Name: Ed Much

Title: Environmental Engineer

Company: Constellation Energy

Sign Date:

Name: Mike Taylor

Title: President

Company: Catalyst Air Management

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

MD602 Brandon Shores 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.

Saturday, January 29, 2011 Page 1 of 13
MD602 Brandon Shores Unit 2

Facility Information:

MD602 Brandon Shores

1000 Brandon Shores Road

Baltimore MD 21226

Contact: Ed Much

Phone: 410-787-9073

Fax: 410-787-5405

Email:

Testing Company:

Catalyst Air Management, Inc.

2502 Byington-Solway Road

Knoxville TN 37931

Contact:Mike Tatlor

Phone: 865-531-0075

Fax: 865-531-0750

Email: mike.taylor@catalystair.com

Air Permit Number:

602

Permitted Source ID/Name:

2 Constellation Brandon Shores Power Plant

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:

Industry/SCC/NAIS

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #:

SCC / Description 10100222 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Subbituminous 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

MD602 Unit 2 372 0 0 0 1416 5520 4 32

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

MD602 Unit 2 Carbon Monoxide Method 10 3 120 0

Total organic compounds 

(TOC) as Propane

MD602 Unit 2 Method 25A 3 120 0

MD602 Unit 2 Antimony Method 29 3 240 0

MD602 Unit 2 Selenium Method 29 3 240 0

MD602 Unit 2 Nickel Method 29 3 240 0

MD602 Unit 2 Lead Method 29 3 240 0

MD602 Unit 2 Arsenic Method 29 3 240 0

Saturday, January 29, 2011 Page 2 of 13
MD602 Brandon Shores Unit 2

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.

MD602 Unit 2 Cobalt Method 29 3 240 0

MD602 Unit 2 Chromium Method 29 3 240 0

MD602 Unit 2 Beryllium Method 29 3 240 0

MD602 Unit 2 Cadmium Method 29 3 240 0

MD602 Unit 2 Manganese Method 29 3 240 0

Organic Condensible 

Particulate

MD602 Unit 2 Method 5/OTM-28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

MD602 Unit 2 Method 5/OTM-28 3 240 0

MD602 Unit 2 Filterable Particulate Method 5/OTM-28 3 240 0

MD602 Unit 2 Total Particulate Method 5/OTM-28 3 240 0

Saturday, January 29, 2011 Page 3 of 13
MD602 Brandon Shores Unit 2

Sampling / Stack Data Results Summary

Location MD602 Unit 2 - 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

Location MD602 Unit 2 - 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

Saturday, January 29, 2011 Page 4 of 13
MD602 Brandon Shores Unit 2

Location MD602 Unit 2 - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 6/9/2010 6/9/2010 6/10/2010

Run Start Time 8:16:00 AM 1:09:00 PM 7:30:00 AM

Run Finish Time 12:08:30 PM 5:01:30 PM 11:22:30 AM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 119.717 124.402 130.948 125.022

Moisture Content of Stack Gas, % 14.47 14.77 14.59 14.610

Moisture Saturation at Stack Gas Temperature, % 14.94 15.24 14.77 14.983

Carbon Dioxide, % 13.2 13.4 12.7 13.100

Oxygen, % 6.7 6.6 7.4 6.900

Average Stack Gas Temperature, °F 129.31 130.06 128.91 129.427

Dry Volumetric Flow Rate, dry scfm 1,600,274.9 1,601,545.8 1,648,056.9 1,616,625.86

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,104,444.1 2,116,218.5 2,167,391.8 2,129,351.46

7

Percent Isokinetic of Sampling Rate, % 93.3 96.9 99.1 96.433

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

Location MD602 Unit 2 - Method 5/OTM-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

Saturday, January 29, 2011 Page 5 of 13
MD602 Brandon Shores Unit 2

Saturday, January 29, 2011 Page 6 of 13
MD602 Brandon Shores Unit 2

Emissions Summary

Location: MD602 Unit 2 - Method 10

Compound: Carbon Monoxide

Average

Run M10-1 M10-2 M10-3

lb/mmBtuO2 2.35E-02 4.03E-02 4.69E-02 0.037

ppm 2.23E+01 3.85E+01 4.51E+01 35.300

ppm@7%O2 2.20E+01 3.77E+01 4.38E+01 34.500

Location: MD602 Unit 2 - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run M25A-1 M25A-2 M25A-3

lb/mmBtuO2 8.07E-04 6.24E-04 4.24E-04 0.001

ppm 4.86E-01 3.79E-01 2.59E-01 0.375

ppm@7%O2 4.79E-01 3.71E-01 2.52E-01 0.367

Location: MD602 Unit 2 - Method 29

Compound: Antimony

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.001 0.001 0.001 0.001

lb/mmBtuO2 2.65E-07 2.53E-07 2.55E-07 0.000

Compound: Arsenic

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.001 0.001 0.001 0.001

lb/mmBtuO2 2.65E-07 2.53E-07 2.55E-07 0.000

Compound: Beryllium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00025 0.00025 0.00025 0.000

lb/mmBtuO2 6.63E-08 6.33E-08 6.37E-08 0.000

Compound: Cadmium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00034 0.0004 0.00028 0.000

lb/mmBtuO2 9.01E-08 1.01E-07 7.14E-08 0.000

Compound: Chromium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00272 0.0017 0.00359 0.003

lb/mmBtuO2 7.21E-07 4.31E-07 9.15E-07 0.000

Compound: Cobalt

Average

RunNumber M29-1 M29-2 M29-3

Saturday, January 29, 2011 Page 7 of 13
MD602 Brandon Shores Unit 2

Process Run Data

Mass_mg 0.00028 0.00025 0.00025 0.000

lb/mmBtuO2 7.42E-08 6.33E-08 6.37E-08 0.000

Compound: Lead

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00054 0.00061 0.0005 0.001

lb/mmBtuO2 1.43E-07 1.55E-07 1.27E-07 0.000

Compound: Manganese

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.02923 0.01824 0.00479 0.017

lb/mmBtuO2 7.75E-06 4.62E-06 1.22E-06 0.000

Compound: Nickel

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00928 0.00623 0.00633 0.007

lb/mmBtuO2 2.46E-06 1.58E-06 1.61E-06 0.000

Compound: Selenium

Average

RunNumber M29-1 M29-2 M29-3

Mass_mg 0.00503 0.00365 0.00641 0.005

lb/mmBtuO2 1.33E-06 9.25E-07 1.63E-06 0.000

Location: MD602 Unit 2 - Method 5/OTM-28

Compound: Filterable Particulate

Average

RunNumber OTM28-1 OTM28-2 OTM28-3

Mass_mg 13 10.3 16.6 13.300

lb/mmBtuO2 3.43E-03 2.43E-03 4.12E-03 0.003

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber OTM28-1 OTM28-2 OTM28-3

Mass_mg 14 17 11 14.000

lb/mmBtuO2 3.69E-03 4.02E-03 2.73E-03 0.003

Compound: Organic Condensible Particulate

Average

RunNumber OTM28-1 OTM28-2 OTM28-3

Mass_mg 3.1 1.7 1.7 2.167

lb/mmBtuO2 8.17E-04 4.02E-04 4.22E-04 0.001

Compound: Total Particulate

Average

RunNumber OTM28-1 OTM28-2 OTM28-3

Mass_mg 30.1 29 29.3 29.467

lb/mmBtuO2 7.93E-03 6.86E-03 7.28E-03 0.007

Saturday, January 29, 2011 Page 8 of 13
MD602 Brandon Shores 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 6715 0

1 Steam Load 3990 1000 lbs/hr 0

1 Fuel Rate 6715 0

2 Heat Input Million Btus/million BTU using O2 6143 0

2 Steam Load 3985 1000 lbs/hr 0

2 Fuel Rate 6143 0

Run Name Value UOM Comments

Target

Value

1 LOW NOX BURNERS 0 0

1 SCR (SELECTIVE CATALYTIC REDUCTION) 0 0

1 BAGHOUSE 0 0

1 WET SCRUBBER 0 0

Saturday, January 29, 2011 Page 9 of 13
MD602 Brandon Shores Unit 2

Sampling / Stack Data Results Detail

Location MD602 Unit 2 - 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

Saturday, January 29, 2011 Page 10 of 13
MD602 Brandon Shores Unit 2

Location MD602 Unit 2 - 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

Saturday, January 29, 2011 Page 11 of 13
MD602 Brandon Shores Unit 2

Location MD602 Unit 2 - Method 29

Average

Run Number M29-1 M29-2 M29-3

Test Date 6/9/2010 6/9/2010 6/10/2010

Run Start Time 8:16:00 AM 1:09:00 PM 7:30:00 AM

Run Finish Time 12:08:30 PM 5:01:30 PM 11:22:30 AM

Net Traversing Points 32 32 32

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.215 0.215 0.215 0.215

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1 1 1 1.000

Barometric Pressure, inches of Mercury 29.72 29.72 29.74 29.727

Average Orifice Meter Differential, inches H2O 0.96 1.02 1.10 1.027

Dry Gas Meter Volume Sampled, cubic feet 126.048 130.903 137.671 131.541

Average Dry Gas Meter Temperature, °F 93.52 93.27 93.27 93.353

Dry Gas Meter Volume Sampled, dscf 119.717 124.402 130.948 125.022

Total Moisture Liquid collected, g 430.4 457.8 475.2 454.467

Volume of Water Vapor, standard cubic feet 20.26 21.55 22.37 21.393

Moisture Content of Stack Gas, % 14.47 14.77 14.59 14.610

Moisture Saturation at Stack Gas Temperature, % 14.94 15.24 14.77 14.983

Dry Mole Fraction 0.8553 0.8523 0.8541 0.854

Carbon Dioxide, % 13.2 13.4 12.7 13.100

Oxygen, % 6.7 6.6 7.4 6.900

Carbon Monoxide & Nitrogen, % 80.1 80 79.9 80.000

Fuel Factor 1.08 1.07 1.06

Dry Molecular Weight, lb/lb-Mole 30.38 30.41 30.33 30.373

Wet Molecular weight, lb/lb-Mole 28.59 28.58 28.53 28.567

Flue Gas Static Pressure, inches of H2O -0.45 -0.45 -0.45 -0.450

Absolute Flue Gas Pressure, inches of Mercury 29.69 29.69 29.71 29.697

Average Stack Gas Temperature, °F 129.31 130.06 128.91 129.427

Average Velocity Head, inches of H2O 0.6031389591

05898

0.608869448

426813

0.639278547

816898

0.617

Average Stack Gas Velocity, feet/second 46.47 46.73 47.86 47.020

Stack Cross-Sectional Area, square feet 754.768 754.768 754.768 754.768

Dry Volumetric Flow Rate, dry scfm 1,600,274.9 1,601,545.8 1,648,056.9 1,616,625.8

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 2,104,444.1 2,116,218.5 2,167,391.8 2,129,351.4

67

Percent Isokinetic of Sampling Rate, % 93.3 96.9 99.1 96.433

Percent Excess Air, % 46.4 45.5 54.0 48.633

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

Round Duct Diameter, inches 372 372 372

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

Saturday, January 29, 2011 Page 12 of 13
MD602 Brandon Shores Unit 2

Location MD602 Unit 2 - Method 5/OTM-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

Saturday, January 29, 2011 Page 13 of 13