Name: C.D. Holley

Title: Vice President F&H System Operation

Company: Dominion Generation

Sign Date: 8/19/2010

Name: Michael P. Martin

Title: Senior Project Manager

Company: TRC Companies, Inc.

Sign Date: 8/19/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 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.

Wednesday, January 12, 2011 Page 1 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Facility Information:

Hopewell Power Station

107 Terminal Street

Hopewell VA 23860

Contact: David Nuckols

Phone: 804-796-6021

Fax: 804-796-6004

Email: david.nuckols@dom.com

Testing Company:

TRC Companies, Inc.

650 Suffolk Street

Lowell MA 01854

Contact:Michael P. Martin

Phone: 978-656-3550

Fax: 978-453-4215

Email: mmartin@trcsolutions.com

Air Permit Number:

10771

Permitted Source ID/Name:

1_2

Permitted Maximum Process Rate:

N/A

Max. Normal Operation Process Rate:

N/A

Target Process Test Rate

N/A

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

 process flow diagram:

Unit 1 & Unit 2 are each a 391 mmBtu/hr spreader stoker coal boiler. Each have overfire air, dry lime FGD, SNCR, 

& a baghouse.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 5167000063 FRS #: 110000342629

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 96 0 0 0 1284 1056 4 6

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 3 120 0

Stack Exit 2,3,7,8-TCDD Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDD Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDD Method 23 3 480 0

Stack Exit 1,2,3,7,8,9-HxCDD Method 23 3 480 0

Wednesday, January 12, 2011 Page 2 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Stack Exit 1,2,3,4,6,7,8-HpCDD Method 23 3 480 0

Stack Exit OCDD Method 23 3 480 0

Stack Exit 2,3,7,8-TCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8-PeCDF Method 23 3 480 0

Stack Exit 2,3,4,7,8-PeCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 2,3,4,6,7,8-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,7,8,9-HxCDF Method 23 3 480 0

Stack Exit 1,2,3,4,6,7,8-HpCDF Method 23 3 480 0

Stack Exit 1,2,3,4,7,8,9-HpCDF Method 23 3 480 0

Stack Exit OCDF Method 23 3 480 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

Stack Exit Other PeCDF Method 23 0

Stack Exit Other HxCDF Method 23 0

Stack Exit Other HpCDF Method 23 0

Stack Exit Total Dioxins Method 23 3 480 0

Stack Exit Total Furans Method 23 3 480 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

Method 25A 3 120 0 NMHC emissions 

only. Methane 

emissions reported in 

excel template.

Stack Exit

Stack Exit Hydrogen Fluoride Method 26A 3 180 0

Stack Exit Hydrogen Chloride Method 26A 3 180 0

Organic Condensible 

Particulate

Stack Exit OTM - 27/28 3 240 0

Stack Exit Filterable Particulate OTM - 27/28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

Stack Exit OTM - 27/28 3 240 0

Stack Exit Total PM2.5 OTM - 27/28 3 240 0

Stack Exit Total Particulate OTM - 27/28 3 240 0

Stack Exit Filterable PM2.5 OTM - 27/28 3 240 0

Stack Exit Cobalt Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Wednesday, January 12, 2011 Page 3 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

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 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 Sulfur Dioxide Method 6C 3 180 0

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

Wednesday, January 12, 2011 Page 4 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 4/23/2010 4/23/2010 4/23/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 110.280 111.851 110.874 111.002

Moisture Content of Stack Gas, % 13.84 13.61 13.40 13.617

Moisture Saturation at Stack Gas Temperature, % 98.90 100.00 100.00 99.633

Carbon Dioxide, % 13.578 13.624 13.634 13.612

Oxygen, % 5.536 5.484 5.482 5.501

Average Stack Gas Temperature, °F 211.21 214.13 214.96 213.433

Dry Volumetric Flow Rate, dry scfm 179,485.1 182,434.4 180,152.3 180,690.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 266,062.7 270,888.1 267,269.1 268,073.300

Percent Isokinetic of Sampling Rate, % 99.3 99.1 99.5 99.300

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 1 2 3

Test Date 4/23/2010 4/23/2010 4/23/2010

Run Start Time 9:50:00 AM 12:20:00 

PM

3:42:00 PM

Run Finish Time 11:50:00 AM 2:20:00 PM 5:42:00 PM

Carbon Dioxide, % 13.578 13.624 13.634 13.612

Oxygen, % 5.536 5.484 5.482 5.501

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, January 12, 2011 Page 5 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 23

Average

Run Number 2 3 4

Test Date 4/20/2010 4/21/2010 4/24/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 480 480 480

Dry Gas Meter Volume Sampled, dscf 454.441 451.286 463.722 456.483

Moisture Content of Stack Gas, % 12.62 13.00 13.61 13.077

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

Carbon Dioxide, % 13.3 13.3 13.4 13.333

Oxygen, % 5.9 5.8 5.8 5.833

Average Stack Gas Temperature, °F 214.49 214.30 213.23 214.007

Dry Volumetric Flow Rate, dry scfm 184,434.7 180,352.4 182,027.4 182,271.500

Actual Wet Volumetric Flue Gas Flow Rate, acfm 267,842.1 265,007.1 269,380.2 267,409.800

Percent Isokinetic of Sampling Rate, % 101.4 103.0 104.8 103.067

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 25A

Average

Run Number 1 2 3

Test Date 4/23/2010 4/23/2010 4/23/2010

Run Start Time 9:50:00 AM 12:20:00 

PM

3:42:00 PM

Run Finish Time 11:50:00 AM 2:20:00 PM 5:42:00 PM

Carbon Dioxide, %

Oxygen, % 5.536 5.484 5.482 5.501

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 13.99 13.87 13.71 13.857

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, January 12, 2011 Page 6 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 4/19/2010 4/20/2010 4/20/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 192 192 192

Dry Gas Meter Volume Sampled, dscf 182.013 179.875 182.262 181.383

Moisture Content of Stack Gas, % 13.92 14.17 14.08 14.057

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

Carbon Dioxide, % 13.59 13.32 13.81 13.573

Oxygen, % 5.56 5.87 5.96 5.797

Average Stack Gas Temperature, °F 216.42 215.96 216.77 216.383

Dry Volumetric Flow Rate, dry scfm 179,842.0 179,547.8 180,742.1 180,043.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 264,645.2 266,032.5 267,842.1 266,173.267

Percent Isokinetic of Sampling Rate, % 102.2 101.2 101.8 101.733

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 29 

Average

Run Number 1 2 3

Test Date 4/22/2010 4/22/2010 4/24/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 223.500 220.844 217.100 220.481

Moisture Content of Stack Gas, % 13.41 14.04 14.01 13.820

Moisture Saturation at Stack Gas Temperature, % 97.79 97.50 100.00 98.430

Carbon Dioxide, % 13.55 13.66 13.43 13.547

Oxygen, % 5.53 5.445 5.63 5.535

Average Stack Gas Temperature, °F 210.73 210.58 213.17 211.493

Dry Volumetric Flow Rate, dry scfm 177,902.6 177,726.3 175,682.8 177,103.900

Actual Wet Volumetric Flue Gas Flow Rate, acfm 261,780.1 263,378.5 261,176.9 262,111.833

Percent Isokinetic of Sampling Rate, % 101.5 100.4 99.8 100.567

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

Wednesday, January 12, 2011 Page 7 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 6C

Average

Run Number 1 2 3

Test Date 4/21/2010 4/22/2010 4/22/2010

Run Start Time 3:51:00 PM 7:11:00 

AM

11:24:00 AM

Run Finish Time 6:51:00 PM 10:11:00 

AM

2:24:00 PM

Carbon Dioxide, % 13.529 13.583 13.53 13.547

Oxygen, % 5.563 5.526 5.534 5.541

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 7E

Average

Run Number 1 2 3

Test Date 4/21/2010 4/22/2010 4/22/2010

Run Start Time 3:51:00 PM 7:11:00 

AM

11:24:00 AM

Run Finish Time 6:51:00 PM 10:11:00 

AM

2:24:00 PM

Carbon Dioxide, % 13.529 13.583 13.53 13.547

Oxygen, % 5.563 5.526 5.534 5.541

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Wednesday, January 12, 2011 Page 8 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - OTM - 27/28

Average

Run Number 1 2 3

Test Date 4/21/2010 4/22/2010 4/22/2010

Run Start Time

Run Finish Time

Net Run Time, minutes 366.5 327 332.25

Dry Gas Meter Volume Sampled, dscf 132.289 121.758 126.092 126.713

Moisture Content of Stack Gas, % 12.89 13.26 13.41 13.187

Moisture Saturation at Stack Gas Temperature, % 100.00 97.46 100.00 99.153

Carbon Dioxide, % 13.49 13.509 13.66 13.553

Oxygen, % 5.572 5.543 5.445 5.520

Average Stack Gas Temperature, °F 215.83 210.58 213.08 213.163

Dry Volumetric Flow Rate, dry scfm 187,799.2 186,917.8 185,697.2 186,804.733

Actual Wet Volumetric Flue Gas Flow Rate, acfm 276,226.3 274,416.7 279,453.3 276,698.767

Percent Isokinetic of Sampling Rate, % 93.0 96.4 98.9 96.100

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

Wednesday, January 12, 2011 Page 9 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.0186 0.00853 0.0105 0.013

lb/mmBtuO2 4.95E-06 2.23E-06 2.77E-06 0.000

ppm 4.77E-03 2.16E-03 2.68E-03 0.003

ppm@7%O2 4.32E-03 1.95E-03 2.42E-03 0.003

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.42E-01 1.30E-01 1.49E-01 0.140

ppm 1.46E+02 1.35E+02 1.54E+02 145.000

ppm@7%O2 1.32E+02 1.22E+02 1.39E+02 131.000

Location: Stack Exit - Method 23

Compound: 1,2,3,4,6,7,8-HpCDD

Average

RunNumber 2 3 4

Mass_mg 0.00000000267 0.0000000019 0.0000000037 0.000

lb/mmBtuO2 1.77E-13 1.26E-13 2.38E-13 0.000

ng/dscm 2.08E-04 1.49E-04 2.82E-04 0.000

ng/dscm@7%O2 1.93E-04 1.37E-04 2.60E-04 0.000

Compound: 1,2,3,4,6,7,8-HpCDF

Average

RunNumber 2 3 4

Mass_mg 0.00000000127 0.00000000183 0.00000000137 0.000

lb/mmBtuO2 8.40E-14 1.21E-13 8.82E-14 0.000

ng/dscm 9.87E-05 1.43E-04 1.04E-04 0.000

ng/dscm@7%O2 9.15E-05 1.32E-04 9.57E-05 0.000

Compound: 1,2,3,4,7,8,9-HpCDF

Average

RunNumber 2 3 4

Mass_mg 0.00000000066 0.00000000071 0.00000000067 0.000

lb/mmBtuO2 4.36E-14 4.70E-14 4.31E-14 0.000

ng/dscm 5.13E-05 5.56E-05 5.10E-05 0.000

ng/dscm@7%O2 4.75E-05 5.12E-05 4.69E-05 0.000

Compound: 1,2,3,4,7,8-HxCDD

Average

RunNumber 2 3 4

Mass_mg 0.00000000092 0.0000000026 0.0000000016 0.000

lb/mmBtuO2 6.08E-14 1.72E-13 1.03E-13 0.000

ng/dscm 7.15E-05 2.03E-04 1.22E-04 0.000

ng/dscm@7%O2 6.63E-05 1.87E-04 1.12E-04 0.000

Wednesday, January 12, 2011 Page 10 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Compound: 1,2,3,4,7,8-HxCDF

Average

RunNumber 2 3 4

Mass_mg 0.00000000097 0.0000000015 0.0000000007 0.000

lb/mmBtuO2 6.41E-14 9.92E-14 4.50E-14 0.000

ng/dscm 7.54E-05 1.17E-04 5.33E-05 0.000

ng/dscm@7%O2 6.99E-05 1.08E-04 4.91E-05 0.000

Compound: 1,2,3,6,7,8-HxCDD

Average

RunNumber 2 3 4

Mass_mg 0.00000000077 0.0000000022 0.00000000179 0.000

lb/mmBtuO2 5.09E-14 1.45E-13 1.15E-13 0.000

ng/dscm 5.98E-05 1.72E-04 1.36E-04 0.000

ng/dscm@7%O2 5.54E-05 1.58E-04 1.25E-04 0.000

Compound: 1,2,3,6,7,8-HxCDF

Average

RunNumber 2 3 4

Mass_mg 0.00000000088 0.0000000013 0.00000000058 0.000

lb/mmBtuO2 5.82E-14 8.60E-14 3.73E-14 0.000

ng/dscm 6.84E-05 1.02E-04 4.42E-05 0.000

ng/dscm@7%O2 6.34E-05 9.39E-05 4.07E-05 0.000

Compound: 1,2,3,7,8,9-HxCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000008 0.0000000022 0.0000000014 0.000

lb/mmBtuO2 5.29E-14 1.45E-13 9.01E-14 0.000

ng/dscm 6.22E-05 1.72E-04 1.07E-04 0.000

ng/dscm@7%O2 5.76E-05 1.58E-04 9.85E-05 0.000

Compound: 1,2,3,7,8,9-HxCDF

Average

RunNumber 2 3 4

Mass_mg 0.0000000011 0.0000000017 0.00000000073 0.000

lb/mmBtuO2 7.27E-14 1.12E-13 4.70E-14 0.000

ng/dscm 8.55E-05 1.33E-04 5.56E-05 0.000

ng/dscm@7%O2 7.92E-05 1.22E-04 5.12E-05 0.000

Compound: 1,2,3,7,8-PeCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000011 0.0000000012 0.0000000013 0.000

lb/mmBtuO2 7.27E-14 7.94E-14 8.37E-14 0.000

ng/dscm 8.55E-05 9.39E-05 9.90E-05 0.000

ng/dscm@7%O2 7.92E-05 8.64E-05 9.11E-05 0.000

Compound: 1,2,3,7,8-PeCDF

Average

RunNumber 2 3 4

Mass_mg 0.0000000011 0.0000000012 0.0000000014 0.000

lb/mmBtuO2 7.27E-14 7.94E-14 9.01E-14 0.000

Wednesday, January 12, 2011 Page 11 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

ng/dscm 8.55E-05 9.39E-05 1.07E-04 0.000

ng/dscm@7%O2 7.92E-05 8.64E-05 9.85E-05 0.000

Compound: 2,3,3',4,4',5,5'-HpCB (PCB189)

Average

RunNumber 2 3 4

Mass_mg 0.00000000045 0.00000000056 0.00000000137 0.000

lb/mmBtuO2 2.97E-14 3.70E-14 8.82E-14 0.000

ng/dscm 3.50E-05 4.38E-05 1.04E-04 0.000

ng/dscm@7%O2 3.24E-05 4.03E-05 9.57E-05 0.000

Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC

Average

RunNumber 2 3 4

Mass_mg 0.00000002192 0.0000000227 0.00000002223 0.000

lb/mmBtuO2 1.45E-12 1.50E-12 1.43E-12 0.000

ng/dscm 1.70E-03 1.78E-03 1.69E-03 0.002

ng/dscm@7%O2 1.58E-03 1.64E-03 1.56E-03 0.002

Compound: 2,3,3',4,4'-PeCB (PCB105)

Average

RunNumber 2 3 4

Mass_mg 0.000000187 0.000000235 0.000000175 0.000

lb/mmBtuO2 1.24E-11 1.55E-11 1.13E-11 0.000

ng/dscm 1.45E-02 1.84E-02 1.33E-02 0.015

ng/dscm@7%O2 1.34E-02 1.69E-02 1.22E-02 0.014

Compound: 2,3',4,4',5,5'-HxCB (PCB167)

Average

RunNumber 2 3 4

Mass_mg 0.00000000841 0.0000000106 0.00000000782 0.000

lb/mmBtuO2 5.56E-13 7.01E-13 5.03E-13 0.000

ng/dscm 6.54E-04 8.30E-04 5.96E-04 0.001

ng/dscm@7%O2 6.06E-04 7.64E-04 5.49E-04 0.001

Compound: 2,3,4,4',5-PeCB (PCB114)

Average

RunNumber 2 3 4

Mass_mg 0.0000000153 0.0000000204 0.0000000099 0.000

lb/mmBtuO2 1.01E-12 1.35E-12 6.37E-13 0.000

ng/dscm 1.19E-03 1.60E-03 7.54E-04 0.001

ng/dscm@7%O2 1.10E-03 1.47E-03 6.94E-04 0.001

Compound: 2,3',4,4',5-PeCB (PCB118)

Average

RunNumber 2 3 4

Mass_mg 0.000000412 0.000000486 0.000000363 0.000

lb/mmBtuO2 2.72E-11 3.21E-11 2.34E-11 0.000

ng/dscm 3.20E-02 3.80E-02 2.76E-02 0.033

ng/dscm@7%O2 2.97E-02 3.50E-02 2.54E-02 0.030

Compound: 2',3,4,4',5-PeCB (PCB123)

Average

RunNumber 2 3 4

Wednesday, January 12, 2011 Page 12 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Mass_mg 0.000000011 0.0000000119 0.0000000069 0.000

lb/mmBtuO2 7.27E-13 7.87E-13 4.44E-13 0.000

ng/dscm 8.55E-04 9.31E-04 5.26E-04 0.001

ng/dscm@7%O2 7.92E-04 8.57E-04 4.84E-04 0.001

Compound: 2,3,4,6,7,8-HxCDF

Average

RunNumber 2 3 4

Mass_mg 0.00000000094 0.0000000014 0.0000000017 0.000

lb/mmBtuO2 6.21E-14 9.26E-14 1.09E-13 0.000

ng/dscm 7.31E-05 1.10E-04 1.29E-04 0.000

ng/dscm@7%O2 6.77E-05 1.01E-04 1.19E-04 0.000

Compound: 2,3,4,7,8-PeCDF

Average

RunNumber 2 3 4

Mass_mg 0.000000001 0.0000000011 0.0000000013 0.000

lb/mmBtuO2 6.61E-14 7.27E-14 8.37E-14 0.000

ng/dscm 7.77E-05 8.61E-05 9.90E-05 0.000

ng/dscm@7%O2 7.20E-05 7.93E-05 9.11E-05 0.000

Compound: 2,3,7,8-TCDD

Average

RunNumber 2 3 4

Mass_mg 0.00000000085 0.0000000024 0.0000000021 0.000

lb/mmBtuO2 5.62E-14 1.59E-13 1.35E-13 0.000

ng/dscm 6.61E-05 1.88E-04 1.60E-04 0.000

ng/dscm@7%O2 6.13E-05 1.73E-04 1.47E-04 0.000

Compound: 2,3,7,8-TCDF

Average

RunNumber 2 3 4

Mass_mg 0.0000000035 0.0000000029 0.0000000041 0.000

lb/mmBtuO2 2.31E-13 1.92E-13 2.64E-13 0.000

ng/dscm 2.72E-04 2.27E-04 3.12E-04 0.000

ng/dscm@7%O2 2.52E-04 2.09E-04 2.87E-04 0.000

Compound: 3,3',4,4',5,5'-HxCB (PCB169)

Average

RunNumber 2 3 4

Mass_mg 0.00000000029 0.00000000054 0.00000000052 0.000

lb/mmBtuO2 1.92E-14 3.57E-14 3.35E-14 0.000

ng/dscm 2.25E-05 4.23E-05 3.96E-05 0.000

ng/dscm@7%O2 2.09E-05 3.89E-05 3.65E-05 0.000

Compound: 3,3',4,4',5-PeCB (PCB126)

Average

RunNumber 2 3 4

Mass_mg 0.0000000018 0.0000000025 0.0000000023 0.000

lb/mmBtuO2 1.19E-13 1.65E-13 1.48E-13 0.000

ng/dscm 1.40E-04 1.96E-04 1.75E-04 0.000

ng/dscm@7%O2 1.30E-04 1.80E-04 1.61E-04 0.000

Wednesday, January 12, 2011 Page 13 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Compound: 3,3',4,4'-TCB (PCB77)

Average

RunNumber 2 3 4

Mass_mg 0.000000192 0.000000215 0.0000000723 0.000

lb/mmBtuO2 1.27E-11 1.42E-11 4.65E-12 0.000

ng/dscm 1.49E-02 1.68E-02 5.51E-03 0.012

ng/dscm@7%O2 1.38E-02 1.55E-02 5.07E-03 0.011

Compound: 3,4,4',5-TCB (PCB81)

Average

RunNumber 2 3 4

Mass_mg 0.0000000115 0.0000000131 0.0000000032 0.000

lb/mmBtuO2 7.60E-13 8.66E-13 2.06E-13 0.000

ng/dscm 8.94E-04 1.03E-03 2.44E-04 0.001

ng/dscm@7%O2 8.28E-04 9.48E-04 2.25E-04 0.001

Compound: OCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000107 0.00000000748 0.00000000969 0.000

lb/mmBtuO2 7.07E-13 4.95E-13 6.24E-13 0.000

ng/dscm 8.32E-04 5.85E-04 7.38E-04 0.001

ng/dscm@7%O2 7.71E-04 5.39E-04 6.79E-04 0.001

Compound: OCDF

Average

RunNumber 2 3 4

Mass_mg 0.0000000049 0.000000003 0.00000000335 0.000

lb/mmBtuO2 3.24E-13 1.98E-13 2.16E-13 0.000

ng/dscm 3.81E-04 2.35E-04 2.55E-04 0.000

ng/dscm@7%O2 3.53E-04 2.16E-04 2.35E-04 0.000

Compound: Other HpCDD

Average

RunNumber 2 3 4

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other HpCDF

Average

RunNumber 2 3 4

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other HxCDD

Average

RunNumber 2 3 4

Mass_mg 0.0000000026 0 0.00000000188 0.000

lb/mmBtuO2 1.72E-13 0.00E+00 1.21E-13 0.000

Wednesday, January 12, 2011 Page 14 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

ng/dscm 2.02E-04 0.00E+00 1.43E-04 0.000

ng/dscm@7%O2 1.87E-04 0.00E+00 1.32E-04 0.000

Compound: Other HxCDF

Average

RunNumber 2 3 4

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other PeCDD

Average

RunNumber 2 3 4

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other PeCDF

Average

RunNumber 2 3 4

Mass_mg 0 0 0 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm 0.00E+00 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Other TCDD

Average

RunNumber 2 3 4

Mass_mg 0.00000000322 0 0 0.000

lb/mmBtuO2 2.13E-13 0.00E+00 0.00E+00 0.000

ng/dscm 2.50E-04 0.00E+00 0.00E+00 0.000

ng/dscm@7%O2 2.32E-04 0.00E+00 0.00E+00 0.000

Compound: Other TCDF

Average

RunNumber 2 3 4

Mass_mg 0 0 0.00000000587 0.000

lb/mmBtuO2 0.00E+00 0.00E+00 3.78E-13 0.000

ng/dscm 0.00E+00 0.00E+00 4.47E-04 0.000

ng/dscm@7%O2 0.00E+00 0.00E+00 4.11E-04 0.000

Compound: Total Dioxins

Average

RunNumber 2 3 4

Mass_mg 0.00000002363 0.00000001998 0.00000002346 0.000

lb/mmBtuO2 1.56E-12 1.32E-12 1.51E-12 0.000

ng/dscm 1.84E-03 1.56E-03 1.79E-03 0.002

ng/dscm@7%O2 1.71E-03 1.44E-03 1.65E-03 0.002

Compound: Total Furans

Average

RunNumber 2 3 4

Wednesday, January 12, 2011 Page 15 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Mass_mg 0.00000001632 0.00000001664 0.00000002177 0.000

lb/mmBtuO2 1.08E-12 1.10E-12 1.40E-12 0.000

ng/dscm 1.27E-03 1.30E-03 1.66E-03 0.001

ng/dscm@7%O2 1.18E-03 1.20E-03 1.53E-03 0.001

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 0.00E+00 0.00E+00 0.00E+00 0.000

ppm 0.00E+00 0.00E+00 0.00E+00 0.000

ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.426 0.49 0.421 0.446

lb/mmBtuO2 6.88E-05 8.17E-05 6.97E-05 0.000

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.424 0.488 0.419 0.444

lb/mmBtuO2 6.84E-05 8.13E-05 6.93E-05 0.000

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.00194 0.00104 0.00183 0.002

lb/mmBtuO2 2.54E-07 1.37E-07 2.49E-07 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.00767 0.00409 0.00786 0.007

lb/mmBtuO2 1.01E-06 5.40E-07 1.07E-06 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.00113 0.000518 0.00142 0.001

lb/mmBtuO2 1.48E-07 6.84E-08 1.93E-07 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000536 0.000215 0.000525 0.000

lb/mmBtuO2 7.03E-08 2.84E-08 7.14E-08 0.000

Wednesday, January 12, 2011 Page 16 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0247 0.0134 0.0233 0.020

lb/mmBtuO2 3.24E-06 1.77E-06 3.17E-06 0.000

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.0125 0.00539 0.0107 0.010

lb/mmBtuO2 1.64E-06 7.12E-07 1.45E-06 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.029 0.0141 0.0238 0.022

lb/mmBtuO2 3.80E-06 1.86E-06 3.24E-06 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.0193 0.00917 0.0194 0.016

lb/mmBtuO2 2.53E-06 1.21E-06 2.64E-06 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.0329 0.0145 0.0265 0.025

lb/mmBtuO2 4.32E-06 1.91E-06 3.60E-06 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0161 0.00827 0.0138 0.013

lb/mmBtuO2 2.11E-06 1.09E-06 1.88E-06 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 2.78E-02 1.91E-02 2.25E-02 0.023

ppm 1.26E+01 8.65E+00 1.02E+01 10.483

ppm@7%O2 1.14E+01 7.82E+00 9.23E+00 9.483

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 2.87E-01 2.85E-01 2.96E-01 0.289

ppm 1.80E+02 1.79E+02 1.87E+02 182.000

ppm@7%O2 1.63E+02 1.62E+02 1.69E+02 164.667

Wednesday, January 12, 2011 Page 17 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Process Run Data

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 105.8 96 97.7 99.833

lb/mmBtuO2 2.35E-02 2.31E-02 2.26E-02 0.023

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 14.3 12.8 11 12.700

lb/mmBtuO2 3.18E-03 3.08E-03 2.54E-03 0.003

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 298.69 228.09 208.19 244.990

lb/mmBtuO2 6.64E-02 5.50E-02 4.81E-02 0.057

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 0.31 3.71 3.61 2.543

lb/mmBtuO2 6.89E-05 8.94E-04 8.35E-04 0.001

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 404.8 327.8 309.5 347.367

lb/mmBtuO2 9.00E-02 7.90E-02 7.16E-02 0.080

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 313.3 244.6 222.8 260.233

lb/mmBtuO2 6.96E-02 5.89E-02 5.15E-02 0.060

Wednesday, January 12, 2011 Page 18 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 768.88 Million Btus/hr Collected during 

run 1 of Method 

6C and 7E

0

1 Coal Feed Rate 28.82 tons/hr Collected during 

run 1 of Method 

6C and 7E

0

1 Total Steam Flow 517.74 1000 lb steam/hr Collected during 

run 1 of Method 

6C and 7E

0

1 Boiler 1 Reactor dP 4.41 in-H2O Collected during 

run 1 of Method 

6C and 7E

0

1 Boiler 2 Reactor dP 3.27 in-H20 Collected during 

run 1 of Method 

6C and 7E

0

1 Total NH3 Flow 54.5 lb/hr Collected during 

run 1 of Method 

6C and 7E

0

1 Total Slurry Flow 156.56 gpm Collected during 

run 1 of Method 

6C and 7E

0

1 Gross MW 68.02 MW Collected during 

run 1 of Method 

6C and 7E

0

1 Flue Gas CO2 11.58 % Collected during 

run 1 of Method 

6C and 7E

0

1 Net MW 62.65 MW Collected during 

run 1 of Method 

6C and 7E

0

2 Heat Input 769.99 Million Btus/hr Collected during 

run 2 of Method 

6C and 7E

0

2 Coal Feed Rate 28.86 tons/hr Collected during 

run 2 of Method 

6C and 7E

0

2 Total Steam Flow 515.68 1000 lb steam/hr Collected during 

run 2 of Method 

6C and 7E

0

2 Boiler 1 Reactor dP 4.26 in-H2O Collected during 

run 2 of Method 

6C and 7E

0

2 Boiler 2 Reactor dP 3.15 in-H20 Collected during 

run 2 of Method 

6C and 7E

0

Wednesday, January 12, 2011 Page 19 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

2 Total NH3 Flow 52.83 lb/hr Collected during 

run 2 of Method 

6C and 7E

0

2 Total Slurry Flow 153.86 gpm Collected during 

run 2 of Method 

6C and 7E

0

2 Gross MW 68.04 MW Collected during 

run 2 of Method 

6C and 7E

0

2 Flue Gas CO2 11.65 % Collected during 

run 2 of Method 

6C and 7E

0

2 Net MW 62.74 MW Collected during 

run 2 of Method 

6C and 7E

0

3 Heat Input 768.7 Million Btus/hr Collected during 

run 3 of Method 

6C and 7E

0

3 Coal Feed Rate 28.81 tons/hr Collected during 

run 3 of Method 

6C and 7E

0

3 Total Steam Flow 517.4 1000 lb steam/hr Collected during 

run 3 of Method 

6C and 7E

0

3 Boiler 1 Reactor dP 4.26 in-H2O Collected during 

run 3 of Method 

6C and 7E

0

3 Boiler 2 Reactor dP 2.96 in-H20 Collected during 

run 3 of Method 

6C and 7E

0

3 Total NH3 Flow 45.53 lb/hr Collected during 

run 3 of Method 

6C and 7E

0

3 Total Slurry Flow 156.91 gpm Collected during 

run 3 of Method 

6C and 7E

0

3 Gross MW 67.91 MW Collected during 

run 3 of Method 

6C and 7E

0

3 Flue Gas CO2 11.63 % Collected during 

run 3 of Method 

6C and 7E

0

3 Net MW 62.63 MW Collected during 

run 3 of Method 

6C and 7E

0

4 Heat Input 773.56 Million Btus/hr Collected during 

M26A run 1

0

4 Coal Feed Rate 28.99 tons/hr Collected during 

M26A run 1

0

Wednesday, January 12, 2011 Page 20 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

4 Total Steam Flow 515.72 1000 lb steam/hr Collected during 

M26A run 1

0

4 Boiler 1 Reactor dP 4.58 in-H2O Collected during 

M26A run 1

0

4 Boiler 2 Reactor dP 3.55 in-H20 Collected during 

M26A run 1

0

4 Total NH3 Flow 71.1 lb/hr Collected during 

M26A run 1

0

4 Total Slurry Flow 162.4 gpm Collected during 

M26A run 1

0

4 Gross MW 68.34 MW Collected during 

M26A run 1

0

4 Flue Gas CO2 11.62 % Collected during 

M26A run 1

0

4 Net MW 63.03 MW Collected during 

M26A run 1

0

5 Heat Input 767.76 Million Btus/hr Collected during 

M26A run 2

0

5 Coal Feed Rate 28.78 tons/hr Collected during 

M26A run 2

0

5 Total Steam Flow 512.11 1000 lb steam/hr Collected during 

M26A run 2

0

5 Boiler 1 Reactor dP 4.61 in-H2O Collected during 

M26A run 2

0

5 Boiler 2 Reactor dP 3.07 in-H20 Collected during 

M26A run 2

0

5 Total NH3 Flow 63.88 lb/hr Collected during 

M26A run 2

0

5 Total Slurry Flow 159.8 gpm Collected during 

M26A run 2

0

5 Gross MW 67.88 MW Collected during 

M26A run 2

0

5 Flue Gas CO2 11.46 % Collected during 

M26A run 2

0

5 Net MW 62.56 MW Collected during 

M26A run 2

0

6 Heat Input 772.6 Million Btus/hr Collected during 

M26A run 3

0

6 Coal Feed Rate 28.96 tons/hr Collected during 

M26A run 3

0

6 Total Steam Flow 515.39 1000 lb steam/hr Collected during 

M26A run 3

0

6 Boiler 1 Reactor dP 4.55 in-H2O Collected during 

M26A run 3

0

6 Boiler 2 Reactor dP 3.29 in-H20 Collected during 

M26A run 3

0

Wednesday, January 12, 2011 Page 21 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

6 Total NH3 Flow 79.35 lb/hr Collected during 

M26A run 3

0

6 Total Slurry Flow 164.91 gpm Collected during 

M26A run 3

0

6 Gross MW 68.34 MW Collected during 

M26A run 3

0

6 Flue Gas CO2 11.48 % Collected during 

M26A run 3

0

6 Net MW 62.95 MW Collected during 

M26A run 3

0

7 Heat Input 771.15 Million Btus/hr Collected during 

M23 run 2

0

7 Coal Feed Rate 28.9 tons/hr Collected during 

M23 run 2

0

7 Total Steam Flow 514.62 1000 lb steam/hr Collected during 

M23 run 2

0

7 Boiler 1 Reactor dP 4.54 in-H2O Collected during 

M23 run 2

0

7 Boiler 2 Reactor dP 3.23 in-H20 Collected during 

M23 run 2

0

7 Total NH3 Flow 74.66 lb/hr Collected during 

M23 run 2

0

7 Total Slurry Flow 163.89 gpm Collected during 

M23 run 2

0

7 Gross MW 68.21 MW Collected during 

M23 run 2

0

7 Flue Gas CO2 11.47 % Collected during 

M23 run 2

0

7 Net MW 62.83 MW Collected during 

M23 run 2

0

8 Heat Input 769.08 Million Btus/hr Collected during 

M23 run 3

0

8 Coal Feed Rate 28.83 tons/hr Collected during 

M23 run 3

0

8 Total Steam Flow 517.74 1000 lb steam/hr Collected during 

M23 run 3

0

8 Boiler 1 Reactor dP 4.47 in-H2O Collected during 

M23 run 3

0

8 Boiler 2 Reactor dP 3.3 in-H20 Collected during 

M23 run 3

0

8 Total NH3 Flow 54.06 lb/hr Collected during 

M23 run 3

0

8 Total Slurry Flow 155.32 gpm Collected during 

M23 run 3

0

8 Gross MW 68.04 MW Collected during 

M23 run 3

0

Wednesday, January 12, 2011 Page 22 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

8 Flue Gas CO2 11.55 % Collected during 

M23 run 3

0

8 Net MW 62.66 MW Collected during 

M23 run 3

0

9 Heat Input 764.15 Million Btus/hr Collected during 

M23 run 4

0

9 Coal Feed Rate 28.64 tons/hr Collected during 

M23 run 4

0

9 Total Steam Flow 516.29 1000 lb steam/hr Collected during 

M23 run 4

0

9 Boiler 1 Reactor dP 4.32 in-H2O Collected during 

M23 run 4

0

9 Boiler 2 Reactor dP 3.14 in-H20 Collected during 

M23 run 4

0

9 Total NH3 Flow 63.59 lb/hr Collected during 

M23 run 4

0

9 Total Slurry Flow 165.67 gpm Collected during 

M23 run 4

0

9 Gross MW 67.57 MW Collected during 

M23 run 4

0

9 Flue Gas CO2 11.77 % Collected during 

M23 run 4

0

9 Net MW 62.26 MW Collected during 

M23 run 4

0

10 Heat Input 768.37 Million Btus/hr Collected during 

OTM-27/28 run 1

0

10 Coal Feed Rate 28.8 tons/hr Collected during 

OTM-27/28 run 1

0

10 Total Steam Flow 517.79 1000 lb steam/hr Collected during 

OTM-27/28 run 1

0

10 Boiler 1 Reactor dP 4.45 in-H2O Collected during 

OTM-27/28 run 1

0

10 Boiler 2 Reactor dP 3.35 in-H20 Collected during 

OTM-27/28 run 1

0

10 Total NH3 Flow 53.85 lb/hr Collected during 

OTM-27/28 run 1

0

10 Total Slurry Flow 155.68 gpm Collected during 

OTM-27/28 run 1

0

10 Gross MW 67.99 MW Collected during 

OTM-27/28 run 1

0

10 Flue Gas CO2 11.56 % Collected during 

OTM-27/28 run 1

0

10 Net MW 62.61 MW Collected during 

OTM-27/28 run 1

0

11 Heat Input 769.92 Million Btus/hr Collected during 

OTM-27/28 run 2

0

Wednesday, January 12, 2011 Page 23 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

11 Coal Feed Rate 28.86 tons/hr Collected during 

OTM-27/28 run 2

0

11 Total Steam Flow 516.36 1000 lb steam/hr Collected during 

OTM-27/28 run 2

0

11 Boiler 1 Reactor dP 4.27 in-H2O Collected during 

OTM-27/28 run 2

0

11 Boiler 2 Reactor dP 3.01 in-H20 Collected during 

OTM-27/28 run 2

0

11 Total NH3 Flow 49.02 lb/hr Collected during 

OTM-27/28 run 2

0

11 Total Slurry Flow 155.29 gpm Collected during 

OTM-27/28 run 2

0

11 Gross MW 68.02 MW Collected during 

OTM-27/28 run 2

0

11 Flue Gas CO2 11.65 % Collected during 

OTM-27/28 run 2

0

11 Net MW 62.73 MW Collected during 

OTM-27/28 run 2

0

12 Heat Input 768.88 Million Btus/hr Collected during 

OTM-27/28 run 3

0

12 Coal Feed Rate 28.82 tons/hr Collected during 

OTM-27/28 run 3

0

12 Total Steam Flow 519.17 1000 lb steam/hr Collected during 

OTM-27/28 run 3

0

12 Boiler 1 Reactor dP 4.32 in-H2O Collected during 

OTM-27/28 run 3

0

12 Boiler 2 Reactor dP 3.33 in-H20 Collected during 

OTM-27/28 run 3

0

12 Total NH3 Flow 45.17 lb/hr Collected during 

OTM-27/28 run 3

0

12 Total Slurry Flow 160.96 gpm Collected during 

OTM-27/28 run 3

0

12 Gross MW 67.94 MW Collected during 

OTM-27/28 run 3

0

12 Flue Gas CO2 11.61 % Collected during 

OTM-27/28 run 3

0

12 Net MW 62.65 MW Collected during 

OTM-27/28 run 3

0

13 Heat Input 770.17 Million Btus/hr Collected during 

M29 run 1

0

13 Coal Feed Rate 28.87 tons/hr Collected during 

M29 run 1

0

13 Total Steam Flow 515.93 1000 lb steam/hr Collected during 

M29 run 1

0

13 Boiler 1 Reactor dP 4.28 in-H2O Collected during 

M29 run 1

0

Wednesday, January 12, 2011 Page 24 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

13 Boiler 2 Reactor dP 3 in-H20 Collected during 

M29 run 1

0

13 Total NH3 Flow 49.78 lb/hr Collected during 

M29 run 1

0

13 Total Slurry Flow 154.8 gpm Collected during 

M29 run 1

0

13 Gross MW 68.04 MW Collected during 

M29 run 1

0

13 Flue Gas CO2 11.66 % Collected during 

M29 run 1

0

13 Net MW 62.75 MW Collected during 

M29 run 1

0

14 Heat Input 768.65 Million Btus/hr Collected during 

M29 run 2

0

14 Coal Feed Rate 28.81 tons/hr Collected during 

M29 run 2

0

14 Total Steam Flow 519.19 1000 lb steam/hr Collected during 

M29 run 2

0

14 Boiler 1 Reactor dP 4.32 in-H2O Collected during 

M29 run 2

0

14 Boiler 2 Reactor dP 3.3 in-H20 Collected during 

M29 run 2

0

14 Total NH3 Flow 44.9 lb/hr Collected during 

M29 run 2

0

14 Total Slurry Flow 160.62 gpm Collected during 

M29 run 2

0

14 Gross MW 67.92 MW Collected during 

M29 run 2

0

14 Flue Gas CO2 11.6 % Collected during 

M29 run 2

0

14 Net MW 62.63 MW Collected during 

M29 run 2

0

15 Heat Input 769.5 Million Btus/hr Collected during 

M29 run 3

0

15 Coal Feed Rate 28.84 tons/hr Collected during 

M29 run 3

0

15 Total Steam Flow 520.55 1000 lb steam/hr Collected during 

M29 run 3

0

15 Boiler 1 Reactor dP 4.41 in-H2O Collected during 

M29 run 3

0

15 Boiler 2 Reactor dP 3.13 in-H20 Collected during 

M29 run 3

0

15 Total NH3 Flow 63.91 lb/hr Collected during 

M29 run 3

0

15 Total Slurry Flow 168.33 gpm Collected during 

M29 run 3

0

Wednesday, January 12, 2011 Page 25 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

15 Gross MW 68.04 MW Collected during 

M29 run 3

0

15 Flue Gas CO2 11.76 % Collected during 

M29 run 3

0

15 Net MW 62.7 MW Collected during 

M29 run 3

0

16 Heat Input 775.53 Million Btus/hr Collected during 

M0011 run 1

0

16 Coal Feed Rate 29.07 tons/hr Collected during 

M0011 run 1

0

16 Total Steam Flow 510.64 1000 lb steam/hr Collected during 

M0011 run 1

0

16 Boiler 1 Reactor dP 4.33 in-H2O Collected during 

M0011 run 1

0

16 Boiler 2 Reactor dP 2.95 in-H20 Collected during 

M0011 run 1

0

16 Total NH3 Flow 48.59 lb/hr Collected during 

M0011 run 1

0

16 Total Slurry Flow 168.46 gpm Collected during 

M0011 run 1

0

16 Gross MW 68.57 MW Collected during 

M0011 run 1

0

16 Flue Gas CO2 11.73 % Collected during 

M0011 run 1

0

16 Net MW 63.19 MW Collected during 

M0011 run 1

0

17 Heat Input 772.99 Million Btus/hr Collected during 

run 1 of Method 

10 and 25A

0

17 Coal Feed Rate 28.97 tons/hr Collected during 

run 1 of Method 

10 and 25A

0

17 Total Steam Flow 509.87 1000 lb steam/hr Collected during 

run 1 of Method 

10 and 25A

0

17 Boiler 1 Reactor dP 4.36 in-H2O Collected during 

run 1 of Method 

10 and 25A

0

17 Boiler 2 Reactor dP 2.99 in-H20 Collected during 

run 1 of Method 

10 and 25A

0

17 Total NH3 Flow 47.09 lb/hr Collected during 

run 1 of Method 

10 and 25A

0

17 Total Slurry Flow 170.73 gpm Collected during 

run 1 of Method 

10 and 25A

0

Wednesday, January 12, 2011 Page 26 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

17 Gross MW 68.39 MW Collected during 

run 1 of Method 

10 and 25A

0

17 Flue Gas CO2 11.6 % Collected during 

run 1 of Method 

10 and 25A

0

17 Net MW 62.98 MW Collected during 

run 1 of Method 

10 and 25A

0

18 Heat Input 767.6 Million Btus/hr Collected during 

run 2 of Method 

0011, 10, and 25A

0

18 Coal Feed Rate 28.77 tons/hr Collected during 

run 2 of Method 

0011, 10, and 25A

0

18 Total Steam Flow 509.31 1000 lb steam/hr Collected during 

run 2 of Method 

0011, 10, and 25A

0

18 Boiler 1 Reactor dP 4.54 in-H2O Collected during 

run 2 of Method 

0011, 10, and 25A

0

18 Boiler 2 Reactor dP 3.5 in-H20 Collected during 

run 2 of Method 

0011, 10, and 25A

0

18 Total NH3 Flow 45.15 lb/hr Collected during 

run 2 of Method 

0011, 10, and 25A

0

18 Total Slurry Flow 176.09 gpm Collected during 

run 2 of Method 

0011, 10, and 25A

0

18 Gross MW 67.97 MW Collected during 

run 2 of Method 

0011, 10, and 25A

0

18 Flue Gas CO2 11.57 % Collected during 

run 2 of Method 

0011, 10, and 25A

0

18 Net MW 62.54 MW Collected during 

run 2 of Method 

0011, 10, and 25A

0

19 Heat Input 766.05 Million Btus/hr Collected during 

run 3 of Method 

0011, 10, and 25A

0

19 Coal Feed Rate 28.71 tons/hr Collected during 

run 3 of Method 

0011, 10, and 25A

0

19 Total Steam Flow 509.33 1000 lb steam/hr Collected during 

run 3 of Method 

0011, 10, and 25A

0

Wednesday, January 12, 2011 Page 27 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

APCD Run Data

Process Lab Run Data

19 Boiler 1 Reactor dP 4.48 in-H2O Collected during 

run 3 of Method 

0011, 10, and 25A

0

19 Boiler 2 Reactor dP 3.77 in-H20 Collected during 

run 3 of Method 

0011, 10, and 25A

0

19 Total NH3 Flow 45.15 lb/hr Collected during 

run 3 of Method 

0011, 10, and 25A

0

19 Total Slurry Flow 174.14 gpm Collected during 

run 3 of Method 

0011, 10, and 25A

0

19 Gross MW 67.83 MW Collected during 

run 3 of Method 

0011, 10, and 25A

0

19 Flue Gas CO2 11.6 % Collected during 

run 3 of Method 

0011, 10, and 25A

0

19 Net MW 62.42 MW Collected during 

run 3 of Method 

0011, 10, and 25A

0

Run Name Value UOM Comments

Target

Value

1 OVERFIRE AIR 0 0

1 DRY LIMESTONE INJECTION 0 0

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

1 BAGHOUSE 0 0

Wednesday, January 12, 2011 Page 28 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 4/23/2010 4/23/2010 4/23/2010

Run Start Time

Run Finish Time

Net Traversing Points 24 24 24

Net Run Time, minutes 120 120 120

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 0.9965 0.9965 0.9965 0.997

Barometric Pressure, inches of Mercury 29.84 29.84 29.84 29.840

Average Orifice Meter Differential, inches H2O 3.03 3.14 3.07 3.080

Dry Gas Meter Volume Sampled, cubic feet 111.306 114.113 113.215 112.878

Average Dry Gas Meter Temperature, °F 73.58 79.50 79.88 77.653

Dry Gas Meter Volume Sampled, dscf 110.280 111.851 110.874 111.002

Total Moisture Liquid collected, g 376.2 374.4 364.6 371.733

Volume of Water Vapor, standard cubic feet 17.71 17.62 17.16 17.497

Moisture Content of Stack Gas, % 13.84 13.61 13.40 13.617

Moisture Saturation at Stack Gas Temperature, % 98.90 100.00 100.00 99.633

Dry Mole Fraction 0.8616 0.8639 0.866 0.864

Carbon Dioxide, % 13.578 13.624 13.634 13.612

Oxygen, % 5.536 5.484 5.482 5.501

Carbon Monoxide & Nitrogen, % 80.886 80.892 80.884 80.887

Fuel Factor 1.13 1.13 1.13

Dry Molecular Weight, lb/lb-Mole 30.39 30.40 30.40 30.397

Wet Molecular weight, lb/lb-Mole 28.68 28.71 28.74 28.710

Flue Gas Static Pressure, inches of H2O -0.85 -0.85 -0.89 -0.863

Absolute Flue Gas Pressure, inches of Mercury 29.78 29.78 29.77 29.777

Average Stack Gas Temperature, °F 211.21 214.13 214.96 213.433

Average Velocity Head, inches of H2O 1.9202522218

2738

1.984267857

89812

1.930548056

9238

1.945

Average Stack Gas Velocity, feet/second 88.22 89.82 88.62 88.887

Stack Cross-Sectional Area, square feet 50.265 50.265 50.265 50.265

Dry Volumetric Flow Rate, dry scfm 179,485.1 182,434.4 180,152.3 180,690.600

Actual Wet Volumetric Flue Gas Flow Rate, acfm 266,062.7 270,888.1 267,269.1 268,073.300

Percent Isokinetic of Sampling Rate, % 99.3 99.1 99.5 99.300

Percent Excess Air, % 35.0 34.6 34.5 34.700

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

Round Duct Diameter, inches 96 96 96

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

Wednesday, January 12, 2011 Page 29 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 10

Average

Run Number 1 2 3

Test Date 4/23/2010 4/23/2010 4/23/2010

Run Start Time 9:50:00 AM 12:20:00 PM 3:42:00 PM

Run Finish Time 11:50:00 AM 2:20:00 PM 5:42:00 PM

Carbon Dioxide, % 13.578 13.624 13.634 13.612

Oxygen, % 5.536 5.484 5.482 5.501

Fuel Factor 1.13 1.13 1.13

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Pre Zero Cylinder Instrument Response 1.59 1.63 1.63 1.617

Calibration Pre Zero Cylinder Bias 0.77 0.79 0.79 0.783

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC41590 CC41590 CC41590

Calibration Pre High Cylinder Instrument Response 204.33 203.51 205.12 204.320

Calibration Pre High Cylinder Bias 1.26 0.85 1.65 1.253

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Post Zero Cylinder Instrument Response 1.63 1.63 1.61 1.623

Calibration Post Zero Cylinder Bias 0.79 0.79 0.78 0.787

Calibration Post Zero Cylinder Drift 0.02 0 0.01 0.010

Calibration Post High Cylinder ID CC41590 CC41590 CC41590

Calibration Post High Cylinder Instrument Response 203.51 205.12 204.3 204.310

Calibration Post High Cylinder Bias 0.85 1.65 1.24 1.247

Calibration Post High Cylinder Drift 0.41 0.8 0.41 0.540

Cavg 148.99 137.48 157.59 148.020

Cavg Units ppmvd ppmvd ppmvd

Cgas 146.4257 134.7206 154.3649 145.170

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, January 12, 2011 Page 30 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 23

Average

Run Number 2 3 4

Test Date 4/20/2010 4/21/2010 4/24/2010

Run Start Time

Run Finish Time

Net Traversing Points 96 96 96

Net Run Time, minutes 480 480 480

Nozzle Diameter, inches 0.216 0.216 0.216 0.216

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9965 0.9965 0.9965 0.997

Barometric Pressure, inches of Mercury 30.18 29.95 29.91 30.013

Average Orifice Meter Differential, inches H2O 3.15 3.06 3.08 3.097

Dry Gas Meter Volume Sampled, cubic feet 459.015 449.316 465.473 457.935

Average Dry Gas Meter Temperature, °F 80.18 68.32 71.96 73.487

Dry Gas Meter Volume Sampled, dscf 454.441 451.286 463.722 456.483

Total Moisture Liquid collected, g 1394.8 1432.1 1551.8 1,459.567

Volume of Water Vapor, standard cubic feet 65.65 67.41 73.04 68.700

Moisture Content of Stack Gas, % 12.62 13.00 13.61 13.077

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

Dry Mole Fraction 0.8738 0.87 0.8639 0.869

Carbon Dioxide, % 13.3 13.3 13.4 13.333

Oxygen, % 5.9 5.8 5.8 5.833

Carbon Monoxide & Nitrogen, % 80.8 80.9 80.8 80.833

Fuel Factor 1.13 1.14 1.13

Dry Molecular Weight, lb/lb-Mole 30.36 30.36 30.38 30.367

Wet Molecular weight, lb/lb-Mole 28.80 28.75 28.70 28.750

Flue Gas Static Pressure, inches of H2O -0.85 -0.85 -0.96 -0.887

Absolute Flue Gas Pressure, inches of Mercury 30.12 29.89 29.84 29.950

Average Stack Gas Temperature, °F 214.49 214.30 213.23 214.007

Average Velocity Head, inches of H2O 1.9669282762

3366

1.908145006

13814

1.968100783

06105

1.948

Average Stack Gas Velocity, feet/second 88.81 87.87 89.32 88.667

Stack Cross-Sectional Area, square feet 50.265 50.265 50.265 50.265

Dry Volumetric Flow Rate, dry scfm 184,434.7 180,352.4 182,027.4 182,271.500

Actual Wet Volumetric Flue Gas Flow Rate, acfm 267,842.1 265,007.1 269,380.2 267,409.800

Percent Isokinetic of Sampling Rate, % 101.4 103.0 104.8 103.067

Percent Excess Air, % 38.2 37.3 37.3 37.600

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

Round Duct Diameter, inches 96 96 96

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

Wednesday, January 12, 2011 Page 31 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 25A

Average

Run Number 1 2 3

Test Date 4/23/2010 4/23/2010 4/23/2010

Run Start Time 9:50:00 AM 12:20:00 PM 3:42:00 PM

Run Finish Time 11:50:00 AM 2:20:00 PM 5:42:00 PM

Carbon Dioxide, %

Oxygen, % 5.536 5.484 5.482 5.501

Fuel Factor 0 0 0

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 13.99 13.87 13.71 13.857

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 2 2 2 2.000

Calibration Pre Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Pre Zero Cylinder Instrument Response 0.023 0.023 0.023 0.023

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC178755 CC178755 CC178755

Calibration Pre High Cylinder Instrument Response 6.85 6.706 6.526 6.694

Calibration Pre High Cylinder Bias -1.36 -3.41 -5.98 -3.583

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Post Zero Cylinder Instrument Response 0.023 0.023 0.023 0.023

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID CC178755 CC178755 CC178755

Calibration Post High Cylinder Instrument Response 6.706 6.526 6.466 6.566

Calibration Post High Cylinder Bias -3.41 -5.98 -6.84 -5.410

Calibration Post High Cylinder Drift 2.05 2.57 0.859999999

999999

1.827

Cavg 0.023 0.023 0.023 0.023

Cavg Units ppmvw ppmvw ppmvw

Cgas 0 0 0 0.000

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units ppmvw ppmvw ppmvw

Wednesday, January 12, 2011 Page 32 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 26A

Average

Run Number 1 2 3

Test Date 4/19/2010 4/20/2010 4/20/2010

Run Start Time

Run Finish Time

Net Traversing Points 48 48 48

Net Run Time, minutes 192 192 192

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 0.9873 0.9873 0.9873 0.987

Barometric Pressure, inches of Mercury 30.32 30.18 30.18 30.227

Average Orifice Meter Differential, inches H2O 2.98 2.98 3.02 2.993

Dry Gas Meter Volume Sampled, cubic feet 185.050 185.203 186.992 185.748

Average Dry Gas Meter Temperature, °F 80.96 85.33 83.44 83.243

Dry Gas Meter Volume Sampled, dscf 182.013 179.875 182.262 181.383

Total Moisture Liquid collected, g 625.4 630.8 634.3 630.167

Volume of Water Vapor, standard cubic feet 29.44 29.69 29.86 29.663

Moisture Content of Stack Gas, % 13.92 14.17 14.08 14.057

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

Dry Mole Fraction 0.8608 0.8583 0.8592 0.859

Carbon Dioxide, % 13.59 13.32 13.81 13.573

Oxygen, % 5.56 5.87 5.96 5.797

Carbon Monoxide & Nitrogen, % 80.85 80.81 80.23 80.630

Fuel Factor 1.13 1.13 1.08

Dry Molecular Weight, lb/lb-Mole 30.40 30.37 30.45 30.407

Wet Molecular weight, lb/lb-Mole 28.67 28.62 28.70 28.663

Flue Gas Static Pressure, inches of H2O -0.85 -0.85 -0.85 -0.850

Absolute Flue Gas Pressure, inches of Mercury 30.26 30.12 30.12 30.167

Average Stack Gas Temperature, °F 216.42 215.96 216.77 216.383

Average Velocity Head, inches of H2O 1.9152095833

2869

1.924082249

49332

1.953380625

4626

1.931

Average Stack Gas Velocity, feet/second 87.75 88.21 88.81 88.257

Stack Cross-Sectional Area, square feet 50.265 50.265 50.265 50.265

Dry Volumetric Flow Rate, dry scfm 179,842.0 179,547.8 180,742.1 180,043.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 264,645.2 266,032.5 267,842.1 266,173.267

Percent Isokinetic of Sampling Rate, % 102.2 101.2 101.8 101.733

Percent Excess Air, % 35.2 38.0 39.2 37.467

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

Round Duct Diameter, inches 96 96 96

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

Wednesday, January 12, 2011 Page 33 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 29 

Average

Run Number 1 2 3

Test Date 4/22/2010 4/22/2010 4/24/2010

Run Start Time

Run Finish Time

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 0.9965 0.9965 0.9965 0.997

Barometric Pressure, inches of Mercury 29.9 29.9 29.91 29.903

Average Orifice Meter Differential, inches H2O 3.02 3.03 2.95 3.000

Dry Gas Meter Volume Sampled, cubic feet 223.709 224.459 218.891 222.353

Average Dry Gas Meter Temperature, °F 70.20 78.39 74.16 74.250

Dry Gas Meter Volume Sampled, dscf 223.500 220.844 217.100 220.481

Total Moisture Liquid collected, g 735.1 766.2 751.2 750.833

Volume of Water Vapor, standard cubic feet 34.60 36.07 35.36 35.343

Moisture Content of Stack Gas, % 13.41 14.04 14.01 13.820

Moisture Saturation at Stack Gas Temperature, % 97.79 97.50 100.00 98.430

Dry Mole Fraction 0.8659 0.8596 0.8599 0.862

Carbon Dioxide, % 13.55 13.66 13.43 13.547

Oxygen, % 5.53 5.445 5.63 5.535

Carbon Monoxide & Nitrogen, % 80.92 80.895 80.94 80.918

Fuel Factor 1.13 1.13 1.14

Dry Molecular Weight, lb/lb-Mole 30.39 30.40 30.37 30.387

Wet Molecular weight, lb/lb-Mole 28.73 28.66 28.64 28.677

Flue Gas Static Pressure, inches of H2O -0.96 -0.96 -0.96 -0.960

Absolute Flue Gas Pressure, inches of Mercury 29.83 29.83 29.84 29.833

Average Stack Gas Temperature, °F 210.73 210.58 213.17 211.493

Average Velocity Head, inches of H2O 1.8667336572

984

1.885466352

58597

1.846337398

70628

1.866

Average Stack Gas Velocity, feet/second 86.80 87.33 86.60 86.910

Stack Cross-Sectional Area, square feet 50.265 50.265 50.265 50.265

Dry Volumetric Flow Rate, dry scfm 177,902.6 177,726.3 175,682.8 177,103.900

Actual Wet Volumetric Flue Gas Flow Rate, acfm 261,780.1 263,378.5 261,176.9 262,111.833

Percent Isokinetic of Sampling Rate, % 101.5 100.4 99.8 100.567

Percent Excess Air, % 34.9 34.2 35.8 34.967

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

Round Duct Diameter, inches 96 96 96

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

Wednesday, January 12, 2011 Page 34 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 6C

Average

Run Number 1 2 3

Test Date 4/21/2010 4/22/2010 4/22/2010

Run Start Time 3:51:00 PM 7:11:00 AM 11:24:00 AM

Run Finish Time 6:51:00 PM 10:11:00 AM 2:24:00 PM

Carbon Dioxide, % 13.529 13.583 13.53 13.547

Oxygen, % 5.563 5.526 5.534 5.541

Fuel Factor 1.13 1.13 1.14

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 3 4 5 4.000

Calibration Pre Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Pre Zero Cylinder Instrument Response 1.884 2.12 1.989 1.998

Calibration Pre Zero Cylinder Bias 1.04 0.62 0.91 0.857

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID CC122146 CC122146 CC122146

Calibration Pre High Cylinder Instrument Response 86.623 88.37 86.02 87.004

Calibration Pre High Cylinder Bias -4.18 -3.71 -3.87 -3.920

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Post Zero Cylinder Instrument Response 0.794 5.324 3.578 3.232

Calibration Post Zero Cylinder Bias -0.16 4.14 2.65 2.210

Calibration Post Zero Cylinder Drift 1.2 3.52 1.74 2.153

Calibration Post High Cylinder ID CC122146 CC122146 CC122146

Calibration Post High Cylinder Instrument Response 85.954 88.842 85.389 86.728

Calibration Post High Cylinder Bias -4.92 -3.19 -4.56 -4.223

Calibration Post High Cylinder Drift 0.74 0.52 0.69 0.650

Cavg 13.059 11.794 12.061 12.305

Cavg Units ppmvd ppmvd ppmvd

Cgas 12.5561 8.6545 10.1825 10.464

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units ppmvw

Wednesday, January 12, 2011 Page 35 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - Method 7E

Average

Run Number 1 2 3

Test Date 4/21/2010 4/22/2010 4/22/2010

Run Start Time 3:51:00 PM 7:11:00 AM 11:24:00 AM

Run Finish Time 6:51:00 PM 10:11:00 AM 2:24:00 PM

Carbon Dioxide, % 13.529 13.583 13.53 13.547

Oxygen, % 5.563 5.526 5.534 5.541

Fuel Factor 1.13 1.13 1.14

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

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

Moisture, % 0 0 0 0.000

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range 0 0 0 0.000

Operating Units

No. Readings/Avg. 0 0 0 0.000

Calibration Set 6 7 8 7.000

Calibration Pre Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Pre Zero Cylinder Instrument Response 0.15 0.32 0.42 0.297

Calibration Pre Zero Cylinder Bias -0.04 0.02 0.03 0.003

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID SG9154467 SG9154467 SG9154467

Calibration Pre High Cylinder Instrument Response 435.02 436.29 438.2 436.503

Calibration Pre High Cylinder Bias -3.32 -3.42 -2.79 -3.177

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC281576 CC281576 CC281576

Calibration Post Zero Cylinder Instrument Response 0.68 0.15 0.83 0.553

Calibration Post Zero Cylinder Bias 0.08 -0.02 0.12 0.060

Calibration Post Zero Cylinder Drift 0.12 0.04 0.09 0.083

Calibration Post High Cylinder ID SG9154467 SG9154467 SG9154467

Calibration Post High Cylinder Instrument Response 432.41 436.96 443.25 437.540

Calibration Post High Cylinder Bias -3.9 -3.27 -1.67 -2.947

Calibration Post High Cylinder Drift 0.58 0.15 1.12 0.617

Cavg 174.46 174.45 183.5 177.470

Cavg Units ppmvd ppmvd ppmvd

Cgas 180.4316 179.329 186.6563 182.139

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Wednesday, January 12, 2011 Page 36 of 37
Utility Boiler MACT ICR - Hopewell Power Station Units 1 & 2

8/19/2010

Location Stack Exit - OTM - 27/28

Average

Run Number 1 2 3

Test Date 4/21/2010 4/22/2010 4/22/2010

Run Start Time

Run Finish Time

Net Traversing Points 12 12 12

Net Run Time, minutes 366.5 327 332.25

Nozzle Diameter, inches 0.138 0.138 0.138 0.138

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9873 0.9873 0.9873 0.987

Barometric Pressure, inches of Mercury 29.95 29.9 29.33 29.727

Average Orifice Meter Differential, inches H2O 0.41 0.42 0.44 0.423

Dry Gas Meter Volume Sampled, cubic feet 131.589 124.349 132.439 129.459

Average Dry Gas Meter Temperature, °F 59.58 72.58 77.33 69.830

Dry Gas Meter Volume Sampled, dscf 132.289 121.758 126.092 126.713

Total Moisture Liquid collected, g 415.7 395.5 414.6 408.600

Volume of Water Vapor, standard cubic feet 19.57 18.62 19.52 19.237

Moisture Content of Stack Gas, % 12.89 13.26 13.41 13.187

Moisture Saturation at Stack Gas Temperature, % 100.00 97.46 100.00 99.153

Dry Mole Fraction 0.8711 0.8674 0.8659 0.868

Carbon Dioxide, % 13.49 13.509 13.66 13.553

Oxygen, % 5.572 5.543 5.445 5.520

Carbon Monoxide & Nitrogen, % 80.938 80.948 80.895 80.927

Fuel Factor 1.14 1.14 1.13

Dry Molecular Weight, lb/lb-Mole 30.38 30.38 30.40 30.387

Wet Molecular weight, lb/lb-Mole 28.78 28.74 28.74 28.753

Flue Gas Static Pressure, inches of H2O -0.85 -0.85 -0.85 -0.850

Absolute Flue Gas Pressure, inches of Mercury 29.89 29.84 29.27 29.667

Average Stack Gas Temperature, °F 215.83 210.58 213.08 213.163

Average Velocity Head, inches of H2O 2.0704771691

0853

2.053390797

4239

2.080910373

61646

2.068

Average Stack Gas Velocity, feet/second 91.59 90.99 92.66 91.747

Stack Cross-Sectional Area, square feet 50.265 50.265 50.265 50.265

Dry Volumetric Flow Rate, dry scfm 187,799.2 186,917.8 185,697.2 186,804.733

Actual Wet Volumetric Flue Gas Flow Rate, acfm 276,226.3 274,416.7 279,453.3 276,698.767

Percent Isokinetic of Sampling Rate, % 93.0 96.4 98.9 96.100

Percent Excess Air, % 35.3 35.0 34.2 34.833

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

Round Duct Diameter, inches 96 96 96

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

Wednesday, January 12, 2011 Page 37 of 37