Name: Eric Dobransky

Title: Plant Manager

Company: Johns Manville

Sign Date:

Name: Randal J. Tysar

Title: Senior Environmental Engineer

Company: BT Environmental Consulting, Inc.

Sign Date:

Permitted Facility Representative / Date Testing Company Representative / Date

Johns Manville Cleburne Texas Residual Risk Data Emissions Test

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 11, 2011 Page 1 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Facility Information:

Johns Manville Cleburne

200 W Ind. Boulevard

Cleburne TX 76031

Contact: Ricardo A Santos

Phone: 817-556-6659

Fax:

Email: santosr@jm.com

Testing Company:

BT Environmental Consulting

2615 Wolcott St.

Ferndale MI 48220

Contact:Barry Boulianne

Phone: 313-449-2361

Fax: 248-548-8073

Email: bboulianne@btecinc.com

Air Permit Number:

946A, PSDTX1025M1

Permitted Source ID/Name:

946A, PSDTX1025M1

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

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

 process flow diagram:

The exhaust stacks to be evaluated by this emissions test program are (1) one exhaust stack (EPN 21) associated 

with the Line 91 electric steel shell melt furnace, (2) four exhaust stacks (EPN 16 through 19) associated with the 

Line 91 Rotary Glass Forming process, (3) one exhaust stack (EPN 20) associated with the Line 91 Curing Oven, 

(4) four exhaust stacks (EPN 1, 2, 4, and 5) associated with the Pot and Marble Forming process, and (5) one 

exhaust stack (EPN 3) associated with the Pot and Marble Curing Oven

For Line 91, glass batch is fed to two electric melters which flow to a forehearth. From the forehearth it flows 

through four spinner modules where the binder is added to form fiberglass. Exhaust from the electric melt furnaces 

and forehearths are routed through a dust collector and then to the ambient air through stack EPN 21. Exhaust from 

the four Line 91 collection modules is routed through four wet scrubbers (one for each collection module) and then 

to the ambient air through exhaust stacks EPN 16 through EPN 19. Exhaust from the curing oven and cooling table 

is routed through a wet scrubber and then to the ambient air through exhaust stack EPN 21.

For the Pot and Marble fiberglass production process, glass marbles are melted by electric pots and then binder is 

added. A mixture of natural gas and combustion air (flame attenuation) then bonds molten glass and fibers. A 

fiberglass mat forms that goes into a curing oven (natural gas and combustion air). Product cools off, it trimmed, 

backed and packaged.

Exhaust from the Pot and Marble mat collection process is routed to the ambient air through four exhaust stacks 

(EPN 1, 2, 4, and 5). Exhaust from the Pot and Marble curing oven is routed to the ambient air through exhaust 

stack EPN 3.

Industry/SCC/NAIS

Sampling Location Information:

AFS #: RN100213719 FRS #: RN100213719

SCC / Description 30501203 Industrial Processes - Mineral Products - Fiberglass Manufacturing - Electric 

Furnace (Wool-type Fiber) 

The following state and federal regulations that apply to the proposed testing:

Tuesday, January 11, 2011 Page 2 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

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.

Sampling Location Information:

Test Parameter Information:

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

EPN 21 51.875 103.75 415 2 0 0 0 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

EPN 21 Hydrogen Fluoride Method 26A 3 64 0

EPN 21 Hydrogen Chloride Method 26A 3 64 0

EPN 21 Total PM2.5 OTM - 27/28 3 192 0

Organic Condensible 

Particulate

EPN 21 OTM - 27/28 3 192 0

Inorganic (Aqueous) 

Condensible Part.

EPN 21 OTM - 27/28 3 192 0

EPN 21 Filterable PM2.5 OTM - 27/28 3 192 0

EPN 21 Cobalt Method 29 3 192 0

EPN 21 Filterable Particulate Method 29 3 192 0

EPN 21 Antimony Method 29 3 192 0

EPN 21 Arsenic Method 29 3 192 0

EPN 21 Beryllium Method 29 3 192 0

EPN 21 Chromium Method 29 3 192 0

EPN 21 Lead Method 29 3 192 0

EPN 21 Manganese Method 29 3 192 0

EPN 21 Nickel Method 29 3 192 0

EPN 21 Selenium Method 29 3 192 0

EPN 21 Cadmium Method 29 3 192 0

EPN 21 Chromium Method 0061 3 240 0

Tuesday, January 11, 2011 Page 3 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Sampling / Stack Data Results Summary

Location EPN 21 - Method 0061

Average

Run Number 1 2 3 

Test Date 9/14/2010 9/15/2010 9/15/2010 

Run Start Time 3:23:00 PM 9:54:00 

AM

2:16:00 PM 

Run Finish Time 7:36:00 PM 1:58:00 PM 6:19:00 PM 

Net Run Time, minutes 240 240 240 

Dry Gas Meter Volume Sampled, dscf 167.210 172.288 172.232 170.577

Moisture Content of Stack Gas, % 3.90 3.98 3.40 3.760

Moisture Saturation at Stack Gas Temperature, % 54.73 56.03 55.79 55.517

Carbon Dioxide, % 0.8 0.5 0.7 0.667

Oxygen, % 20.2 20.7 20.5 20.467

Average Stack Gas Temperature, °F 180.33 181.42 181.19 180.980

Dry Volumetric Flow Rate, dry scfm 19,025.2 18,336.6 18,289.6 18,550.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 25,573.2 24,692.6 24,490.0 24,918.600

Percent Isokinetic of Sampling Rate, % 92.7 99.1 99.4 97.067

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 11, 2011 Page 4 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Location EPN 21 - Method 26A

Average

Run Number 1 2 3 

Test Date 9/14/2010 9/14/2010 9/14/2010 

Run Start Time 10:12:00 AM 12:04:00 

PM

1:42:00 PM 

Run Finish Time 11:24:00 AM 1:18:00 PM 2:55:00 PM 

Net Run Time, minutes 64 64 64 

Dry Gas Meter Volume Sampled, dscf 43.522 47.637 47.131 46.097

Moisture Content of Stack Gas, % 5.64 4.15 4.58 4.790

Moisture Saturation at Stack Gas Temperature, % 58.46 60.08 59.26 59.267

Carbon Dioxide, % 0.4 0.5 0.5 0.467

Oxygen, % 20.3 20.8 20.8 20.633

Average Stack Gas Temperature, °F 183.44 184.69 184.06 184.063

Dry Volumetric Flow Rate, dry scfm 18,662.6 19,180.9 18,646.6 18,830.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 25,599.6 25,951.9 25,317.8 25,623.100

Percent Isokinetic of Sampling Rate, % 97.6 103.9 105.8 102.433

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 11, 2011 Page 5 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Location EPN 21 - Method 29

Average

Run Number 1 2 3 

Test Date 9/14/2010 9/15/2010 9/15/2010 

Run Start Time 3:38:00 PM 9:54:00 

AM

2:24:00 PM 

Run Finish Time 7:10:00 PM 1:37:00 PM 6:00:00 PM 

Net Run Time, minutes 192 192 192 

Dry Gas Meter Volume Sampled, dscf 134.397 143.480 142.185 140.021

Moisture Content of Stack Gas, % 4.01 3.14 3.60 3.583

Moisture Saturation at Stack Gas Temperature, % 64.57 52.76 43.19 53.507

Carbon Dioxide, % 0.8 0.5 0.7 0.667

Oxygen, % 20.2 20.7 20.5 20.467

Average Stack Gas Temperature, °F 187.88 178.71 169.85 178.813

Dry Volumetric Flow Rate, dry scfm 18,186.9 19,734.8 20,063.6 19,328.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 24,763.0 26,233.7 26,445.0 25,813.900

Percent Isokinetic of Sampling Rate, % 103.1 101.4 98.8 101.100

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 11, 2011 Page 6 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Location EPN 21 - OTM - 27/28

Average

Run Number 1 2 3 

Test Date 9/15/2010 9/16/2010 9/16/2010 

Run Start Time 6:30:00 PM 7:55:00 

AM

11:51:00 AM 

Run Finish Time 9:47:00 PM 11:12:00 

AM

3:08:00 PM 

Net Run Time, minutes 193 195.3 192 

Dry Gas Meter Volume Sampled, dscf 73.659 73.428 72.136 73.074

Moisture Content of Stack Gas, % 3.12 3.81 3.10 3.343

Moisture Saturation at Stack Gas Temperature, % 52.59 55.67 67.87 58.710

Carbon Dioxide, % 0.6 0.8 0.8 0.733

Oxygen, % 20.6 20.4 20.4 20.467

Average Stack Gas Temperature, °F 178.63 181.06 190.19 183.293

Dry Volumetric Flow Rate, dry scfm 19,251.8 19,354.7 19,133.4 19,246.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 25,546.8 26,039.9 25,899.0 25,828.567

Percent Isokinetic of Sampling Rate, % 110.2 108.0 109.2 109.133

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 11, 2011 Page 7 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Emissions Summary

Location: EPN 21 - Method 0061

Compound: Chromium

Average

RunNumber 1 2 3 

Mass_mg 0.0016 0.0003 0.0003 0.001

Elb/hr 2.41E-05 4.22E-06 4.21E-06 0.000

mg/dscm 3.38E-04 6.15E-05 6.15E-05 0.000

Location: EPN 21 - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3 

Mass_mg 0.2 0.2 0.2 0.200

Elb/hr 1.13E-02 1.07E-02 1.05E-02 0.011

mg/dscm 1.62E-01 1.48E-01 1.50E-01 0.153

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3 

Mass_mg 0.2 0.2 0.2 0.200

Elb/hr 1.13E-02 1.07E-02 1.05E-02 0.011

mg/dscm 1.62E-01 1.48E-01 1.50E-01 0.153

Location: EPN 21 - Method 29

Compound: Antimony

Average

RunNumber 1 2 3 

Mass_mg 0.0008 0.0008 0.0008 0.001

Elb/hr 1.43E-05 1.46E-05 1.49E-05 0.000

mg/dscm 2.10E-04 1.97E-04 1.99E-04 0.000

Compound: Arsenic

Average

RunNumber 1 2 3 

Mass_mg 0.0008 0.0008 0.0008 0.001

Elb/hr 1.43E-05 1.46E-05 1.49E-05 0.000

mg/dscm 2.10E-04 1.97E-04 1.99E-04 0.000

Compound: Beryllium

Average

RunNumber 1 2 3 

Mass_mg 0.0002 0.0002 0.0002 0.000

Elb/hr 3.58E-06 3.64E-06 3.73E-06 0.000

mg/dscm 5.26E-05 4.92E-05 4.97E-05 0.000

Compound: Cadmium

Average

RunNumber 1 2 3 

Mass_mg 0.0002 0.0002 0.0002 0.000

Elb/hr 3.58E-06 3.64E-06 3.73E-06 0.000

Tuesday, January 11, 2011 Page 8 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

mg/dscm 5.26E-05 4.92E-05 4.97E-05 0.000

Compound: Chromium

Average

RunNumber 1 2 3 

Mass_mg 0.00512 0.00149 0.011 0.006

Elb/hr 9.16E-05 2.71E-05 2.05E-04 0.000

mg/dscm 1.35E-03 3.67E-04 2.73E-03 0.001

Compound: Cobalt

Average

RunNumber 1 2 3 

Mass_mg 0.00031 0.0002 0.00028 0.000

Elb/hr 5.55E-06 3.64E-06 5.23E-06 0.000

mg/dscm 8.15E-05 4.92E-05 6.96E-05 0.000

Compound: Filterable Particulate

Average

RunNumber 1 2 3 

Mass_mg 7.8 4.8 11.4 8.000

Elb/hr 1.40E-01 8.73E-02 2.13E-01 0.147

mg/dscm 2.05E+00 1.18E+00 2.83E+00 2.020

Compound: Lead

Average

RunNumber 1 2 3 

Mass_mg 0.00329 0.0016 0.00293 0.003

Elb/hr 5.89E-05 2.91E-05 5.47E-05 0.000

mg/dscm 8.65E-04 3.94E-04 7.28E-04 0.001

Compound: Manganese

Average

RunNumber 1 2 3 

Mass_mg 0.0021 0.0016 0.0035 0.002

Elb/hr 3.76E-05 2.91E-05 6.53E-05 0.000

mg/dscm 5.52E-04 3.94E-04 8.69E-04 0.001

Compound: Nickel

Average

RunNumber 1 2 3 

Mass_mg 0.01155 0.00165 0.00815 0.007

Elb/hr 2.07E-04 3.00E-05 1.52E-04 0.000

mg/dscm 3.04E-03 4.06E-04 2.02E-03 0.002

Compound: Selenium

Average

RunNumber 1 2 3 

Mass_mg 0.002 0.0032 0.002 0.002

Elb/hr 3.58E-05 5.82E-05 3.73E-05 0.000

mg/dscm 5.26E-04 7.88E-04 4.97E-04 0.001

Location: EPN 21 - OTM - 27/28

Tuesday, January 11, 2011 Page 9 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Compound: Filterable PM2.5

Average

RunNumber 1 2 3 

Mass_mg 2.8 1.5 7.6 3.967

Elb/hr 9.68E-02 5.23E-02 2.67E-01 0.139

mg/dscm 1.34E+00 7.22E-01 3.72E+00 1.927

Compound: Inorganic (Aqueous) Condensible P

Average

RunNumber 1 2 3 

Mass_mg 7.5 2.4 1.3 3.733

Elb/hr 2.59E-01 8.37E-02 4.56E-02 0.129

mg/dscm 3.60E+00 1.15E+00 6.37E-01 1.796

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3 

Mass_mg 1.7 1 1 1.233

Elb/hr 5.88E-02 3.49E-02 3.51E-02 0.043

mg/dscm 8.15E-01 4.81E-01 4.90E-01 0.595

Compound: Total PM2.5

Average

RunNumber 1 2 3 

Mass_mg 12 4.9 9.9 8.933

Elb/hr 4.15E-01 1.71E-01 3.47E-01 0.311

mg/dscm 5.75E+00 2.36E+00 4.85E+00 4.320

Tuesday, January 11, 2011 Page 10 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Process Run Data

APCD Run Data

Process Lab Run Data

Run Name Value UOM Comments

Target

Value

1 0 0

Run Name Value UOM Comments

1 0

1 0

Tuesday, January 11, 2011 Page 11 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Sampling / Stack Data Results Detail

Location EPN 21 - Method 0061

Average

Run Number 1 2 3 

Test Date 9/14/2010 9/15/2010 9/15/2010 

Run Start Time 3:23:00 PM 9:54:00 AM 2:16:00 PM 

Run Finish Time 7:36:00 PM 1:58:00 PM 6:19:00 PM 

Net Traversing Points 48 48 48 

Net Run Time, minutes 240 240 240 

Nozzle Diameter, inches 0.326 0.326 0.326 0.326

Pitot Tube Coefficient 0.81 0.81 0.806 0.809

Dry Gas Meter Calibration Factor 0.99 0.99 0.99 0.990

Barometric Pressure, inches of Mercury 29.34 29.36 29.34 29.347

Average Orifice Meter Differential, inches H2O 1.59 1.59 1.58 1.587

Dry Gas Meter Volume Sampled, cubic feet 176.821 180.749 182.066 179.879

Average Dry Gas Meter Temperature, °F 84.21 80.27 84.00 82.827

Dry Gas Meter Volume Sampled, dscf 167.210 172.288 172.232 170.577

Total Moisture Liquid collected, g 144.3 151.7 129 141.667

Volume of Water Vapor, standard cubic feet 6.79 7.14 6.07 6.667

Moisture Content of Stack Gas, % 3.90 3.98 3.40 3.760

Moisture Saturation at Stack Gas Temperature, % 54.73 56.03 55.79 55.517

Dry Mole Fraction 0.961 0.9602 0.966 0.962

Carbon Dioxide, % 0.8 0.5 0.7 0.667

Oxygen, % 20.2 20.7 20.5 20.467

Carbon Monoxide & Nitrogen, % 79 78.8 78.8 78.867

Fuel Factor 0.88 0.40 0.57 

Dry Molecular Weight, lb/lb-Mole 28.94 28.91 28.93 28.927

Wet Molecular weight, lb/lb-Mole 28.51 28.48 28.56 28.517

Flue Gas Static Pressure, inches of H2O -17 -17 -17 -17.000

Absolute Flue Gas Pressure, inches of Mercury 28.09 28.11 28.09 28.097

Average Stack Gas Temperature, °F 180.33 181.42 181.19 180.980

Average Velocity Head, inches of H2O 0.2199214245

80349

0.204648134

421969

0.2038153255

86187

0.209

Average Stack Gas Velocity, feet/second 29.04 28.04 27.81 28.297

Stack Cross-Sectional Area, square feet 14.677 14.677 14.677 14.677

Dry Volumetric Flow Rate, dry scfm 19,025.2 18,336.6 18,289.6 18,550.467

Actual Wet Volumetric Flue Gas Flow Rate, acfm 25,573.2 24,692.6 24,490.0 24,918.600

Percent Isokinetic of Sampling Rate, % 92.7 99.1 99.4 97.067

Percent Excess Air, % 3,079.3 20,058.1 6,761.2 9,966.200

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Round Duct Diameter, inches 51.875 51.875 51.875 

Rectangular Duct Width, inches 0 0 0 

Rectangular Duct Length, inches 0 0 0 

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 11, 2011 Page 12 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Location EPN 21 - Method 26A

Average

Run Number 1 2 3 

Test Date 9/14/2010 9/14/2010 9/14/2010 

Run Start Time 10:12:00 AM 12:04:00 PM 1:42:00 PM 

Run Finish Time 11:24:00 AM 1:18:00 PM 2:55:00 PM 

Net Traversing Points 16 16 16 

Net Run Time, minutes 64 64 64 

Nozzle Diameter, inches 0.317 0.317 0.317 0.317

Pitot Tube Coefficient 0.806 0.806 0.806 0.806

Dry Gas Meter Calibration Factor 1.009 1.009 1.009 1.009

Barometric Pressure, inches of Mercury 29.42 29.42 29.42 29.420

Average Orifice Meter Differential, inches H2O 1.61 1.65 1.57 1.610

Dry Gas Meter Volume Sampled, cubic feet 44.360 48.890 48.610 47.287

Average Dry Gas Meter Temperature, °F 76.09 79.84 82.41 79.447

Dry Gas Meter Volume Sampled, dscf 43.522 47.637 47.131 46.097

Total Moisture Liquid collected, g 55.3 43.8 48 49.033

Volume of Water Vapor, standard cubic feet 2.60 2.06 2.26 2.307

Moisture Content of Stack Gas, % 5.64 4.15 4.58 4.790

Moisture Saturation at Stack Gas Temperature, % 58.46 60.08 59.26 59.267

Dry Mole Fraction 0.9436 0.9585 0.9542 0.952

Carbon Dioxide, % 0.4 0.5 0.5 0.467

Oxygen, % 20.3 20.8 20.8 20.633

Carbon Monoxide & Nitrogen, % 79.3 78.7 78.7 78.900

Fuel Factor 1.50 0.20 0.20 

Dry Molecular Weight, lb/lb-Mole 28.88 28.91 28.91 28.900

Wet Molecular weight, lb/lb-Mole 28.27 28.46 28.41 28.380

Flue Gas Static Pressure, inches of H2O -17 -17 -17 -17.000

Absolute Flue Gas Pressure, inches of Mercury 28.17 28.17 28.17 28.170

Average Stack Gas Temperature, °F 183.44 184.69 184.06 184.063

Average Velocity Head, inches of H2O 0.2202582039

84221

0.227473658

336838

0.2163443403

70814

0.221

Average Stack Gas Velocity, feet/second 29.07 29.47 28.75 29.097

Stack Cross-Sectional Area, square feet 14.677 14.677 14.677 14.677

Dry Volumetric Flow Rate, dry scfm 18,662.6 19,180.9 18,646.6 18,830.033

Actual Wet Volumetric Flue Gas Flow Rate, acfm 25,599.6 25,951.9 25,317.8 25,623.100

Percent Isokinetic of Sampling Rate, % 97.6 103.9 105.8 102.433

Percent Excess Air, % 3,195.8 -89,655.2 -89,655.2 -58,704.867

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Round Duct Diameter, inches 51.875 51.875 51.875 

Rectangular Duct Width, inches 0 0 0 

Rectangular Duct Length, inches 0 0 0 

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 11, 2011 Page 13 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Location EPN 21 - Method 29

Average

Run Number 1 2 3 

Test Date 9/14/2010 9/15/2010 9/15/2010 

Run Start Time 3:38:00 PM 9:54:00 AM 2:24:00 PM 

Run Finish Time 7:10:00 PM 1:37:00 PM 6:00:00 PM 

Net Traversing Points 48 48 48 

Net Run Time, minutes 192 192 192 

Nozzle Diameter, inches 0.317 0.317 0.317 0.317

Pitot Tube Coefficient 0.808 0.808 0.807 0.808

Dry Gas Meter Calibration Factor 1.009 1.009 1.009 1.009

Barometric Pressure, inches of Mercury 29.34 29.36 29.34 29.347

Average Orifice Meter Differential, inches H2O 1.47 1.69 1.74 1.633

Dry Gas Meter Volume Sampled, cubic feet 139.547 146.985 146.788 144.440

Average Dry Gas Meter Temperature, °F 84.44 77.82 81.69 81.317

Dry Gas Meter Volume Sampled, dscf 134.397 143.480 142.185 140.021

Total Moisture Liquid collected, g 119.1 98.7 112.9 110.233

Volume of Water Vapor, standard cubic feet 5.61 4.65 5.31 5.190

Moisture Content of Stack Gas, % 4.01 3.14 3.60 3.583

Moisture Saturation at Stack Gas Temperature, % 64.57 52.76 43.19 53.507

Dry Mole Fraction 0.9599 0.9686 0.964 0.964

Carbon Dioxide, % 0.8 0.5 0.7 0.667

Oxygen, % 20.2 20.7 20.5 20.467

Carbon Monoxide & Nitrogen, % 79 78.8 78.8 78.867

Fuel Factor 0.88 0.40 0.57 

Dry Molecular Weight, lb/lb-Mole 28.94 28.91 28.93 28.927

Wet Molecular weight, lb/lb-Mole 28.50 28.57 28.54 28.537

Flue Gas Static Pressure, inches of H2O -17 -17 -17 -17.000

Absolute Flue Gas Pressure, inches of Mercury 28.09 28.11 28.09 28.097

Average Stack Gas Temperature, °F 187.88 178.71 169.85 178.813

Average Velocity Head, inches of H2O 0.2047056492

70905

0.233917321

947419

0.2411830603

68968

0.227

Average Stack Gas Velocity, feet/second 28.12 29.79 30.03 29.313

Stack Cross-Sectional Area, square feet 14.677 14.677 14.677 14.677

Dry Volumetric Flow Rate, dry scfm 18,186.9 19,734.8 20,063.6 19,328.433

Actual Wet Volumetric Flue Gas Flow Rate, acfm 24,763.0 26,233.7 26,445.0 25,813.900

Percent Isokinetic of Sampling Rate, % 103.1 101.4 98.8 101.100

Percent Excess Air, % 3,079.3 20,058.1 6,761.2 9,966.200

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Round Duct Diameter, inches 51.875 51.875 51.875 

Rectangular Duct Width, inches 0 0 0 

Rectangular Duct Length, inches 0 0 0 

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 11, 2011 Page 14 of 15
Johns Manville Cleburne Texas Residual Risk Data Emissions Test

Location EPN 21 - OTM - 27/28

Average

Run Number 1 2 3 

Test Date 9/15/2010 9/16/2010 9/16/2010 

Run Start Time 6:30:00 PM 7:55:00 AM 11:51:00 AM 

Run Finish Time 9:47:00 PM 11:12:00 AM 3:08:00 PM 

Net Traversing Points 16 16 16 

Net Run Time, minutes 193 195.3 192 

Nozzle Diameter, inches 0.22 0.22 0.22 0.220

Pitot Tube Coefficient 0.808 0.808 0.808 0.808

Dry Gas Meter Calibration Factor 1.009 1.009 1.006 1.008

Barometric Pressure, inches of Mercury 29.4 29.32 29.34 29.353

Average Orifice Meter Differential, inches H2O 0.47 0.47 0.47 0.470

Dry Gas Meter Volume Sampled, cubic feet 76.130 74.960 74.490 75.193

Average Dry Gas Meter Temperature, °F 81.69 73.59 78.50 77.927

Dry Gas Meter Volume Sampled, dscf 73.659 73.428 72.136 73.074

Total Moisture Liquid collected, g 50.3 61.8 49.1 53.733

Volume of Water Vapor, standard cubic feet 2.37 2.91 2.31 2.530

Moisture Content of Stack Gas, % 3.12 3.81 3.10 3.343

Moisture Saturation at Stack Gas Temperature, % 52.59 55.67 67.87 58.710

Dry Mole Fraction 0.9688 0.9619 0.969 0.967

Carbon Dioxide, % 0.6 0.8 0.8 0.733

Oxygen, % 20.6 20.4 20.4 20.467

Carbon Monoxide & Nitrogen, % 78.8 78.8 78.8 78.800

Fuel Factor 0.50 0.63 0.63 

Dry Molecular Weight, lb/lb-Mole 28.92 28.94 28.94 28.933

Wet Molecular weight, lb/lb-Mole 28.58 28.52 28.60 28.567

Flue Gas Static Pressure, inches of H2O -17 -17 -17 -17.000

Absolute Flue Gas Pressure, inches of Mercury 28.15 28.07 28.09 28.103

Average Stack Gas Temperature, °F 178.63 181.06 190.19 183.293

Average Velocity Head, inches of H2O 0.2222546436

24922

0.228901418

267701

0.2239561535

60164

0.225

Average Stack Gas Velocity, feet/second 29.01 29.57 29.41 29.330

Stack Cross-Sectional Area, square feet 14.677 14.677 14.677 14.677

Dry Volumetric Flow Rate, dry scfm 19,251.8 19,354.7 19,133.4 19,246.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 25,546.8 26,039.9 25,899.0 25,828.567

Percent Isokinetic of Sampling Rate, % 110.2 108.0 109.2 109.133

Percent Excess Air, % 10,137.8 5,059.5 5,059.5 6,752.267

F-Factor, dscfm/MMBtu @ %O2 0 0 0 0.000

Round Duct Diameter, inches 51.875 51.875 51.875 

Rectangular Duct Width, inches 0 0 0 

Rectangular Duct Length, inches 0 0 0 

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Tuesday, January 11, 2011 Page 15 of 15