### 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: James River Cogeneration Company 50950
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 116 960 720 4 116 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location
Carbon Monoxide Method 10 3 120 0 Stack Exit Formaldehyde Method 0011 3 120 0 Stack Exit Total organic compounds

(TOC) as Propane Method 25A 3 120 0 Stack Exit

Hydrogen Fluoride Method 26A 3 180 0 Stack Exit Hydrogen Chloride Method 26A 3 180 0 Stack Exit 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. Sulfur Dioxide Method 6C 3 180 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### 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