon Monoxide Method 10 3 120 0

Stack Exit Formaldehyde Method 0011 3 180 0

Stack Exit Other TCDD Method 23 0

Stack Exit Other PeCDD Method 23 0

Stack Exit Other HxCDD Method 23 0

Stack Exit Other HpCDD Method 23 0

Stack Exit Other TCDF Method 23 0

Monday, January 17, 2011 Page 2 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

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.

Stack Exit Other PeCDF Method 23 0

Stack Exit Other HxCDF Method 23 0

Stack Exit Other HpCDF Method 23 0

Stack Exit 3,3',4,4'-TCB (PCB77) Method 23 3 480 0

Stack Exit 3,4,4',5-TCB (PCB81) Method 23 3 480 0

Stack Exit 2,3,3',4,4'-PeCB (PCB105) Method 23 3 480 0

Stack Exit 2,3,4,4',5-PeCB (PCB114) Method 23 3 480 0

Stack Exit 2,3',4,4',5-PeCB (PCB118) Method 23 3 480 0

Stack Exit 2',3,4,4',5-PeCB (PCB123) Method 23 3 480 0

Stack Exit 3,3',4,4',5-PeCB (PCB126) Method 23 3 480 0

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Stack Exit Method 23 3 480 0

Stack Exit 2,3',4,4',5,5'-HxCB (PCB167) Method 23 3 480 0

Stack Exit 3,3',4,4',5,5'-HxCB (PCB169) Method 23 3 480 0

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Stack Exit Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Inorganic (Aqueous) 

Condensible Part.

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Organic Condensible 

Particulate

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 120 0

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Monday, January 17, 2011 Page 3 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

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.

None

Monday, January 17, 2011 Page 4 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number M0011-1 M0011-2 M0011-3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 7:36:00 AM 11:32:00 

AM

3:40:00 PM

Run Finish Time 10:33:00 AM 2:51:00 PM 6:35:00 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 135.571 130.747 128.219 131.512

Moisture Content of Stack Gas, % 7.08 7.39 7.30 7.257

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

Carbon Dioxide, % 14.72 14.79 14.77 14.760

Oxygen, % 4.28 4.1 4.1 4.160

Average Stack Gas Temperature, °F 412.00 410.67 407.17 409.947

Dry Volumetric Flow Rate, dry scfm 158,724.9 159,763.0 155,912.2 158,133.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 288,572.0 290,987.0 282,557.2 287,372.067

Percent Isokinetic of Sampling Rate, % 105.7 101.3 101.8 102.933

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - 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

Monday, January 17, 2011 Page 5 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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 Exit - 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

Monday, January 17, 2011 Page 6 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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 Exit - 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

Monday, January 17, 2011 Page 7 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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 Exit - 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

Monday, January 17, 2011 Page 8 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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 Exit - 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

Monday, January 17, 2011 Page 9 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber M0011-1 M0011-2 M0011-3

Mass_mg 0.01934 0.01249 0.01565 0.016

Elb/hr 3.00E-03 2.02E-03 2.52E-03 0.003

lb/mmBtuO2 3.87E-06 2.56E-06 3.27E-06 0.000

ppm 4.04E-03 2.70E-03 3.45E-03 0.003

ppm@7%O2 3.38E-03 2.23E-03 2.85E-03 0.003

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

Elb/hr 5.92E+01 9.71E+01 4.69E+01 67.733

lb/mmBtuO2 6.90E-02 1.11E-01 5.46E-02 0.078

ppm 7.68E+01 1.27E+02 6.18E+01 88.533

ppm@7%O2 6.45E+01 1.04E+02 5.11E+01 73.200

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 7.86E-01 2.60E-01 9.03E-01 0.650

lb/mmBtuO2 9.17E-04 3.00E-04 1.05E-03 0.001

ppm 6.48E-01 2.15E-01 7.57E-01 0.540

ppm@7%O2 5.45E-01 1.78E-01 6.26E-01 0.450

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 35.843 34.336 32.136 34.105

Elb/hr 6.09E+00 5.56E+00 5.40E+00 5.683

lb/mmBtuO2 7.60E-03 7.28E-03 6.95E-03 0.007

mg/dscm 9.90E+00 9.58E+00 9.15E+00 9.543

mg/dscm@7%O2 8.28E+00 7.93E+00 7.57E+00 7.927

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0.251 0.248 0.238 0.246

Elb/hr 4.26E-02 4.02E-02 4.00E-02 0.041

lb/mmBtuO2 5.32E-05 5.26E-05 5.15E-05 0.000

mg/dscm 6.93E-02 6.92E-02 6.78E-02 0.069

mg/dscm@7%O2 5.80E-02 5.73E-02 5.61E-02 0.057

Location: Stack Exit - Method 29

Monday, January 17, 2011 Page 10 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00036 0.00063 0.02771 0.010

Elb/hr 4.28E-05 7.38E-05 3.31E-03 0.001

lb/mmBtuO2 5.38E-08 9.41E-08 4.34E-06 0.000

mg/dscm 7.08E-05 1.23E-04 5.76E-03 0.002

mg/dscm@7%O2 5.86E-05 1.02E-04 4.73E-03 0.002

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00149 0.0013 0.01003 0.004

Elb/hr 1.77E-04 1.52E-04 1.20E-03 0.001

lb/mmBtuO2 2.23E-07 1.94E-07 1.57E-06 0.000

mg/dscm 2.93E-04 2.55E-04 2.09E-03 0.001

mg/dscm@7%O2 2.42E-04 2.12E-04 1.72E-03 0.001

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00009 0.0001 0.00018 0.000

Elb/hr 1.07E-05 1.17E-05 2.15E-05 0.000

lb/mmBtuO2 1.34E-08 1.49E-08 2.82E-08 0.000

mg/dscm 1.77E-05 1.96E-05 3.74E-05 0.000

mg/dscm@7%O2 1.46E-05 1.63E-05 3.07E-05 0.000

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00073 0.00015 0.00201 0.001

Elb/hr 8.69E-05 1.76E-05 2.40E-04 0.000

lb/mmBtuO2 1.09E-07 2.24E-08 3.15E-07 0.000

mg/dscm 1.44E-04 2.94E-05 4.18E-04 0.000

mg/dscm@7%O2 1.19E-04 2.44E-05 3.43E-04 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00693 0.00484 0.01298 0.008

Elb/hr 8.25E-04 5.67E-04 1.55E-03 0.001

lb/mmBtuO2 1.03E-06 7.23E-07 2.03E-06 0.000

mg/dscm 1.36E-03 9.49E-04 2.70E-03 0.002

mg/dscm@7%O2 1.13E-03 7.88E-04 2.22E-03 0.001

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00187 0.00079 0.00128 0.001

Elb/hr 2.23E-04 9.25E-05 1.53E-04 0.000

lb/mmBtuO2 2.79E-07 1.18E-07 2.01E-07 0.000

mg/dscm 3.68E-04 1.55E-04 2.66E-04 0.000

mg/dscm@7%O2 3.04E-04 1.29E-04 2.18E-04 0.000

Monday, January 17, 2011 Page 11 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00532 0.00151 0.03913 0.015

Elb/hr 6.33E-04 1.77E-04 4.68E-03 0.002

lb/mmBtuO2 7.94E-07 2.26E-07 6.13E-06 0.000

mg/dscm 1.05E-03 2.96E-04 8.14E-03 0.003

mg/dscm@7%O2 8.69E-04 2.46E-04 6.68E-03 0.003

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.02351 0.01091 0.01985 0.018

Elb/hr 2.80E-03 1.28E-03 2.37E-03 0.002

lb/mmBtuO2 3.51E-06 1.63E-06 3.11E-06 0.000

mg/dscm 4.62E-03 2.14E-03 4.13E-03 0.004

mg/dscm@7%O2 3.82E-03 1.78E-03 3.39E-03 0.003

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00526 0.00246 0.00644 0.005

Elb/hr 6.26E-04 2.88E-04 7.70E-04 0.001

lb/mmBtuO2 7.86E-07 3.67E-07 1.01E-06 0.000

mg/dscm 1.03E-03 4.82E-04 1.34E-03 0.001

mg/dscm@7%O2 8.52E-04 4.00E-04 1.10E-03 0.001

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00604 0.00196 0.00129 0.003

Elb/hr 7.19E-04 2.30E-04 1.54E-04 0.000

lb/mmBtuO2 9.02E-07 2.93E-07 2.02E-07 0.000

mg/dscm 1.19E-03 3.84E-04 2.68E-04 0.001

mg/dscm@7%O2 9.85E-04 3.19E-04 2.20E-04 0.001

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 2.50E+02 2.59E+02 2.52E+02 253.667

lb/mmBtuO2 2.92E-01 2.98E-01 2.94E-01 0.295

ppm 1.42E+02 1.48E+02 1.45E+02 145.000

ppm@7%O2 1.19E+02 1.22E+02 1.20E+02 120.333

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 2.60E+02 2.57E+02 2.50E+02 255.667

lb/mmBtuO2 3.03E-01 2.96E-01 2.92E-01 0.297

ppm 2.05E+02 2.04E+02 2.01E+02 203.333

Monday, January 17, 2011 Page 12 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Process Run Data

ppm@7%O2 1.72E+02 1.69E+02 1.66E+02 169.000

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber M027/8-1 M027/8-3 M027/8-5

Mass_mg 56.06 45.39 33.59 45.013

Elb/hr 8.21E+00 7.62E+00 5.72E+00 7.183

gr/dscf 6.04E-03 5.56E-03 4.14E-03 0.005

lb/mmBtuO2 1.05E-02 9.63E-03 7.18E-03 0.009

Compound: Filterable PM2.5

Average

RunNumber M027/8-1 M027/8-3 M027/8-5

Mass_mg 43.02 23.62 10.42 25.687

Elb/hr 6.30E+00 3.96E+00 1.77E+00 4.010

gr/dscf 4.63E-03 2.90E-03 1.28E-03 0.003

lb/mmBtuO2 8.05E-03 5.01E-03 2.23E-03 0.005

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber M027/8-1 M027/8-3 M027/8-5

Mass_mg 85.55 59.05 67.81 70.803

Elb/hr 1.25E+01 9.91E+00 1.15E+01 11.303

gr/dscf 9.22E-03 7.24E-03 8.35E-03 0.008

lb/mmBtuO2 1.60E-02 1.25E-02 1.45E-02 0.014

Compound: Organic Condensible Particulate

Average

RunNumber M027/8-1 M027/8-3 M027/8-5

Mass_mg 2.25 1.65 3.89 2.597

Elb/hr 3.30E-01 2.77E-01 6.62E-01 0.423

gr/dscf 2.42E-04 2.02E-04 4.79E-04 0.000

lb/mmBtuO2 4.21E-04 3.50E-04 8.32E-04 0.001

Compound: Total Particulate

Average

RunNumber M027/8-1 M027/8-3 M027/8-5

Mass_mg 143.86 106.09 105.29 118.413

Elb/hr 2.11E+01 1.78E+01 1.79E+01 18.933

gr/dscf 1.55E-02 1.30E-02 1.30E-02 0.014

lb/mmBtuO2 2.69E-02 2.25E-02 2.25E-02 0.024

Compound: Total PM2.5

Average

RunNumber M027/8-1 M027/8-3 M027/8-5

Mass_mg 130.82 84.32 82.12 99.087

Elb/hr 1.92E+01 1.41E+01 1.40E+01 15.767

gr/dscf 1.41E-02 1.03E-02 1.01E-02 0.012

lb/mmBtuO2 2.45E-02 1.79E-02 1.76E-02 0.020

Monday, January 17, 2011 Page 13 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Burned 60.8 1000 Lbs/hr 0 OTM027/8 - Run 1

2 Coal Burned 60.8 1000 Lbs/hr M29 & M30B Run 

1

0

3 Coal Burned 59.4 1000 Lbs/hr 0 M0010 Run 1

1 Average Heat Input 782 MMBtu/hr 0 OTM027/8 - Run 1

2 Average Heat Input 782 MMBtu/hr M29 & M30B Run 

1

0

3 Average Heat Input 834 MMBtu/hr 0 M0010 Run 1

1 Steam Output 543 1000 lb steam/hr 0 OTM027/8 - Run 1

2 Steam Output 543 1000 lb steam/hr M29 & M30B Run 

1

0

3 Steam Output 545 1000 lb steam/hr 0 M0010 Run 1

1 Unit Net Electric Generation 58 MWh 0 OTM027/8 - Run 1

4 Coal Burned 59.4 1000 Lbs/hr M29 & M30B Run 

2

0

4 Average Heat Input 799 MMBtu/hr M29 & M30B Run 

2

0

4 Steam Output 542 1000 lb steam/hr M29 & M30B Run 

2

0

4 Unit Net Electric Generation 58 MWh M29 & M30B Run 

2

0

5 Coal Burned 59.8 1000 Lbs/hr Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 1

0

5 Average Heat Input 808 MMBtu/hr Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 1

0

5 Steam Output 539 1000 lb steam/hr Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 1

0

5 Unit Net Electric Generation 58 MWh Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 1

0

6 Coal Burned 59.8 1000 Lbs/hr Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 2

0

Monday, January 17, 2011 Page 14 of 26
Morgantown Energy Facility ICR Testing

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6 Average Heat Input 793 MMBtu/hr Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 2

0

6 Steam Output 536 1000 lb steam/hr Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 2

0

6 Unit Net Electric Generation 58 MWh Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 2

0

7 Coal Burned 59.8 1000 Lbs/hr Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 3

0

7 Average Heat Input 793 MMBtu/hr Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 3

0

7 Steam Output 532 1000 lb steam/hr Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 3

0

7 Unit Net Electric Generation 58 MWh Methods 3A, 6C, 

7E, 10, 18, 25A, 

26A, 0011, & 

0031 Run 3

0

8 Coal Burned 55.5 1000 Lbs/hr M0010 & OTM 

027/8 Run 2

0

8 Average Heat Input 810 MMBtu/hr M0010 & OTM 

027/8 Run 2

0

8 Steam Output 534 1000 lb steam/hr M0010 & OTM 

027/8 Run 2

0

8 Unit Net Electric Generation 58 MWh M0010 & OTM 

027/8 Run 2

0

9 Coal Burned 56.3 1000 Lbs/hr 0 M0010 Run 3

9 Average Heat Input 757 MMBtu/hr 0 M0010 Run 3

9 Steam Output 530 1000 lb steam/hr 0 M0010 Run 3

9 Unit Net Electric Generation 58 MWh 0 M0010 Run 3

10 Coal Burned 55.5 1000 Lbs/hr 0 M29 & 30B Run 3

10 Average Heat Input 782 MMBtu/hr 0 M29 & 30B Run 3

10 Steam Output 528 1000 lb steam/hr 0 M29 & 30B Run 3

10 Unit Net Electric Generation 57.5 MWh 0 M29 & 30B Run 3

11 Coal Burned 56.3 1000 Lbs/hr 0 OTM027/8 Run 3

11 Average Heat Input 757 MMBtu/hr 0 OTM027/8 Run 3

Monday, January 17, 2011 Page 15 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

APCD Run Data

Process Lab Run Data

11 Steam Output 530 1000 lb steam/hr 0 OTM027/8 Run 3

11 Unit Net Electric Generation 58 MWh 0 OTM027/8 Run 3

Run Name Value UOM Comments

Target

Value

1 BAGHOUSE 0 0

1 0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

1 Fuel Mercury Content 0 ppm

1 Fuel Cadmium Content 0 ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 0 ppm

1 Fuel Arsenic Content 0 ppm

1 Fuel Chromium Content 0 ppm

1 Fuel Beryllium Content 0 ppm

1 Fuel Lead Content 0 ppm

1 Fuel Manganese Content 0 ppm

1 Fuel Chlorine Content 0 ppm

1 Fuel Fluorine Content 0 ppm

Monday, January 17, 2011 Page 16 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number M0011-1 M0011-2 M0011-3

Test Date 4/29/2010 4/29/2010 4/29/2010

Run Start Time 7:36:00 AM 11:32:00 AM 3:40:00 PM

Run Finish Time 10:33:00 AM 2:51:00 PM 6:35:00 PM

Net Traversing Points 2 2 2

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.25 0.25 0.25 0.250

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9983 0.9983 0.9983 0.998

Barometric Pressure, inches of Mercury 29.29 29.29 29.29 29.290

Average Orifice Meter Differential, inches H2O 1.75 1.82 1.72 1.763

Dry Gas Meter Volume Sampled, cubic feet 138.378 137.360 135.295 137.011

Average Dry Gas Meter Temperature, °F 69.00 84.58 86.83 80.137

Dry Gas Meter Volume Sampled, dscf 135.571 130.747 128.219 131.512

Total Moisture Liquid collected, g 219.4 221.8 214.5 218.567

Volume of Water Vapor, standard cubic feet 10.33 10.44 10.10 10.290

Moisture Content of Stack Gas, % 7.08 7.39 7.30 7.257

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

Dry Mole Fraction 0.9292 0.9261 0.927 0.927

Carbon Dioxide, % 14.72 14.79 14.77 14.760

Oxygen, % 4.28 4.1 4.1 4.160

Carbon Monoxide & Nitrogen, % 81 81.11 81.13 81.080

Fuel Factor 1.13 1.14 1.14

Dry Molecular Weight, lb/lb-Mole 30.53 30.53 30.53 30.530

Wet Molecular weight, lb/lb-Mole 29.64 29.60 29.62 29.620

Flue Gas Static Pressure, inches of H2O -0.59 -0.58 -0.6 -0.590

Absolute Flue Gas Pressure, inches of Mercury 29.25 29.25 29.25 29.250

Average Stack Gas Temperature, °F 412.00 410.67 407.17 409.947

Average Velocity Head, inches of H2O 0.7731572875

10174

0.786313400

681963

0.744991610

643783

0.768

Average Stack Gas Velocity, feet/second 63.33 63.86 62.01 63.067

Stack Cross-Sectional Area, square feet 75.944 75.944 75.944 75.944

Dry Volumetric Flow Rate, dry scfm 158,724.9 159,763.0 155,912.2 158,133.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 288,572.0 290,987.0 282,557.2 287,372.067

Percent Isokinetic of Sampling Rate, % 105.7 101.3 101.8 102.933

Percent Excess Air, % 25.0 23.7 23.7 24.133

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

Round Duct Diameter, inches 118 118 118

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Monday, January 17, 2011 Page 17 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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

Monday, January 17, 2011 Page 18 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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

Monday, January 17, 2011 Page 19 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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

Monday, January 17, 2011 Page 20 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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

Monday, January 17, 2011 Page 21 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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

Monday, January 17, 2011 Page 22 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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

Monday, January 17, 2011 Page 23 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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

Monday, January 17, 2011 Page 24 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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

Monday, January 17, 2011 Page 25 of 26
Morgantown Energy Facility ICR Testing

8/24/2010

Location Stack Exit - 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

Monday, January 17, 2011 Page 26 of 26