Name: Lois Knowlson

Title: Senior Environmental Engineer

Company: PSEG Fossil, LLC

Sign Date: 9/2/2010

Name: Anthony Fortunato

Title: Senior Test Engineer

Company: PSEG Maplewood Testing Services

Sign Date: 9/2/2010

Permitted Facility Representative / Date Testing Company Representative / Date

PSEG Mercer 1 EGU ICR MACT

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 17
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Facility Information:

PSEG Mercer Generating Station

2512 Lamberton Road

Hamilton NJ 08611

Contact: Robert Silakoski

Phone: 609-599-7001

Fax: 609-393-3866

Email: robert.silakoski@pseg.com

Testing Company:

Maplewood Testing Services

200 Boyden Avenue

Maplewood NJ 07040

Contact: Anthony Fortunato

Phone: 973-761-1005

Fax: 973-761-1015

Email: anthony.fortunato2@pseg.com

Air Permit Number:

61057-BOP07004

Permitted Source ID/Name:

U1 Mercer Unit 1

Permitted Maximum Process Rate:

3350 MMBtu per hour or 341 MW

Max. Normal Operation Process Rate:

3350 MMBtu per hour or 341 

Target Process Test Rate

N/A

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

 process flow diagram:

Wet-bottom, faced-fired, pulverized-coal, electric generating unit, utlizing bituminous coal; emissions are controlled 

by activated carbon injection, fabric filter (baghouse), SCR and ESP

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 3402100021 FRS #: 110000582236

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 25 265.9 265.9 25 600 2550 4 24

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Stack Exit % H2O Method 1 - 4 3 180 0

Stack Exit Carbon Monoxide Method 10 3 120 0

Regulation Description Compound Limit Unit

NJAC 7:27-4.2a Total Particulate 335 lb/hr

NJAC 7:27-27.7(a) (Based on annual weighted average of 

all valid stack emission tests performed for four 

consecutive quarters weighted by MW-hr)

Mercury 3 mg/MW-hr

Tuesday, February 22, 2011 Page 2 of 17
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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.

As per ICR, potassium permanganate impingers were not used as Hg was measured using Method 30B.

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

Stack Exit Cobalt Method 29 0

Stack Exit Nickel Method 29 3 240 0

Stack Exit Selenium Method 29 3 240 0

Stack Exit Antimony Method 29 3 240 0

Stack Exit Lead Method 29 3 240 0

Stack Exit Arsenic Method 29 3 240 0

Stack Exit Chromium Method 29 3 240 0

Stack Exit Filterable Particulate Method 29 3 240 0

Stack Exit Cadmium Method 29 3 240 0

Stack Exit Manganese Method 29 3 240 0

Stack Exit Beryllium Method 29 3 240 0

Stack Exit Co2 Method 3A CO2 3 240 0

Stack Exit Co2 Method 3A CO2 3 120 0

Stack Exit O2 Method 3A O2 3 120 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 3 240 0

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

Stack Exit Filterable Particulate Method 5 3 240 0

Filterable Particulate Method 5/OTM-28 3 240 0 Use only for wet 

stacks. Delete 

OTM27/OTM28 test.

Stack Exit

Stack Exit Sulfur Dioxide Method 6C 3 180 0

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

Tuesday, February 22, 2011 Page 3 of 17
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Tuesday, February 22, 2011 Page 4 of 17
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Tuesday, February 22, 2011 Page 5 of 17
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Sampling / Stack Data Results Summary

Location Stack Exit - Method 29 

Average

Run Number 1 3 4

Test Date 2/17/2010 2/18/2010 2/18/2010

Run Start Time 9:15:00 AM 8:17:00 

AM

3:19:00 PM

Run Finish Time 1:32:00 PM 12:23:00 

PM

7:34:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 140.870 139.771 153.403 144.681

Moisture Content of Stack Gas, % 6.96 7.17 7.11 7.080

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

Carbon Dioxide, % 12 11.3 12.1 11.800

Oxygen, % 7.08 8.01 6.86 7.317

Average Stack Gas Temperature, °F 307.88 310.96 314.38 311.073

Dry Volumetric Flow Rate, dry scfm 654,505.1 651,413.9 704,916.0 670,278.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,040,804.8 1,041,688.6 1,130,361.8 1,070,951.73

3

Percent Isokinetic of Sampling Rate, % 98.7 98.4 99.8 98.967

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, February 22, 2011 Page 6 of 17
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Location Stack Exit - OTM - 27/28

Average

Run Number 1 3 4

Test Date 2/17/2010 2/18/2010 2/18/2010

Run Start Time 9:08:00 AM 8:02:00 

AM

3:13:00 PM

Run Finish Time 3:04:00 PM 1:50:00 PM 9:13:00 PM

Net Run Time, minutes 342.91 341.51 349.36

Dry Gas Meter Volume Sampled, dscf 126.121 122.887 126.825 125.278

Moisture Content of Stack Gas, % 6.80 7.03 7.02 6.950

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

Carbon Dioxide, % 12 12 12.1 12.033

Oxygen, % 7.08 7 6.86 6.980

Average Stack Gas Temperature, °F 310.42 313.67 318.58 314.223

Dry Volumetric Flow Rate, dry scfm 664,895.5 662,429.4 715,996.0 681,106.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,059,364.3 1,061,426.5 1,152,456.4 1,091,082.40

0

Percent Isokinetic of Sampling Rate, % 93.3 59.8 101.6 84.900

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

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, February 22, 2011 Page 7 of 17
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Emissions Summary

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 3 4

Mass_mg 0.00096 0.0006 0.00056 0.001

Elb/hr 5.90E-04 3.70E-04 3.40E-04 0.000

lb/mmBtuO2 2.22E-07 1.50E-07 1.17E-07 0.000

mg/dscm 2.41E-04 1.52E-04 1.29E-04 0.000

mg/dscm@7%O2 2.42E-04 1.64E-04 1.28E-04 0.000

Compound: Arsenic

Average

RunNumber 1 3 4

Mass_mg 0.00138 0.00113 0.0012 0.001

Elb/hr 8.48E-04 6.97E-04 7.29E-04 0.001

lb/mmBtuO2 3.19E-07 2.83E-07 2.51E-07 0.000

mg/dscm 3.46E-04 2.86E-04 2.76E-04 0.000

mg/dscm@7%O2 3.48E-04 3.08E-04 2.73E-04 0.000

Compound: Beryllium

Average

RunNumber 1 3 4

Mass_mg 0.00108 0.00058 0.00058 0.001

Elb/hr 6.64E-04 3.58E-04 3.53E-04 0.000

lb/mmBtuO2 2.50E-07 1.45E-07 1.21E-07 0.000

mg/dscm 2.71E-04 1.47E-04 1.34E-04 0.000

mg/dscm@7%O2 2.73E-04 1.59E-04 1.33E-04 0.000

Compound: Cadmium

Average

RunNumber 1 3 4

Mass_mg 0.00068 0.00038 0.00038 0.000

Elb/hr 4.18E-04 2.34E-04 2.31E-04 0.000

lb/mmBtuO2 1.57E-07 9.50E-08 7.95E-08 0.000

mg/dscm 1.70E-04 9.60E-05 8.75E-05 0.000

mg/dscm@7%O2 1.71E-04 1.04E-04 8.66E-05 0.000

Compound: Chromium

Average

RunNumber 1 3 4

Mass_mg 0.00417 0.00197 0.00202 0.003

Elb/hr 2.56E-03 1.21E-03 1.23E-03 0.002

lb/mmBtuO2 9.65E-07 4.93E-07 4.23E-07 0.000

mg/dscm 1.05E-03 4.98E-04 4.65E-04 0.001

mg/dscm@7%O2 1.06E-03 5.37E-04 4.60E-04 0.001

Compound: Cobalt

Average

RunNumber 1 3 4

Mass_mg 0.00024 0.00014 0.00014 0.000

Elb/hr 1.47E-04 8.63E-05 8.51E-05 0.000

Tuesday, February 22, 2011 Page 8 of 17
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lb/mmBtuO2 5.56E-08 3.50E-08 2.93E-08 0.000

mg/dscm 6.02E-05 3.54E-05 3.22E-05 0.000

mg/dscm@7%O2 6.05E-05 3.82E-05 3.19E-05 0.000

Compound: Filterable Particulate

Average

RunNumber 1 3 4

Mass_mg 0.3 0.66 0.36 0.440

Elb/hr 1.84E-01 4.07E-01 2.19E-01 0.270

lb/mmBtuO2 6.94E-05 1.65E-04 7.53E-05 0.000

mg/dscm 7.52E-02 1.67E-01 8.29E-02 0.108

mg/dscm@7%O2 7.56E-02 1.80E-01 8.21E-02 0.113

Compound: Lead

Average

RunNumber 1 3 4

Mass_mg 0.001164 0.000702 0.00058 0.001

Elb/hr 7.15E-04 4.33E-04 3.53E-04 0.001

lb/mmBtuO2 2.69E-07 1.76E-07 1.21E-07 0.000

mg/dscm 2.92E-04 1.77E-04 1.34E-04 0.000

mg/dscm@7%O2 2.94E-04 1.91E-04 1.33E-04 0.000

Compound: Manganese

Average

RunNumber 1 3 4

Mass_mg 0.00479 0.0029 0.00229 0.003

Elb/hr 2.94E-03 1.79E-03 1.39E-03 0.002

lb/mmBtuO2 1.11E-06 7.25E-07 4.79E-07 0.000

mg/dscm 1.20E-03 7.33E-04 5.27E-04 0.001

mg/dscm@7%O2 1.21E-03 7.90E-04 5.22E-04 0.001

Compound: Nickel

Average

RunNumber 1 3 4

Mass_mg 0.0045 0.00244 0.002 0.003

Elb/hr 2.77E-03 1.50E-03 1.22E-03 0.002

lb/mmBtuO2 1.04E-06 6.10E-07 4.18E-07 0.000

mg/dscm 1.13E-03 6.17E-04 4.60E-04 0.001

mg/dscm@7%O2 1.14E-03 6.65E-04 4.55E-04 0.001

Compound: Selenium

Average

RunNumber 1 3 4

Mass_mg 0.031 0.0276 0.032 0.030

Elb/hr 1.91E-02 1.70E-02 1.95E-02 0.019

lb/mmBtuO2 7.18E-06 6.90E-06 6.70E-06 0.000

mg/dscm 7.77E-03 6.97E-03 7.37E-03 0.007

mg/dscm@7%O2 7.81E-03 7.52E-03 7.30E-03 0.008

Location: Stack Exit - OTM - 27/28

Compound: Filterable Particulate

Average

RunNumber 1 3 4

Tuesday, February 22, 2011 Page 9 of 17
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Mass_mg 6 5.6 5.6 5.733

Elb/hr 4.18E+00 3.99E+00 4.18E+00 4.117

Elb/min 6.97E-02 6.66E-02 6.97E-02 0.069

gr/dscf 7.34E-04 7.03E-04 6.81E-04 0.001

lb/mmBtuO2 1.55E-03 1.48E-03 1.42E-03 0.001

mg/dscm 1.68E+00 1.61E+00 1.56E+00 1.617

Compound: Filterable PM2.5

Average

RunNumber 1 3 4

Mass_mg 5.5 5.1 5.1 5.233

Elb/hr 3.84E+00 3.64E+00 3.81E+00 3.763

Elb/min 6.39E-02 6.06E-02 6.35E-02 0.063

gr/dscf 6.73E-04 6.40E-04 6.21E-04 0.001

lb/mmBtuO2 1.42E-03 1.35E-03 1.29E-03 0.001

mg/dscm 1.54E+00 1.47E+00 1.42E+00 1.477

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 3 4

Mass_mg 260 72 5.2 112.400

Elb/hr 1.81E+02 5.13E+01 3.88E+00 78.727

Elb/min 3.02E+00 8.56E-01 6.47E-02 1.314

gr/dscf 3.18E-02 9.04E-03 6.33E-04 0.014

lb/mmBtuO2 6.72E-02 1.90E-02 1.32E-03 0.029

mg/dscm 7.28E+01 2.07E+01 1.45E+00 31.650

Compound: Organic Condensible Particulate

Average

RunNumber 1 3 4

Mass_mg 1.1 1.6 1.4 1.367

Elb/hr 7.67E-01 1.14E+00 1.05E+00 0.986

Elb/min 1.28E-02 1.90E-02 1.74E-02 0.016

gr/dscf 1.35E-04 2.01E-04 1.70E-04 0.000

lb/mmBtuO2 2.84E-04 4.22E-04 3.54E-04 0.000

mg/dscm 3.08E-01 4.60E-01 3.90E-01 0.386

Compound: Total Particulate

Average

RunNumber 1 3 4

Mass_mg 267.1 79.2 12.2 119.500

Elb/hr 1.86E+02 5.65E+01 9.11E+00 83.870

Elb/min 3.10E+00 9.41E-01 1.52E-01 1.398

gr/dscf 3.27E-02 9.95E-03 1.48E-03 0.015

lb/mmBtuO2 6.91E-02 2.09E-02 3.09E-03 0.031

mg/dscm 7.48E+01 2.28E+01 3.40E+00 33.667

Compound: Total PM2.5

Average

RunNumber 1 3 4

Mass_mg 266.6 78.7 11.7 119.000

Elb/hr 1.86E+02 5.61E+01 8.74E+00 83.613

Elb/min 3.10E+00 9.35E-01 1.46E-01 1.394

gr/dscf 3.26E-02 9.88E-03 1.42E-03 0.015

Tuesday, February 22, 2011 Page 10 of 17
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Process Run Data

lb/mmBtuO2 6.89E-02 2.08E-02 2.96E-03 0.031

mg/dscm 7.47E+01 2.26E+01 3.26E+00 33.520

Tuesday, February 22, 2011 Page 11 of 17
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Process Run Data

Run Name Value UOM Comments

Target

Value

1 Coal Burned 0.09 1000 Tons/hr MER1Group 4 

Run 1M29 Start 

2/17/2010 9:15 

End 

2/17/201013:32

0

3 Coal Burned 0.073 1000 Tons/hr MER1 Group 4 

Run 3 M29 Start 

2/18/2010 8:17 

End 2/18/2010 

12:33

0

1 Unit Gross Electrical Output 286 Mwe MER1Group 4 

Run 1M29 Start 

2/17/2010 9:15 

End 

2/17/201013:32

0

1 Unit Net Electric Generation 265 MWh MER1Group 4 

Run 1M29 Start 

2/17/2010 9:15 

End 

2/17/201013:32

0

4 Coal Burned 0.088 1000 Tons/hr MER1 Group 4 

Run 3 

OTM027/028 Start 

2/18/2010 8:02 

End 2/18/2010 

13:50

0

4 Unit Gross Electrical Output 287 Mwe MER1 Group 4 

Run 3 

OTM027/028 Start 

2/18/2010 8:02 

End 2/18/2010 

13:50

0

4 Unit Net Electric Generation 265 MWh MER1 Group 4 

Run 3 

OTM027/028 Start 

2/18/2010 8:02 

End 2/18/2010 

13:50

0

1 Sorbent injection 386 lbs/hr MER1Group 4 

Run 1M29 Start 

2/17/2010 9:15 

End 

2/17/201013:32

0

2 Coal Burned 0.09 1000 Tons/hr MER1 Group 4 

Run 1 M30B Start 

2/17/2010 9:33 

End 2/17/2010 

12:03

0

Tuesday, February 22, 2011 Page 12 of 17
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2 Unit Gross Electrical Output 286 Mwe MER1 Group 4 

Run 1 M30B Start 

2/17/2010 9:33 

End 2/17/2010 

12:03

0

2 Unit Net Electric Generation 265 MWh MER1 Group 4 

Run 1 M30B Start 

2/17/2010 9:33 

End 2/17/2010 

12:03

0

2 Sorbent injection 386 lbs/hr MER1 Group 4 

Run 1 M30B Start 

2/17/2010 9:33 

End 2/17/2010 

12:03

0

3 Unit Gross Electrical Output 287 Mwe MER1 Group 4 

Run 3 M29 Start 

2/18/2010 8:17 

End 2/18/2010 

12:33

0

3 Unit Net Electric Generation 265 MWh MER1 Group 4 

Run 3 M29 Start 

2/18/2010 8:17 

End 2/18/2010 

12:33

0

3 Sorbent injection 386 lbs/hr MER1 Group 4 

Run 3 M29 Start 

2/18/2010 8:17 

End 2/18/2010 

12:33

0

4 Sorbent injection 374 lbs/hr MER1 Group 4 

Run 3 

OTM027/028 Start 

2/18/2010 8:02 

End 2/18/2010 

13:50

0

5 Coal Burned 0.09 1000 Tons/hr MER1 Group 4 

Run 1 

OTM027/028 Start 

2/17/2010 9:08 

End 2/17/2010 

15:04

0

5 Unit Gross Electrical Output 286 Mwe MER1 Group 4 

Run 1 

OTM027/028 Start 

2/17/2010 9:08 

End 2/17/2010 

15:04

0

Tuesday, February 22, 2011 Page 13 of 17
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5 Unit Net Electric Generation 265 MWh MER1 Group 4 

Run 1 

OTM027/028 Start 

2/17/2010 9:08 

End 2/17/2010 

15:04

0

5 Sorbent injection 385 lbs/hr MER1 Group 4 

Run 1 

OTM027/028 Start 

2/17/2010 9:08 

End 2/17/2010 

15:04

0

6 Coal Burned 0.072 1000 Tons/hr MER1 Group 4 

Run 3 M30B Start 

2/18/2010 8:13 

End 2/18/2010 

10:43

0

6 Unit Gross Electrical Output 287 Mwe MER1 Group 4 

Run 3 M30B Start 

2/18/2010 8:13 

End 2/18/2010 

10:43

0

6 Unit Net Electric Generation 265 MWh MER1 Group 4 

Run 3 M30B Start 

2/18/2010 8:13 

End 2/18/2010 

10:43

0

6 Sorbent injection 386 lbs/hr MER1 Group 4 

Run 3 M30B Start 

2/18/2010 8:13 

End 2/18/2010 

10:43

0

7 Coal Burned 0.093 1000 Tons/hr MER1 Group 4 

Run 4 M29 Start 

2/18/2010 15:19 

End 2/18/2010 

19:34

0

7 Unit Gross Electrical Output 312 Mwe MER1 Group 4 

Run 4 M29 Start 

2/18/2010 15:19 

End 2/18/2010 

19:34

0

7 Unit Net Electric Generation 289 MWh MER1 Group 4 

Run 4 M29 Start 

2/18/2010 15:19 

End 2/18/2010 

19:34

0

Tuesday, February 22, 2011 Page 14 of 17
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APCD Run Data

7 Sorbent injection 363 lbs/hr MER1 Group 4 

Run 4 M29 Start 

2/18/2010 15:19 

End 2/18/2010 

19:34

0

8 Coal Burned 0.093 1000 Tons/hr MER1 Group 4 

Run 4 

OTM027/028 Start 

2/18/2010 15:13 

End 2/18/2010 

21:13

0

8 Unit Gross Electrical Output 312 Mwe MER1 Group 4 

Run 4 

OTM027/028 Start 

2/18/2010 15:13 

End 2/18/2010 

21:13

0

8 Unit Net Electric Generation 289 MWh MER1 Group 4 

Run 4 

OTM027/028 Start 

2/18/2010 15:13 

End 2/18/2010 

21:13

0

8 Sorbent injection 347 lbs/hr MER1 Group 4 

Run 4 

OTM027/028 Start 

2/18/2010 15:13 

End 2/18/2010 

21:13

0

9 Coal Burned 0.093 1000 Tons/hr MER1 Group 4 

Run 4 M30B Start 

2/18/2010 15:15 

End 2/18/2010 

17:30

0

9 Unit Gross Electrical Output 312 Mwe MER1 Group 4 

Run 4 M30B Start 

2/18/2010 15:15 

End 2/18/2010 

17:30

0

9 Unit Net Electric Generation 289 MWh MER1 Group 4 

Run 4 M30B Start 

2/18/2010 15:15 

End 2/18/2010 

17:30

0

9 Sorbent injection 366 lbs/hr MER1 Group 4 

Run 4 M30B Start 

2/18/2010 15:15 

End 2/18/2010 

17:30

0

Target

Value Tuesday, February 22, 2011 Page 15 of 17
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Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 ELECTROSTATIC PRECIPITATOR (CD1) 0 0

1 ACTIVATED CARBON ADSORPTION (CD22) 0 0

1 BAGHOUSE (CD27) 0 0

1 SCR (SELECTIVE CATALYTIC REDUCTION) 

(CD19(

0 0

Run Name Value UOM Comments

1 Fuel Higher Heating Value 0 Btu/lb

1 Fuel Moisture 0 %

1 Fuel Mercury Content 0 ppm

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 16 of 17
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Sampling / Stack Data Results Detail

Location Stack Exit - Method 29 

Average

Run Number 1 3 4

Test Date 2/17/2010 2/18/2010 2/18/2010

Run Start Time 9:15:00 AM 8:17:00 AM 3:19:00 PM

Run Finish Time 1:32:00 PM 12:23:00 PM 7:34:00 PM

Net Traversing Points 24 24 24

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.286 0.286 0.286 0.286

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9849 0.9849 0.9849 0.985

Barometric Pressure, inches of Mercury 29.465 29.485 29.51 29.487

Average Orifice Meter Differential, inches H2O 1.26 1.24 1.50 1.333

Dry Gas Meter Volume Sampled, cubic feet 144.657 144.050 157.605 148.771

Average Dry Gas Meter Temperature, °F 67.54 69.79 68.92 68.750

Dry Gas Meter Volume Sampled, dscf 140.870 139.771 153.403 144.681

Total Moisture Liquid collected, g 223.7 229.3 249.5 234.167

Volume of Water Vapor, standard cubic feet 10.53 10.79 11.74 11.020

Moisture Content of Stack Gas, % 6.96 7.17 7.11 7.080

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

Dry Mole Fraction 0.9304 0.9283 0.9289 0.929

Carbon Dioxide, % 12 11.3 12.1 11.800

Oxygen, % 7.08 8.01 6.86 7.317

Carbon Monoxide & Nitrogen, % 80.92 80.69 81.04 80.883

Fuel Factor 1.15 1.14 1.16

Dry Molecular Weight, lb/lb-Mole 30.20 30.13 30.21 30.180

Wet Molecular weight, lb/lb-Mole 29.35 29.26 29.34 29.317

Flue Gas Static Pressure, inches of H2O -0.7 -0.7 -0.66 -0.687

Absolute Flue Gas Pressure, inches of Mercury 29.41 29.43 29.46 29.433

Average Stack Gas Temperature, °F 307.88 310.96 314.38 311.073

Average Velocity Head, inches of H2O 0.2720782768

88104

0.270762368

594494

0.318609234

527635

0.287

Average Stack Gas Velocity, feet/second 35.33 35.36 38.37 36.353

Stack Cross-Sectional Area, square feet 490.992 490.992 490.992 490.992

Dry Volumetric Flow Rate, dry scfm 654,505.1 651,413.9 704,916.0 670,278.333

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,040,804.8 1,041,688.6 1,130,361.8 1,070,951.7

33

Percent Isokinetic of Sampling Rate, % 98.7 98.4 99.8 98.967

Percent Excess Air, % 49.6 60.3 47.2 52.367

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

Round Duct Diameter, inches 25 25 25

Rectangular Duct Width, inches 265.9 265.9 265.9

Rectangular Duct Length, inches 265.9 265.9 265.9

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, February 22, 2011 Page 17 of 17
PSEG Mercer 1 EGU ICR MACT

9/2/2010

Location Stack Exit - OTM - 27/28

Average

Run Number 1 3 4

Test Date 2/17/2010 2/18/2010 2/18/2010

Run Start Time 9:08:00 AM 8:02:00 AM 3:13:00 PM

Run Finish Time 3:04:00 PM 1:50:00 PM 9:13:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 342.91 341.51 349.36

Nozzle Diameter, inches 0.231 0.286 0.212 0.243

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9808 0.9849 0.9908 0.986

Barometric Pressure, inches of Mercury 29.45 29.485 29.525 29.487

Average Orifice Meter Differential, inches H2O 0.47 0.46 0.46 0.463

Dry Gas Meter Volume Sampled, cubic feet 128.450 125.430 128.830 127.570

Average Dry Gas Meter Temperature, °F 59.75 63.67 65.00 62.807

Dry Gas Meter Volume Sampled, dscf 126.121 122.887 126.825 125.278

Total Moisture Liquid collected, g 195.4 197.3 203.3 198.667

Volume of Water Vapor, standard cubic feet 9.20 9.29 9.57 9.353

Moisture Content of Stack Gas, % 6.80 7.03 7.02 6.950

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

Dry Mole Fraction 0.932 0.9297 0.9298 0.931

Carbon Dioxide, % 12 12 12.1 12.033

Oxygen, % 7.08 7 6.86 6.980

Carbon Monoxide & Nitrogen, % 80.92 81 81.04 80.987

Fuel Factor 1.15 1.16 1.16

Dry Molecular Weight, lb/lb-Mole 30.20 30.20 30.21 30.203

Wet Molecular weight, lb/lb-Mole 29.37 29.34 29.35 29.353

Flue Gas Static Pressure, inches of H2O -0.7 -0.7 -0.66 -0.687

Absolute Flue Gas Pressure, inches of Mercury 29.40 29.43 29.48 29.437

Average Stack Gas Temperature, °F 310.42 313.67 318.58 314.223

Average Velocity Head, inches of H2O 0.2810669502

3309

0.281013101

466941

0.329764255

57079

0.297

Average Stack Gas Velocity, feet/second 35.96 36.03 39.12 37.037

Stack Cross-Sectional Area, square feet 490.992 490.992 490.992 490.992

Dry Volumetric Flow Rate, dry scfm 664,895.5 662,429.4 715,996.0 681,106.967

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,059,364.3 1,061,426.5 1,152,456.4 1,091,082.4

00

Percent Isokinetic of Sampling Rate, % 93.3 59.8 101.6 84.900

Percent Excess Air, % 49.6 48.7 47.2 48.500

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

Round Duct Diameter, inches 25 25 25

Rectangular Duct Width, inches 265.9 265.9 265.9

Rectangular Duct Length, inches 265.9 265.9 265.9

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, February 22, 2011 Page 18 of 17