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

Boil2 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
Boil2 MACT HAP EDR Carneys Point

9/2/2010

Facility Information:

Chambers Cogeneration LP. BOIL2

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:

BOIL2 Boiler #2

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 0 0 0 3780 960 1 12

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

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

Tuesday, January 25, 2011 Page 2 of 24
Boil2 MACT HAP EDR Carneys Point

9/2/2010

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

2,3,3',4,4',5/2,3,3',4,4',5'-

HxCB (PCBs156/157)

Stack Exit 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

2,3,3',4,4',5,5'-HpCB 

(PCB189)

Stack Exit Method 23 3 480 0

Stack Exit Total PCBs Method 23 3 480 0

Stack Exit Total TEQ Method 23 3 480 0

Total organic compounds 

(TOC) as Propane

Stack Exit Method 25A 3 120 0

Stack Exit Hydrogen Chloride Method 26 3 180 0

Stack Exit Hydrogen Fluoride Method 26 3 180 0

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
Boil2 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

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

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

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, January 25, 2011 Page 4 of 24
Boil2 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 3/11/2010 3/11/2010 3/11/2010

Run Start Time 7:00:00 AM 9:10:00 

AM

11:20:00 AM

Run Finish Time 9:02:00 AM 11:12:00 

AM

1:24:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 82.319 85.232 81.163 82.905

Moisture Content of Stack Gas, % 13.16 12.96 13.35 13.157

Moisture Saturation at Stack Gas Temperature, % 50.39 51.59 50.74 50.907

Carbon Dioxide, % 14.97 15.1 14.95 15.007

Oxygen, % 4.83 4.75 4.91 4.830

Average Stack Gas Temperature, °F 179.33 180.42 179.67 179.807

Dry Volumetric Flow Rate, dry scfm 314,039.4 310,286.4 315,144.8 313,156.867

Actual Wet Volumetric Flue Gas Flow Rate, acfm 439,054.3 433,258.1 441,504.8 437,939.067

Percent Isokinetic of Sampling Rate, % 102.7 104.0 100.9 102.533

F-Factor, dscfm/MMBtu @ %O2 9671 9671 9671 9,671.000

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
Boil2 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
Boil2 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
Boil2 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
Boil2 MACT HAP EDR Carneys Point

9/2/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.00182 0.00254 0.00248 0.002

Elb/hr 9.18E-04 1.22E-03 1.27E-03 0.001

gr/dscf 3.41E-07 4.60E-07 4.72E-07 0.000

lb/mmBtuO2 6.13E-07 8.22E-07 8.52E-07 0.000

mg/dscm 7.81E-04 1.05E-03 1.08E-03 0.001

ppm 6.25E-04 8.43E-04 8.64E-04 0.001

ppm@7%O2 5.41E-04 7.26E-04 7.51E-04 0.001

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.56E-02 2.15E-02 1.91E-02 0.019

ppm 1.71E+01 2.36E+01 2.08E+01 20.500

ppm@7%O2 1.48E+01 2.03E+01 1.81E+01 17.733

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 4.24E-04 2.54E-04 3.35E-04 0.000

lb/mmBtuO2 7.63E-04 4.55E-04 6.05E-04 0.001

mg/dscm 9.71E-01 5.82E-01 7.67E-01 0.773

ppm 5.30E-01 3.17E-01 4.18E-01 0.422

ppm@7%O2 4.58E-01 2.73E-01 3.63E-01 0.365

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 2 3 1

Mass_mg 0.16 0.19 0.37 0.240

Elb/hr 5.64E-02 6.87E-02 1.34E-01 0.086

lb/mmBtuO2 3.61E-05 4.36E-05 8.84E-05 0.000

mg/dscm 4.72E-02 5.77E-02 1.13E-01 0.073

mg/dscm@7%O2 4.02E-02 4.85E-02 9.83E-02 0.062

Compound: Hydrogen Fluoride

Average

RunNumber 2 3 1

Mass_mg 0.04 0.04 0.04 0.040

Elb/hr 1.41E-02 1.45E-02 1.44E-02 0.014

lb/mmBtuO2 9.02E-06 9.18E-06 9.55E-06 0.000

mg/dscm 1.18E-02 1.21E-02 1.22E-02 0.012

mg/dscm@7%O2 1.00E-02 1.02E-02 1.06E-02 0.010

Tuesday, January 25, 2011 Page 9 of 24
Boil2 MACT HAP EDR Carneys Point

9/2/2010

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 3 2

Mass_mg 0.0001 0.000216 0.0001 0.000

Elb/hr 2.24E-05 4.91E-05 2.25E-05 0.000

lb/mmBtuO2 1.51E-08 3.12E-08 1.38E-08 0.000

mg/dscm 1.88E-05 4.06E-05 1.86E-05 0.000

mg/dscm@7%O2 1.67E-05 3.62E-05 1.60E-05 0.000

Compound: Arsenic

Average

RunNumber 1 3 2

Mass_mg 0.00031 0.000187 0.000382 0.000

Elb/hr 6.94E-05 4.25E-05 8.59E-05 0.000

lb/mmBtuO2 4.69E-08 2.70E-08 5.29E-08 0.000

mg/dscm 5.82E-05 3.51E-05 7.09E-05 0.000

mg/dscm@7%O2 5.17E-05 3.13E-05 6.12E-05 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000025 0.000025 0.000025 0.000

Elb/hr 5.59E-06 5.62E-06 5.68E-06 0.000

lb/mmBtuO2 3.78E-09 3.46E-09 3.61E-09 0.000

mg/dscm 4.69E-06 4.64E-06 4.69E-06 0.000

mg/dscm@7%O2 4.16E-06 4.00E-06 4.18E-06 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.002606 0.000162 0.000101 0.001

Elb/hr 5.83E-04 3.64E-05 2.30E-05 0.000

lb/mmBtuO2 3.94E-07 2.24E-08 1.46E-08 0.000

mg/dscm 4.89E-04 3.01E-05 1.90E-05 0.000

mg/dscm@7%O2 4.34E-04 2.60E-05 1.69E-05 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.0001 0.001784 0.002119 0.001

Elb/hr 2.24E-05 4.01E-04 4.82E-04 0.000

lb/mmBtuO2 1.51E-08 2.47E-07 3.06E-07 0.000

mg/dscm 1.88E-05 3.31E-04 3.98E-04 0.000

mg/dscm@7%O2 1.67E-05 2.86E-04 3.54E-04 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.001381 0.001396 0.001363 0.001

Elb/hr 3.09E-04 3.14E-04 3.10E-04 0.000

lb/mmBtuO2 2.09E-07 1.93E-07 1.97E-07 0.000

mg/dscm 2.59E-04 2.59E-04 2.56E-04 0.000

Tuesday, January 25, 2011 Page 10 of 24
Boil2 MACT HAP EDR Carneys Point

9/2/2010

mg/dscm@7%O2 2.30E-04 2.23E-04 2.28E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.00284 0.001656 0.001909 0.002

Elb/hr 6.35E-04 3.72E-04 4.34E-04 0.000

lb/mmBtuO2 4.30E-07 2.29E-07 2.76E-07 0.000

mg/dscm 5.33E-04 3.08E-04 3.58E-04 0.000

mg/dscm@7%O2 4.73E-04 2.66E-04 3.19E-04 0.000

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.003386 0.002333 0.00257 0.003

Elb/hr 7.58E-04 5.24E-04 5.84E-04 0.001

lb/mmBtuO2 5.12E-07 3.23E-07 3.71E-07 0.000

mg/dscm 6.36E-04 4.33E-04 4.83E-04 0.001

mg/dscm@7%O2 5.65E-04 3.74E-04 4.30E-04 0.000

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0001 0.0001 0.0001 0.000

Elb/hr 2.24E-05 2.25E-05 2.27E-05 0.000

lb/mmBtuO2 1.51E-08 1.38E-08 1.44E-08 0.000

mg/dscm 1.88E-05 1.86E-05 1.88E-05 0.000

mg/dscm@7%O2 1.67E-05 1.60E-05 1.67E-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 1.69E-01 1.54E-01 1.82E-01 0.168

mg/dscm 2.16E+02 2.01E+02 2.41E+02 219.333

mg/dscm@7%O2 1.88E+02 1.71E+02 2.03E+02 187.333

ppm 8.11E+01 7.56E+01 9.03E+01 82.333

ppm@7%O2 7.05E+01 6.43E+01 7.60E+01 70.267

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 1.30E-01 1.16E-01 1.33E-01 0.126

mg/dscm 1.66E+02 1.52E+02 1.76E+02 164.667

mg/dscm@7%O2 1.44E+02 1.29E+02 1.48E+02 140.333

ppm 8.69E+01 7.97E+01 9.21E+01 86.233

ppm@7%O2 7.56E+01 6.78E+01 7.75E+01 73.633

Location: Stack Exit - OTM - 27/28

Tuesday, January 25, 2011 Page 11 of 24
Boil2 MACT HAP EDR Carneys Point

9/2/2010

Process Run Data

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 1.2 0.5 0.4 0.700

lb/mmBtuO2 2.70E-04 1.03E-04 8.55E-05 0.000

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 1.2 0.5 0.4 0.700

lb/mmBtuO2 2.70E-04 1.03E-04 8.55E-05 0.000

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 37.5 45.1 35 39.200

lb/mmBtuO2 8.42E-03 9.32E-03 7.48E-03 0.008

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 2 1.1 1.6 1.567

lb/mmBtuO2 4.49E-04 2.27E-04 3.42E-04 0.000

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 40.7 46.6 37 41.433

lb/mmBtuO2 9.14E-03 9.63E-03 7.91E-03 0.009

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 40.7 46.6 37 41.433

lb/mmBtuO2 9.14E-03 9.63E-03 7.91E-03 0.009

Tuesday, January 25, 2011 Page 12 of 24
Boil2 MACT HAP EDR Carneys Point

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Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 1072.1 Million Btus/hr 0 3/11/10

2 Heat Input 1069.5 Million Btus/hr 0 3/12/10

3 Heat Input 1004.2 Million Btus/hr 0 3/13/10

1 Average Heat Input 1072.1 MMBtu/hr 0 avg 3/11/10

2 Average Heat Input 1069.5 MMBtu/hr 0 avg 3/12/10

3 Average Heat Input 1004.2 MMBtu/hr 0 avg 3/13/10

1 Steam Output 267 1000 lb steam/hr 0 avg 3/11/10

2 Steam Output 297.2 1000 lb steam/hr 0

3 Steam Output 291.2 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 0.07 0 KPPH, avg 3/11/10

2 Fuel Oil Firing Rate 0.07 0 KPPH, avg 3/12/10

3 Fuel Oil Firing Rate 0.06 0 KPPH, avg 3/13/10

1 Flue Gas Flow Rate dscfm see individual test 

runs

0

2 Flue Gas Flow Rate dscfm see individual test 

runs

0

3 Flue Gas Flow Rate 0 dscfm see individual test 

runs

0

1 Pressure Drop Across FGD (if applicable) 1.4 in H20 0 DCS JP1PT29

2 Pressure Drop Across FGD (if applicable) 1.5 in H20 0 DCS JP1PT29

3 Pressure Drop Across FGD (if applicable) 1.3 in H20 0 DCS JP1PT29

1 FGD Scrubber Liquor pH 0 pH not applicable - 

spray dryer 

absorber

0

2 FGD Scrubber Liquor pH 0 pH not applicable - 

spray dryer 

absorber

0

Tuesday, January 25, 2011 Page 13 of 24
Boil2 MACT HAP EDR Carneys Point

9/2/2010

3 FGD Scrubber Liquor pH 0 pH not applicable - 

spray dryer 

absorber

0

1 FGD Scrubber Liquor Flow Rate 38.9 gal/min 0 DCS JP1FT21

2 FGD Scrubber Liquor Flow Rate 39.8 gal/min 0 DCS JP1FT21

3 FGD Scrubber Liquor Flow Rate 36.2 gal/min 0 DCS JP1FT21

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

97 lb/hr 0 lime, avg 3/11/10

2 Sorbent Type and Sorbent Injection Rate (if 

applicable)

112 lb/hr 0 lime, avg 3/12/10

3 Sorbent Type and Sorbent Injection Rate (if 

applicable)

92 lb/hr 0 Lime, avg 3/13/10

1 Flue Gas Oxygen Content 6.04 % 0 wet, avg 3/11/10

2 Flue Gas Oxygen Content 5.78 % 0 wet, avg 3/12/10

3 Flue Gas Oxygen Content 6.03 % 0 wet, avg 3/13/10

1 Flue Gas Carbon Dioxide Content 11.1 % 0 wet, avg 3/11/10

2 Flue Gas Carbon Dioxide Content 11.3 % 0 wet, avg 3/12/10

3 Flue Gas Carbon Dioxide Content 10.9 % 0 wet, avg 3/13/10

1 Flue Gas Moisture Content 10.27 % 0 avg 3/11/10

2 Flue Gas Moisture Content 11.21 % 0

3 Flue Gas Moisture Content 11.79 % 0 avg 3/13/10

1 Flue Gas Sampling Point Temperature 178.4 Deg F 0 avg 3/11/10

2 Flue Gas Sampling Point Temperature 177.9 Deg F 0

3 Flue Gas Sampling Point Temperature 176.8 Deg F 0 avg 3/13/10

1 Flue Gas Pressure in. Hg see individual test 

runs

29.89

2 Flue Gas Pressure in. Hg see individual test 

runs

29.89

3 Flue Gas Pressure 0 in. Hg see individual test 

runs

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
Boil2 MACT HAP EDR Carneys Point

9/2/2010

APCD Run Data

Process Lab Run Data

1 Unit Net Electric Generation 1715.9 MWh 0 total 3/11/10

2 Unit Net Electric Generation 1746.1 MWh 0 total 3/12/10

3 Unit Net Electric Generation 1529 MWh 0 total 3/13/10

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

Run Name Value UOM Comments

1 Fuel Higher Heating Value 13354 Btu/lb

2 Fuel Higher Heating Value 13246 Btu/lb

3 Fuel Higher Heating Value 13168 Btu/lb

1 Fuel Moisture 4.48 %

2 Fuel Moisture 5.23 %

3 Fuel Moisture 5.85 %

1 Fuel Mercury Content 0.12 ppm

2 Fuel Mercury Content 0.11 ppm

3 Fuel Mercury Content ppm

1 Fuel Cadmium Content 0.02 ppm

2 Fuel Cadmium Content 0.2 ppm

3 Fuel Cadmium Content ppm

1 Ultimate/Proximate Analysis 0

2 Ultimate/Proximate Analysis 0

3 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content 10 ppm

2 Fuel Nickel Content 11 ppm

3 Fuel Nickel Content ppm

1 Fuel Arsenic Content 7 ppm

2 Fuel Arsenic Content 8 ppm

3 Fuel Arsenic Content ppm

1 Fuel Chromium Content 14 ppm

2 Fuel Chromium Content 14 ppm

3 Fuel Chromium Content ppm

1 Fuel Beryllium Content 1.1 ppm

2 Fuel Beryllium Content 1.1 ppm

Tuesday, January 25, 2011 Page 15 of 24
Boil2 MACT HAP EDR Carneys Point

9/2/2010

3 Fuel Beryllium Content ppm

1 Fuel Lead Content 4 ppm

2 Fuel Lead Content 4 ppm

3 Fuel Lead Content ppm

1 Fuel Manganese Content 11 ppm

2 Fuel Manganese Content 12 ppm

3 Fuel Manganese Content ppm

1 Fuel Chlorine Content 888 ppm

2 Fuel Chlorine Content 929 ppm

3 Fuel Chlorine Content 1036 ppm

1 Fuel Fluorine Content 62 ppm

2 Fuel Fluorine Content 70 ppm

3 Fuel Fluorine Content 79 ppm

Tuesday, January 25, 2011 Page 16 of 24
Boil2 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 3/11/2010 3/11/2010 3/11/2010

Run Start Time 7:00:00 AM 9:10:00 AM 11:20:00 AM

Run Finish Time 9:02:00 AM 11:12:00 AM 1:24:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.175 0.178 0.175 0.176

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.01 0.97 1.01 0.997

Barometric Pressure, inches of Mercury 29.95 29.97 29.97 29.963

Average Orifice Meter Differential, inches H2O 1.55 1.43 1.54 1.507

Dry Gas Meter Volume Sampled, cubic feet 82.177 89.305 81.324 84.269

Average Dry Gas Meter Temperature, °F 74.92 79.42 77.25 77.197

Dry Gas Meter Volume Sampled, dscf 82.319 85.232 81.163 82.905

Total Moisture Liquid collected, g 265.1 269.7 265.5 266.767

Volume of Water Vapor, standard cubic feet 12.48 12.69 12.50 12.557

Moisture Content of Stack Gas, % 13.16 12.96 13.35 13.157

Moisture Saturation at Stack Gas Temperature, % 50.39 51.59 50.74 50.907

Dry Mole Fraction 0.8684 0.8704 0.8665 0.868

Carbon Dioxide, % 14.97 15.1 14.95 15.007

Oxygen, % 4.83 4.75 4.91 4.830

Carbon Monoxide & Nitrogen, % 80.2 80.15 80.14 80.163

Fuel Factor 1.07 1.07 1.07

Dry Molecular Weight, lb/lb-Mole 30.59 30.61 30.59 30.597

Wet Molecular weight, lb/lb-Mole 28.93 28.98 28.91 28.940

Flue Gas Static Pressure, inches of H2O -1.5 -1.5 -1.5 -1.500

Absolute Flue Gas Pressure, inches of Mercury 29.84 29.86 29.86 29.853

Average Stack Gas Temperature, °F 179.33 180.42 179.67 179.807

Average Velocity Head, inches of H2O 2.2731058170

4145

2.215001573

24915

2.297227711

36837

2.262

Average Stack Gas Velocity, feet/second 93.17 91.94 93.69 92.933

Stack Cross-Sectional Area, square feet 78.540 78.540 78.540 78.540

Dry Volumetric Flow Rate, dry scfm 314,039.4 310,286.4 315,144.8 313,156.867

Actual Wet Volumetric Flue Gas Flow Rate, acfm 439,054.3 433,258.1 441,504.8 437,939.067

Percent Isokinetic of Sampling Rate, % 102.7 104.0 100.9 102.533

Percent Excess Air, % 29.5 28.9 30.2 29.533

F-Factor, dscfm/MMBtu @ %O2 9671 9671 9671 9,671.000

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
Boil2 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
Boil2 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
Boil2 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
Boil2 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
Boil2 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
Boil2 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
Boil2 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