Name: Rolf Dinsmore

Title: Compliance Supervisor

Company: Chambers Cogeneration, LP, ORIS 10

Sign Date: 9/2/2010

Name: Lenny D. Katerynczuk

Title: Project Manager

Company: AirNova, Inc.

Sign Date: 9/2/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Boil1 MACT HAP EDR Carneys Point

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Tuesday, January 25, 2011 Page 1 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Facility Information:

Chambers Cogeneration LP. BOIL1

500 Shell Road

Carneys Point NJ 08069

Contact: Rolf Dinsmore

Phone: 856-351-6386

Fax: 856-351-6399

Email: RolfDinsmore@cogentrix.com

Testing Company:

Air Nova Inc.

585 Clayton Avenue

Pennsauken NJ 08019

Contact:Lenny Katerynczuk

Phone: 856-486-1500

Fax: 856-486-9896

Email: Lenny@airnova.com

Air Permit Number:

10566

Permitted Source ID/Name:

BOIL1 Boiler #1

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 0 315 80 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
Boil1 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
Boil1 MACT HAP EDR Carneys Point

9/2/2010

The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

See attached test report

Organic Condensible 

Particulate

OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total PM2.5 OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Total Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

Filterable Particulate OTM - 27/28 3 240 0 Use only for dry 

stacks. Delete Method 

5/OTM28 tests.

Stack Exit

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
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Sampling / Stack Data Results Summary

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 3/10/2010 3/10/2010 3/10/2010

Run Start Time 1:10:00 PM 3:18:00 PM 5:25:00 PM

Run Finish Time 3:13:00 PM 5:20:00 PM 7:27:00 PM

Net Run Time, minutes 120 120 120

Dry Gas Meter Volume Sampled, dscf 83.313 80.604 84.398 82.772

Moisture Content of Stack Gas, % 12.36 12.29 12.30 12.317

Moisture Saturation at Stack Gas Temperature, % 52.69 52.06 53.72 52.823

Carbon Dioxide, % 14.28 14.42 14.57 14.423

Oxygen, % 5.3 5.32 5.38 5.333

Average Stack Gas Temperature, °F 181.33 180.75 182.17 181.417

Dry Volumetric Flow Rate, dry scfm 307,499.0 308,257.8 309,538.6 308,431.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 427,461.8 428,074.4 430,854.7 428,796.967

Percent Isokinetic of Sampling Rate, % 102.6 102.5 103.3 102.800

F-Factor, dscfm/MMBtu @ %O2 9592 9592 9592 9,592.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Tuesday, January 25, 2011 Page 5 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Tuesday, January 25, 2011 Page 6 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Location Stack Exit - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Tuesday, January 25, 2011 Page 7 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Fuel Type

Fw

Fc

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Run Time, minutes

Dry Gas Meter Volume Sampled, dscf

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Carbon Dioxide, %

Oxygen, %

Average Stack Gas Temperature, °F

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

F-Factor, dscfm/MMBtu @ %O2

Fw

Fc

Tuesday, January 25, 2011 Page 8 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Emissions Summary

Location: Stack Exit - Method 0011

Compound: Formaldehyde

Average

RunNumber 1 2 3

Mass_mg 0.00212 0.0026 0.0032 0.003

Elb/hr 1.04E-03 1.32E-03 1.55E-03 0.001

gr/dscf 3.93E-07 4.98E-07 5.85E-07 0.000

lb/mmBtuO2 7.21E-07 9.15E-07 1.08E-06 0.000

mg/dscm 8.99E-04 1.14E-03 1.34E-03 0.001

ppm 7.20E-04 9.12E-04 1.07E-03 0.001

ppm@7%O2 6.42E-04 8.14E-04 9.58E-04 0.001

Location: Stack Exit - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 4.81E-02 3.65E-02 4.70E-02 0.044

ppm 5.12E+01 3.90E+01 5.01E+01 46.767

ppm@7%O2 4.59E+01 3.48E+01 4.49E+01 41.867

Location: Stack Exit - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 0.00E+00 0.00E+00 0.000

gr/dscf 9.29E-05 3.28E-04 8.38E-05 0.000

lb/mmBtuO2 1.71E-04 6.02E-04 1.55E-04 0.000

mg/dscm 2.13E-01 7.50E-01 1.92E-01 0.385

ppm 1.16E-01 4.09E-01 1.05E-01 0.210

ppm@7%O2 1.03E-01 3.65E-01 9.40E-02 0.187

Location: Stack Exit - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.35 0.14 0.09 0.193

Elb/hr 1.20E-01 4.78E-02 3.13E-02 0.066

lb/mmBtuO2 7.60E-05 3.08E-05 2.04E-05 0.000

mg/dscm 9.55E-02 3.87E-02 2.55E-02 0.053

mg/dscm@7%O2 8.43E-02 3.41E-02 2.26E-02 0.047

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.03 0.04 0.03 0.033

Elb/hr 1.03E-02 1.37E-02 1.04E-02 0.011

lb/mmBtuO2 6.52E-06 8.79E-06 6.80E-06 0.000

mg/dscm 8.19E-03 1.10E-02 8.50E-03 0.009

mg/dscm@7%O2 7.23E-03 9.70E-03 7.54E-03 0.008

Tuesday, January 25, 2011 Page 9 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location: Stack Exit - Method 29 

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000194 0.0001 0.0001 0.000

Elb/hr 4.37E-05 2.34E-05 2.22E-05 0.000

lb/mmBtuO2 2.79E-08 1.63E-08 1.53E-08 0.000

mg/dscm 3.48E-05 2.01E-05 1.91E-05 0.000

mg/dscm@7%O2 3.11E-05 1.81E-05 1.71E-05 0.000

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.000793 0.000673 0.000869 0.001

Elb/hr 1.78E-04 1.57E-04 1.93E-04 0.000

lb/mmBtuO2 1.14E-07 1.09E-07 1.33E-07 0.000

mg/dscm 1.42E-04 1.35E-04 1.66E-04 0.000

mg/dscm@7%O2 1.27E-04 1.21E-04 1.48E-04 0.000

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000042 0.000031 0.000048 0.000

Elb/hr 9.45E-06 7.25E-06 1.07E-05 0.000

lb/mmBtuO2 6.04E-09 5.04E-09 7.35E-09 0.000

mg/dscm 7.52E-06 6.24E-06 9.14E-06 0.000

mg/dscm@7%O2 6.72E-06 5.61E-06 8.16E-06 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.000283 0.000142 0.0001 0.000

Elb/hr 6.37E-05 3.32E-05 2.22E-05 0.000

lb/mmBtuO2 4.07E-08 2.31E-08 1.53E-08 0.000

mg/dscm 5.07E-05 2.86E-05 1.91E-05 0.000

mg/dscm@7%O2 4.53E-05 2.57E-05 1.71E-05 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.005934 0.011283 0.006459 0.008

Elb/hr 1.34E-03 2.64E-03 1.44E-03 0.002

lb/mmBtuO2 8.54E-07 1.83E-06 9.90E-07 0.000

mg/dscm 1.06E-03 2.27E-03 1.23E-03 0.002

mg/dscm@7%O2 9.47E-04 2.04E-03 1.10E-03 0.001

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.001807 0.001989 0.0016 0.002

Elb/hr 4.07E-04 4.65E-04 3.56E-04 0.000

lb/mmBtuO2 2.60E-07 3.23E-07 2.45E-07 0.000

mg/dscm 3.24E-04 4.00E-04 3.05E-04 0.000

Tuesday, January 25, 2011 Page 10 of 24
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mg/dscm@7%O2 2.89E-04 3.59E-04 2.72E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.003477 0.003446 0.003779 0.004

Elb/hr 7.83E-04 8.06E-04 8.40E-04 0.001

lb/mmBtuO2 5.00E-07 5.60E-07 5.79E-07 0.000

mg/dscm 6.23E-04 6.93E-04 7.20E-04 0.001

mg/dscm@7%O2 5.57E-04 6.23E-04 6.43E-04 0.001

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.012573 0.013624 0.008088 0.011

Elb/hr 2.83E-03 3.19E-03 1.80E-03 0.003

lb/mmBtuO2 1.81E-06 2.21E-06 1.24E-06 0.000

mg/dscm 2.25E-03 2.74E-03 1.54E-03 0.002

mg/dscm@7%O2 2.01E-03 2.46E-03 1.38E-03 0.002

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.0001 0.0001 0.0001 0.000

Elb/hr 2.25E-05 2.34E-05 2.22E-05 0.000

lb/mmBtuO2 1.44E-08 1.63E-08 1.53E-08 0.000

mg/dscm 1.79E-05 2.01E-05 1.91E-05 0.000

mg/dscm@7%O2 1.60E-05 1.81E-05 1.71E-05 0.000

Location: Stack Exit - Method 6C

Compound: Sulfur Dioxide

Average

Run 1 2 3

Elb/hr 0.00E+00 0.00E+00 0.000

lb/mmBtuO2 1.58E-01 1.59E-01 1.61E-01 0.159

mg/dscm 1.98E+02 2.00E+02 2.01E+02 199.667

mg/dscm@7%O2 1.75E+02 1.76E+02 1.78E+02 176.333

ppm 7.43E+01 7.49E+01 7.56E+01 74.933

ppm@7%O2 6.56E+01 6.60E+01 6.70E+01 66.200

Location: Stack Exit - Method 7E

Compound: Nitrogen oxides (NOx)

Average

Run 1 2 3

Elb/hr 0.00E+00 0.00E+00 0.00E+00 0.000

lb/mmBtuO2 1.34E-01 1.36E-01 1.32E-01 0.134

mg/dscm 1.69E+02 1.71E+02 1.65E+02 168.333

mg/dscm@7%O2 1.49E+02 1.51E+02 1.46E+02 148.667

ppm 8.83E+01 8.96E+01 8.61E+01 88.000

ppm@7%O2 7.79E+01 7.90E+01 7.63E+01 77.733

Location: Stack Exit - OTM - 27/28

Tuesday, January 25, 2011 Page 11 of 24
Boil1 MACT HAP EDR Carneys Point

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Process Run Data

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 2 1.6 3.3 2.300

lb/mmBtuO2 4.27E-04 3.74E-04 7.48E-04 0.001

Compound: Filterable PM2.5

Average

RunNumber 1 2 3

Mass_mg 2 1.6 3.3 2.300

lb/mmBtuO2 4.27E-04 3.74E-04 7.48E-04 0.001

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 8.9 43.1 14 22.000

lb/mmBtuO2 1.90E-03 1.01E-02 3.17E-03 0.005

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 2 1.9 1.1 1.667

lb/mmBtuO2 4.27E-04 4.44E-04 2.49E-04 0.000

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 12.9 47.6 18.4 26.300

lb/mmBtuO2 2.75E-03 1.11E-02 4.17E-03 0.006

Compound: Total PM2.5

Average

RunNumber 1 2 3

Mass_mg 12.9 47.6 18.4 26.300

lb/mmBtuO2 2.75E-03 1.11E-02 4.17E-03 0.006

Tuesday, January 25, 2011 Page 12 of 24
Boil1 MACT HAP EDR Carneys Point

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Process Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input 1767.1 Million Btus/hr applies to M6, 7E, 

26A

0

2 Heat Input 1598 Million Btus/hr applies to runs 

1&2 of M29, 

OTM27/28

0

3 Heat Input 1466.9 Million Btus/hr applies to M0011, 

10, 25A, runs 3 of 

M29, OTM27/28

0

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

2 Average Heat Input 1598 MMBtu/hr 0 avg 3/9/10

3 Average Heat Input 1466.9 MMBtu/hr 0 avg 3/10/10

1 Steam Output 723.1 1000 lb steam/hr 0 avg 3/8/10

2 Steam Output 633.5 1000 lb steam/hr 0

3 Steam Output 568.3 1000 lb steam/hr 0

1 Synfuel Firing Rate 0 0

2 Synfuel Firing Rate 0 0

3 Synfuel Firing Rate 0 0

1 Petroleum Coke Firing Rate 0 0

2 Petroleum Coke Firing Rate 0 0

3 Petroleum Coke Firing Rate 0 0

1 Coal Gas Firing Rate 0 0

2 Coal Gas Firing Rate 0 0

3 Coal Gas Firing Rate 0 0

1 Fuel Oil Firing Rate 0.03 0 KPPH, avg 3/8/10

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

3 Fuel Oil Firing Rate 0.02 0 KPPH, avg 3/10/10

1 Flue Gas Flow Rate 330775 dscfm 0

2 Flue Gas Flow Rate 323472 dscfm 0

3 Flue Gas Flow Rate 0 dscfm 0

1 Pressure Drop Across FGD (if applicable) 1.1 in H20 0 DCS JP1PT29

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

3 Pressure Drop Across FGD (if applicable) 0.9 in H20 0 DCS JP1PT29

1 FGD Scrubber Liquor pH 0 pH not applicable - 

spray dryer 

absorber

0

Tuesday, January 25, 2011 Page 13 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

2 FGD Scrubber Liquor pH 0 pH not applicable - 

spray dryer 

absorber

0

3 FGD Scrubber Liquor pH 0 pH not applicable - 

spray dryer 

absorber

0

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

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

3 FGD Scrubber Liquor Flow Rate 46.7 gal/min 0 DCS JP1FT21

1 Sorbent Type and Sorbent Injection Rate (if 

applicable)

249 lb/hr 0 lime, avg 3/8/10

2 Sorbent Type and Sorbent Injection Rate (if 

applicable)

224 lb/hr 0 lime, avg 3/9/10

3 Sorbent Type and Sorbent Injection Rate (if 

applicable)

206 lb/hr 0 Lime, avg 3/10/10

1 Flue Gas Oxygen Content 5.9 % 0 wet, avg 3/8/10

2 Flue Gas Oxygen Content 6.56 % 0 wet, avg 3/9/10

3 Flue Gas Oxygen Content 6.67 % 0 wet, avg 3/10/10

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

2 Flue Gas Carbon Dioxide Content 10 % 0 wet, avg 3/9/10

3 Flue Gas Carbon Dioxide Content 9.9 % 0 wet, avg 3/10/10

1 Flue Gas Moisture Content 12.58 % 0 avg 3/8/10

2 Flue Gas Moisture Content 12.55 % 0

3 Flue Gas Moisture Content 12.64 % 0 avg 3/10/10

1 Flue Gas Sampling Point Temperature 176.3 Deg F 0 avg 3/8/10

2 Flue Gas Sampling Point Temperature 176.6 Deg F 0

3 Flue Gas Sampling Point Temperature 176.1 Deg F 0 avg 3/10/10

1 Flue Gas Pressure 29.89 in. Hg 29.89

2 Flue Gas Pressure 29.82 in. Hg 29.89

3 Flue Gas Pressure 0 in. Hg 29.89

1 Standard Pressure 29.92 in. Hg 0

2 Standard Pressure 29.92 in. Hg 0

3 Standard Pressure 29.92 in. Hg 0

1 Standard Temperature 68 Deg F 0

2 Standard Temperature 68 Deg F 0

3 Standard Temperature 68 Deg F 0

1 Unit Gross Electrical Output 77 MW 0

2 Unit Gross Electrical Output 77 MW 0

3 Unit Gross Electrical Output 77 MW 0

Tuesday, January 25, 2011 Page 14 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

APCD Run Data

Process Lab Run Data

1 Unit Net Electric Generation 3455.2 MWh total BOTH 

BOILERS 3/8/10

0

2 Unit Net Electric Generation 3102.9 MWh total BOTH 

BOILERS 3/9/10

0

3 Unit Net Electric Generation 2961.1 MWh total BOTH 

BOILERS 3/10/10

0

4 Heat Input 0 Million Btus/hr 0

4 Average Heat Input 0 MMBtu/hr 0

4 Steam Output 0 1000 lb steam/hr 0

4 Synfuel Firing Rate 0 0

4 Petroleum Coke Firing Rate 0 0

4 Coal Gas Firing Rate 0 0

4 Fuel Oil Firing Rate 0 0

4 Flue Gas Flow Rate 0 dscfm 0

4 Pressure Drop Across FGD (if applicable) 0 in H20 0

4 FGD Scrubber Liquor pH 0 pH 0

4 FGD Scrubber Liquor Flow Rate 0 gal/min 0

4 Sorbent Type and Sorbent Injection Rate (if 

applicable)

0 lb/hr 0

4 Flue Gas Oxygen Content 0 % 0

4 Flue Gas Carbon Dioxide Content 0 % 0

4 Flue Gas Moisture Content 0 % 0

4 Flue Gas Sampling Point Temperature 0 Deg F 0

4 Flue Gas Pressure 0 in. Hg 29.89

4 Standard Pressure 0 in. Hg 0

4 Standard Temperature 0 Deg F 0

4 Unit Gross Electrical Output 0 MW 0

4 Unit Net Electric Generation 0 MWh 0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 1 N/A 1

1 OVERFIRE AIR 1 N/A 1

1 SCR (SELECTIVE CATALYTIC REDUCTION) 1 1

1 SPRAY DRYER 1 1

1 BAGHOUSE 1 1

Tuesday, January 25, 2011 Page 15 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Run Name Value UOM Comments

1 Fuel Higher Heating Value 13139 Btu/lb

1 Fuel Moisture 6.3 %

1 Fuel Mercury Content ppm

1 Fuel Cadmium Content ppm

1 Ultimate/Proximate Analysis 0

1 Fuel Nickel Content ppm

1 Fuel Arsenic Content ppm

1 Fuel Chromium Content ppm

1 Fuel Beryllium Content ppm

1 Fuel Lead Content ppm

1 Fuel Manganese Content ppm

1 Fuel Chlorine Content 937 ppm

1 Fuel Fluorine Content 76 ppm

2 Fuel Higher Heating Value 1E+05 Btu/lb

2 Fuel Moisture 4.71 %

2 Fuel Mercury Content 0.13 ppm

2 Fuel Cadmium Content 0.2 ppm

2 Ultimate/Proximate Analysis 0

2 Fuel Nickel Content 10 ppm

2 Fuel Arsenic Content 8 ppm

2 Fuel Chromium Content 15 ppm

2 Fuel Beryllium Content 1.1 ppm

2 Fuel Lead Content 4 ppm

2 Fuel Manganese Content 11 ppm

2 Fuel Chlorine Content 1048 ppm

2 Fuel Fluorine Content ppm

3 Fuel Higher Heating Value 13370 Btu/lb

3 Fuel Moisture 5.06 %

3 Fuel Mercury Content 0.11 ppm

3 Fuel Cadmium Content 0.2 ppm

3 Ultimate/Proximate Analysis 0

3 Fuel Nickel Content 9 ppm

3 Fuel Arsenic Content 6 ppm

3 Fuel Chromium Content 14 ppm

3 Fuel Beryllium Content 1 ppm

3 Fuel Lead Content 4 ppm

3 Fuel Manganese Content 12 ppm

3 Fuel Chlorine Content 930 ppm

3 Fuel Fluorine Content ppm

Tuesday, January 25, 2011 Page 16 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Sampling / Stack Data Results Detail

Location Stack Exit - Method 0011

Average

Run Number 1 2 3

Test Date 3/10/2010 3/10/2010 3/10/2010

Run Start Time 1:10:00 PM 3:18:00 PM 5:25:00 PM

Run Finish Time 3:13:00 PM 5:20:00 PM 7:27:00 PM

Net Traversing Points 12 12 12

Net Run Time, minutes 120 120 120

Nozzle Diameter, inches 0.178 0.175 0.178 0.177

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.97 1.01 0.97 0.983

Barometric Pressure, inches of Mercury 29.95 29.93 29.93 29.937

Average Orifice Meter Differential, inches H2O 1.40 1.49 1.43 1.440

Dry Gas Meter Volume Sampled, cubic feet 88.060 81.853 89.999 86.637

Average Dry Gas Meter Temperature, °F 83.75 83.71 88.25 85.237

Dry Gas Meter Volume Sampled, dscf 83.313 80.604 84.398 82.772

Total Moisture Liquid collected, g 249.6 239.8 251.6 247.000

Volume of Water Vapor, standard cubic feet 11.75 11.29 11.84 11.627

Moisture Content of Stack Gas, % 12.36 12.29 12.30 12.317

Moisture Saturation at Stack Gas Temperature, % 52.69 52.06 53.72 52.823

Dry Mole Fraction 0.8764 0.8771 0.877 0.877

Carbon Dioxide, % 14.28 14.42 14.57 14.423

Oxygen, % 5.3 5.32 5.38 5.333

Carbon Monoxide & Nitrogen, % 80.42 80.26 80.05 80.243

Fuel Factor 1.09 1.08 1.07

Dry Molecular Weight, lb/lb-Mole 30.50 30.52 30.55 30.523

Wet Molecular weight, lb/lb-Mole 28.96 28.98 29.01 28.983

Flue Gas Static Pressure, inches of H2O -1.6 -1.6 -1.6 -1.600

Absolute Flue Gas Pressure, inches of Mercury 29.83 29.81 29.81 29.817

Average Stack Gas Temperature, °F 181.33 180.75 182.17 181.417

Average Velocity Head, inches of H2O 2.1493210531

1452

2.157474030

16937

2.182794248

82284

2.163

Average Stack Gas Velocity, feet/second 90.71 90.84 91.43 90.993

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

Dry Volumetric Flow Rate, dry scfm 307,499.0 308,257.8 309,538.6 308,431.800

Actual Wet Volumetric Flue Gas Flow Rate, acfm 427,461.8 428,074.4 430,854.7 428,796.967

Percent Isokinetic of Sampling Rate, % 102.6 102.5 103.3 102.800

Percent Excess Air, % 33.2 33.5 34.1 33.600

F-Factor, dscfm/MMBtu @ %O2 9592 9592 9592 9,592.000

Round Duct Diameter, inches 120 120 120

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Tuesday, January 25, 2011 Page 17 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - Method 10

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Tuesday, January 25, 2011 Page 18 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - Method 25A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Tuesday, January 25, 2011 Page 19 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - Method 26A

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Tuesday, January 25, 2011 Page 20 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - Method 29 

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Tuesday, January 25, 2011 Page 21 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - Method 6C

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Tuesday, January 25, 2011 Page 22 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - Method 7E

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Carbon Dioxide, %

Oxygen, %

Fuel Factor

Dry Volumetric Flow Rate, dry scfm

F-Factor, dscfm/MMBtu @ %O2

Moisture, %

Analyzer Make

Analyzer Model

Analyzer Serial Number

Operating Range

Operating Units

No. Readings/Avg.

Calibration Set

Calibration Pre Zero Cylinder ID

Calibration Pre Zero Cylinder Instrument Response

Calibration Pre Zero Cylinder Bias

Calibration Pre Zero Cylinder Drift

Calibration Pre High Cylinder ID

Calibration Pre High Cylinder Instrument Response

Calibration Pre High Cylinder Bias

Calibration Pre High Cylinder Drift

Calibration Post Zero Cylinder ID

Calibration Post Zero Cylinder Instrument Response

Calibration Post Zero Cylinder Bias

Calibration Post Zero Cylinder Drift

Calibration Post High Cylinder ID

Calibration Post High Cylinder Instrument Response

Calibration Post High Cylinder Bias

Calibration Post High Cylinder Drift

Cavg

Cavg Units

Cgas

Cgas Units

Fuel Type

Fw

Fc

Cgasw

Cgasw Units

Tuesday, January 25, 2011 Page 23 of 24
Boil1 MACT HAP EDR Carneys Point

9/2/2010

Location Stack Exit - OTM - 27/28

Average

Run Number

Test Date

Run Start Time

Run Finish Time

Net Traversing Points

Net Run Time, minutes

Nozzle Diameter, inches

Pitot Tube Coefficient

Dry Gas Meter Calibration Factor

Barometric Pressure, inches of Mercury

Average Orifice Meter Differential, inches H2O

Dry Gas Meter Volume Sampled, cubic feet

Average Dry Gas Meter Temperature, °F

Dry Gas Meter Volume Sampled, dscf

Total Moisture Liquid collected, g

Volume of Water Vapor, standard cubic feet

Moisture Content of Stack Gas, %

Moisture Saturation at Stack Gas Temperature, %

Dry Mole Fraction

Carbon Dioxide, %

Oxygen, %

Carbon Monoxide & Nitrogen, %

Fuel Factor

Dry Molecular Weight, lb/lb-Mole

Wet Molecular weight, lb/lb-Mole

Flue Gas Static Pressure, inches of H2O

Absolute Flue Gas Pressure, inches of Mercury

Average Stack Gas Temperature, °F

Average Velocity Head, inches of H2O

Average Stack Gas Velocity, feet/second

Stack Cross-Sectional Area, square feet

Dry Volumetric Flow Rate, dry scfm

Actual Wet Volumetric Flue Gas Flow Rate, acfm

Percent Isokinetic of Sampling Rate, %

Percent Excess Air, %

F-Factor, dscfm/MMBtu @ %O2

Round Duct Diameter, inches

Rectangular Duct Width, inches

Rectangular Duct Length, inches

Fw

Fc

Tuesday, January 25, 2011 Page 24 of 24