Final Test Report 

for

123958 Owens Corning Newark Section 114 Testing

Based on information and belief formed I have reviewed all testing details and 

after reasonable inquiry, I certify that the results in this test report and hereby 

statements and information in this test certify that the test report is authentic and

report are true, accurate, and complete. accurate.

/ /

Permitted Facility Representative / Date Testing Company Representative / 

Name: Mike Pettis Name: Mike Denomme

Title: ISB Environmental Leader Title: Project Manager

Company: Owens Corning Company: LEHDER Environmental

Sign Date: 28/02/2012 Sign Date: 27/02/2012

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123958 Owens Corning Newark Section 114 Testing

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Facility Information: Testing Company:

Owens Corning Newark Plant LEHDER Environmental Services

400 Case Avenue 704 Mara Street, Suite 210

Newark OH 43055 Point Edward ON N7V 1X4

Contact: Mark Arnold Contact:Mike Denomme

Phone: 740-328-2410 Phone: 519-336-4101

Fax: 740-328-2302 Fax: 519-336-4311

Email: mark.arnold@owenscorning.com Email: mdenomme@lehder.com

Industry/SCC/NAIS 327993 AFS #: 3908900006 FRS #: 110000498710

Air Permit Number: Permitted Source ID/Name:

145020185 28-94 A3 Furnace

Permitted Maximum Process Max. Normal Operation Process Target Process Test 

None

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

Furnace (Wool-type Fiber) 

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

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

or

Raw materials required to produceglass are mixed together as a batch and continuously charged into a refractorybricked, gas-fired, glass-melting furnace. A dry electrostatic precipitator (DEP) baghouse unit treats the effluent gases 

from the A3 Furnace.

Sampling Location Information:

 Round Duct Rect. Duct Equiv. Distance from Distance from Number of Min.Travers 

Location Diam. Length /Width Diam upstream dist. downstream dist. Traverse Ports Points

A3 Furnace 18.75 0 0 0 215 94 2 8

Test Parameter Information:

 Target Test Number of Test Run Sample 

Location Parameter Method Duration Points Comments

A3 Furnace Chromium Method 29 3 240 0

A3 Furnace Filterable Particulate Method 29 3 240 0

A3 Furnace Chromium Method 0061 3 240 0

A3 Furnace Hexavalent Chromium Method 0061 3 240 0

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.

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 process flow diagram: See LEHDER Report 123958

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Sampling / Stack Data Results 

Location A3 Furnace - Method 0061

Average

Run Number 1 2 3

Test Date 07/02/2012 08/02/2012 09/02/2012

Run Start Time 8:46:00 AM 8:16:00 AM 8:17:00 AM

Run Finish Time 12:56:00 12:25:00 12:23:00 

PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 181.156 178.092 180.637 179.962

Moisture Content of Stack Gas, % 3.54 4.25 3.78 3.857

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

Carbon Dioxide, % 2.1 2 2 2.033

Oxygen, % 17.7 17.7 18 17.800

Average Stack Gas Temperature, °F 254.08 249.52 252.94 252.180

Dry Volumetric Flow Rate, dry scfm 7,633.6 7,483.5 7,651.0 7,589.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 10,959.1 10,757.8 10,975.2 10,897.367

Percent Isokinetic of Sampling Rate, % 102.1 102.4 101.6 102.033

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

Fw 0 0 0 0.000

Fc 0 0 0 0.000

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Location A3 Furnace - Method 29

Average

Run Number 1 2 3

Test Date 07/02/2012 08/02/2012 09/02/2012

Run Start Time 8:45:00 AM 8:16:00 AM 8:16:00 AM

Run Finish Time 12:56:00 12:25:00 12:25:00 

PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 173.804 172.930 174.074 173.603

Moisture Content of Stack Gas, % 3.90 3.95 3.74 3.863

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

Carbon Dioxide, % 2.1 2 1.9 2.000

Oxygen, % 17.7 17.7 17.7 17.700

Average Stack Gas Temperature, °F 253.50 248.63 251.69 251.273

Dry Volumetric Flow Rate, dry scfm 7,407.6 7,405.4 7,502.1 7,438.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 10,665.8 10,599.1 10,738.3 10,667.733

Percent Isokinetic of Sampling Rate, % 100.9 100.5 99.8 100.400

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

Fw 0 0 0 0.000

Fc 0 0 0 0.000

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Emissions Summary

Location: A3 Furnace - Method 0061

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.136 0.192 0.238 1.89E-01

Elb/hr 7.58E-04 1.07E-03 1.33E-03 1.05E-03

mg/dscm 2.65E-02 3.81E-02 4.65E-02 3.70E-02

Compound: Hexavalent Chromium

Average

RunNumber 1 2 3

Mass_mg 0.128 0.203 0.235 1.89E-01

Elb/hr 7.13E-04 1.13E-03 1.32E-03 1.05E-03

mg/dscm 2.50E-02 4.03E-02 4.59E-02 3.71E-02

Location: A3 Furnace - Method 29

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.1477 0.2592 0.3614 2.56E-01

Elb/hr 8.33E-04 1.47E-03 2.06E-03 1.45E-03

mg/dscm 3.00E-02 5.29E-02 7.33E-02 5.21E-02

Compound: Filterable Particulate

Average

RunNumber 1 2 3

Mass_mg 29.7 44.1 63.8 4.59E+01

Elb/hr 1.67E-01 2.50E-01 3.64E-01 2.60E-01

mg/dscm 6.04E+00 9.01E+00 1.29E+01 9.32E+00

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Process Run Data

Target

Run Name Value UOM Value Comments

1 Material Processed 0 Tons/hr 0

APCD Run Data

Target

Run Name Value UOM Value Comments

1 ELECTROSTATIC PRECIPITATOR 22.7 KV 22 Run #1

2 ELECTROSTATIC PRECIPITATOR 22.5 KV 22 Run #2

3 ELECTROSTATIC PRECIPITATOR 23.6 KV 22 Run #3

Process Lab Run Data

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Sampling / Stack Data Results Detail

Location A3 Furnace - Method 0061

Average

Run Number 1 2 3

Test Date 07/02/2012 08/02/2012 09/02/2012

Run Start Time 8:46:00 AM 8:16:00 AM 8:17:00 AM

Run Finish Time 12:56:00 PM 12:25:00 12:23:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.1845 0.1845 0.1845 0.185

Pitot Tube Coefficient 0.843 0.843 0.843 0.843

Dry Gas Meter Calibration Factor 0.9919 0.9919 0.9919 0.992

Barometric Pressure, inches of Mercury 29.33 29.32 29.38 29.343

Average Orifice Meter Differential, inches H2O 1.55 1.50 1.57 1.540

Dry Gas Meter Volume Sampled, cubic feet 176.885 173.632 178.124 176.214

Average Dry Gas Meter Temperature, °F 43.24 42.25 49.11 44.867

Dry Gas Meter Volume Sampled, dscf 181.156 178.092 180.637 179.962

Total Moisture Liquid collected, g 141.3 167.9 150.9 153.367

Volume of Water Vapor, standard cubic feet 6.65 7.90 7.10 7.217

Moisture Content of Stack Gas, % 3.54 4.25 3.78 3.857

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

Dry Mole Fraction 0.9646 0.9575 0.9622 0.961

Carbon Dioxide, % 2.1 2 2 2.033

Oxygen, % 17.7 17.7 18 17.800

Carbon Monoxide & Nitrogen, % 80.2 80.3 80 80.167

Fuel Factor 1.52 1.60 1.45

Dry Molecular Weight, lb/lb-Mole 29.04 29.03 29.04 29.037

Wet Molecular weight, lb/lb-Mole 28.65 28.56 28.62 28.610

Flue Gas Static Pressure, inches of H2O -1.45 -1.45 -1.45 -1.450

Absolute Flue Gas Pressure, inches of Mercury 29.22 29.21 29.27 29.233

Average Stack Gas Temperature, °F 254.08 249.52 252.94 252.180

Average Velocity Head, inches of H2O 2.049355333 1.98035069 2.060019296 2.030

15963 37511 03793

Average Stack Gas Velocity, feet/second 95.28 93.53 95.42 94.743

Stack Cross-Sectional Area, square feet 1.917 1.917 1.917 1.917

Dry Volumetric Flow Rate, dry scfm 7,633.6 7,483.5 7,651.0 7,589.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 10,959.1 10,757.8 10,975.2 10,897.367

Percent Isokinetic of Sampling Rate, % 102.1 102.4 101.6 102.033

Percent Excess Air, % 509.7 505.8 576.9 530.800

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

Round Duct Diameter, inches 18.75 18.75 18.75

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

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Location A3 Furnace - Method 29

Average

Run Number 1 2 3

Test Date 07/02/2012 08/02/2012 09/02/2012

Run Start Time 8:45:00 AM 8:16:00 AM 8:16:00 AM

Run Finish Time 12:56:00 PM 12:25:00 12:25:00 PM

Net Traversing Points 48 48 48

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.1845 0.1845 0.1845 0.185

Pitot Tube Coefficient 0.824 0.824 0.824 0.824

Dry Gas Meter Calibration Factor 0.9991 0.9991 0.9991 0.999

Barometric Pressure, inches of Mercury 29.33 29.32 29.38 29.343

Average Orifice Meter Differential, inches H2O 1.76 1.76 1.82 1.780

Dry Gas Meter Volume Sampled, cubic feet 167.438 166.017 169.463 167.639

Average Dry Gas Meter Temperature, °F 40.38 38.47 46.58 41.810

Dry Gas Meter Volume Sampled, dscf 173.804 172.930 174.074 173.603

Total Moisture Liquid collected, g 150 151 143.7 148.233

Volume of Water Vapor, standard cubic feet 7.06 7.11 6.76 6.977

Moisture Content of Stack Gas, % 3.90 3.95 3.74 3.863

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

Dry Mole Fraction 0.961 0.9605 0.9626 0.961

Carbon Dioxide, % 2.1 2 1.9 2.000

Oxygen, % 17.7 17.7 17.7 17.700

Carbon Monoxide & Nitrogen, % 80.2 80.3 80.4 80.300

Fuel Factor 1.52 1.60 1.68

Dry Molecular Weight, lb/lb-Mole 29.04 29.03 29.01 29.027

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

Flue Gas Static Pressure, inches of H2O -1.45 -1.45 -1.45 -1.450

Absolute Flue Gas Pressure, inches of Mercury 29.22 29.21 29.27 29.233

Average Stack Gas Temperature, °F 253.50 248.63 251.69 251.273

Average Velocity Head, inches of H2O 2.030171927 2.01659883 2.065992318 2.038

56489 707764 13392

Average Stack Gas Velocity, feet/second 92.73 92.15 93.36 92.747

Stack Cross-Sectional Area, square feet 1.917 1.917 1.917 1.917

Dry Volumetric Flow Rate, dry scfm 7,407.6 7,405.4 7,502.1 7,438.367

Actual Wet Volumetric Flue Gas Flow Rate, acfm 10,665.8 10,599.1 10,738.3 10,667.733

Percent Isokinetic of Sampling Rate, % 100.9 100.5 99.8 100.400

Percent Excess Air, % 509.7 505.8 502.0 505.833

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

Round Duct Diameter, inches 18.75 18.75 18.75

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

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Included Attachments:

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