Name: Dana L. Rieves

Title: Compliance Supervisor

Company: James River Cogeneartoin Company

Sign Date:

Name: Lenny Katerynczuk

Title: Project Manager

Company: AirNova, Inc.

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Hopewell MACT ICR Testing Unit No. 1

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Thursday, February 17, 2011 Page 1 of 16
Hopewell MACT ICR Testing Unit No. 1

Facility Information:

James River Cogeneration Company

912 East Randolph Road

Hopewell VA 23860

Contact: Dana L. Rieves

Phone: 804-541-4001 ext 204

Fax:

Email: danarieves@cogentrix.com

Testing Company:

AirNova, Inc.

5845 Clayton Avenue

Pennsauken NJ 08109

Contact:Lenny D. Katerynczuk

Phone: 856-486-1500

Fax: 856-486-9896

Email: lenny@airnova.com

Air Permit Number:

50950

Permitted Source ID/Name:

50950 James River Cogeneration Company

Permitted Maximum Process Rate:

200 MMBtu/hr (157,500 lbs steam/hr)

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:

Unit 1 consists of three (3) 200 million Btu heat input per hour bituminous coal-fired Foster Wheeler boilers. Each 

of the boilers that make up Unit 1 have a dedicated scrubber and bagfilter and are routed to a common turbine stack 

that is shared by all three boilers.

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 5167000055 FRS #: 110000740422

SCC / Description 10100205 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Traveling Grate (Overfeed) Stoker (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 116 0 0 116 960 720 4 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 3 120 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

Regulation Description Compound Limit Unit

CAA Section 114 0

Thursday, February 17, 2011 Page 2 of 16
Hopewell MACT ICR Testing Unit No. 1

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.

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Thursday, February 17, 2011 Page 3 of 16
Hopewell MACT ICR Testing Unit No. 1

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011 

Average

Run Number 1 2 3

Test Date 5/5/2010 5/5/2010 5/5/2010

Run Start Time 7:43:00 AM 10:35:00 

AM

1:17:00 PM

Run Finish Time 9:57:00 AM 12:48:00 

PM

3:30:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 91.995 93.721 91.758 92.491

Moisture Content of Stack Gas, % 10.90 10.73 10.78 10.803

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

Carbon Dioxide, % 12.92 13.14 13.11 13.057

Oxygen, % 6.3 6.18 6.26 6.247

Average Stack Gas Temperature, °F 214.75 219.33 219.25 217.777

Dry Volumetric Flow Rate, dry scfm 165,616.9 169,348.1 165,433.1 166,799.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 236,906.1 243,423.3 238,139.1 239,489.500

Percent Isokinetic of Sampling Rate, % 99.7 99.3 99.5 99.500

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

Thursday, February 17, 2011 Page 4 of 16
Hopewell MACT ICR Testing Unit No. 1

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

Thursday, February 17, 2011 Page 5 of 16
Hopewell MACT ICR Testing Unit No. 1

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

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

Thursday, February 17, 2011 Page 6 of 16
Hopewell MACT ICR Testing Unit No. 1

Emissions Summary

Location: Stack Exit - Method 0011 

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.0078 0.0085 0.0103 0.009

lb/mmBtuO2 2.62E-06 2.78E-06 3.46E-06 0.000

ppm 2.40E-03 2.57E-03 3.18E-03 0.003

ppm@7%O2 2.28E-03 2.43E-03 3.02E-03 0.003

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 4.83E-01 5.92E-01 4.19E-01 0.498

ppm 4.74E+02 5.87E+02 4.13E+02 491.333

ppm@7%O2 4.51E+02 5.54E+02 3.92E+02 465.667

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

lb/mmBtuO2 3.59E-04 8.00E-04 1.85E-03 0.001

ppm 2.24E-01 5.03E-01 1.16E+00 0.629

ppm@7%O2 2.13E-01 4.75E-01 1.10E+00 0.596

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 129 166 241 178.667

lb/mmBtuO2 2.92E-02 3.63E-02 5.37E-02 0.040

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.69 0.69 0.78 0.720

lb/mmBtuO2 1.56E-04 1.51E-04 1.74E-04 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

lb/mmBtuO2 5.94E-01 4.51E-01 4.23E-01 0.489

ppm 2.72E+02 2.05E+02 1.91E+02 222.667

ppm@7%O2 2.43E+02 1.84E+02 1.73E+02 200.000

Location: Stack Exit - Method 7E

Thursday, February 17, 2011 Page 7 of 16
Hopewell MACT ICR Testing Unit No. 1

Process Run Data

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

lb/mmBtuO2 2.83E-01 3.05E-01 3.19E-01 0.302

ppm 1.80E+02 1.93E+02 2.01E+02 191.333

ppm@7%O2 1.61E+02 1.73E+02 1.82E+02 172.000

Thursday, February 17, 2011 Page 8 of 16
Hopewell MACT ICR Testing Unit No. 1

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 647 MMBtu/hr 0

2 Heat Input 637 MMBtu/hr 0

3 Heat Input 653 MMBtu/hr 0

1 Steam Output 510 1000lb/hr 0

1 Flue Gas Flow Rate 153691 dscfm 0

1 Pressure Drop Across FGD 2.5 in H2O 0

1 Sorbent Injection Rate 13.7 gal/min 0

1 Unit Gross Electric Output 41.7 MW 0

1 Unit Net Electric Output 44.9 MWh 0

2 Steam Output 515 1000lb/hr 0

2 Flue Gas Flow Rate 157630 dscfm 0

2 Sorbent Injection Rate 12.9 gal/min 0

2 Unit Gross Electric Output 42.7 MW 0

2 Unit Net Electric Output 46.3 MWh 0

3 Steam Output 512 1000lb/hr 0

3 Flue Gas Flow Rate 159308 dscfm 0

3 Sorbent Injection Rate 9.5 gal/min 0

3 Unit Gross Electric Output 42.1 MW 0

3 Unit Net Electric Output 45.8 MWh 0

Run Name Value UOM Comments

Target

Value

1 SCRUBBER 90 % 90

2 SCRUBBER 90 % 90

3 SCRUBBER 90 % 90

1 FABRIC FILTER 99.1 % 99.1

2 FABRIC FILTER 99.1 % 99.1

3 FABRIC FILTER 99.1 % 99.1

Run Name Value UOM Comments

1 Fuel Higher Heating Value (dry) 12830 Btu/lb

1 Fuel Higher Heating Value (wet) 13618 Btu/lb

Thursday, February 17, 2011 Page 9 of 16
Hopewell MACT ICR Testing Unit No. 1

2 Fuel Higher Heating Value (dry) 12637 Btu/lb

2 Fuel Higher Heating Value (wet) 13502 Btu/lb

3 Fuel Higher Heating Value (dry) 12745 Btu/lb

3 Fuel Higher Heating Value (wet) 13643 Btu/lb

Thursday, February 17, 2011 Page 10 of 16
Hopewell MACT ICR Testing Unit No. 1

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011 

Average

Run Number 1 2 3

Test Date 5/5/2010 5/5/2010 5/5/2010

Run Start Time 7:43:00 AM 10:35:00 AM 1:17:00 PM

Run Finish Time 9:57:00 AM 12:48:00 PM 3:30:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

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 0.99 0.99 0.99 0.990

Barometric Pressure, inches of Mercury 30.01 30.01 29.98 30.000

Average Orifice Meter Differential, inches H2O 2.06 2.21 2.11 2.127

Dry Gas Meter Volume Sampled, cubic feet 93.839 97.134 96.424 95.799

Average Dry Gas Meter Temperature, °F 77.50 86.33 93.25 85.693

Dry Gas Meter Volume Sampled, dscf 91.995 93.721 91.758 92.491

Total Moisture Liquid collected, g 239.1 239.4 235.6 238.033

Volume of Water Vapor, standard cubic feet 11.25 11.27 11.09 11.203

Moisture Content of Stack Gas, % 10.90 10.73 10.78 10.803

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

Dry Mole Fraction 0.891 0.8927 0.8922 0.892

Carbon Dioxide, % 12.92 13.14 13.11 13.057

Oxygen, % 6.3 6.18 6.26 6.247

Carbon Monoxide & Nitrogen, % 80.78 80.68 80.63 80.697

Fuel Factor 1.13 1.12 1.12

Dry Molecular Weight, lb/lb-Mole 30.32 30.35 30.35 30.340

Wet Molecular weight, lb/lb-Mole 28.98 29.02 29.02 29.007

Flue Gas Static Pressure, inches of H2O -0.2 -0.2 -0.2 -0.200

Absolute Flue Gas Pressure, inches of Mercury 30.00 30.00 29.97 29.990

Average Stack Gas Temperature, °F 214.75 219.33 219.25 217.777

Average Velocity Head, inches of H2O 0.7232151549

11831

0.759528697

466816

0.726159347

036486

0.736

Average Stack Gas Velocity, feet/second 53.80 55.28 54.08 54.387

Stack Cross-Sectional Area, square feet 73.391 73.391 73.391 73.391

Dry Volumetric Flow Rate, dry scfm 165,616.9 169,348.1 165,433.1 166,799.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 236,906.1 243,423.3 238,139.1 239,489.500

Percent Isokinetic of Sampling Rate, % 99.7 99.3 99.5 99.500

Percent Excess Air, % 41.9 40.9 41.7 41.500

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

Round Duct Diameter, inches 116 116 116

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

Thursday, February 17, 2011 Page 11 of 16
Hopewell MACT ICR Testing Unit No. 1

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

Thursday, February 17, 2011 Page 12 of 16
Hopewell MACT ICR Testing Unit No. 1

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

Thursday, February 17, 2011 Page 13 of 16
Hopewell MACT ICR Testing Unit No. 1

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

Thursday, February 17, 2011 Page 14 of 16
Hopewell MACT ICR Testing Unit No. 1

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

Thursday, February 17, 2011 Page 15 of 16
Hopewell MACT ICR Testing Unit No. 1

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

Thursday, February 17, 2011 Page 16 of 16