### 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.

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### NJ2378 BL England Unit 2

Facility Information: NJ2378 BL England Unit 2 900 N. Shore Rd.
Beasley's Point NJ08223 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 TN37931 Contact:Mike Taylor Phone:865-531-0075 Fax: 865-531-0750 Email: mike.taylor@catalystair.com

Air Permit Number: 2378 Permitted Source ID/Name: BL England Generating Station 2 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 / Description10100202 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 1596 2316 2 0 12 0 0

Target Parameter Test Method Number of

Test Runs Test Run

Duration Sample

Points Comments Location Chlorine Method 26A 2 180 0 NJ2378 BL2Hydrogen Fluoride Method 26A 2 180 0 NJ2378 BL2Hydrogen Chloride Method 26A 2 180 0 NJ2378 BL2



### Tuesday, February 08, 2011 Page 2 of 7

### NJ2378 BL England Unit 2

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### 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 AM1:35:00 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



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### 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



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### 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 1275 Million Btus/million BTU using O2 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 1423 Million Btus/million BTU using O2 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

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### 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 AM10:30:00 AM Run Finish Time 10:56:00 AM1:35:00 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 190480.660754077

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



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