Name: Andrew Shawl

Title: Environmental Manager

Company: BL England

Sign Date:

Name: Mike Taylor

Title: President

Company: Catalyst Air Management

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

NJ2378 BL England Unit 2

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 08, 2011 Page 1 of 7
NJ2378 BL England Unit 2

Facility Information:

NJ2378 BL England Unit 2

900 N. Shore Rd.

Beasley's Point NJ 08223

Contact: Andrew Shawl

Phone: 609-390-5113

Fax: 609-390-5149

Email: andrew.shawl@blengland.com

Testing Company:

Catalyst Air Management

2502 Byington-Solway Rd

Knoxville TN 37931

Contact:Mike Taylor

Phone: 865-531-0075

Fax: 865-531-0750

Email: mike.taylor@catalystair.com

Air Permit Number:

2378

Permitted Source ID/Name:

2 BL England Generating Station

Permitted Maximum Process Rate: Max. Normal Operation Process Rate: Target Process Test Rate

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

 process flow diagram:

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.

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

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

NJ2378 BL2 180 0 0 0 1596 2316 2 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

NJ2378 BL2 Chlorine Method 26A 2 180 0

NJ2378 BL2 Hydrogen Fluoride Method 26A 2 180 0

NJ2378 BL2 Hydrogen Chloride Method 26A 2 180 0

Tuesday, February 08, 2011 Page 2 of 7
NJ2378 BL England Unit 2

Tuesday, February 08, 2011 Page 3 of 7
NJ2378 BL England Unit 2

Sampling / Stack Data Results Summary

Location NJ2378 BL2 - Method 26A

Average

Run Number M26A-1 M26A-2

Test Date 6/16/2010 6/16/2010

Run Start Time 7:32:00 AM 10:30:00 

AM

Run Finish Time 10:56:00 AM 1:35:00 PM

Net Run Time, minutes 180 180

Dry Gas Meter Volume Sampled, dscf 106.764 102.241 104.503

Moisture Content of Stack Gas, % 13.62 13.41 13.515

Moisture Saturation at Stack Gas Temperature, % 14.08 14.08 14.080

Carbon Dioxide, % 13 13 13.000

Oxygen, % 6.4 6.4 6.400

Average Stack Gas Temperature, °F 127.04 127.04 127.040

Dry Volumetric Flow Rate, dry scfm 408,763.1 396,750.0 402,756.550

Actual Wet Volumetric Flue Gas Flow Rate, acfm 531,099.3 514,240.7 522,670.000

Percent Isokinetic of Sampling Rate, % 103.6 102.2 102.900

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

Fw 10640 10640 10,640.000

Fc 1800 1800 1,800.000

Tuesday, February 08, 2011 Page 4 of 7
NJ2378 BL England Unit 2

Emissions Summary

Process Run Data

Location: NJ2378 BL2 - Method 26A

Compound: Chlorine

Average

RunNumber M26A-1 M26A-2

Mass_mg 1.2 1.2 1.200

lb/mmBtuO2 3.49E-04 3.65E-04 0.000

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2

Mass_mg 3.4 3.4 3.400

lb/mmBtuO2 9.90E-04 1.03E-03 0.001

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2

Mass_mg 0.2 0.2 0.200

lb/mmBtuO2 5.82E-05 6.08E-05 0.000

Tuesday, February 08, 2011 Page 5 of 7
NJ2378 BL England Unit 2

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Heat Input Million Btus/million BTU using O2 1275 0

1 Steam Rate 976 1000 lbs/hr 0

1 Fuel Rate 120000 lbs/hr 0

1 Unit Load 110 MW 0

2 Heat Input Million Btus/million BTU using O2 1423 0

2 Steam Rate 1203 1000 lbs/hr 0

2 Fuel Rate 120000 lbs/hr 0

2 Unit Load 110 MW 0

Run Name Value UOM Comments

Target

Value

1 OVERFIRE AIR 0 0

1 SELECTIVE NONCATALYTIC REDUCTION 

FOR NOX

0 0

1 ACTIVATED CARBON ADSORPTION 0 0

1 ELECTROSTATIC PRECIPITATOR 0

1 WET SCRUBBER 87000 gal/min 0

Tuesday, February 08, 2011 Page 6 of 7
NJ2378 BL England Unit 2

Sampling / Stack Data Results Detail

Location NJ2378 BL2 - Method 26A

Average

Run Number M26A-1 M26A-2

Test Date 6/16/2010 6/16/2010

Run Start Time 7:32:00 AM 10:30:00 AM

Run Finish Time 10:56:00 AM 1:35:00 PM

Net Traversing Points 12 12

Net Run Time, minutes 180 180

Nozzle Diameter, inches 0.213 0.213 0.213

Pitot Tube Coefficient 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.01 1.01 1.010

Barometric Pressure, inches of Mercury 29.67 29.67 29.670

Average Orifice Meter Differential, inches H2O 1.05 0.99 1.020

Dry Gas Meter Volume Sampled, cubic feet 112.475 107.839 110.157

Average Dry Gas Meter Temperature, °F 98.56 99.15 98.855

Dry Gas Meter Volume Sampled, dscf 106.764 102.241 104.503

Total Moisture Liquid collected, g 357.8 336.3 347.050

Volume of Water Vapor, standard cubic feet 16.84 15.83 16.335

Moisture Content of Stack Gas, % 13.62 13.41 13.515

Moisture Saturation at Stack Gas Temperature, % 14.08 14.08 14.080

Dry Mole Fraction 0.8638 0.8659 0.865

Carbon Dioxide, % 13 13 13.000

Oxygen, % 6.4 6.4 6.400

Carbon Monoxide & Nitrogen, % 80.6 80.6 80.600

Fuel Factor 1.12 1.12

Dry Molecular Weight, lb/lb-Mole 30.34 30.34 30.340

Wet Molecular weight, lb/lb-Mole 28.66 28.69 28.675

Flue Gas Static Pressure, inches of H2O -0.44 -0.45 -0.445

Absolute Flue Gas Pressure, inches of Mercury 29.64 29.64 29.640

Average Stack Gas Temperature, °F 127.04 127.04 127.040

Average Velocity Head, inches of H2O 0.7041695365

19048

0.660754077

364797

0.682

Average Stack Gas Velocity, feet/second 50.09 48.50 49.295

Stack Cross-Sectional Area, square feet 176.715 176.715 176.715

Dry Volumetric Flow Rate, dry scfm 408,763.1 396,750.0 402,756.550

Actual Wet Volumetric Flue Gas Flow Rate, acfm 531,099.3 514,240.7 522,670.000

Percent Isokinetic of Sampling Rate, % 103.6 102.2 102.900

Percent Excess Air, % 43.0 43.0 43.000

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

Round Duct Diameter, inches 180 180

Rectangular Duct Width, inches 0 0

Rectangular Duct Length, inches 0 0

Fw 10640 10640 10,640.000

Fc 1800 1800 1,800.000

Tuesday, February 08, 2011 Page 7 of 7