### Name: Lois A. Knowlson

Title: Senior Environmental Engineer Company: PSEG Environmental Sign Date: 9/3/2010 Name: Anthony Fortunato Title: Senior Testing Supervisor Company:Maplewood Testing Services Sign Date: 9/3/2010 Permitted Facility Representative / Date Testing Company Representative / Date 

## PSEG Sewaren Unit 4 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, February 22, 2011 Page 1 of 45

### PSEG Sewaren Unit 4
9/3/2010 Facility Information: PSEG Sewaren Generating Station 2411
751 Cliff Road

Sewaren NJ07077 Contact:Joseph D. Krejsa Phone:732-750-2001 Fax: Email: joseph.krejsa@pseg.com Testing Company: PSEG Maplewood Testing Services 200 Boyden Avenue

Maplewood NJ07040 Contact:Anthony Fortunato Phone:973-761-1005 Fax: Email:anthony.fortunato2@pseg.com

Air Permit Number: 2411-BOP08001 Permitted Source ID/Name: Unit 4 U4 Permitted Maximum Process Rate: 1700 MMBtu/hr Max. Normal Operation Process Rate: 1700 MMBtu/hr Target Process Test Rate N/A

Description of the source (including control equipment). Please see the attachments for source or process flow diagram: Sewaren Unit 4 is a dual-fuel (natural gas and #6 fuel oil) single-furnance, wet bottom, balanced draft, two-drum natural circulation steam generator with vertically adjustable tangential corner burners manufactured by Combustion Engineering (July 1951) for electricity generation. No emissions control devices are installed on this unit. Industry/SCC/NAIS221112

Sampling Location Information:

Test Parameter Information: AFS #:110000869150 FRS #:110000801614

SCC / Description10100404 External Combustion Boilers - Electric Generation - Residual Oil - Grade 6 Oil: Tangential Firing

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 14.263 487 1579 4 14.263 24 151.7 151.7

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 Regulation Description Compound Limit Unit NJAC 7:27-4.2(a) Particulate 160 lb/hr NJAC 7:27-16.8(b)1 Volatile Organic Compounds (total) 50 ppm corrected
NJAC 7:27-16.8(b)2 Carbon Monoxide 100 ppm corrected



### Tuesday, February 22, 2011 Page 2 of 45

### PSEG Sewaren Unit 4
9/3/2010 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 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 organic compounds

(TOC) as Propane Method 25A 3 120 0 PSEG believes that the Method 25A THC test results for Run 1-1 should be 4.65E-4lb/mmBtu and 1.89E1 lb/hr. PSEG unable to determine why the ERT is reporting 2.32E-4 lb/mmBtu and 0.095 lb/hr. Stack Exit

Hydrogen Fluoride Method 26A 3 180 0 Stack Exit Hydrogen Chloride Method 26A 3 180 0 Stack Exit Hydrogen Fluoride Method 26 3 180 0 Stack Exit Hydrogen Chloride Method 26 3 180 0 Stack Exit


### Tuesday, February 22, 2011 Page 3 of 45

### PSEG Sewaren Unit 4
9/3/2010

The following describes any modifications and/or deviations to the applicable test methods. If alternative methods were requested, see the attachments for documentation of request AND approval, including dates.
None Filterable PM2.5 OTM - 27/28 3 240 0 Use only for dry stacks. Delete Method 5/OTM28 tests. Stack Exit

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

Inorganic (Aqueous)

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

Organic Condensible

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

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

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

Beryllium Method 29 3 240 0 Stack Exit Cobalt Method 29 0 Stack Exit Nickel Method 29 3 240 0 Stack Exit Antimony Method 29 3 240 0 Stack Exit Arsenic Method 29 3 240 0 Stack Exit Selenium Method 29 3 240 0 Stack Exit Lead Method 29 3 240 0 Stack Exit Filterable Particulate Method 29 3 240 0 Stack Exit Chromium Method 29 3 240 0 Stack Exit Manganese Method 29 3 240 0 Stack Exit Cadmium Method 29 3 240 0 Stack Exit O2 Method 3A O2 3 240 0 Stack Exit O2 Method 3A O2 3 120 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 3 480 0 Stack Exit Co2 Method 3A CO2 3 480 0 Stack Exit Total 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

Organic Condensible

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, February 22, 2011 Page 4 of 45

### PSEG Sewaren Unit 4
9/3/2010

Tuesday, February 22, 2011 Page 5 of 45

### PSEG Sewaren Unit 4
9/3/2010

Tuesday, February 22, 2011 Page 6 of 45

### PSEG Sewaren Unit 4
9/3/2010 Sampling / Stack Data Results Summary



### LocationStack Exit - Method 0011 Average Run Number 1 2 3
Test Date 6/4/2010 6/4/2010 6/4/2010 Run Start Time 7:06:00 AM 10:08:00 AM 1:18:00 PM

Run Finish Time 9:22:00 AM 12:22:00 PM 3:31:00 PM

Net Run Time, minutes 120 120 120 Dry Gas Meter Volume Sampled, dscf 72.146 70.865 74.042 72.351 Moisture Content of Stack Gas, % 5.41 5.47 5.79 5.557 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 4.344 4.318 4.305 4.322 Oxygen, % 15.222 15.234 15.237 15.231 Average Stack Gas Temperature, °F 214.33 219.04 222.92 218.763 Dry Volumetric Flow Rate, dry scfm 229,463.3 222,694.8 230,858.0227,672.033 Actual Wet Volumetric Flue Gas Flow Rate, acfm 312,112.8 305,113.1 319,400.3 312,208.733 Percent Isokinetic of Sampling Rate, % 96.5 97.7 98.5 97.567 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Location Stack Exit - Method 10 Average Run Number 1-1 1-2 1-3
Test Date 6/4/2010 6/4/2010 6/4/2010 Run Start Time 7:15:00 AM 10:10:00 AM 1:19:00 PM

Run Finish Time 9:19:00 AM 12:14:00 PM 3:23:00 PM

Carbon Dioxide, % 4.344 4.318 4.305 4.322 Oxygen, % 15.222 15.234 15.237 15.231 Dry Volumetric Flow Rate, dry scfm 229604.2 222554.8 230858227,672.333 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 5.41 5.47 5.79 5.557 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 7 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 23 Average Run Number 1 2 3
Test Date 6/1/2010 6/2/2010 6/3/2010 Run Start Time 6:00:00 AM 7:40:00 AM 2:27:00 AM

Run Finish Time 9:45:00 PM 11:16:00 PM 6:12:00 PM

Net Run Time, minutes 480 480 480 Dry Gas Meter Volume Sampled, dscf 287.092 305.056 297.596 296.581 Moisture Content of Stack Gas, % 5.36 5.22 4.99 5.190 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 4.225 4.249 4.276 4.250 Oxygen, % 15.277 15.294 15.195 15.255 Average Stack Gas Temperature, °F 213.63 217.63 303.25 244.837 Dry Volumetric Flow Rate, dry scfm 222,691.2 235,198.5 217,976.2225,288.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 303,962.4 321,701.6 335,797.0320,487.000 Percent Isokinetic of Sampling Rate, % 99.0 99.6 104.1 100.900 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### LocationStack Exit - Method 25A Average Run Number 1-1 1-2 1-3
Test Date 6/4/2010 6/4/2010 6/4/2010 Run Start Time 7:15:00 AM 10:10:00 AM 1:19:00 PM

Run Finish Time 9:19:00 AM 12:14:00 PM 3:23:00 PM

Carbon Dioxide, % 4.344 4.318 4.305 4.322 Oxygen, % 15.222 15.234 15.237 15.231 Dry Volumetric Flow Rate, dry scfm 229604.2 222554.8 230858227,672.333 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 5.41 5.47 5.79 5.557 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 8 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 26A Average Run Number 1 2 3
Test Date 6/1/2010 6/1/2010 6/3/2010 Run Start Time 9:12:00 AM 11:38:00 AM 3:59:00 PM

Run Finish Time 10:34:00 AM 12:48:00 PM 5:09:00 PM

Net Run Time, minutes 60 60 60 Dry Gas Meter Volume Sampled, dscf 36.769 37.781 36.104 36.885 Moisture Content of Stack Gas, % 7.71 7.72 7.48 7.637 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 4.096 4.266 4.346 4.236 Oxygen, % 15.37 15.257 15.192 15.273 Average Stack Gas Temperature, °F 229.83 218.21 229.42 225.820 Dry Volumetric Flow Rate, dry scfm 222,153.7 236,198.5 219,561.1 225,971.100 Actual Wet Volumetric Flue Gas Flow Rate, acfm 315,756.5 331,769.7 313,742.9320,423.033 Percent Isokinetic of Sampling Rate, % 101.6 98.2 100.3 100.033 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 9 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 29 Average Run Number 2 3 4
Test Date 6/2/2010 6/2/2010 6/3/2010 Run Start Time 9:25:00 AM4:10:00 PM 9:00:00 AM Run Finish Time 3:19:00 PM 10:02:00 PM 2:49:00 PM

Net Run Time, minutes 336 336 336 Dry Gas Meter Volume Sampled, dscf 219.573 218.882 216.450 218.302 Moisture Content of Stack Gas, % 7.06 6.81 7.13 7.000 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 6.2 6.2 6.4 6.267 Oxygen, % 12.8 12.7 12.5 12.667 Average Stack Gas Temperature, °F 240.75 242.54 243.63 242.307 Dry Volumetric Flow Rate, dry scfm 312,401.1 311,651.5 310,152.5 311,401.700 Actual Wet Volumetric Flue Gas Flow Rate, acfm 448,656.2 448,272.7 449,711.0448,879.967 Percent Isokinetic of Sampling Rate, % 99.7 99.6 99.0 99.433 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### LocationStack Exit - Method 6C Average Run Number 1-1 1-2 1-3
Test Date 6/4/2010 6/4/2010 6/4/2010 Run Start Time 7:15:00 AM 10:10:00 AM 1:19:00 PM

Run Finish Time 9:14:00 AM 12:14:00 PM 3:23:00 PM

Carbon Dioxide, % 4.344 4.318 4.305 4.322 Oxygen, % 15.222 15.234 15.237 15.231 Dry Volumetric Flow Rate, dry scfm 224759.9 217795.8 226006.6222,854.100 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 5.41 5.47 5.79 5.557 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 10 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 6C 3 Average Run Number 3-1 3-2 3-3
Test Date 6/1/2010 6/1/2010 6/3/2010 Run Start Time 9:14:00 AM 11:40:00 AM 4:01:00 PM

Run Finish Time 10:20:00 AM 12:40:00 PM 5:11:00 PM

Carbon Dioxide, % 4.096 4.266 4.346 4.236 Oxygen, % 15.37 15.257 15.192 15.273 Dry Volumetric Flow Rate, dry scfm 222153.7 235993.7 219494225,880.467 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 7.71 7.72 7.78 7.737 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Location Stack Exit - Method 7E Average Run Number 3-1 3-2 3-3
Test Date 6/1/2010 6/1/2010 6/3/2010 Run Start Time 9:14:00 AM 11:40:00 AM 4:01:00 PM

Run Finish Time 10:20:00 AM 12:40:00 PM 5:11:00 PM

Carbon Dioxide, % 4.096 4.266 4.346 4.236 Oxygen, % 15.37 15.257 15.192 15.273 Dry Volumetric Flow Rate, dry scfm 219995.4 231026.6 218381 223,134.333 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000 Moisture, % 7.71 7.72 7.78 7.737 Fuel Type Oil Oil Oil
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 11 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - OTM - 27/28 Average Run Number 2 3 4
Test Date 6/2/2010 6/2/2010 6/3/2010 Run Start Time 9:25:00 AM4:10:00 PM 9:00:00 AM Run Finish Time 3:13:00 PM 10:04:00 PM 2:40:00 PM

Net Run Time, minutes 334.39 338.59 324.67 Dry Gas Meter Volume Sampled, dscf 124.260 120.922 123.303 122.828 Moisture Content of Stack Gas, % 6.52 7.05 7.26 6.943 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Carbon Dioxide, % 6.2 6.2 6.4 6.267 Oxygen, % 12.8 12.7 12.5 12.667 Average Stack Gas Temperature, °F 233.58 236.67 237.67 235.973 Dry Volumetric Flow Rate, dry scfm 309,526.2 303,047.9 296,979.1 303,184.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 437,437.4 456,423.1 427,561.0440,473.833 Percent Isokinetic of Sampling Rate, % 101.7 99.8 108.3 103.267 F-Factor, dscfm/MMBtu @ %O2 9190 9190 9190 9,190.000
Fw 10320 10320 10320 10,320.000
Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 12 of 45

### PSEG Sewaren Unit 4
9/3/2010 Emissions Summary



### Location: Stack Exit - Method 0011 Compound: Formaldehyde Average RunNumber 2 3 1 Mass_mg 0.19 0.12 0.32 0.210 lb/mmBtuO2 2.00E-04 1.21E-04 3.31E-04 0.000



### Location: Stack Exit - Method 10 Compound: Carbon Monoxide Average Run 1-1 1-2 1-3 Elb/hr -4.19E-01 0.00E+00 0.00E+00 -0.140 gr/dscf -2.13E-04 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 -1.03E-03 0.00E+00 0.00E+00 0.000 mg/dscm -4.87E-01 0.00E+00 0.00E+00 -0.162 ppm -4.18E-01 0.00E+00 0.00E+00 -0.139 ppm@7%O2 -1.02E+00 0.00E+00 0.00E+00 -0.340



### Location: Stack Exit - Method 23 Compound: 1,2,3,4,6,7,8-HpCDD Average RunNumber 1 2 3 Mass_mg 0.0000000032 0.000000002 0.0000000019 0.000 lb/mmBtuO2 8.39E-13 4.95E-13 4.74E-13 0.000 ng/dscm 3.94E-04 2.32E-04 2.26E-04 0.000 ng/dscm@7%O2 9.74E-04 5.75E-04 5.51E-04 0.001 

### Compound: 1,2,3,4,6,7,8-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000023 0.0000000011 0.0000000012 0.000 lb/mmBtuO2 6.03E-13 2.72E-13 2.99E-13 0.000 ng/dscm 2.83E-04 1.27E-04 1.42E-04 0.000 ng/dscm@7%O2 7.00E-04 3.15E-04 3.46E-04 0.000 

### Compound: 1,2,3,4,7,8,9-HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000013 0.0000000012 0.0000000012 0.000 lb/mmBtuO2 3.41E-13 2.97E-13 2.99E-13 0.000 ng/dscm 1.60E-04 1.39E-04 1.42E-04 0.000 ng/dscm@7%O2 3.96E-04 3.45E-04 3.46E-04 0.000 

### Compound: 1,2,3,4,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000011 0.0000000012 0.0000000011 0.000 lb/mmBtuO2 2.89E-13 2.97E-13 2.74E-13 0.000 ng/dscm 1.35E-04 1.39E-04 1.31E-04 0.000 ng/dscm@7%O2 3.34E-04 3.45E-04 3.19E-04 0.000



### Tuesday, February 22, 2011 Page 13 of 45

### PSEG Sewaren Unit 4
9/3/2010 Compound: 1,2,3,4,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000125 0.00000000097 0.000000001 0.000 lb/mmBtuO2 3.28E-13 2.40E-13 2.49E-13 0.000 ng/dscm 1.54E-04 1.12E-04 1.19E-04 0.000 ng/dscm@7%O2 3.81E-04 2.78E-04 2.90E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000011 0.0000000013 0.0000000011 0.000 lb/mmBtuO2 2.89E-13 3.22E-13 2.74E-13 0.000 ng/dscm 1.35E-04 1.51E-04 1.31E-04 0.000 ng/dscm@7%O2 3.34E-04 3.74E-04 3.19E-04 0.000 

### Compound: 1,2,3,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.00000000113 0.00000000094 0.000000001 0.000 lb/mmBtuO2 2.96E-13 2.33E-13 2.49E-13 0.000 ng/dscm 1.39E-04 1.09E-04 1.19E-04 0.000 ng/dscm@7%O2 3.44E-04 2.70E-04 2.90E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000011 0.0000000012 0.0000000011 0.000 lb/mmBtuO2 2.89E-13 2.97E-13 2.74E-13 0.000 ng/dscm 1.35E-04 1.39E-04 1.31E-04 0.000 ng/dscm@7%O2 3.34E-04 3.45E-04 3.19E-04 0.000 

### Compound: 1,2,3,7,8,9-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000013 0.0000000012 0.0000000013 0.000 lb/mmBtuO2 3.41E-13 2.97E-13 3.24E-13 0.000 ng/dscm 1.60E-04 1.39E-04 1.54E-04 0.000 ng/dscm@7%O2 3.96E-04 3.45E-04 3.75E-04 0.000 

### Compound: 1,2,3,7,8-PeCDD Average RunNumber 1 2 3 Mass_mg 0.0000000011 0.000000001 0.0000000011 0.000 lb/mmBtuO2 2.89E-13 2.48E-13 2.74E-13 0.000 ng/dscm 1.35E-04 1.16E-04 1.31E-04 0.000 ng/dscm@7%O2 3.34E-04 2.88E-04 3.19E-04 0.000 

### Compound: 1,2,3,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000012 0.0000000012 0.0000000011 0.000 lb/mmBtuO2 3.15E-13 2.97E-13 2.74E-13 0.000



### Tuesday, February 22, 2011 Page 14 of 45

### PSEG Sewaren Unit 4
9/3/2010 ng/dscm 1.48E-04 1.39E-04 1.31E-04 0.000 ng/dscm@7%O2 3.66E-04 3.45E-04 3.19E-04 0.000 

### Compound: 2,3,3',4,4',5,5'-HpCB (PCB189) Average RunNumber 1 2 3 Mass_mg 0.0000000037 0.0000000027 0.0000000035 0.000 lb/mmBtuO2 9.71E-13 6.69E-13 8.73E-13 0.000 ng/dscm 4.55E-04 3.13E-04 4.15E-04 0.000 ng/dscm@7%O2 1.12E-03 7.76E-04 1.01E-03 0.001 

### Compound: 2,3,3',4,4',5/2,3,3',4,4',5'-HxCB (PC Average RunNumber 1 2 3 Mass_mg 0.000000054 0.000000041 0.000000029 0.000 lb/mmBtuO2 1.42E-11 1.02E-11 7.23E-12 0.000 ng/dscm 6.64E-03 4.75E-03 3.44E-03 0.005 ng/dscm@7%O2 1.64E-02 1.18E-02 8.38E-03 0.012 

### Compound: 2,3,3',4,4'-PeCB (PCB105) Average RunNumber 1 2 3 Mass_mg 0.00000027 0.00000019 0.00000012 0.000 lb/mmBtuO2 7.08E-11 4.70E-11 2.99E-11 0.000 ng/dscm 3.32E-02 2.20E-02 1.42E-02 0.023 ng/dscm@7%O2 8.21E-02 5.45E-02 3.46E-02 0.057 

### Compound: 2,3',4,4',5,5'-HxCB (PCB167) Average RunNumber 1 2 3 Mass_mg 0.000000022 0.000000015 0.000000011 0.000 lb/mmBtuO2 5.77E-12 3.71E-12 2.74E-12 0.000 ng/dscm 2.71E-03 1.74E-03 1.31E-03 0.002 ng/dscm@7%O2 6.70E-03 4.31E-03 3.19E-03 0.005 

### Compound: 2,3,4,4',5-PeCB (PCB114) Average RunNumber 1 2 3 Mass_mg 0.000000018 0.0000000011 0.0000000079 0.000 lb/mmBtuO2 4.72E-12 2.72E-13 1.97E-12 0.000 ng/dscm 2.21E-03 1.27E-04 9.38E-04 0.001 ng/dscm@7%O2 5.46E-03 3.15E-04 2.29E-03 0.003 

### Compound: 2,3',4,4',5-PeCB (PCB118) Average RunNumber 1 2 3 Mass_mg 0.00000081 0.00000054 0.00000034 0.000 lb/mmBtuO2 2.12E-10 1.34E-10 8.48E-11 0.000 ng/dscm 9.97E-02 6.25E-02 4.04E-02 0.068 ng/dscm@7%O2 2.46E-01 1.55E-01 9.84E-02 0.166 

### Compound: 2',3,4,4',5-PeCB (PCB123) Average RunNumber 1 2 3


### Tuesday, February 22, 2011 Page 15 of 45

### PSEG Sewaren Unit 4
9/3/2010 Mass_mg 0.000000012 0.0000000083 0.0000000052 0.000 lb/mmBtuO2 3.15E-12 2.06E-12 1.30E-12 0.000 ng/dscm 1.48E-03 9.61E-04 6.17E-04 0.001 ng/dscm@7%O2 3.66E-03 2.38E-03 1.50E-03 0.003 

### Compound: 2,3,4,6,7,8-HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000011 0.0000000011 0.0000000012 0.000 lb/mmBtuO2 2.89E-13 2.72E-13 2.99E-13 0.000 ng/dscm 1.35E-04 1.27E-04 1.42E-04 0.000 ng/dscm@7%O2 3.34E-04 3.15E-04 3.46E-04 0.000 

### Compound: 2,3,4,7,8-PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000024 0.0000000016 0.0000000021 0.000 lb/mmBtuO2 6.30E-13 3.96E-13 5.24E-13 0.000 ng/dscm 2.95E-04 1.85E-04 2.49E-04 0.000 ng/dscm@7%O2 7.29E-04 4.59E-04 6.07E-04 0.001 

### Compound: 2,3,7,8-TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000014 0.0000000012 0.0000000011 0.000 lb/mmBtuO2 3.67E-13 2.97E-13 2.74E-13 0.000 ng/dscm 1.72E-04 1.39E-04 1.31E-04 0.000 ng/dscm@7%O2 4.25E-04 3.45E-04 3.19E-04 0.000 

### Compound: 2,3,7,8-TCDF Average RunNumber 1 2 3 Mass_mg 0.000000004 0.0000000031 0.0000000034 0.000 lb/mmBtuO2 1.05E-12 7.68E-13 8.48E-13 0.000 ng/dscm 4.92E-04 3.59E-04 4.04E-04 0.000 ng/dscm@7%O2 1.22E-03 8.90E-04 9.84E-04 0.001 

### Compound: 3,3',4,4',5,5'-HxCB (PCB169) Average RunNumber 1 2 3 Mass_mg 0.0000000029 0.0000000034 0.0000000031 0.000 lb/mmBtuO2 7.61E-13 8.42E-13 7.73E-13 0.000 ng/dscm 3.57E-04 3.94E-04 3.68E-04 0.000 ng/dscm@7%O2 8.83E-04 9.77E-04 8.97E-04 0.001 

### Compound: 3,3',4,4',5-PeCB (PCB126) Average RunNumber 1 2 3 Mass_mg 0.000000003 0.0000000052 0.0000000029 0.000 lb/mmBtuO2 7.87E-13 1.29E-12 7.23E-13 0.000 ng/dscm 3.69E-04 6.02E-04 3.44E-04 0.000 ng/dscm@7%O2 9.12E-04 1.49E-03 8.38E-04 0.001



### Tuesday, February 22, 2011 Page 16 of 45

### PSEG Sewaren Unit 4
9/3/2010 Compound: 3,3',4,4'-TCB (PCB77) Average RunNumber 1 2 3 Mass_mg 0.000000065 0.000000028 0.000000019 0.000 lb/mmBtuO2 1.70E-11 6.93E-12 4.74E-12 0.000 ng/dscm 8.00E-03 3.24E-03 2.26E-03 0.005 ng/dscm@7%O2 1.98E-02 8.03E-03 5.51E-03 0.011 

### Compound: 3,4,4',5-TCB (PCB81) Average RunNumber 1 2 3 Mass_mg 0.0000000034 0.0000000028 0.0000000038 0.000 lb/mmBtuO2 8.92E-13 6.93E-13 9.48E-13 0.000 ng/dscm 4.18E-04 3.24E-04 4.51E-04 0.000 ng/dscm@7%O2 1.03E-03 8.03E-04 1.10E-03 0.001 

### Compound: OCDD Average RunNumber 1 2 3 Mass_mg 0.000000018 0.000000012 0.0000000125 0.000 lb/mmBtuO2 4.72E-12 2.97E-12 3.12E-12 0.000 ng/dscm 2.21E-03 1.39E-03 1.48E-03 0.002 ng/dscm@7%O2 5.46E-03 3.45E-03 3.61E-03 0.004 

### Compound: OCDF Average RunNumber 1 2 3 Mass_mg 0.0000000039 0.000000003 0.0000000034 0.000 lb/mmBtuO2 1.02E-12 7.43E-13 8.48E-13 0.000 ng/dscm 4.80E-04 3.47E-04 4.04E-04 0.000 ng/dscm@7%O2 1.19E-03 8.60E-04 9.84E-04 0.001 

### Compound: Other HpCDD Average RunNumber 1 2 3 Mass_mg 0.0000000032 0.000000002 0.0000000019 0.000 lb/mmBtuO2 8.39E-13 4.95E-13 4.74E-13 0.000 ng/dscm 3.94E-04 2.32E-04 2.26E-04 0.000 ng/dscm@7%O2 9.74E-04 5.75E-04 5.51E-04 0.001 

### Compound: Other HpCDF Average RunNumber 1 2 3 Mass_mg 0.0000000026 0.0000000013 0.0000000014 0.000 lb/mmBtuO2 6.82E-13 3.22E-13 3.49E-13 0.000 ng/dscm 3.20E-04 1.51E-04 1.66E-04 0.000 ng/dscm@7%O2 7.91E-04 3.74E-04 4.04E-04 0.001 

### Compound: Other HxCDD Average RunNumber 1 2 3 Mass_mg 0.0000000078 0.0000000055 0.0000000052 0.000 lb/mmBtuO2 2.05E-12 1.36E-12 1.30E-12 0.000



### Tuesday, February 22, 2011 Page 17 of 45

### PSEG Sewaren Unit 4
9/3/2010 ng/dscm 9.60E-04 6.37E-04 6.17E-04 0.001 ng/dscm@7%O2 2.37E-03 1.58E-03 1.50E-03 0.002 

### Compound: Other HxCDF Average RunNumber 1 2 3 Mass_mg 0.0000000024 0.000000001 0.0000000011 0.000 lb/mmBtuO2 6.30E-13 2.48E-13 2.74E-13 0.000 ng/dscm 2.95E-04 1.16E-04 1.31E-04 0.000 ng/dscm@7%O2 7.29E-04 2.88E-04 3.19E-04 0.000 

### Compound: Other PeCDD Average RunNumber 1 2 3 Mass_mg 0.0000000021 0.0000000011 0.0000000011 0.000 lb/mmBtuO2 5.51E-13 2.72E-13 2.74E-13 0.000 ng/dscm 2.58E-04 1.27E-04 1.31E-04 0.000 ng/dscm@7%O2 6.38E-04 3.15E-04 3.19E-04 0.000 

### Compound: Other PeCDF Average RunNumber 1 2 3 Mass_mg 0.0000000024 0.000000005 0.0000000044 0.000 lb/mmBtuO2 6.30E-13 1.24E-12 1.10E-12 0.000 ng/dscm 2.95E-04 5.79E-04 5.22E-04 0.000 ng/dscm@7%O2 7.29E-04 1.44E-03 1.27E-03 0.001 

### Compound: Other TCDD Average RunNumber 1 2 3 Mass_mg 0.0000000046 0.0000000022 0.0000000016 0.000 lb/mmBtuO2 1.21E-12 5.45E-13 3.99E-13 0.000 ng/dscm 5.66E-04 2.55E-04 1.90E-04 0.000 ng/dscm@7%O2 1.40E-03 6.32E-04 4.63E-04 0.001 

### Compound: Other TCDF Average RunNumber 1 2 3 Mass_mg 0.0000000108 0.0000000069 0.0000000077 0.000 lb/mmBtuO2 2.83E-12 1.71E-12 1.92E-12 0.000 ng/dscm 1.33E-03 7.99E-04 9.14E-04 0.001 ng/dscm@7%O2 3.29E-03 1.98E-03 2.23E-03 0.003 

### Compound: Total Dioxins Average RunNumber 1 2 3 Mass_mg 0.0000000357 0.0000000228 0.0000000223 0.000 lb/mmBtuO2 9.36E-12 5.65E-12 5.56E-12 0.000 ng/dscm 4.39E-03 2.64E-03 2.65E-03 0.003 ng/dscm@7%O2 1.09E-02 6.55E-03 6.46E-03 0.008 

### Compound: Total Furans Average RunNumber 1 2 3


### Tuesday, February 22, 2011 Page 18 of 45

### PSEG Sewaren Unit 4
9/3/2010 Mass_mg 0.0000000221 0.0000000172 0.000000018 0.000 lb/mmBtuO2 5.80E-12 4.26E-12 4.49E-12 0.000 ng/dscm 2.72E-03 1.99E-03 2.14E-03 0.002 ng/dscm@7%O2 6.72E-03 4.93E-03 5.21E-03 0.006



### Location: Stack Exit - Method 25A 

### Compound: Total organic compounds (TOC) as Average Run 1-1 1-2 1-3 Elb/hr 9.43E-02 0.00E+00 0.00E+00 0.031 gr/dscf 4.79E-05 0.00E+00 0.00E+00 0.000 lb/mmBtuO2 2.32E-04 0.00E+00 0.00E+00 0.000 mg/dscm 1.10E-01 0.00E+00 0.00E+00 0.037 ppm 5.98E-02 0.00E+00 0.00E+00 0.020 ppm@7%O2 1.46E-01 0.00E+00 0.00E+00 0.049



### Location: Stack Exit - Method 26A Compound: Hydrogen Chloride Average RunNumber 3 1 2 Mass_mg 0.45 0.4 0.47 0.440 Elb/hr 3.62E-01 3.20E-01 3.89E-01 0.357 lb/mmBtuO2 9.25E-04 8.33E-04 9.33E-04 0.001 mg/dscm 4.40E-01 3.84E-01 4.39E-01 0.421 mg/dscm@7%O2 1.07E+00 9.65E-01 1.08E+00 1.038 

### Compound: Hydrogen Fluoride Average RunNumber 3 1 2 Mass_mg 0.11 0.11 0.11 0.110 Elb/hr 8.85E-02 8.79E-02 9.10E-02 0.089 lb/mmBtuO2 2.26E-04 2.29E-04 2.18E-04 0.000 mg/dscm 1.08E-01 1.06E-01 1.03E-01 0.106 mg/dscm@7%O2 2.63E-01 2.66E-01 2.54E-01 0.261



### Location: Stack Exit - Method 29 Compound: Antimony Average RunNumber 3 2 4 Mass_mg 0.30723 0.3012 0.3152 0.308 Elb/hr 5.79E-02 5.67E-02 5.97E-02 0.058 lb/mmBtuO2 7.25E-05 7.17E-05 7.34E-05 0.000 mg/dscm 4.96E-02 4.85E-02 5.14E-02 0.050 mg/dscm@7%O2 8.41E-02 8.32E-02 8.51E-02 0.084 

### Compound: Arsenic Average RunNumber 3 2 4 Mass_mg 0.008 0.00828 0.00844 0.008 Elb/hr 1.51E-03 1.56E-03 1.60E-03 0.002 lb/mmBtuO2 1.89E-06 1.97E-06 1.97E-06 0.000 mg/dscm 1.29E-03 1.33E-03 1.38E-03 0.001



### Tuesday, February 22, 2011 Page 19 of 45

### PSEG Sewaren Unit 4
9/3/2010 mg/dscm@7%O2 2.19E-03 2.28E-03 2.28E-03 0.002 

### Compound: Beryllium Average RunNumber 3 2 4 Mass_mg 0.0021 0.00196 0.00209 0.002 Elb/hr 3.96E-04 3.69E-04 3.96E-04 0.000 lb/mmBtuO2 4.95E-07 4.67E-07 4.87E-07 0.000 mg/dscm 3.39E-04 3.15E-04 3.41E-04 0.000 mg/dscm@7%O2 5.75E-04 5.41E-04 5.64E-04 0.001 

### Compound: Cadmium Average RunNumber 3 2 4 Mass_mg 0.000324 0.000324 0.000306 0.000 Elb/hr 6.10E-05 6.10E-05 5.80E-05 0.000 lb/mmBtuO2 7.64E-08 7.71E-08 7.13E-08 0.000 mg/dscm 5.23E-05 5.21E-05 4.99E-05 0.000 mg/dscm@7%O2 8.87E-05 8.94E-05 8.26E-05 0.000 

### Compound: Chromium Average RunNumber 3 4 2 Mass_mg 0.00543 0.00571 0.00762 0.006 Elb/hr 1.02E-03 1.08E-03 1.43E-03 0.001 lb/mmBtuO2 1.28E-06 1.33E-06 1.81E-06 0.000 mg/dscm 8.76E-04 9.32E-04 1.23E-03 0.001 mg/dscm@7%O2 1.48E-03 1.54E-03 2.11E-03 0.002 

### Compound: Cobalt Average RunNumber 3 2 4 Mass_mg 0.1510825 0.15506 0.15705 0.154 Elb/hr 2.85E-02 2.92E-02 2.98E-02 0.029 lb/mmBtuO2 3.56E-05 3.69E-05 3.66E-05 0.000 mg/dscm 2.44E-02 2.49E-02 2.56E-02 0.025 mg/dscm@7%O2 4.14E-02 4.27E-02 4.24E-02 0.042 

### Compound: Filterable Particulate Average RunNumber 3 2 4 Mass_mg 44.1 46.3 58.6 49.667 Elb/hr 8.31E+00 8.71E+00 1.11E+01 9.373 lb/mmBtuO2 1.04E-02 1.10E-02 1.36E-02 0.012 mg/dscm 7.12E+00 7.45E+00 9.56E+00 8.043 mg/dscm@7%O2 1.21E+01 1.28E+01 1.58E+01 13.567 

### Compound: Lead Average RunNumber 3 4 2 Mass_mg 0.02327 0.02413 0.02412 0.024 Elb/hr 4.38E-03 4.57E-03 4.54E-03 0.004 lb/mmBtuO2 5.49E-06 5.62E-06 5.74E-06 0.000 mg/dscm 3.75E-03 3.94E-03 3.88E-03 0.004


### Tuesday, February 22, 2011 Page 20 of 45

### PSEG Sewaren Unit 4
9/3/2010 mg/dscm@7%O2 6.36E-03 6.52E-03 6.66E-03 0.007 

### Compound: Manganese Average RunNumber 3 4 2 Mass_mg 0.2554 0.2636 0.2617 0.260 Elb/hr 4.81E-02 5.00E-02 4.93E-02 0.049 lb/mmBtuO2 6.03E-05 6.14E-05 6.23E-05 0.000 mg/dscm 4.12E-02 4.30E-02 4.21E-02 0.042 mg/dscm@7%O2 6.98E-02 7.12E-02 7.22E-02 0.071 

### Compound: Nickel Average RunNumber 3 4 2 Mass_mg 2.5917 2.6743 2.6611175 2.642 Elb/hr 4.88E-01 5.07E-01 5.01E-01 0.499 lb/mmBtuO2 6.11E-04 6.23E-04 6.34E-04 0.001 mg/dscm 4.18E-01 4.36E-01 4.28E-01 0.427 mg/dscm@7%O2 7.09E-01 7.21E-01 7.34E-01 0.721 

### Compound: Selenium Average RunNumber 3 4 2 Mass_mg 0.0039 0.0047 0.0045 0.004 Elb/hr 7.35E-04 8.91E-04 8.47E-04 0.001 lb/mmBtuO2 9.20E-07 1.09E-06 1.07E-06 0.000 mg/dscm 6.29E-04 7.67E-04 7.24E-04 0.001 mg/dscm@7%O2 1.07E-03 1.27E-03 1.24E-03 0.001



### Location: Stack Exit - Method 6C Compound: Sulfur Dioxide Average Run 1-1 1-2 1-3 Elb/hr 1.16E+02 1.12E+02 1.15E+02 114.333 lb/mmBtuO2 2.90E-01 2.91E-01 2.88E-01 0.290 mg/dscm 1.37E+02 1.38E+02 1.36E+02 137.000 mg/dscm@7%O2 3.35E+02 3.39E+02 3.34E+02 336.000 ppm 5.16E+01 5.17E+01 5.11E+01 51.467 ppm@7%O2 1.26E+02 1.27E+02 1.25E+02 126.000



### Location: Stack Exit - Method 6C 3 Compound: Sulfur Dioxide Average Run 3-1 3-2 3-3 Elb/hr 1.06E+02 1.18E+02 1.12E+02 112.000 lb/mmBtuO2 2.77E-01 2.83E-01 2.86E-01 0.282 mg/dscm 1.28E+02 1.33E+02 1.36E+02 132.333 mg/dscm@7%O2 3.22E+02 3.28E+02 3.31E+02 327.000 ppm 4.80E+01 4.99E+01 5.12E+01 49.700 ppm@7%O2 1.21E+02 1.23E+02 1.25E+02 123.000



### Location: Stack Exit - Method 7E



### Tuesday, February 22, 2011 Page 21 of 45

### PSEG Sewaren Unit 4
9/3/2010

Process Run Data Compound: Nitrogen oxides (NOx) Average Run 3-1 3-2 3-3 Elb/hr 7.90E+01 8.65E+01 8.04E+01 81.967 lb/mmBtuO2 2.08E-01 2.12E-01 2.06E-01 0.209 mg/dscm 9.59E+01 1.00E+02 9.82E+01 98.033 mg/dscm@7%O2 2.41E+02 2.46E+02 2.39E+02 242.000 ppm 5.02E+01 5.23E+01 5.14E+01 51.300 ppm@7%O2 1.26E+02 1.29E+02 1.25E+02 126.667



### Location: Stack Exit - OTM - 27/28 Compound: Filterable Particulate Average RunNumber 3 2 4 Mass_mg 37.5 35.6 38.5 37.200 lb/mmBtuO2 1.60E-02 1.50E-02 1.57E-02 0.016 

### Compound: Filterable PM2.5 Average RunNumber 3 2 4 Mass_mg 35.2 31.4 35 33.867 lb/mmBtuO2 1.50E-02 1.32E-02 1.43E-02 0.014 

### Compound: Inorganic (Aqueous) Condensible Pa Average RunNumber 3 2 4 Mass_mg 2.4 1.5 3.4 2.433 lb/mmBtuO2 1.02E-03 6.31E-04 1.39E-03 0.001 

### Compound: Organic Condensible Particulate Average RunNumber 3 2 4 Mass_mg 0.9 1.5 0.8 1.067 lb/mmBtuO2 3.84E-04 6.31E-04 3.27E-04 0.000 

### Compound: Total Particulate Average RunNumber 3 2 4 Mass_mg 40.8 38.6 42.7 40.700 lb/mmBtuO2 1.74E-02 1.62E-02 1.75E-02 0.017 

### Compound: Total PM2.5 Average RunNumber 3 2 4 Mass_mg 38.5 34.4 39.2 37.367 lb/mmBtuO2 1.64E-02 1.45E-02 1.60E-02 0.016



### Tuesday, February 22, 2011 Page 22 of 45

### PSEG Sewaren Unit 4
9/3/2010 Process Run Data



### Run Name Value UOM Comments Target Value 1 Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 1 M0010 Start 6/4/2010 7:06 End 6/4/2010 9:22 0



### 1 Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 1 M0010 Start 6/4/2010 7:06 End 6/4/2010 9:22 0

1 Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 1 M0010 Start 6/4/2010 7:06 End 6/4/2010 9:22 0

2 Fuel Oil Firing Rate 2562 gal/hr SEW4 Group 1 Run 2 M25A (TOC as propane) Start 6/4/2010 10:10 End 6/4/2010 12:14 0

2 Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 2 M25A (TOC as propane) Start 6/4/2010 10:10 End 6/4/2010 12:14 0



### 2 Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 2 M25A (TOC as propane) Start 6/4/2010 10:10 End 6/4/2010 12:14SEW4 Group 1 Run 2 M25A (TOC as propane) Start 6/4/2010 10:10 End 6/4/2010 12:14 0

3 Fuel Oil Firing Rate 2542 gal/hr SEW4 Group 2 Run 2 M23 Start 6/2/2010 23:16 End 6/3/2010 7:40 0

3 Unit Gross Electrical Output 30 Mwe SEW4 Group 2 Run 2 M23 Start 6/2/2010 23:16 End 6/3/2010 7:40 0

Tuesday, February 22, 2011 Page 23 of 45

### PSEG Sewaren Unit 4
9/3/2010 3 Unit Net Electric Generation 28 MWh SEW4 Group 2 Run 2 M23 Start 6/2/2010 23:16 End 6/3/2010 7:40 0

4 Fuel Oil Firing Rate 4980 gal/hr SEW4 Group 4 Run 2 M29 Start 6/2/2010 9:25 End 6/2/2010 15:19 0

4 Unit Gross Electrical Output 71 Mwe SEW4 Group 4 Run 2 M29 Start 6/2/2010 9:25 End 6/2/2010 15:19 0

4 Unit Net Electric Generation 67 MWh SEW4 Group 4 Run 2 M29 Start 6/2/2010 9:25 End 6/2/2010 15:19 0

5 Fuel Oil Firing Rate 4978 gal/hr SEW4 Group 4 Run 3 OTM027/028 Start 6/2/2010 16:10 End 6/2/2010 22:04 0



### 5 Unit Gross Electrical Output 71 Mwe SEW4 Group 4 Run 3 OTM027/028 Start 6/2/2010 16:10 End 6/2/2010 22:04 0

5 Unit Net Electric Generation 67 MWh SEW4 Group 4 Run 3 OTM027/028 Start 6/2/2010 16:10 End 6/2/2010 22:04 0



### 6 Fuel Oil Firing Rate 4978 gal/hr SEW4 Group 4 Run 3 M30B Start 6/2/2010 15:49 End 6/2/2010 21:49 0

6 Unit Gross Electrical Output 71 Mwe SEW4 Group 4 Run 3 M30B Start 6/2/2010 15:49 End 6/2/2010 21:49 0

6 Unit Net Electric Generation 67 MWh SEW4 Group 4 Run 3 M30B Start 6/2/2010 15:49 End 6/2/2010 21:49 0



### Tuesday, February 22, 2011 Page 24 of 45

### PSEG Sewaren Unit 4
9/3/2010
7 Fuel Oil Firing Rate 5056 gal/hr SEW4 Group 4 Run 4 M29 Start 6/3/2010 9:00 End 6/3/2010 14:49 0

7 Unit Gross Electrical Output 71 Mwe SEW4 Group 4 Run 4 M29 Start 6/3/2010 9:00 End 6/3/2010 14:49 0

7 Unit Net Electric Generation 67 MWh SEW4 Group 4 Run 4 M29 Start 6/3/2010 9:00 End 6/3/2010 14:49 0

8 Fuel Oil Firing Rate 5056 gal/hr SEW4 Group 4 Run 4 OTM027/028 Start 6/3/2010 9:00 End 6/3/2010 14:40 0

8 Unit Gross Electrical Output 71 Mwe SEW4 Group 4 Run 4 OTM027/028 Start 6/3/2010 9:00 End 6/3/2010 14:40 0



### 8 Unit Net Electric Generation 67 MWh SEW4 Group 4 Run 4 OTM027/028 Start 6/3/2010 9:00 End 6/3/2010 14:40 0

9 Fuel Oil Firing Rate 5055 gal/hr SEW4 Group 4 Run 4 M30B Start 6/3/2010 8:58 End 6/3/2010 14:58 0

9 Unit Gross Electrical Output 71 Mwe SEW4 Group 4 Run 4 M30B Start 6/3/2010 8:58 End 6/3/2010 14:58 0

9 Unit Net Electric Generation 67 MWh SEW4 Group 4 Run 4 M30B Start 6/3/2010 8:58 End 6/3/2010 14:58 0

10Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 1 M0011 Start 6/4/2010 7:06 End 6/4/2010 9:22 0

10Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 1 M0011 Start 6/4/2010 7:06 End 6/4/2010 9:22 0



### Tuesday, February 22, 2011 Page 25 of 45

### PSEG Sewaren Unit 4
9/3/2010 10Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 1 M0011 Start 6/4/2010 7:06 End 6/4/2010 9:22 0



### 11Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Runs 1-4 M0031 Start 6/4/2010 7:10 End 6/4/2010 9:17 0

11Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Runs 1-4 M0031 Start 6/4/2010 7:10 End 6/4/2010 9:17 0

11Unit Net Electric Generation 28 MWh SEW4 Group 1 Runs 1-4 M0031 Start 6/4/2010 7:10 End 6/4/2010 9:17 0

12Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 1 M6C (SO2) Start 6/4/2010 7:15 End 6/4/2010 9:19 0

12Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 1 M6C (SO2) Start 6/4/2010 7:15 End 6/4/2010 9:19 0



### 12Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 1 M6C (SO2) Start 6/4/2010 7:15 End 6/4/2010 9:19 0

13Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 1 M10 (CO) Start 6/4/2010 7:15 End 6/4/2010 9:19 0

13Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 1 M10 (CO) Start 6/4/2010 7:15 End 6/4/2010 9:19 0

13Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 1 M10 (CO) Start 6/4/2010 7:15 End 6/4/2010 9:19 0



### Tuesday, February 22, 2011 Page 26 of 45

### PSEG Sewaren Unit 4
9/3/2010 14Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 1 M25A (TOC as propane) Start 6/4/2010 7:15 End 6/4/2010 9:19 0



### 14Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 1 M25A (TOC as propane) Start 6/4/2010 7:15 End 6/4/2010 9:19 0

14Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 1 M25A (TOC as propane) Start 6/4/2010 7:15 End 6/4/2010 9:19 0



### 15Fuel Oil Firing Rate 2562 gal/hr SEW4 Group 1 Run 2 M0010 Start 6/4/2010 10:08 End 6/4/2010 12:22 0

15Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 2 M0010 Start 6/4/2010 10:08 End 6/4/2010 12:22 0

15Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 2 M0010 Start 6/4/2010 10:08 End 6/4/2010 12:22 0

16Fuel Oil Firing Rate 2562 gal/hr SEW4 Group 1 Run 2 M0011 Start 6/4/2010 10:08 End 6/4/2010 12:22 0

16Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 2 M0011 Start 6/4/2010 10:08 End 6/4/2010 12:22 0



### 16Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 2 M0011 Start 6/4/2010 10:08 End 6/4/2010 12:22 0

Tuesday, February 22, 2011 Page 27 of 45

### PSEG Sewaren Unit 4
9/3/2010 17Fuel Oil Firing Rate 2562 gal/hr SEW4 Group 1 Runs 5-8 M0031 Start 6/4/2010 10:09 End 6/4/2010 12:17 0



### 17Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Runs 5-8 M0031 Start 6/4/2010 10:09 End 6/4/2010 12:17 0

17Unit Net Electric Generation 28 MWh SEW4 Group 1 Runs 5-8 M0031 Start 6/4/2010 10:09 End 6/4/2010 12:17 0

18Fuel Oil Firing Rate 2562 gal/hr SEW4 Group 1 Run 2 M6C (SO2) Start 6/4/2010 10:10 End 6/4/2010 12:14 0

18Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 2 M6C (SO2) Start 6/4/2010 10:10 End 6/4/2010 12:14 0

18Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 2 M6C (SO2) Start 6/4/2010 10:10 End 6/4/2010 12:14 0



### 19Fuel Oil Firing Rate 2562 gal/hr SEW4 Group 1 Run 2 M10 (CO) Start 6/4/2010 10:10 End 6/4/2010 12:14 0

19Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 2 M10 (CO) Start 6/4/2010 10:10 End 6/4/2010 12:14 0

19Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 2 M10 (CO) Start 6/4/2010 10:10 End 6/4/2010 12:14 0

20Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 3 M0010 Start 6/4/2010 13:18 End 6/4/2010 15:31 0



### Tuesday, February 22, 2011 Page 28 of 45

### PSEG Sewaren Unit 4
9/3/2010 20Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 3 M0010 Start 6/4/2010 13:18 End 6/4/2010 15:31 0



### 20Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 3 M0010 Start 6/4/2010 13:18 End 6/4/2010 15:31 0

21Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 3 M0011 Start 6/4/2010 13:18 End 6/4/2010 15:31 0

21Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 3 M0011 Start 6/4/2010 13:18 End 6/4/2010 15:31 0

21Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 3 M0011 Start 6/4/2010 13:18 End 6/4/2010 15:31 0

22Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Runs 9-12 M0031 Start 6/4/2010 13:10 End 6/4/2010 15:31 0



### 22Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Runs 9-12 M0031 Start 6/4/2010 13:10 End 6/4/2010 15:31 0

22Unit Net Electric Generation 28 MWh SEW4 Group 1 Runs 9-12 M0031 Start 6/4/2010 13:10 End 6/4/2010 15:31 0

23Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 3 M6C (SO2) Start 6/4/2010 13:19 End 6/4/2010 15:23 0

23Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 3 M6C (SO2) Start 6/4/2010 13:19 End 6/4/2010 15:23 0



### Tuesday, February 22, 2011 Page 29 of 45

### PSEG Sewaren Unit 4
9/3/2010 23Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 3 M6C (SO2) Start 6/4/2010 13:19 End 6/4/2010 15:23 0



### 24Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 3 M10 (CO) Start 6/4/2010 13:19 End 6/4/2010 15:23 0

24Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 3 M10 (CO) Start 6/4/2010 13:19 End 6/4/2010 15:23 0

24Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 3 M10 (CO) Start 6/4/2010 13:19 End 6/4/2010 15:23 0

25Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 3 M25A (TOC as propane) Start 6/4/2010 13:19 End 6/4/2010 15:23 0



### 25Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 3 M25A (TOC as propane) Start 6/4/2010 13:19 End 6/4/2010 15:23 0

25Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 3 M25A (TOC as propane) Start 6/4/2010 13:19 End 6/4/2010 15:23 0

26Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 1 M18 (CH4) Start 6/4/2010 16:26 End 6/4/2010 16:30 0



### 26Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 1 M18 (CH4) Start 6/4/2010 16:26 End 6/4/2010 16:30 0

Tuesday, February 22, 2011 Page 30 of 45

### PSEG Sewaren Unit 4
9/3/2010 26Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 1 M18 (CH4) Start 6/4/2010 16:26 End 6/4/2010 16:30 0



### 27Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 2 M18 (CH4) Start 6/4/2010 16:33 End 6/4/2010 16:36 0

27Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 2 M18 (CH4) Start 6/4/2010 16:33 End 6/4/2010 16:36 0

27Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 2 M18 (CH4) Start 6/4/2010 16:33 End 6/4/2010 16:36 0

28Fuel Oil Firing Rate 2561 gal/hr SEW4 Group 1 Run 3 M18 (CH4) Start 6/4/2010 16:39 End 6/4/2010 16:43 0

28Unit Gross Electrical Output 30 Mwe SEW4 Group 1 Run 3 M18 (CH4) Start 6/4/2010 16:39 End 6/4/2010 16:43 0



### 28Unit Net Electric Generation 28 MWh SEW4 Group 1 Run 3 M18 (CH4) Start 6/4/2010 16:39 End 6/4/2010 16:43 0

29Fuel Oil Firing Rate 2564 gal/hr SEW4 Group 2 Run 1 M23 Start 6/1/2010 21:45 End 6/2/2010 6:00 0

29Unit Gross Electrical Output 30 Mwe SEW4 Group 2 Run 1 M23 Start 6/1/2010 21:45 End 6/2/2010 6:00 0

29Unit Net Electric Generation 28 MWh SEW4 Group 2 Run 1 M23 Start 6/1/2010 21:45 End 6/2/2010 6:00 0

30Fuel Oil Firing Rate 2552 gal/hr SEW4 Group 2 Run 3 M23 Start 6/3/2010 18:12 End 6/4/2010 2:27 0

Tuesday, February 22, 2011 Page 31 of 45

### PSEG Sewaren Unit 4
9/3/2010 30Unit Gross Electrical Output 30 Mwe SEW4 Group 2 Run 3 M23 Start 6/3/2010 18:12 End 6/4/2010 2:27 0

30Unit Net Electric Generation 28 MWh SEW4 Group 2 Run 3 M23 Start 6/3/2010 18:12 End 6/4/2010 2:27 0

31Fuel Oil Firing Rate 2564 gal/hr SEW4 Group 3 Run 1 M26A Start 6/1/2010 9:12 End 6/1/2010 10:34 0

31Unit Gross Electrical Output 30 Mwe SEW4 Group 3 Run 1 M26A Start 6/1/2010 9:12 End 6/1/2010 10:34 0

31Unit Net Electric Generation 28 MWh SEW4 Group 3 Run 1 M26A Start 6/1/2010 9:12 End 6/1/2010 10:34 0

32Fuel Oil Firing Rate 2564 gal/hr SEW4 Group 3 Run 1 M6C (SO2) Start 6/1/2010 9:14 End 6/1/2010 10:20 0

32Unit Gross Electrical Output 30 Mwe SEW4 Group 3 Run 1 M6C (SO2) Start 6/1/2010 9:14 End 6/1/2010 10:20 0



### 32Unit Net Electric Generation 28 MWh SEW4 Group 3 Run 1 M6C (SO2) Start 6/1/2010 9:14 End 6/1/2010 10:20 0

33Fuel Oil Firing Rate 2564 gal/hr SEW4 Group 3 Run 1 M7E (NOx) Start 6/1/2010 9:14 End 6/1/2010 10:20 0

33Unit Gross Electrical Output 30 Mwe SEW4 Group 3 Run 1 M7E (NOx) Start 6/1/2010 9:14 End 6/1/2010 10:20 0

33Unit Net Electric Generation 28 MWh SEW4 Group 3 Run 1 M7E (NOx) Start 6/1/2010 9:14 End 6/1/2010 10:20 0



### Tuesday, February 22, 2011 Page 32 of 45

### PSEG Sewaren Unit 4
9/3/2010 34Fuel Oil Firing Rate 2563 gal/hr SEW4 Group 3 Run 2 M26A Start 6/1/2010 11:38 End 6/1/2010 12:48 0



### 34Unit Gross Electrical Output 30 Mwe SEW4 Group 3 Run 2 M26A Start 6/1/2010 11:38 End 6/1/2010 12:48 0

34Unit Net Electric Generation 28 MWh SEW4 Group 3 Run 2 M26A Start 6/1/2010 11:38 End 6/1/2010 12:48 0

35Fuel Oil Firing Rate 2563 gal/hr SEW4 Group 3 Run 2 M6C (SO2) Start 6/1/2010 11:40 End 6/1/2010 12:40 0

35Unit Gross Electrical Output 30 Mwe SEW4 Group 3 Run 2 M6C (SO2) Start 6/1/2010 11:40 End 6/1/2010 12:40 0

35Unit Net Electric Generation 28 MWh SEW4 Group 3 Run 2 M6C (SO2) Start 6/1/2010 11:40 End 6/1/2010 12:40 0



### 36Fuel Oil Firing Rate 2563 gal/hr SEW4 Group 3 Run 2 M7E (NOx) Start 6/1/2010 11:40 End 6/1/2010 12:40 0

36Unit Gross Electrical Output 30 Mwe SEW4 Group 3 Run 2 M7E (NOx) Start 6/1/2010 11:40 End 6/1/2010 12:40 0

36Unit Net Electric Generation 28 MWh SEW4 Group 3 Run 2 M7E (NOx) Start 6/1/2010 11:40 End 6/1/2010 12:40 0

37Fuel Oil Firing Rate 2541 gal/hr SEW4 Group 3 Run 3 M26A Start 6/3/2010 15:59 End 6/3/2010 17:09 0



### Tuesday, February 22, 2011 Page 33 of 45

### PSEG Sewaren Unit 4
9/3/2010 37Unit Gross Electrical Output 31 Mwe SEW4 Group 3 Run 3 M26A Start 6/3/2010 15:59 End 6/3/2010 17:09 0



### 37Unit Net Electric Generation 29 MWh SEW4 Group 3 Run 3 M26A Start 6/3/2010 15:59 End 6/3/2010 17:09 0

38Fuel Oil Firing Rate 2541 gal/hr SEW4 Group 3 Run 3 M6C (SO2) Start 6/3/2010 16:01 End 6/3/2010 17:11 0

38Unit Gross Electrical Output 31 Mwe SEW4 Group 3 Run 3 M6C (SO2) Start 6/3/2010 16:01 End 6/3/2010 17:11 0

38Unit Net Electric Generation 29 MWh SEW4 Group 3 Run 3 M6C (SO2) Start 6/3/2010 16:01 End 6/3/2010 17:11 0

39Fuel Oil Firing Rate 2541 gal/hr SEW4 Group 3 Run 3 M7E (NOx) Start 6/3/2010 16:01 End 6/3/2010 17:11 0



### 39Unit Gross Electrical Output 31 Mwe SEW4 Group 3 Run 3 M7E (NOx) Start 6/3/2010 16:01 End 6/3/2010 17:11 0

39Unit Net Electric Generation 29 MWh SEW4 Group 3 Run 3 M7E (NOx) Start 6/3/2010 16:01 End 6/3/2010 17:11 0

40Fuel Oil Firing Rate 4980 gal/hr SEW4 Group 4 Run 2 OTM027/028 Start 6/2/2010 9:25 End 6/2/2010 15:13 0

40Unit Gross Electrical Output 71 Mwe SEW4 Group 4 Run 2 OTM027/028 Start 6/2/2010 9:25 End 6/2/2010 15:13 0



### Tuesday, February 22, 2011 Page 34 of 45

### PSEG Sewaren Unit 4
9/3/2010

APCD Run Data

Process Lab Run Data 40Unit Net Electric Generation 67 MWh SEW4 Group 4 Run 2 OTM027/028 Start 6/2/2010 9:25 End 6/2/2010 15:13 0



### 41Fuel Oil Firing Rate 4980 gal/hr SEW4 Group 4 Run 2 M30B Start 6/2/2010 9:19 End 6/2/2010 15:19 0

41Unit Gross Electrical Output 71 Mwe SEW4 Group 4 Run 2 M30B Start 6/2/2010 9:19 End 6/2/2010 15:19 0

41Unit Net Electric Generation 67 MWh SEW4 Group 4 Run 2 M30B Start 6/2/2010 9:19 End 6/2/2010 15:19 0

42Fuel Oil Firing Rate 4978 gal/hr SEW4 Group 4 Run 3 M29 Start 6/2/2010 16:10 End 6/2/2010 22:02 0



### 42Unit Gross Electrical Output 71 Mwe SEW4 Group 4 Run 3 M29 Start 6/2/2010 16:10 End 6/2/2010 22:02 0

42Unit Net Electric Generation 67 MWh SEW4 Group 4 Run 3 M29 Start 6/2/2010 16:10 End 6/2/2010 22:02 0

1 Heat Input 0 Million Btus/million BTU using O2 0

Run Name Value UOM Comments Target Value 

### 1 No control devices on Sewaren Unit 4 0 0
1 0 0
1 0 0

Run Name ValueUOM Comments 

### 1 Fuel Higher Heating Value 0 Btu/lb 1 Fuel Moisture 0 % 1 Fuel Mercury Content 0 ppm



### Tuesday, February 22, 2011 Page 35 of 45

### PSEG Sewaren Unit 4
9/3/2010 1 Fuel Cadmium Content 0 ppm 

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

### 1 Fuel Beryllium Content 0 ppm 1 Fuel Lead Content 0 ppm 1 Fuel Manganese Content 0 ppm 

### 1 Fuel Chlorine Content 0 ppm 1 Fuel Fluorine Content 0 ppm

Tuesday, February 22, 2011 Page 36 of 45

### PSEG Sewaren Unit 4
9/3/2010 Sampling / Stack Data Results Detail



### LocationStack Exit - Method 0011 Average Run Number 1 2 3 Test Date 6/4/2010 6/4/2010 6/4/2010 Run Start Time 7:06:00 AM10:08:00 AM 1:18:00 PM Run Finish Time 9:22:00 AM12:22:00 PM 3:31:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 120 120 120 Nozzle Diameter, inches 0.282 0.282 0.282 0.282 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9845 0.9845 0.9845 0.985 Barometric Pressure, inches of Mercury 29.71 29.72 29.7 29.710 Average Orifice Meter Differential, inches H2O 1.29 1.23 1.34 1.287 Dry Gas Meter Volume Sampled, cubic feet 75.652 75.019 78.925 76.532 Average Dry Gas Meter Temperature, °F 82.98 88.27 91.85 87.700 Dry Gas Meter Volume Sampled, dscf 72.146 70.865 74.042 72.351 Total Moisture Liquid collected, g 87.8 87.1 96.6 90.500 Volume of Water Vapor, standard cubic feet 4.13 4.10 4.55 4.260 Moisture Content of Stack Gas, % 5.41 5.47 5.79 5.557 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9459 0.9453 0.9421 0.944 Carbon Dioxide, % 4.344 4.318 4.305 4.322 Oxygen, % 15.222 15.234 15.237 15.231 Carbon Monoxide & Nitrogen, % 80.434 80.448 80.458 80.447 Fuel Factor 1.31 1.31 1.32 Dry Molecular Weight, lb/lb-Mole 29.30 29.30 29.30 29.300 Wet Molecular weight, lb/lb-Mole 28.69 28.68 28.65 28.673 Flue Gas Static Pressure, inches of H2O -0.18 -0.18 -0.18 -0.180 Absolute Flue Gas Pressure, inches of Mercury 29.70 29.71 29.69 29.700 Average Stack Gas Temperature, °F 214.33 219.04 222.92 218.763 Average Velocity Head, inches of H2O 0.2596215632 995660.246412717

4884210.267932805

226047 0.258
Average Stack Gas Velocity, feet/second 32.55 31.82 33.31 32.560 Stack Cross-Sectional Area, square feet 159.812 159.812 159.812 159.812 Dry Volumetric Flow Rate, dry scfm 229,463.3 222,694.8 230,858.0227,672.033 Actual Wet Volumetric Flue Gas Flow Rate, acfm 312,112.8 305,113.1 319,400.3312,208.733 Percent Isokinetic of Sampling Rate, % 96.5 97.7 98.5 97.567 Percent Excess Air, % 253.2 253.7 253.8 253.567 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 14.263 14.263 14.263 Rectangular Duct Width, inches 151.7 151.7 151.7 Rectangular Duct Length, inches 151.7 151.7 151.7 Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 37 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 10 Average Run Number 1-1 1-2 1-3 Test Date 6/4/2010 6/4/2010 6/4/2010 Run Start Time 7:15:00 AM10:10:00 AM 1:19:00 PM Run Finish Time 9:19:00 AM12:14:00 PM 3:23:00 PM Carbon Dioxide, % 4.344 4.318 4.305 4.322 Oxygen, % 15.222 15.234 15.237 15.231 Fuel Factor 1.31 1.31 1.32 Dry Volumetric Flow Rate, dry scfm 229604.2 222554.8 230858227,672.333 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 5.41 5.47 5.79 5.557 Analyzer Make Thermo Scientific Thermo

Scientific Thermo

Scientific Analyzer Model 48i 48i 48i Analyzer Serial Number CMO0846005 2CMO846005

2CMO846005

2 Operating Range 100.1 100.1 100.1 100.100 Operating Units ppm ppm ppm No. Readings/Avg. 120 120 120 120.000 Calibration Set 111 111 111 111.000 Calibration Pre Zero Cylinder ID Nitrogen-CONitrogen-CONitrogen-CO Calibration Pre Zero Cylinder Instrument Response 0.512 0.341 0.097 0.317 Calibration Pre Zero Cylinder Bias 0.54 0.36 0.12 0.340 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID ALM055217- CO-MidALM055217

-CO-MidALM055217-

CO-Mid Calibration Pre High Cylinder Instrument Response 51.147 50.83 50.195 50.724 Calibration Pre High Cylinder Bias -0.02 -0.34 -0.98 -0.447 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Nitrogen-CONitrogen-CONitrogen-CO Calibration Post Zero Cylinder Instrument Response 0.341 0.097 0.195 0.211 Calibration Post Zero Cylinder Bias 0.36 0.12 0.22 0.233 Calibration Post Zero Cylinder Drift 0.18 0.24 0.1 0.173 Calibration Post High Cylinder ID ALM055217- CO-MidALM055217

-CO-MidALM055217-

CO-Mid Calibration Post High Cylinder Instrument Response 50.83 50.195 50.585 50.537 Calibration Post High Cylinder Bias -0.34 -0.98 -0.59 -0.637 Calibration Post High Cylinder Drift 0.32 0.64 0.39 0.450 Cavg 0.011 -0.074 -0.128 -0.064 Cavg Units ppmvd ppmvd ppmvd Cgas -0.4183 0 0 -0.139 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 22, 2011 Page 38 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 23 Average Run Number 1 2 3 Test Date 6/1/2010 6/2/2010 6/3/2010 Run Start Time 6:00:00 AM7:40:00 AM 2:27:00 AM Run Finish Time 9:45:00 PM11:16:00 PM 6:12:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 480 480 480 Nozzle Diameter, inches 0.282 0.282 0.283 0.282 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9882 0.9882 0.9982 0.992 Barometric Pressure, inches of Mercury 29.56 29.64 29.56 29.587 Average Orifice Meter Differential, inches H2O 1.16 1.31 1.27 1.247 Dry Gas Meter Volume Sampled, cubic feet 301.914 318.941 317.552 312.802 Average Dry Gas Meter Temperature, °F 83.67 82.17 97.38 87.740 Dry Gas Meter Volume Sampled, dscf 287.092 305.056 297.596 296.581 Total Moisture Liquid collected, g 345.4 356.7 331.8 344.633 Volume of Water Vapor, standard cubic feet 16.26 16.79 15.62 16.223 Moisture Content of Stack Gas, % 5.36 5.22 4.99 5.190 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9464 0.9478 0.9501 0.948 Carbon Dioxide, % 4.225 4.249 4.276 4.250 Oxygen, % 15.277 15.294 15.195 15.255 Carbon Monoxide & Nitrogen, % 80.498 80.457 80.529 80.495 Fuel Factor 1.33 1.32 1.33 Dry Molecular Weight, lb/lb-Mole 29.29 29.29 29.29 29.290 Wet Molecular weight, lb/lb-Mole 28.68 28.70 28.73 28.703 Flue Gas Static Pressure, inches of H2O -0.18 -0.26 -0.18 -0.207 Absolute Flue Gas Pressure, inches of Mercury 29.55 29.62 29.55 29.573 Average Stack Gas Temperature, °F 213.63 217.63 303.25 244.837 Average Velocity Head, inches of H2O 0.2452290255 679980.273827716

6463960.264511847

603664 0.261
Average Stack Gas Velocity, feet/second 31.70 33.55 35.02 33.423 Stack Cross-Sectional Area, square feet 159.812 159.812 159.812 159.812 Dry Volumetric Flow Rate, dry scfm 222,691.2 235,198.5 217,976.2225,288.633 Actual Wet Volumetric Flue Gas Flow Rate, acfm 303,962.4 321,701.6 335,797.0320,487.000 Percent Isokinetic of Sampling Rate, % 99.0 99.6 104.1 100.900 Percent Excess Air, % 255.7 257.2 250.6 254.500 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 14.263 14.263 14.263 Rectangular Duct Width, inches 151.7 151.7 151.7 Rectangular Duct Length, inches 151.7 151.7 151.7 Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 39 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 25A Average Run Number 1-1 1-2 1-3 Test Date 6/4/2010 6/4/2010 6/4/2010 Run Start Time 7:15:00 AM10:10:00 AM 1:19:00 PM Run Finish Time 9:19:00 AM12:14:00 PM 3:23:00 PM Carbon Dioxide, % 4.344 4.318 4.305 4.322 Oxygen, % 15.222 15.234 15.237 15.231 Fuel Factor 1.31 1.31 1.32 Dry Volumetric Flow Rate, dry scfm 229604.2 222554.8 230858227,672.333 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 5.41 5.47 5.79 5.557 Analyzer Make Thermo Electron Thermo

Electron Thermo

Electron Analyzer Model 51C 51C 51C Analyzer Serial Number 032720220303272022030327202203327,202,203 .000 Operating Range 10 10 10 10.000 Operating Units ppm ppm ppm No. Readings/Avg. 120 120 120 120.000 Calibration Set 252 252 252 252.000 Calibration Pre Zero Cylinder ID NitrogenC3H8 NitrogenC3H8 NitrogenC3H8 Calibration Pre Zero Cylinder Instrument Response -0.046 0.026 -0.124 -0.048 Calibration Pre Zero Cylinder Bias -0.12 0.6 -0.9 -0.140 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID ZZZ00000- THC-LowZZZ00000-

THC-Low ZZZ00000-

THC-Low Calibration Pre High Cylinder Instrument Response 2.888 2.807 2.939 2.878 Calibration Pre High Cylinder Bias 0.3 -0.51 0.81 0.200 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID NitrogenC3H8 NitrogenC3H8 NitrogenC3H8 Calibration Post Zero Cylinder Instrument Response 0.026 -0.124 0.046 -0.017 Calibration Post Zero Cylinder Bias 0.6 -0.9 0.8 0.167 Calibration Post Zero Cylinder Drift 0.72 1.5 1.7 1.307 Calibration Post High Cylinder ID ZZZ00000- THC-LowZZZ00000-

THC-Low ZZZ00000-

THC-Low Calibration Post High Cylinder Instrument Response 2.807 2.939 2.978 2.908 Calibration Post High Cylinder Bias -0.51 0.81 1.2 0.500 Calibration Post High Cylinder Drift 0.81 1.32 0.39 0.840 Cavg 0.047 -0.952 -0.229 -0.378 Cavg Units ppmvd ppmvd ppmvd Cgas 0.0598 0 0 0.020 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 22, 2011 Page 40 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 26A Average Run Number 1 2 3 Test Date 6/1/2010 6/1/2010 6/3/2010 Run Start Time 9:12:00 AM11:38:00 AM 3:59:00 PM Run Finish Time 10:34:00 AM12:48:00 PM 5:09:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 60 60 60 Nozzle Diameter, inches 0.282 0.282 0.283 0.282 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9882 0.9882 0.9882 0.988 Barometric Pressure, inches of Mercury 29.81 29.66 29.56 29.677 Average Orifice Meter Differential, inches H2O 1.26 1.42 1.23 1.303 Dry Gas Meter Volume Sampled, cubic feet 39.171 40.613 39.058 39.614 Average Dry Gas Meter Temperature, °F 95.54 97.96 99.38 97.627 Dry Gas Meter Volume Sampled, dscf 36.769 37.781 36.104 36.885 Total Moisture Liquid collected, g 65.3 67.2 62.1 64.867 Volume of Water Vapor, standard cubic feet 3.07 3.16 2.92 3.050 Moisture Content of Stack Gas, % 7.71 7.72 7.48 7.637 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9229 0.9228 0.9252 0.924 Carbon Dioxide, % 4.096 4.266 4.346 4.236 Oxygen, % 15.37 15.257 15.192 15.273 Carbon Monoxide & Nitrogen, % 80.534 80.477 80.462 80.491 Fuel Factor 1.35 1.32 1.31 Dry Molecular Weight, lb/lb-Mole 29.27 29.29 29.30 29.287 Wet Molecular weight, lb/lb-Mole 28.40 28.42 28.45 28.423 Flue Gas Static Pressure, inches of H2O -0.18 -0.18 -0.17 -0.177 Absolute Flue Gas Pressure, inches of Mercury 29.80 29.65 29.55 29.667 Average Stack Gas Temperature, °F 229.83 218.21 229.42 225.820 Average Velocity Head, inches of H2O 0.2579668651 455810.288376472

8557860.253085386

527665 0.266
Average Stack Gas Velocity, feet/second 32.93 34.60 32.72 33.417 Stack Cross-Sectional Area, square feet 159.812 159.812 159.812 159.812 Dry Volumetric Flow Rate, dry scfm 222,153.7 236,198.5 219,561.1225,971.100 Actual Wet Volumetric Flue Gas Flow Rate, acfm 315,756.5 331,769.7 313,742.9320,423.033 Percent Isokinetic of Sampling Rate, % 101.6 98.2 100.3 100.033 Percent Excess Air, % 260.9 254.8 251.1 255.600 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 14.263 14.263 14.263 Rectangular Duct Width, inches 151.7 151.7 151.7 Rectangular Duct Length, inches 151.7 151.7 151.7 Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 41 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 29 Average Run Number 2 3 4 Test Date 6/2/2010 6/2/2010 6/3/2010 Run Start Time 9:25:00 AM4:10:00 PM 9:00:00 AM Run Finish Time 3:19:00 PM10:02:00 PM 2:49:00 PM Net Traversing Points 24 24 24 Net Run Time, minutes 336 336 336 Nozzle Diameter, inches 0.248 0.248 0.248 0.248 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9882 0.9882 0.9882 0.988 Barometric Pressure, inches of Mercury 29.74 29.685 29.595 29.673 Average Orifice Meter Differential, inches H2O 1.44 1.42 1.44 1.433 Dry Gas Meter Volume Sampled, cubic feet 234.964 233.282 233.814 234.020 Average Dry Gas Meter Temperature, °F 96.96 93.67 99.50 96.710 Dry Gas Meter Volume Sampled, dscf 219.573 218.882 216.450 218.302 Total Moisture Liquid collected, g 354.4 339.7 353.4 349.167 Volume of Water Vapor, standard cubic feet 16.68 15.99 16.63 16.433 Moisture Content of Stack Gas, % 7.06 6.81 7.13 7.000 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9294 0.9319 0.9287 0.930 Carbon Dioxide, % 6.2 6.2 6.4 6.267 Oxygen, % 12.8 12.7 12.5 12.667 Carbon Monoxide & Nitrogen, % 81 81.1 81.1 81.067 Fuel Factor 1.31 1.32 1.31 Dry Molecular Weight, lb/lb-Mole 29.50 29.50 29.52 29.507 Wet Molecular weight, lb/lb-Mole 28.69 28.72 28.70 28.703 Flue Gas Static Pressure, inches of H2O 0.17 0.17 0.17 0.170 Absolute Flue Gas Pressure, inches of Mercury 29.75 29.70 29.61 29.687 Average Stack Gas Temperature, °F 240.75 242.54 243.63 242.307 Average Velocity Head, inches of H2O 0.5171538774 009680.514597162

2092250.515246218

941005 0.516
Average Stack Gas Velocity, feet/second 46.79 46.75 46.90 46.813 Stack Cross-Sectional Area, square feet 159.812 159.812 159.812 159.812 Dry Volumetric Flow Rate, dry scfm 312,401.1 311,651.5 310,152.5311,401.700 Actual Wet Volumetric Flue Gas Flow Rate, acfm 448,656.2 448,272.7 449,711.0448,879.967 Percent Isokinetic of Sampling Rate, % 99.7 99.6 99.0 99.433 Percent Excess Air, % 149.1 145.8 140.3 145.067 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 14.263 14.263 14.263 Rectangular Duct Width, inches 151.7 151.7 151.7 Rectangular Duct Length, inches 151.7 151.7 151.7 Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 42 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 6C Average Run Number 1-1 1-2 1-3 Test Date 6/4/2010 6/4/2010 6/4/2010 Run Start Time 7:15:00 AM10:10:00 AM 1:19:00 PM Run Finish Time 9:14:00 AM12:14:00 PM 3:23:00 PM Carbon Dioxide, % 4.344 4.318 4.305 4.322 Oxygen, % 15.222 15.234 15.237 15.231 Fuel Factor 1.31 1.31 1.32 Dry Volumetric Flow Rate, dry scfm 224759.9 217795.8 226006.6222,854.100 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 5.41 5.47 5.79 5.557 Analyzer Make Ametek Ametek Ametek Analyzer Model 921 CE 921CE 921CE Analyzer Serial Number AE-921-6434 AE-921- 6434AE-921-6434
Operating Range 205.9 205.9 205.9 205.900 Operating Units ppm ppm ppm No. Readings/Avg. 120 120 120 120.000 Calibration Set 411 411 411 411.000 Calibration Pre Zero Cylinder ID Nitrogen-SO2 NitrogenSO2Nitrogen-SO2
Calibration Pre Zero Cylinder Instrument Response 2.262 2.066 2.164 2.164 Calibration Pre Zero Cylinder Bias 1.34 1.25 1.29 1.293 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID ALM045659- SO2-MidALM045659

-SO2-MidALM045659-

SO2-Mid Calibration Pre High Cylinder Instrument Response 96.027 94.748 96.125 95.633 Calibration Pre High Cylinder Bias -1.72 -2.34 -1.67 -1.910 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Nitrogen-SO2 NitrogenSO2Nitrogen-SO2
Calibration Post Zero Cylinder Instrument Response 2.066 2.164 2.164 2.131 Calibration Post Zero Cylinder Bias 1.25 1.29 1.29 1.277 Calibration Post Zero Cylinder Drift 9.0000000000 0001E-02 0.04 0 0.043
Calibration Post High Cylinder ID ALM045659- SO2-MidALM045659

-SO2-MidALM045659-

SO2-Mid Calibration Post High Cylinder Instrument Response 94.748 96.125 95.928 95.600 Calibration Post High Cylinder Bias -2.34 -1.67 -1.77 -1.927 Calibration Post High Cylinder Drift 0.62 0.67 0.1 0.463 Cavg 50.734 50.834 50.621 50.730 Cavg Units ppmvd ppmvd ppmvd Cgas 51.5796 51.6835 51.1093 51.457 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 22, 2011 Page 43 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 6C 3 Average Run Number 3-1 3-2 3-3 Test Date 6/1/2010 6/1/2010 6/3/2010 Run Start Time 9:14:00 AM11:40:00 AM 4:01:00 PM Run Finish Time 10:20:00 AM12:40:00 PM 5:11:00 PM Carbon Dioxide, % 4.096 4.266 4.346 4.236 Oxygen, % 15.37 15.257 15.192 15.273 Fuel Factor 1.35 1.32 1.31 Dry Volumetric Flow Rate, dry scfm 222153.7 235993.7 219494225,880.467 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 7.71 7.72 7.78 7.737 Analyzer Make Ametek Ametek Ametek Analyzer Model 921CE 921CE 921CE Analyzer Serial Number AE-921-6434 AD-921- 6434AE-921-6434
Operating Range 201 201 412 271.333 Operating Units ppm ppm ppm No. Readings/Avg. 60 60 60 60.000 Calibration Set 3 3 61 22.333 Calibration Pre Zero Cylinder ID Nitrogen-SO2 NitrogenSO2Nitrogen-SO2
Calibration Pre Zero Cylinder Instrument Response -0.097 2.447 1.911 1.420 Calibration Pre Zero Cylinder Bias 0.1 1.37 0.66 0.710 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID ALM000000- SO2-MidALM000000

-SO2-MidALM045659-

SO2-Mid Calibration Pre High Cylinder Instrument Response 93.886 94.963 95.757 94.869 Calibration Pre High Cylinder Bias -2.97 -2.44 -1.17 -2.193 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Nitrogen-SO2 NitrogenSO2Nitrogen-SO2
Calibration Post Zero Cylinder Instrument Response 0.783 3.23 3.319 2.444 Calibration Post Zero Cylinder Bias 0.54 1.76 1 1.100 Calibration Post Zero Cylinder Drift 0.44 0.39 0.34 0.390 Calibration Post High Cylinder ID ALM000000- SO2-MidALM000000

-SO2-MidALM045659-

SO2-Mid Calibration Post High Cylinder Instrument Response 95.844 91.047 97.467 94.786 Calibration Post High Cylinder Bias -2 -4.38 -0.76 -2.380 Calibration Post High Cylinder Drift 0.97 1.94 0.41 1.107 Cavg 45.742 47.872 51.188 48.267 Cavg Units ppmvd ppmvd ppmvd Cgas 48.0301 49.9448 51.1583 49.711 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 22, 2011 Page 44 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - Method 7E Average Run Number 3-1 3-2 3-3 Test Date 6/1/2010 6/1/2010 6/3/2010 Run Start Time 9:14:00 AM11:40:00 AM 4:01:00 PM Run Finish Time 10:20:00 AM12:40:00 PM 5:11:00 PM Carbon Dioxide, % 4.096 4.266 4.346 4.236 Oxygen, % 15.37 15.257 15.192 15.273 Fuel Factor 1.35 1.32 1.31 Dry Volumetric Flow Rate, dry scfm 219995.4 231026.6 218381223,134.333 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Moisture, % 7.71 7.72 7.78 7.737 Analyzer Make ThermoElectro

n Thermo Electron Thermo

Electron Analyzer Model 42CLS 42 CLS 42CLS Analyzer Serial Number 032820242703282024270328202427328,202,427 .000 Operating Range 201 201 198 200.000 Operating Units ppm ppm ppm No. Readings/Avg. 60 60 60 60.000 Calibration Set 41 41 51 44.333 Calibration Pre Zero Cylinder ID Nitrogen-NOx NitrogenNOx NitrogenNOx Calibration Pre Zero Cylinder Instrument Response 0.098 0.294 0.679 0.357 Calibration Pre Zero Cylinder Bias 0 0.1 0.29 0.130 Calibration Pre Zero Cylinder Drift 0 0 0 0.000 Calibration Pre High Cylinder ID AAL021731- NOx-MidAAL021731-

NOx-MidALM045659-

NOx-Mid Calibration Pre High Cylinder Instrument Response 94.611 95.641 92.702 94.318 Calibration Pre High Cylinder Bias -1.42 -0.9 -1.45 -1.257 Calibration Pre High Cylinder Drift 0 0 0 0.000 Calibration Post Zero Cylinder ID Nitrogen-NOx NitrogenNOx NitrogenNOx Calibration Post Zero Cylinder Instrument Response 0.294 0.49 0.679 0.488 Calibration Post Zero Cylinder Bias 0.1 0.2 0.29 0.197 Calibration Post Zero Cylinder Drift 0.1 0.1 0 0.067 Calibration Post High Cylinder ID AAL021731- NOx-MidAAL021731-

NOx-MidALM045659-

NOx-Mid Calibration Post High Cylinder Instrument Response 87.593 96.623 92.653 92.290 Calibration Post High Cylinder Bias -4.91 -0.41 -1.47 -2.263 Calibration Post High Cylinder Drift 2.33 0.49 0.02 0.947 Cavg 45.88 50.541 48.316 48.246 Cavg Units ppmvd ppmvd ppmvd Cgas 50.1536 52.2756 51.366 51.265 Cgas Units ppmvd ppmvd ppmvd Fuel Type Oil Oil Oil Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000 Cgasw 0 0 0 0.000 Cgasw Units



### Tuesday, February 22, 2011 Page 45 of 45

### PSEG Sewaren Unit 4
9/3/2010
Location Stack Exit - OTM - 27/28 Average Run Number 2 3 4 Test Date 6/2/2010 6/2/2010 6/3/2010 Run Start Time 9:25:00 AM4:10:00 PM 9:00:00 AM Run Finish Time 3:13:00 PM10:04:00 PM 2:40:00 PM Net Traversing Points 12 12 12 Net Run Time, minutes 334.39 338.59 324.67 Nozzle Diameter, inches 0.186 0.186 0.186 0.186 Pitot Tube Coefficient 0.84 0.84 0.84 0.840 Dry Gas Meter Calibration Factor 0.9845 0.9845 0.9845 0.985 Barometric Pressure, inches of Mercury 29.74 28.185 29.595 29.173 Average Orifice Meter Differential, inches H2O 0.46 0.48 0.48 0.473 Dry Gas Meter Volume Sampled, cubic feet 131.852 136.902 131.968 133.574 Average Dry Gas Meter Temperature, °F 88.88 95.08 90.96 91.640 Dry Gas Meter Volume Sampled, dscf 124.260 120.922 123.303 122.828 Total Moisture Liquid collected, g 183.9 194.9 205.1 194.633 Volume of Water Vapor, standard cubic feet 8.66 9.17 9.65 9.160 Moisture Content of Stack Gas, % 6.52 7.05 7.26 6.943 Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000 Dry Mole Fraction 0.9348 0.9295 0.9274 0.931 Carbon Dioxide, % 6.2 6.2 6.4 6.267 Oxygen, % 12.8 12.7 12.5 12.667 Carbon Monoxide & Nitrogen, % 81 81.1 81.1 81.067 Fuel Factor 1.31 1.32 1.31 Dry Molecular Weight, lb/lb-Mole 29.50 29.50 29.52 29.507 Wet Molecular weight, lb/lb-Mole 28.75 28.69 28.68 28.707 Flue Gas Static Pressure, inches of H2O 0.17 0.17 0.17 0.170 Absolute Flue Gas Pressure, inches of Mercury 29.75 28.20 29.61 29.187 Average Stack Gas Temperature, °F 233.58 236.67 237.67 235.973 Average Velocity Head, inches of H2O 0.4976509775 034120.510276432

248620.469207798

192785 0.492
Average Stack Gas Velocity, feet/second 45.62 47.60 44.59 45.937 Stack Cross-Sectional Area, square feet 159.812 159.812 159.812 159.812 Dry Volumetric Flow Rate, dry scfm 309,526.2 303,047.9 296,979.1303,184.400 Actual Wet Volumetric Flue Gas Flow Rate, acfm 437,437.4 456,423.1 427,561.0440,473.833 Percent Isokinetic of Sampling Rate, % 101.7 99.8 108.3 103.267 Percent Excess Air, % 149.1 145.8 140.3 145.067 F-Factor, dscfm/MMBtu @ %O2 9190 9190 91909,190.000 Round Duct Diameter, inches 14.263 14.263 14.263 Rectangular Duct Width, inches 151.7 151.7 151.7 Rectangular Duct Length, inches 151.7 151.7 151.7 Fw 10320 10320 1032010,320.000 Fc 1420 1420 1420 1,420.000



### Tuesday, February 22, 2011 Page 46 of 45