### Name: Rolf Dinsmore

Title: Compliance Supervisor Company: Chambers Cogeneration, LP, ORIS 10 Sign Date: 9/2/2010 Name: Lenny D. Katerynczuk Title: Project Manager Company: AirNova, Inc. Sign Date: 9/2/2010 Permitted Facility Representative / Date Testing Company Representative / Date 

## Boil1 MACT HAP EDR Carneys Point

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.

Tuesday, January 25, 2011 Page 1 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010 Facility Information: Chambers Cogeneration LP. BOIL1
500 Shell Road

Carneys Point NJ 08069 Contact: Rolf Dinsmore Phone: 856-351-6386 Fax: 856-351-6399 Email: RolfDinsmore@cogentrix.com Testing Company:
Air Nova Inc. 585 Clayton Avenue

Pennsauken NJ 08019 Contact: Lenny Katerynczuk Phone: 856-486-1500 Fax: 856-486-9896 Email: Lenny@airnova.com

Air Permit Number: 10566 Permitted Source ID/Name: Boiler #1 BOIL1 Permitted Maximum Process Rate: 1260 Klbs/Hr Steam Max. Normal Operation Process Rate: 1260 Klbs/Hr Steam Target Process Test Rate 1200 Klbs/Hr Steam

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: The Carneys Point Generating plant uses PA/WV bituminous pulverzized coal. The coal is burned in low nox burners utilizing overfire air. A selective catalytic reducer uses ammonia to reduce Nox. The flue gas then passes through an air preheater, spray dry absorber to reduce Sox, and fabric baghouse. Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information: AFS #: 3403300071 FRS #: 110017403264

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 120 315 80 1 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location % H2O Method 1 - 4 3 180 0 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



### Tuesday, January 25, 2011 Page 2 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010 1,2,3,7,8,9-HxCDD Method 23 3 480 0 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 Stack Exit 2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157) 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 Stack Exit 2,3,3',4,4',5,5'-HpCB

(PCB189) Method 23 3 480 0 Stack Exit

Total PCBs Method 23 3 480 0 Stack Exit Total TEQ Method 23 3 480 0 Stack Exit Total organic compounds

(TOC) as Propane Method 25A 3 120 0 Stack Exit
Hydrogen Chloride Method 26 3 180 0 Stack Exit Hydrogen Fluoride Method 26 3 180 0 Stack Exit Hydrogen Chloride Method 26A 3 180 0 run date is 3/8 not 4/10 - ERT entry error Stack Exit
Hydrogen Fluoride Method 26A 3 180 0 run date is 3/8 not 4/10 - ERT entry error Stack Exit
Inorganic (Aqueous)

Condensible Part. OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit



### Tuesday, January 25, 2011 Page 3 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010

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. See attached test report

Organic Condensible Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Total Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

Arsenic Method 29 3 240 0 Stack Exit Manganese Method 29 3 240 0 Stack Exit Nickel Method 29 3 240 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit Chromium Method 29 3 240 0 Stack Exit Cadmium Method 29 3 240 0 Stack Exit Lead Method 29 3 240 0 Stack Exit Beryllium Method 29 3 240 0 Stack Exit Antimony Method 29 3 240 0 Stack Exit Co2 Method 3A CO2 3 120 0 Stack Exit Co2 Method 3A CO2 3 240 0 Stack Exit O2 Method 3A O2 3 240 0 Stack Exit O2 Method 3A O2 3 480 0 Stack Exit Co2 Method 3A CO2 3 480 0 Stack Exit O2 Method 3A O2 3 120 0 Stack Exit Organic Condensible

Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Inorganic (Aqueous)

Condensible Part. Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Total Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Filterable Particulate Method 5 3 240 0 Stack Exit Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet stacks. Delete OTM27/OTM28 test. Stack Exit

Sulfur Dioxide Method 6C 3 180 0 Stack Exit Nitrogen oxides (NOx) Method 7E 3 180 0 Stack Exit



### Tuesday, January 25, 2011 Page 4 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010 Sampling / Stack Data Results Summary



### Location Stack Exit - Method 0011 Average Run Number 1 2 3
Test Date 3/10/2010 3/10/2010 3/10/2010 Run Start Time 1:10:00 PM 3:18:00 PM 5:25:00 PM Run Finish Time 3:13:00 PM 5:20:00 PM 7:27:00 PM Net Run Time, minutes 120 120 120 Dry Gas Meter Volume Sampled, dscf 83.313 80.604 84.398 82.772 Moisture Content of Stack Gas, % 12.36 12.29 12.30 12.317 Moisture Saturation at Stack Gas Temperature, % 52.69 52.06 53.72 52.823 Carbon Dioxide, % 14.28 14.42 14.57 14.423 Oxygen, % 5.3 5.32 5.38 5.333 Average Stack Gas Temperature, °F 181.33 180.75 182.17 181.417 Dry Volumetric Flow Rate, dry scfm 307,499.0 308,257.8 309,538.6 308,431.800 Actual Wet Volumetric Flue Gas Flow Rate, acfm 427,461.8 428,074.4 430,854.7 428,796.967 Percent Isokinetic of Sampling Rate, % 102.6 102.5 103.3 102.800 F-Factor, dscfm/MMBtu @ %O2 9592 9592 9592 9,592.000
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



### Tuesday, January 25, 2011 Page 5 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - Method 25A Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Location Stack Exit - Method 26A Average Run Number
Test Date Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Tuesday, January 25, 2011 Page 6 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - Method 29 Average Run Number
Test Date Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Location Stack Exit - Method 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



### Tuesday, January 25, 2011 Page 7 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - Method 7E Average Run Number
Test Date Run Start Time
Run Finish Time Carbon Dioxide, % Oxygen, % Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Fuel Type
Fw
Fc



### Location Stack Exit - OTM - 27/28 Average Run Number
Test Date Run Start Time
Run Finish Time Net Run Time, minutes Dry Gas Meter Volume Sampled, dscf Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Carbon Dioxide, % Oxygen, % Average Stack Gas Temperature, °F Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % F-Factor, dscfm/MMBtu @ %O2
Fw
Fc



### Tuesday, January 25, 2011 Page 8 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010 Emissions Summary



### Location: Stack Exit - Method 0011 Compound: Formaldehyde Average RunNumber 1 2 3 Mass_mg 0.00212 0.0026 0.0032 0.003 Elb/hr 1.04E-03 1.32E-03 1.55E-03 0.001 gr/dscf 3.93E-07 4.98E-07 5.85E-07 0.000 lb/mmBtuO2 7.21E-07 9.15E-07 1.08E-06 0.000 mg/dscm 8.99E-04 1.14E-03 1.34E-03 0.001 ppm 7.20E-04 9.12E-04 1.07E-03 0.001 ppm@7%O2 6.42E-04 8.14E-04 9.58E-04 0.001



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run 1 2 3 lb/mmBtuO2 4.81E-02 3.65E-02 4.70E-02 0.044 ppm 5.12E+01 3.90E+01 5.01E+01 46.767 ppm@7%O2 4.59E+01 3.48E+01 4.49E+01 41.867



### Location: Stack Exit - Method 25A Compound: Total organic compounds (TOC) as Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.000 gr/dscf 9.29E-05 3.28E-04 8.38E-05 0.000 lb/mmBtuO2 1.71E-04 6.02E-04 1.55E-04 0.000 mg/dscm 2.13E-01 7.50E-01 1.92E-01 0.385 ppm 1.16E-01 4.09E-01 1.05E-01 0.210 ppm@7%O2 1.03E-01 3.65E-01 9.40E-02 0.187



### Location: Stack Exit - Method 26A 

### Compound: Hydrogen Chloride Average RunNumber 1 2 3 Mass_mg 0.35 0.14 0.09 0.193 Elb/hr 1.20E-01 4.78E-02 3.13E-02 0.066 lb/mmBtuO2 7.60E-05 3.08E-05 2.04E-05 0.000 mg/dscm 9.55E-02 3.87E-02 2.55E-02 0.053 mg/dscm@7%O2 8.43E-02 3.41E-02 2.26E-02 0.047 

### Compound: Hydrogen Fluoride Average RunNumber 1 2 3 Mass_mg 0.03 0.04 0.03 0.033 Elb/hr 1.03E-02 1.37E-02 1.04E-02 0.011 lb/mmBtuO2 6.52E-06 8.79E-06 6.80E-06 0.000 mg/dscm 8.19E-03 1.10E-02 8.50E-03 0.009 mg/dscm@7%O2 7.23E-03 9.70E-03 7.54E-03 0.008



### Tuesday, January 25, 2011 Page 9 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010 Location: Stack Exit - Method 29 

### Compound: Antimony Average RunNumber 1 2 3 Mass_mg 0.000194 0.0001 0.0001 0.000 Elb/hr 4.37E-05 2.34E-05 2.22E-05 0.000 lb/mmBtuO2 2.79E-08 1.63E-08 1.53E-08 0.000 mg/dscm 3.48E-05 2.01E-05 1.91E-05 0.000 mg/dscm@7%O2 3.11E-05 1.81E-05 1.71E-05 0.000 

### Compound: Arsenic Average RunNumber 1 2 3 Mass_mg 0.000793 0.000673 0.000869 0.001 Elb/hr 1.78E-04 1.57E-04 1.93E-04 0.000 lb/mmBtuO2 1.14E-07 1.09E-07 1.33E-07 0.000 mg/dscm 1.42E-04 1.35E-04 1.66E-04 0.000 mg/dscm@7%O2 1.27E-04 1.21E-04 1.48E-04 0.000 

### Compound: Beryllium Average RunNumber 1 2 3 Mass_mg 0.000042 0.000031 0.000048 0.000 Elb/hr 9.45E-06 7.25E-06 1.07E-05 0.000 lb/mmBtuO2 6.04E-09 5.04E-09 7.35E-09 0.000 mg/dscm 7.52E-06 6.24E-06 9.14E-06 0.000 mg/dscm@7%O2 6.72E-06 5.61E-06 8.16E-06 0.000 

### Compound: Cadmium Average RunNumber 1 2 3 Mass_mg 0.000283 0.000142 0.0001 0.000 Elb/hr 6.37E-05 3.32E-05 2.22E-05 0.000 lb/mmBtuO2 4.07E-08 2.31E-08 1.53E-08 0.000 mg/dscm 5.07E-05 2.86E-05 1.91E-05 0.000 mg/dscm@7%O2 4.53E-05 2.57E-05 1.71E-05 0.000 

### Compound: Chromium Average RunNumber 1 2 3 Mass_mg 0.005934 0.011283 0.006459 0.008 Elb/hr 1.34E-03 2.64E-03 1.44E-03 0.002 lb/mmBtuO2 8.54E-07 1.83E-06 9.90E-07 0.000 mg/dscm 1.06E-03 2.27E-03 1.23E-03 0.002 mg/dscm@7%O2 9.47E-04 2.04E-03 1.10E-03 0.001 

### Compound: Lead Average RunNumber 1 2 3 Mass_mg 0.001807 0.001989 0.0016 0.002 Elb/hr 4.07E-04 4.65E-04 3.56E-04 0.000 lb/mmBtuO2 2.60E-07 3.23E-07 2.45E-07 0.000 mg/dscm 3.24E-04 4.00E-04 3.05E-04 0.000



### Tuesday, January 25, 2011 Page 10 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010 mg/dscm@7%O2 2.89E-04 3.59E-04 2.72E-04 0.000 

### Compound: Manganese Average RunNumber 1 2 3 Mass_mg 0.003477 0.003446 0.003779 0.004 Elb/hr 7.83E-04 8.06E-04 8.40E-04 0.001 lb/mmBtuO2 5.00E-07 5.60E-07 5.79E-07 0.000 mg/dscm 6.23E-04 6.93E-04 7.20E-04 0.001 mg/dscm@7%O2 5.57E-04 6.23E-04 6.43E-04 0.001 

### Compound: Nickel Average RunNumber 1 2 3 Mass_mg 0.012573 0.013624 0.008088 0.011 Elb/hr 2.83E-03 3.19E-03 1.80E-03 0.003 lb/mmBtuO2 1.81E-06 2.21E-06 1.24E-06 0.000 mg/dscm 2.25E-03 2.74E-03 1.54E-03 0.002 mg/dscm@7%O2 2.01E-03 2.46E-03 1.38E-03 0.002 

### Compound: Selenium Average RunNumber 1 2 3 Mass_mg 0.0001 0.0001 0.0001 0.000 Elb/hr 2.25E-05 2.34E-05 2.22E-05 0.000 lb/mmBtuO2 1.44E-08 1.63E-08 1.53E-08 0.000 mg/dscm 1.79E-05 2.01E-05 1.91E-05 0.000 mg/dscm@7%O2 1.60E-05 1.81E-05 1.71E-05 0.000



### Location: Stack Exit - Method 6C Compound: Sulfur Dioxide Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 1.58E-01 1.59E-01 1.61E-01 0.159 mg/dscm 1.98E+02 2.00E+02 2.01E+02 199.667 mg/dscm@7%O2 1.75E+02 1.76E+02 1.78E+02 176.333 ppm 7.43E+01 7.49E+01 7.56E+01 74.933 ppm@7%O2 6.56E+01 6.60E+01 6.70E+01 66.200



### Location: Stack Exit - Method 7E Compound: Nitrogen oxides (NOx) Average Run 1 2 3 Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 1.34E-01 1.36E-01 1.32E-01 0.134 mg/dscm 1.69E+02 1.71E+02 1.65E+02 168.333 mg/dscm@7%O2 1.49E+02 1.51E+02 1.46E+02 148.667 ppm 8.83E+01 8.96E+01 8.61E+01 88.000 ppm@7%O2 7.79E+01 7.90E+01 7.63E+01 77.733



### Location: Stack Exit - OTM - 27/28



### Tuesday, January 25, 2011 Page 11 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010

Process Run Data Compound: Filterable Particulate Average RunNumber 1 2 3 Mass_mg 2 1.6 3.3 2.300 lb/mmBtuO2 4.27E-04 3.74E-04 7.48E-04 0.001 

### Compound: Filterable PM2.5 Average RunNumber 1 2 3 Mass_mg 2 1.6 3.3 2.300 lb/mmBtuO2 4.27E-04 3.74E-04 7.48E-04 0.001 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 1 2 3 Mass_mg 8.9 43.1 14 22.000 lb/mmBtuO2 1.90E-03 1.01E-02 3.17E-03 0.005 

### Compound: Organic Condensible Particulate Average RunNumber 1 2 3 Mass_mg 2 1.9 1.1 1.667 lb/mmBtuO2 4.27E-04 4.44E-04 2.49E-04 0.000 

### Compound: Total Particulate Average RunNumber 1 2 3 Mass_mg 12.9 47.6 18.4 26.300 lb/mmBtuO2 2.75E-03 1.11E-02 4.17E-03 0.006 

### Compound: Total PM2.5 Average RunNumber 1 2 3 Mass_mg 12.9 47.6 18.4 26.300 lb/mmBtuO2 2.75E-03 1.11E-02 4.17E-03 0.006



### Tuesday, January 25, 2011 Page 12 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010 Process Run Data



### Run Name Value UOM Comments Target Value 1 Heat Input 1767.1 Million Btus/hr applies to M6, 7E, 26A 0



### 2 Heat Input 1598 Million Btus/hr applies to runs 1&2 of M29, OTM27/28 0

3 Heat Input 1466.9 Million Btus/hr applies to M0011, 10, 25A, runs 3 of M29, OTM27/28 0

1 Average Heat Input 1767.1 MMBtu/hr avg 3/8/10 0


### 2 Average Heat Input 1598 MMBtu/hr avg 3/9/10 0
3 Average Heat Input 1466.9 MMBtu/hr avg 3/10/10 0
1 Steam Output 723.1 1000 lb steam/hr avg 3/8/10 0


### 2 Steam Output 633.5 1000 lb steam/hr 0
3 Steam Output 568.3 1000 lb steam/hr 0
1 Synfuel Firing Rate 0 0


### 2 Synfuel Firing Rate 0 0
3 Synfuel Firing Rate 0 0
1 Petroleum Coke Firing Rate 0 0


### 2 Petroleum Coke Firing Rate 0 0
3 Petroleum Coke Firing Rate 0 0
1 Coal Gas Firing Rate 0 0


### 2 Coal Gas Firing Rate 0 0
3 Coal Gas Firing Rate 0 0
1 Fuel Oil Firing Rate 0.03 KPPH, avg 3/8/10 0


### 2 Fuel Oil Firing Rate 0.03 KPPH, avg 3/9/10 0
3 Fuel Oil Firing Rate 0.02 KPPH, avg 3/10/10 0


### 1 Flue Gas Flow Rate 330775 dscfm 0
2 Flue Gas Flow Rate 323472 dscfm 0
3 Flue Gas Flow Rate 0 dscfm 0


### 1 Pressure Drop Across FGD (if applicable) 1.1 in H20 DCS JP1PT29 0
2 Pressure Drop Across FGD (if applicable) 1 in H20 DCS JP1PT29 0
3 Pressure Drop Across FGD (if applicable) 0.9 in H20 DCS JP1PT29 0


### 1 FGD Scrubber Liquor pH 0 pH not applicable - spray dryer absorber 0

Tuesday, January 25, 2011 Page 13 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010 2 FGD Scrubber Liquor pH 0 pH not applicable - spray dryer absorber 0

3 FGD Scrubber Liquor pH 0 pH not applicable - spray dryer absorber 0



### 1 FGD Scrubber Liquor Flow Rate 49.2 gal/min DCS JP1FT21 0
2 FGD Scrubber Liquor Flow Rate 46.2 gal/min DCS JP1FT21 0


### 3 FGD Scrubber Liquor Flow Rate 46.7 gal/min DCS JP1FT21 0
1 Sorbent Type and Sorbent Injection Rate (if applicable) 249 lb/hr lime, avg 3/8/10 0

2 Sorbent Type and Sorbent Injection Rate (if applicable) 224 lb/hr lime, avg 3/9/10 0

3 Sorbent Type and Sorbent Injection Rate (if applicable) 206 lb/hr Lime, avg 3/10/10 0



### 1 Flue Gas Oxygen Content 5.9 % wet, avg 3/8/10 0
2 Flue Gas Oxygen Content 6.56 % wet, avg 3/9/10 0
3 Flue Gas Oxygen Content 6.67 % wet, avg 3/10/10 0


### 1 Flue Gas Carbon Dioxide Content 10.6 % wet, avg 3/8/10 0
2 Flue Gas Carbon Dioxide Content 10 % wet, avg 3/9/10 0
3 Flue Gas Carbon Dioxide Content 9.9 % wet, avg 3/10/10 0


### 1 Flue Gas Moisture Content 12.58 % avg 3/8/10 0
2 Flue Gas Moisture Content 12.55 % 0
3 Flue Gas Moisture Content 12.64 % avg 3/10/10 0


### 1 Flue Gas Sampling Point Temperature 176.3 Deg F avg 3/8/10 0
2 Flue Gas Sampling Point Temperature 176.6 Deg F 0
3 Flue Gas Sampling Point Temperature 176.1 Deg F avg 3/10/10 0


### 1 Flue Gas Pressure 29.89 in. Hg 29.89
2 Flue Gas Pressure 29.82 in. Hg 29.89
3 Flue Gas Pressure 0 in. Hg 29.89


### 1 Standard Pressure 29.92 in. Hg 0
2 Standard Pressure 29.92 in. Hg 0
3 Standard Pressure 29.92 in. Hg 0


### 1 Standard Temperature 68 Deg F 0
2 Standard Temperature 68 Deg F 0
3 Standard Temperature 68 Deg F 0


### 1 Unit Gross Electrical Output 77 MW 0
2 Unit Gross Electrical Output 77 MW 0
3 Unit Gross Electrical Output 77 MW 0



### Tuesday, January 25, 2011 Page 14 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010

APCD Run Data

Process Lab Run Data 1 Unit Net Electric Generation 3455.2 MWh total BOTH BOILERS 3/8/10 0



### 2 Unit Net Electric Generation 3102.9 MWh total BOTH BOILERS 3/9/10 0

3 Unit Net Electric Generation 2961.1 MWh total BOTH BOILERS 3/10/10 0

4 Heat Input 0 Million Btus/hr 0
4 Average Heat Input 0 MMBtu/hr 0


### 4 Steam Output 0 1000 lb steam/hr 0
4 Synfuel Firing Rate 0 0
4 Petroleum Coke Firing Rate 0 0


### 4 Coal Gas Firing Rate 0 0
4 Fuel Oil Firing Rate 0 0
4 Flue Gas Flow Rate 0 dscfm 0


### 4 Pressure Drop Across FGD (if applicable) 0 in H20 0
4 FGD Scrubber Liquor pH 0 pH 0
4 FGD Scrubber Liquor Flow Rate 0 gal/min 0


### 4 Sorbent Type and Sorbent Injection Rate (if applicable) 0 lb/hr 0

4 Flue Gas Oxygen Content 0 % 0


### 4 Flue Gas Carbon Dioxide Content 0 % 0
4 Flue Gas Moisture Content 0 % 0
4 Flue Gas Sampling Point Temperature 0 Deg F 0


### 4 Flue Gas Pressure 0 in. Hg 29.89
4 Standard Pressure 0 in. Hg 0
4 Standard Temperature 0 Deg F 0


### 4 Unit Gross Electrical Output 0 MW 0
4 Unit Net Electric Generation 0 MWh 0



### Run Name Value UOM Comments Target Value 1 LOW NOX BURNERS 1 N/A 1


### 1 OVERFIRE AIR 1 N/A 1
1 SCR (SELECTIVE CATALYTIC REDUCTION) 1 1
1 SPRAY DRYER 1 1


### 1 BAGHOUSE 1 1

Tuesday, January 25, 2011 Page 15 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010

Run Name Value UOM Comments 

### 1 Fuel Higher Heating Value 13139 Btu/lb 1 Fuel Moisture 6.3 % 1 Fuel Mercury Content ppm 

### 1 Fuel Cadmium Content ppm 1 Ultimate/Proximate Analysis 0 1 Fuel Nickel Content ppm 1 Fuel Arsenic Content ppm 

### 1 Fuel Chromium Content ppm 1 Fuel Beryllium Content ppm 1 Fuel Lead Content ppm 

### 1 Fuel Manganese Content ppm 1 Fuel Chlorine Content 937 ppm 1 Fuel Fluorine Content 76 ppm 2 Fuel Higher Heating Value 1E+05 Btu/lb 

### 2 Fuel Moisture 4.71 % 2 Fuel Mercury Content 0.13 ppm 2 Fuel Cadmium Content 0.2 ppm 

### 2 Ultimate/Proximate Analysis 0 2 Fuel Nickel Content 10 ppm 2 Fuel Arsenic Content 8 ppm 2 Fuel Chromium Content 15 ppm 

### 2 Fuel Beryllium Content 1.1 ppm 2 Fuel Lead Content 4 ppm 2 Fuel Manganese Content 11 ppm 

### 2 Fuel Chlorine Content 1048 ppm 2 Fuel Fluorine Content ppm 3 Fuel Higher Heating Value 13370 Btu/lb 3 Fuel Moisture 5.06 % 

### 3 Fuel Mercury Content 0.11 ppm 3 Fuel Cadmium Content 0.2 ppm 3 Ultimate/Proximate Analysis 0 

### 3 Fuel Nickel Content 9 ppm 3 Fuel Arsenic Content 6 ppm 3 Fuel Chromium Content 14 ppm 3 Fuel Beryllium Content 1 ppm 

### 3 Fuel Lead Content 4 ppm 3 Fuel Manganese Content 12 ppm 3 Fuel Chlorine Content 930 ppm 

### 3 Fuel Fluorine Content ppm

Tuesday, January 25, 2011 Page 16 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010 Sampling / Stack Data Results Detail



### Location Stack Exit - Method 0011 Average Run Number 1 2 3 Test Date 3/10/2010 3/10/2010 3/10/2010 Run Start Time 1:10:00 PM 3:18:00 PM 5:25:00 PM Run Finish Time 3:13:00 PM 5:20:00 PM 7:27:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 120 120 120 Nozzle Diameter, inches 0.178 0.175 0.178 0.177 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.97 1.01 0.97 0.983 Barometric Pressure, inches of Mercury 29.95 29.93 29.93 29.937 Average Orifice Meter Differential, inches H2O 1.40 1.49 1.43 1.440 Dry Gas Meter Volume Sampled, cubic feet 88.060 81.853 89.999 86.637 Average Dry Gas Meter Temperature, °F 83.75 83.71 88.25 85.237 Dry Gas Meter Volume Sampled, dscf 83.313 80.604 84.398 82.772 Total Moisture Liquid collected, g 249.6 239.8 251.6 247.000 Volume of Water Vapor, standard cubic feet 11.75 11.29 11.84 11.627 Moisture Content of Stack Gas, % 12.36 12.29 12.30 12.317 Moisture Saturation at Stack Gas Temperature, % 52.69 52.06 53.72 52.823 Dry Mole Fraction 0.8764 0.8771 0.877 0.877 Carbon Dioxide, % 14.28 14.42 14.57 14.423 Oxygen, % 5.3 5.32 5.38 5.333 Carbon Monoxide & Nitrogen, % 80.42 80.26 80.05 80.243 Fuel Factor 1.09 1.08 1.07 Dry Molecular Weight, lb/lb-Mole 30.50 30.52 30.55 30.523 Wet Molecular weight, lb/lb-Mole 28.96 28.98 29.01 28.983 Flue Gas Static Pressure, inches of H2O -1.6 -1.6 -1.6 -1.600 Absolute Flue Gas Pressure, inches of Mercury 29.83 29.81 29.81 29.817 Average Stack Gas Temperature, °F 181.33 180.75 182.17 181.417 Average Velocity Head, inches of H2O 2.1493210531 1452 2.157474030

16937 2.182794248

82284 2.163
Average Stack Gas Velocity, feet/second 90.71 90.84 91.43 90.993 Stack Cross-Sectional Area, square feet 78.540 78.540 78.540 78.540 Dry Volumetric Flow Rate, dry scfm 307,499.0 308,257.8 309,538.6 308,431.800 Actual Wet Volumetric Flue Gas Flow Rate, acfm 427,461.8 428,074.4 430,854.7 428,796.967 Percent Isokinetic of Sampling Rate, % 102.6 102.5 103.3 102.800 Percent Excess Air, % 33.2 33.5 34.1 33.600 F-Factor, dscfm/MMBtu @ %O2 9592 9592 9592 9,592.000 Round Duct Diameter, inches 120 120 120 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



### Tuesday, January 25, 2011 Page 17 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - Method 10 Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



### Tuesday, January 25, 2011 Page 18 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - Method 25A Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



### Tuesday, January 25, 2011 Page 19 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - Method 26A Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Tuesday, January 25, 2011 Page 20 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - Method 29 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Tuesday, January 25, 2011 Page 21 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - Method 6C Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



### Tuesday, January 25, 2011 Page 22 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - Method 7E Average Run Number Test Date Run Start Time Run Finish Time Carbon Dioxide, % Oxygen, % Fuel Factor Dry Volumetric Flow Rate, dry scfm F-Factor, dscfm/MMBtu @ %O2 Moisture, % Analyzer Make Analyzer Model Analyzer Serial Number Operating Range Operating Units No. Readings/Avg. Calibration Set Calibration Pre Zero Cylinder ID Calibration Pre Zero Cylinder Instrument Response Calibration Pre Zero Cylinder Bias Calibration Pre Zero Cylinder Drift Calibration Pre High Cylinder ID Calibration Pre High Cylinder Instrument Response Calibration Pre High Cylinder Bias Calibration Pre High Cylinder Drift Calibration Post Zero Cylinder ID Calibration Post Zero Cylinder Instrument Response Calibration Post Zero Cylinder Bias Calibration Post Zero Cylinder Drift Calibration Post High Cylinder ID Calibration Post High Cylinder Instrument Response Calibration Post High Cylinder Bias Calibration Post High Cylinder Drift Cavg Cavg Units Cgas Cgas Units Fuel Type Fw Fc Cgasw Cgasw Units



### Tuesday, January 25, 2011 Page 23 of 24

### Boil1 MACT HAP EDR Carneys Point
9/2/2010
Location Stack Exit - OTM - 27/28 Average Run Number Test Date Run Start Time Run Finish Time Net Traversing Points Net Run Time, minutes Nozzle Diameter, inches Pitot Tube Coefficient Dry Gas Meter Calibration Factor Barometric Pressure, inches of Mercury Average Orifice Meter Differential, inches H2O Dry Gas Meter Volume Sampled, cubic feet Average Dry Gas Meter Temperature, °F Dry Gas Meter Volume Sampled, dscf Total Moisture Liquid collected, g Volume of Water Vapor, standard cubic feet Moisture Content of Stack Gas, % Moisture Saturation at Stack Gas Temperature, % Dry Mole Fraction Carbon Dioxide, % Oxygen, % Carbon Monoxide & Nitrogen, % Fuel Factor Dry Molecular Weight, lb/lb-Mole Wet Molecular weight, lb/lb-Mole Flue Gas Static Pressure, inches of H2O Absolute Flue Gas Pressure, inches of Mercury Average Stack Gas Temperature, °F Average Velocity Head, inches of H2O Average Stack Gas Velocity, feet/second Stack Cross-Sectional Area, square feet Dry Volumetric Flow Rate, dry scfm Actual Wet Volumetric Flue Gas Flow Rate, acfm Percent Isokinetic of Sampling Rate, % Percent Excess Air, % F-Factor, dscfm/MMBtu @ %O2 Round Duct Diameter, inches Rectangular Duct Width, inches Rectangular Duct Length, inches Fw Fc



### Tuesday, January 25, 2011 Page 24 of 24