Name: Mary Ann Keon

Title: Environmental Director

Company: Boral Industries

Sign Date: 2/25/2011

Name: Tommy Lotz, Jr.

Title: Project Manager

Company: TRC Environmental

Sign Date: 2/25/2011

Permitted Facility Representative / Date Testing Company Representative / Date

Boral Muskogee Outlet

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, March 15, 2011 Page 1 of 12
Boral Muskogee Outlet

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Facility Information:

Boral Bricks of Texas, LP

3101 W. 53rd Street, South

Muskogee OK 74401

Contact: Mary Ann Keon

Phone: 770-645-4529

Fax:

Email: maryann.keon@boral.com

Testing Company:

TRC Environmental

108 Yeager Circle

Pelham AL 35124

Contact:Tommy Lotz, Jr.

Phone: 205-358-3203

Fax: 205-358-7492

Email: telotz@TRCsolutions.com

Air Permit Number:

2003-086-TVR (M-2)

Permitted Source ID/Name:

EU-04 Tunnel Kiln

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

11.39 tons per hour

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

 process flow diagram:

The source is a gas fired tunnel kiln. Emissions are controlled by a dry sorbent injection fabric filter (DIFF)

Industry/SCC/NAIS 327121

Sampling Location Information:

Test Parameter Information:

AFS #: 4010100012 FRS #: 100045588

SCC / Description 30500311 Industrial Processes - Mineral Products - Brick Manufacture - Curing and Firing: 

Gas-fired Tunnel Kilns 

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

Outlet 45 0 0 0 480 282 2 16

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Outlet % H2O Method 1 - 4 3 64 0

Outlet Flowrate Method 1 - 4 3 64 0

Outlet Hydrogen Chloride Method 26A 3 64 0

Outlet Chlorine Method 26A 3 64 0

Outlet Hydrogen Fluoride Method 26A 3 64 0

Outlet Chromium Method 29 3 64 0

Regulation Description Compound Limit Unit

2003-086-TVR (M-2) PM 117.86 TPY

Tuesday, March 15, 2011 Page 2 of 12
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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.

Outlet Beryllium Method 29 3 64 0

Outlet Antimony Method 29 3 64 0

Outlet Cadmium Method 29 3 64 0

Outlet Lead Method 29 3 64 0

Outlet Selenium Method 29 3 64 0

Outlet Mercury Method 29 3 64 0

Outlet Manganese Method 29 3 64 0

Outlet Cobalt Method 29 3 64 0

Outlet Nickel Method 29 3 64 0

Filterable 

Particulate

Outlet Method 29 3 64 0

Outlet Arsenic Method 29 3 64 0

Outlet O2 Method 3A O2 3 60 0

Tuesday, March 15, 2011 Page 3 of 12
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Sampling / Stack Data Results Summary

Location Outlet - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 11/15/2010 11/16/2010 11/16/2010

Run Start Time 3:55:00 PM 8:50:00 

AM

11:05:00 AM

Run Finish Time 4:55:00 PM 9:50:00 

AM

12:05:00 PM

Net Run Time, minutes 64 64 64

Dry Gas Meter Volume Sampled, dscf 54.544 55.259 48.187 52.663

Moisture Content of Stack Gas, % 3.25 3.58 3.39 3.407

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 1.5 1.6 1.6 1.567

Oxygen, % 18.3 18 17.9 18.067

Average Stack Gas Temperature, °F 350.94 357.69 356.81 355.147

Dry Volumetric Flow Rate, dry scfm 14,976.7 15,189.5 14,081.3 14,749.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 23,830.7 24,486.8 22,631.2 23,649.567

Percent Isokinetic of Sampling Rate, % 99.1 99.0 93.1 97.067

F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000

Fw 10610 10610 10610 10,610.000

Fc 1040 1040 1040 1,040.000

Tuesday, March 15, 2011 Page 4 of 12
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Location Outlet - Method 29

Average

Run Number M29/5-1 M29/5-2 M29/5-3

Test Date 11/15/2010 11/16/2010 11/16/2010

Run Start Time 3:55:00 PM 8:50:00 

AM

11:05:00 AM

Run Finish Time 4:55:00 PM 9:50:00 

AM

12:05:00 PM

Net Run Time, minutes 64 64 64

Dry Gas Meter Volume Sampled, dscf 43.322 37.794 34.071 38.396

Moisture Content of Stack Gas, % 3.41 3.15 3.16 3.240

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Carbon Dioxide, % 1.5 1.6 1.6 1.567

Oxygen, % 18.3 18 17.9 18.067

Average Stack Gas Temperature, °F 354.25 363.81 362.13 360.063

Dry Volumetric Flow Rate, dry scfm 12,286.4 10,426.6 9,424.3 10,712.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 19,662.3 16,859.1 15,209.0 17,243.467

Percent Isokinetic of Sampling Rate, % 99.4 102.2 101.9 101.167

F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000

Fw 10610 10610 10610 10,610.000

Fc 1040 1040 1040 1,040.000

Location Outlet - Method 3A O2

Average

Run Number 1 2 3

Test Date 11/15/2010 11/16/2010 11/16/2010

Run Start Time 3:55:00 PM 8:50:00 

AM

11:05:00 AM

Run Finish Time 4:55:00 PM 9:50:00 

AM

12:05:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000

Moisture, % 0 0 0 0.000

Fuel Type Gas - Natural Gas - 

Natural

Gas - Natural

Fw 10610 10610 10610 10,610.000

Fc 1040 1040 1040 1,040.000

Tuesday, March 15, 2011 Page 5 of 12
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Emissions Summary

Location: Outlet - Method 26A

Compound: Chlorine

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0 0 0 0.000

Eg/hr 0.00E+00 0.00E+00 0.00E+00 0.000

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

ppm 0.00E+00 0.00E+00 0.00E+00 0.000

ppm@7%O2 0.00E+00 0.00E+00 0.00E+00 0.000

Compound: Hydrogen Chloride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0.2 0.29 0.06 0.183

Eg/hr 3.29E+00 4.78E+00 1.05E+00 3.040

Elb/hr 7.26E-03 1.05E-02 2.32E-03 0.007

ppm 8.54E-02 1.22E-01 2.90E-02 0.079

ppm@7%O2 4.57E-01 5.85E-01 1.34E-01 0.392

Compound: Hydrogen Fluoride

Average

RunNumber M26A-1 M26A-2 M26A-3

Mass_mg 0.03 0.05 0 0.027

Eg/hr 4.94E-01 8.25E-01 0.00E+00 0.440

Elb/hr 1.09E-03 1.82E-03 0.00E+00 0.001

ppm 2.33E-02 3.84E-02 0.00E+00 0.021

ppm@7%O2 1.25E-01 1.84E-01 0.00E+00 0.103

Location: Outlet - Method 29

Compound: Antimony

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.0057 0.0004 0.0004 0.002

Elb/hr 2.14E-04 1.46E-05 1.46E-05 0.000

mg/dscm 4.65E-03 3.74E-04 4.15E-04 0.002

mg/dscm@7%O2 2.49E-02 1.79E-03 1.92E-03 0.010

Compound: Arsenic

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.0421 0 0 0.014

Elb/hr 1.58E-03 0.00E+00 0.00E+00 0.001

mg/dscm 3.43E-02 0.00E+00 0.00E+00 0.011

mg/dscm@7%O2 1.83E-01 0.00E+00 0.00E+00 0.061

Compound: Beryllium

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.00248 0 0 0.001

Elb/hr 9.30E-05 0.00E+00 0.00E+00 0.000

mg/dscm 2.02E-03 0.00E+00 0.00E+00 0.001

Tuesday, March 15, 2011 Page 6 of 12
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mg/dscm@7%O2 1.08E-02 0.00E+00 0.00E+00 0.004

Compound: Cadmium

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.00072 0.001 0.00054 0.001

Elb/hr 2.70E-05 3.65E-05 1.98E-05 0.000

mg/dscm 5.87E-04 9.35E-04 5.60E-04 0.001

mg/dscm@7%O2 3.14E-03 4.48E-03 2.59E-03 0.003

Compound: Chromium

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.0145 0.0055 0.0029 0.008

Elb/hr 5.44E-04 2.01E-04 1.06E-04 0.000

mg/dscm 1.18E-02 5.14E-03 3.01E-03 0.007

mg/dscm@7%O2 6.31E-02 2.46E-02 1.39E-02 0.034

Compound: Cobalt

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0 0 0.0001 0.000

Elb/hr 0.00E+00 0.00E+00 3.66E-06 0.000

mg/dscm 0.00E+00 0.00E+00 1.04E-04 0.000

mg/dscm@7%O2 0.00E+00 0.00E+00 4.82E-04 0.000

Compound: Filterable Particulate

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 2 1.8 0.8 1.533

Elb/hr 7.50E-02 6.57E-02 2.93E-02 0.057

mg/dscm 1.63E+00 1.68E+00 8.29E-01 1.380

mg/dscm@7%O2 8.71E+00 8.05E+00 3.84E+00 6.867

Compound: Lead

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.0004 0.0005 0.0003 0.000

Elb/hr 1.50E-05 1.82E-05 1.10E-05 0.000

mg/dscm 3.26E-04 4.67E-04 3.11E-04 0.000

mg/dscm@7%O2 1.74E-03 2.24E-03 1.44E-03 0.002

Compound: Manganese

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.0095 0.0039 0.0023 0.005

Elb/hr 3.56E-04 1.42E-04 8.42E-05 0.000

mg/dscm 7.75E-03 3.64E-03 2.38E-03 0.005

mg/dscm@7%O2 4.14E-02 1.74E-02 1.10E-02 0.023

Compound: Mercury

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.0023 0.0016 0.0023 0.002

Tuesday, March 15, 2011 Page 7 of 12
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Process Run Data

Elb/hr 8.63E-05 5.84E-05 8.42E-05 0.000

mg/dscm 1.88E-03 1.50E-03 2.38E-03 0.002

mg/dscm@7%O2 1.01E-02 7.19E-03 1.10E-02 0.009

Compound: Nickel

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.0109 0.0142 0.0034 0.010

Elb/hr 4.09E-04 5.18E-04 1.24E-04 0.000

mg/dscm 8.89E-03 1.33E-02 3.52E-03 0.009

mg/dscm@7%O2 4.75E-02 6.37E-02 1.63E-02 0.043

Compound: Selenium

Average

RunNumber M29/5-1 M29/5-2 M29/5-3

Mass_mg 0.0003 0.0004 0.0004 0.000

Elb/hr 1.13E-05 1.46E-05 1.46E-05 0.000

mg/dscm 2.45E-04 3.74E-04 4.15E-04 0.000

mg/dscm@7%O2 1.31E-03 1.79E-03 1.92E-03 0.002

Tuesday, March 15, 2011 Page 8 of 12
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Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 Brick Produced 11.39 Tons/hr 11.4

2 Brick Produced 11.39 Tons/hr 11.4

3 Brick Produced 11.39 Tons/hr 11.4

1 Lime Feed Rate 115 lbs/hr 115

2 Lime Feed Rate 115 lbs/hr 115

3 Lime Feed Rate 115 lbs/hr 115

Run Name Value UOM Comments

Target

Value

1 DRY LIMESTONE INJECTION 0 0

1 FABRIC FILTER 0 0

Tuesday, March 15, 2011 Page 9 of 12
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Sampling / Stack Data Results Detail

Location Outlet - Method 26A

Average

Run Number M26A-1 M26A-2 M26A-3

Test Date 11/15/2010 11/16/2010 11/16/2010

Run Start Time 3:55:00 PM 8:50:00 AM 11:05:00 AM

Run Finish Time 4:55:00 PM 9:50:00 AM 12:05:00 PM

Net Traversing Points 16 16 16

Net Run Time, minutes 64 64 64

Nozzle Diameter, inches 0.341 0.341 0.341 0.341

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 1.0099 1.0099 1.0099 1.010

Barometric Pressure, inches of Mercury 29.86 29.82 29.82 29.833

Average Orifice Meter Differential, inches H2O 2.44 2.52 2.17 2.377

Dry Gas Meter Volume Sampled, cubic feet 54.272 54.420 47.710 52.134

Average Dry Gas Meter Temperature, °F 72.69 66.63 69.00 69.440

Dry Gas Meter Volume Sampled, dscf 54.544 55.259 48.187 52.663

Total Moisture Liquid collected, g 38.9 43.5 36 39.467

Volume of Water Vapor, standard cubic feet 1.83 2.05 1.69 1.857

Moisture Content of Stack Gas, % 3.25 3.58 3.39 3.407

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9675 0.9642 0.9661 0.966

Carbon Dioxide, % 1.5 1.6 1.6 1.567

Oxygen, % 18.3 18 17.9 18.067

Carbon Monoxide & Nitrogen, % 80.2 80.4 80.5 80.367

Fuel Factor 1.73 1.81 1.88

Dry Molecular Weight, lb/lb-Mole 28.97 28.98 28.97 28.973

Wet Molecular weight, lb/lb-Mole 28.61 28.59 28.60 28.600

Flue Gas Static Pressure, inches of H2O -0.13 -0.13 -0.13 -0.130

Absolute Flue Gas Pressure, inches of Mercury 29.85 29.81 29.81 29.823

Average Stack Gas Temperature, °F 350.94 357.69 356.81 355.147

Average Velocity Head, inches of H2O 0.264 0.276 0.236 0.259

Average Stack Gas Velocity, feet/second 35.96 36.95 34.15 35.687

Stack Cross-Sectional Area, square feet 11.045 11.045 11.045 11.045

Dry Volumetric Flow Rate, dry scfm 14,976.7 15,189.5 14,081.3 14,749.167

Actual Wet Volumetric Flue Gas Flow Rate, acfm 23,830.7 24,486.8 22,631.2 23,649.567

Percent Isokinetic of Sampling Rate, % 99.1 99.0 93.1 97.067

Percent Excess Air, % 637.0 558.0 534.0 576.333

F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000

Round Duct Diameter, inches 45 45 45

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10610 10610 10610 10,610.000

Fc 1040 1040 1040 1,040.000

Tuesday, March 15, 2011 Page 10 of 12
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Location Outlet - Method 29

Average

Run Number M29/5-1 M29/5-2 M29/5-3

Test Date 11/15/2010 11/16/2010 11/16/2010

Run Start Time 3:55:00 PM 8:50:00 AM 11:05:00 AM

Run Finish Time 4:55:00 PM 9:50:00 AM 12:05:00 PM

Net Traversing Points 16 16 16

Net Run Time, minutes 64 64 64

Nozzle Diameter, inches 0.335 0.335 0.335 0.335

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9826 0.9826 0.9826 0.983

Barometric Pressure, inches of Mercury 29.86 29.82 29.82 29.833

Average Orifice Meter Differential, inches H2O 1.54 1.10 0.91 1.183

Dry Gas Meter Volume Sampled, cubic feet 43.245 37.435 34.220 38.300

Average Dry Gas Meter Temperature, °F 58.81 53.56 60.50 57.623

Dry Gas Meter Volume Sampled, dscf 43.322 37.794 34.071 38.396

Total Moisture Liquid collected, g 32.5 26.1 23.6 27.400

Volume of Water Vapor, standard cubic feet 1.53 1.23 1.11 1.290

Moisture Content of Stack Gas, % 3.41 3.15 3.16 3.240

Moisture Saturation at Stack Gas Temperature, % 100.00 100.00 100.00 100.000

Dry Mole Fraction 0.9659 0.9685 0.9684 0.968

Carbon Dioxide, % 1.5 1.6 1.6 1.567

Oxygen, % 18.3 18 17.9 18.067

Carbon Monoxide & Nitrogen, % 80.2 80.4 80.5 80.367

Fuel Factor 1.73 1.81 1.88

Dry Molecular Weight, lb/lb-Mole 28.97 28.98 28.97 28.973

Wet Molecular weight, lb/lb-Mole 28.60 28.63 28.62 28.617

Flue Gas Static Pressure, inches of H2O -0.13 -0.13 -0.13 -0.130

Absolute Flue Gas Pressure, inches of Mercury 29.85 29.81 29.81 29.823

Average Stack Gas Temperature, °F 354.25 363.81 362.13 360.063

Average Velocity Head, inches of H2O 0.179 0.130 0.106 0.138

Average Stack Gas Velocity, feet/second 29.67 25.44 22.95 26.020

Stack Cross-Sectional Area, square feet 11.045 11.045 11.045 11.045

Dry Volumetric Flow Rate, dry scfm 12,286.4 10,426.6 9,424.3 10,712.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 19,662.3 16,859.1 15,209.0 17,243.467

Percent Isokinetic of Sampling Rate, % 99.4 102.2 101.9 101.167

Percent Excess Air, % 637.0 558.0 534.0 576.333

F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000

Round Duct Diameter, inches 45 45 45

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10610 10610 10610 10,610.000

Fc 1040 1040 1040 1,040.000

Tuesday, March 15, 2011 Page 11 of 12
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Location Outlet - Method 3A O2

Average

Run Number 1 2 3

Test Date 11/15/2010 11/16/2010 11/16/2010

Run Start Time 3:55:00 PM 8:50:00 AM 11:05:00 AM

Run Finish Time 4:55:00 PM 9:50:00 AM 12:05:00 PM

Carbon Dioxide, % 0 0 0 0.000

Oxygen, % 0 0 0 0.000

Fuel Factor 0 0 0

Dry Volumetric Flow Rate, dry scfm 0 0 0 0.000

F-Factor, dscfm/MMBtu @ %O2 8710 8710 8710 8,710.000

Moisture, % 0 0 0 0.000

Analyzer Make Servomex Servomex Servomex #Error

Analyzer Model 1440 1440 1440 1,440.000

Analyzer Serial Number #Num!

Operating Range 20 0 0 6.667

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID CC207920 CC207920 CC207920

Calibration Pre Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Pre Zero Cylinder Bias 0 0 0 0.000

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID SG9134085B

AL

SG9134085B

AL

SG9134085B

AL

Calibration Pre High Cylinder Instrument Response 9.8 9.8 9.8 9.800

Calibration Pre High Cylinder Bias 0.5 0.5 0.5 0.500

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID CC207920 CC207920 CC207920

Calibration Post Zero Cylinder Instrument Response 0 0 0 0.000

Calibration Post Zero Cylinder Bias 0 0 0 0.000

Calibration Post Zero Cylinder Drift 0 0 0 0.000

Calibration Post High Cylinder ID SG9134085B

AL

SG9134085B

AL

SG9134085B

AL

Calibration Post High Cylinder Instrument Response 10 9.8 9.8 9.867

Calibration Post High Cylinder Bias 1.5 0.5 0.5 0.833

Calibration Post High Cylinder Drift 1 0 0 0.333

Cavg 18.4 17.9 17.8 18.033

Cavg Units ppmvd ppmvd ppmvd

Cgas 18.3219 18.0059 17.9053 18.078

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Gas - Natural Gas - Natural Gas - Natural

Fw 10610 10610 10610 10,610.000

Fc 1040 1040 1040 1,040.000

Cgasw 0 0 0 0.000

Cgasw Units

Tuesday, March 15, 2011 Page 12 of 12