Name: Jim Lovell

Title: VP - Manufacturing

Company: Industrial Insulation Group, LLC

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

Industrial Insulation Group LLC Phenix City, Alabama Residual Risk 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.

Friday, January 28, 2011 Page 1 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Facility Information:

Industrial Insulation Group LLC - Phenix C

908 John Bussey Drive

Phenix City AL 36869

Contact: Jessie Payne

Phone: 713-657-0152

Fax: 334-298-5429

Email: paynej@iig-llc.com

Testing Company:

BT Environmental Consulting INC

2615 Wolcott St

Ferndale MI 48220

Contact:Barry Boulianne

Phone: 248-548-8072

Fax:

Email: BBoulianne@btecinc.com

Air Permit Number:

0125040021

Permitted Source ID/Name:

Cupola

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:

Basalt, dolomite, and limestone are fed to a coke-fired cupola furnace and melted to be formed into mineral wool. 

Emissions from this cupola are exhausted through a baghouse, a regenerative thermal oxidizer and a single exhaust 

stack (Stack 101). The stack is 8.5 feet in diameter and is equipped with four test ports, each six inches in diameter.

After being formed into mineral wool, the mat is fed through curing ovens where the mineral wool resin reaction is 

cured. Emissions from the curing ovens are exhausted through a filterhouse, an afterburner, and a single exhaust 

stack (Stack 102). This stack is 26 inches in diameter.

Industry/SCC/NAIS 327993

Sampling Location Information:

Test Parameter Information:

AFS #: FRS #: 110000369770

SCC / Description 30501299 Industrial Processes - Mineral Products - Fiberglass Manufacturing - Other Not 

Classified 

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

Cupola 102.756 0 0 2 0 0 0 12

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

Cupola Chromium 0061 3 180 0

Cupola Hydrogen Chloride Method 26A 3 60 0

Cupola Hydrogen Fluoride Method 26A 3 60 0

Friday, January 28, 2011 Page 2 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk 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.

Organic Condensible 

Particulate

Cupola OTM - 27/28 3 194 0

Inorganic (Aqueous) 

Condensible Part.

Cupola OTM - 27/28 3 194 0

Cupola Total PM2.5 OTM - 27/28 3 194 0

Cupola Filterable PM2.5 OTM - 27/28 3 194 0

Cupola Chromium Method 29 3 192 0

Cupola Filterable Particulate Method 29 3 192 0

Cupola Antimony Method 29 3 192 0

Cupola Arsenic Method 29 3 192 0

Cupola Cadmium Method 29 3 192 0

Cupola Cobalt Method 29 3 192 0

Cupola Lead Method 29 3 192 0

Cupola Manganese Method 29 3 192 0

Cupola Nickel Method 29 3 192 0

Cupola Selenium Method 29 3 192 0

Cupola Beryllium Method 29 3 192 0

Friday, January 28, 2011 Page 3 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Sampling / Stack Data Results Summary

Location Cupola - 0061

Average

Run Number 1 2 3 

Test Date 10/27/2010 10/28/2010 10/28/2010 

Run Start Time 12:30:00 PM 9:15:00 

AM

12:40:00 PM 

Run Finish Time 3:40:00 PM 12:21:00 

PM

3:45:00 PM 

Net Run Time, minutes 180 180 180 

Dry Gas Meter Volume Sampled, dscf 130.928 132.586 130.528 131.347

Moisture Content of Stack Gas, % 4.49 4.60 4.58 4.557

Moisture Saturation at Stack Gas Temperature, % 77.71 56.76 56.04 63.503

Carbon Dioxide, % 1.01 1.12 1.13 1.087

Oxygen, % 19.84 19.76 19.76 19.787

Average Stack Gas Temperature, °F 199.31 184.86 184.31 189.493

Dry Volumetric Flow Rate, dry scfm 89,476.3 89,448.7 88,143.2 89,022.733

Actual Wet Volumetric Flue Gas Flow Rate, acfm 117,688.9 114,475.4 112,609.5 114,924.600

Percent Isokinetic of Sampling Rate, % 100.0 101.3 101.2 100.833

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

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, January 28, 2011 Page 4 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Location Cupola - Method 26A

Average

Run Number 1 2 3 

Test Date 10/26/2010 10/27/2010 10/27/2010 

Run Start Time 6:01:00 PM 12:30:00 

PM

2:45:00 PM 

Run Finish Time 7:08:00 PM 2:40:00 PM 3:48:00 PM 

Net Run Time, minutes 60 60 60 

Dry Gas Meter Volume Sampled, dscf 41.920 43.796 42.743 42.820

Moisture Content of Stack Gas, % 4.60 5.34 5.06 5.000

Moisture Saturation at Stack Gas Temperature, % 48.69 86.78 89.83 75.100

Carbon Dioxide, % 0.9 1.01 1.01 0.973

Oxygen, % 19.8 19.84 19.84 19.827

Average Stack Gas Temperature, °F 177.25 204.67 206.25 196.057

Dry Volumetric Flow Rate, dry scfm 90,528.5 90,082.6 89,922.7 90,177.933

Actual Wet Volumetric Flue Gas Flow Rate, acfm 116,237.6 120,522.3 120,522.3 119,094.067

Percent Isokinetic of Sampling Rate, % 103.9 109.1 106.7 106.567

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

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, January 28, 2011 Page 5 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Location Cupola - Method 29

Average

Run Number 1 2 3 

Test Date 10/26/2010 10/26/2010 10/27/2010 

Run Start Time 10:10:00 AM 12:31:00 

PM

8:05:00 AM 

Run Finish Time 1:27:00 PM 5:36:00 PM 11:56:00 AM 

Net Run Time, minutes 192 192 192 

Dry Gas Meter Volume Sampled, dscf 129.140 129.657 133.934 130.910

Moisture Content of Stack Gas, % 4.80 4.35 5.01 4.720

Moisture Saturation at Stack Gas Temperature, % 62.97 50.50 82.81 65.427

Carbon Dioxide, % 0.96 0.87 1.01 0.947

Oxygen, % 19.78 19.73 19.62 19.710

Average Stack Gas Temperature, °F 189.17 178.85 202.48 190.167

Dry Volumetric Flow Rate, dry scfm 89,180.5 91,041.8 89,992.6 90,071.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 116,341.3 116,963.3 119,347.4 117,550.667

Percent Isokinetic of Sampling Rate, % 101.6 99.9 104.4 101.967

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

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Location Cupola - OTM - 27/28

Average

Run Number 1 2 3 

Test Date 10/26/2010 10/26/2010 10/27/2010 

Run Start Time 10:10:00 AM 2:15:00 PM 8:37:00 AM 

Run Finish Time 1:28:00 PM 5:39:00 PM 11:56:00 AM 

Net Run Time, minutes 194.8 194.8 191.3 

Dry Gas Meter Volume Sampled, dscf 72.268 73.754 72.639 72.887

Moisture Content of Stack Gas, % 4.86 4.54 4.26 4.553

Moisture Saturation at Stack Gas Temperature, % 67.37 64.33 80.63 70.777

Carbon Dioxide, % 0.96 0.87 1.01 0.947

Oxygen, % 19.78 19.73 19.62 19.710

Average Stack Gas Temperature, °F 192.33 190.17 201.17 194.557

Dry Volumetric Flow Rate, dry scfm 91,379.4 92,495.2 91,720.4 91,865.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 119,865.7 120,522.3 120,487.7 120,291.900

Percent Isokinetic of Sampling Rate, % 95.4 96.2 97.3 96.300

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

Fw 0 0 0 0.000

Fc 0 0 0 0.000

Friday, January 28, 2011 Page 6 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Friday, January 28, 2011 Page 7 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Emissions Summary

Location: Cupola - 0061

Compound: Chromium

Average

RunNumber 1 2 3 

Mass_mg 0.00152 0.0004 0.0004 0.001

Elb/hr 1.37E-04 3.57E-05 3.57E-05 0.000

mg/dscm 4.10E-04 1.07E-04 1.08E-04 0.000

Location: Cupola - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3 

Mass_mg 0.23 0.2 0.2 0.210

Elb/hr 6.57E-02 5.44E-02 5.57E-02 0.059

mg/dscm 1.94E-01 1.61E-01 1.65E-01 0.173

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3 

Mass_mg 0.38 0.2 0.2 0.260

Elb/hr 1.09E-01 5.44E-02 5.57E-02 0.073

mg/dscm 3.20E-01 1.61E-01 1.65E-01 0.215

Location: Cupola - Method 29

Compound: Antimony

Average

RunNumber 1 2 3 

Mass_mg 0.0008 0.0008 0.0008 0.001

Elb/hr 7.31E-05 7.43E-05 7.11E-05 0.000

mg/dscm 2.19E-04 2.18E-04 2.11E-04 0.000

Compound: Arsenic

Average

RunNumber 1 2 3 

Mass_mg 0.0008 0.0008 0.0008 0.001

Elb/hr 7.31E-05 7.43E-05 7.11E-05 0.000

mg/dscm 2.19E-04 2.18E-04 2.11E-04 0.000

Compound: Beryllium

Average

RunNumber 1 2 3 

Mass_mg 0.0002 0.0002 0.0002 0.000

Elb/hr 1.83E-05 1.86E-05 1.78E-05 0.000

mg/dscm 5.47E-05 5.45E-05 5.27E-05 0.000

Compound: Cadmium

Average

RunNumber 1 2 3 

Mass_mg 0.00139 0.00601 0.00026 0.003

Elb/hr 1.27E-04 5.58E-04 2.31E-05 0.000

Friday, January 28, 2011 Page 8 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

mg/dscm 3.80E-04 1.64E-03 6.86E-05 0.001

Compound: Chromium

Average

RunNumber 1 2 3 

Mass_mg 0.0045 0.0035 0.0017 0.003

Elb/hr 4.11E-04 3.25E-04 1.51E-04 0.000

mg/dscm 1.23E-03 9.53E-04 4.48E-04 0.001

Compound: Cobalt

Average

RunNumber 1 2 3 

Mass_mg 0.00276 0.00361 0.00076 0.002

Elb/hr 2.52E-04 3.35E-04 6.75E-05 0.000

mg/dscm 7.55E-04 9.83E-04 2.00E-04 0.001

Compound: Filterable Particulate

Average

RunNumber 1 2 3 

Mass_mg 39.1 22.7 49.7 37.167

Elb/hr 3.57E+00 2.11E+00 4.42E+00 3.367

mg/dscm 1.07E+01 6.18E+00 1.31E+01 9.993

Compound: Lead

Average

RunNumber 1 2 3 

Mass_mg 0.0065 0.0204 0.0015 0.009

Elb/hr 5.94E-04 1.89E-03 1.33E-04 0.001

mg/dscm 1.78E-03 5.56E-03 3.96E-04 0.003

Compound: Manganese

Average

RunNumber 1 2 3 

Mass_mg 0.0036 0.0049 0.0015 0.003

Elb/hr 3.29E-04 4.55E-04 1.33E-04 0.000

mg/dscm 9.85E-04 1.33E-03 3.96E-04 0.001

Compound: Nickel

Average

RunNumber 1 2 3 

Mass_mg 0.0054 0.0079 0.0048 0.006

Elb/hr 4.93E-04 7.34E-04 4.27E-04 0.001

mg/dscm 1.48E-03 2.15E-03 1.27E-03 0.002

Compound: Selenium

Average

RunNumber 1 2 3 

Mass_mg 0.0155 0.015 0.0219 0.017

Elb/hr 1.42E-03 1.39E-03 1.95E-03 0.002

mg/dscm 4.24E-03 4.09E-03 5.78E-03 0.005

Location: Cupola - OTM - 27/28

Friday, January 28, 2011 Page 9 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Compound: Filterable PM2.5

Average

RunNumber 1 2 3 

Mass_mg 33.4 24.7 43.8 33.967

Elb/hr 5.59E+00 4.10E+00 7.32E+00 5.670

mg/dscm 1.63E+01 1.18E+01 2.13E+01 16.467

Compound: Inorganic (Aqueous) Condensible P

Average

RunNumber 1 2 3 

Mass_mg 39 47 49 45.000

Elb/hr 6.52E+00 7.80E+00 8.18E+00 7.500

mg/dscm 1.91E+01 2.25E+01 2.38E+01 21.800

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3 

Mass_mg 1.7 3.5 1.7 2.300

Elb/hr 2.84E-01 5.81E-01 2.84E-01 0.383

mg/dscm 8.31E-01 1.68E+00 8.27E-01 1.113

Compound: Total PM2.5

Average

RunNumber 1 2 3 

Mass_mg 74.1 75.2 94.5 81.267

Elb/hr 1.24E+01 1.25E+01 1.58E+01 13.567

mg/dscm 3.62E+01 3.60E+01 4.59E+01 39.367

Friday, January 28, 2011 Page 10 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Process Run Data

APCD Run Data

Process Lab Run Data

Friday, January 28, 2011 Page 11 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Sampling / Stack Data Results Detail

Location Cupola - 0061

Average

Run Number 1 2 3 

Test Date 10/27/2010 10/28/2010 10/28/2010 

Run Start Time 12:30:00 PM 9:15:00 AM 12:40:00 PM 

Run Finish Time 3:40:00 PM 12:21:00 PM 3:45:00 PM 

Net Traversing Points 36 36 36 

Net Run Time, minutes 180 180 180 

Nozzle Diameter, inches 0.293 0.293 0.293 0.293

Pitot Tube Coefficient 0.805 0.805 0.805 0.805

Dry Gas Meter Calibration Factor 1.011 1.011 1.011 1.011

Barometric Pressure, inches of Mercury 29.73 29.92 29.94 29.863

Average Orifice Meter Differential, inches H2O 1.44 1.40 1.35 1.397

Dry Gas Meter Volume Sampled, cubic feet 133.725 133.124 131.869 132.906

Average Dry Gas Meter Temperature, °F 83.68 77.82 81.44 80.980

Dry Gas Meter Volume Sampled, dscf 130.928 132.586 130.528 131.347

Total Moisture Liquid collected, g 130.7 135.9 133.2 133.267

Volume of Water Vapor, standard cubic feet 6.15 6.40 6.27 6.273

Moisture Content of Stack Gas, % 4.49 4.60 4.58 4.557

Moisture Saturation at Stack Gas Temperature, % 77.71 56.76 56.04 63.503

Dry Mole Fraction 0.9551 0.954 0.9542 0.954

Carbon Dioxide, % 1.01 1.12 1.13 1.087

Oxygen, % 19.84 19.76 19.76 19.787

Carbon Monoxide & Nitrogen, % 79.15 79.12 79.11 79.127

Fuel Factor 1.05 1.02 1.01 

Dry Molecular Weight, lb/lb-Mole 28.96 28.97 28.97 28.967

Wet Molecular weight, lb/lb-Mole 28.47 28.47 28.47 28.470

Flue Gas Static Pressure, inches of H2O 0.2 0.2 0.2 0.200

Absolute Flue Gas Pressure, inches of Mercury 29.74 29.93 29.95 29.873

Average Stack Gas Temperature, °F 199.31 184.86 184.31 189.493

Average Velocity Head, inches of H2O 0.3145294579

23245

0.306183384

871847

0.2968255418

54279

0.306

Average Stack Gas Velocity, feet/second 34.06 33.13 32.59 33.260

Stack Cross-Sectional Area, square feet 57.589 57.589 57.589 57.589

Dry Volumetric Flow Rate, dry scfm 89,476.3 89,448.7 88,143.2 89,022.733

Actual Wet Volumetric Flue Gas Flow Rate, acfm 117,688.9 114,475.4 112,609.5 114,924.600

Percent Isokinetic of Sampling Rate, % 100.0 101.3 101.2 100.833

Percent Excess Air, % 1,879.5 1,752.3 1,756.4 1,796.067

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

Round Duct Diameter, inches 102.756 102.756 102.756 

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

Friday, January 28, 2011 Page 12 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Location Cupola - Method 26A

Average

Run Number 1 2 3 

Test Date 10/26/2010 10/27/2010 10/27/2010 

Run Start Time 6:01:00 PM 12:30:00 PM 2:45:00 PM 

Run Finish Time 7:08:00 PM 2:40:00 PM 3:48:00 PM 

Net Traversing Points 12 12 12 

Net Run Time, minutes 60 60 60 

Nozzle Diameter, inches 0.28 0.28 0.28 0.280

Pitot Tube Coefficient 0.805 0.805 0.805 0.805

Dry Gas Meter Calibration Factor 1.013 1.013 1.013 1.013

Barometric Pressure, inches of Mercury 29.46 29.73 29.66 29.617

Average Orifice Meter Differential, inches H2O 1.23 1.36 1.36 1.317

Dry Gas Meter Volume Sampled, cubic feet 43.761 44.959 44.356 44.359

Average Dry Gas Meter Temperature, °F 91.46 87.42 92.08 90.320

Dry Gas Meter Volume Sampled, dscf 41.920 43.796 42.743 42.820

Total Moisture Liquid collected, g 42.9 52.5 48.5 47.967

Volume of Water Vapor, standard cubic feet 2.02 2.47 2.28 2.257

Moisture Content of Stack Gas, % 4.60 5.34 5.06 5.000

Moisture Saturation at Stack Gas Temperature, % 48.69 86.78 89.83 75.100

Dry Mole Fraction 0.954 0.9466 0.9494 0.950

Carbon Dioxide, % 0.9 1.01 1.01 0.973

Oxygen, % 19.8 19.84 19.84 19.827

Carbon Monoxide & Nitrogen, % 79.3 79.15 79.15 79.200

Fuel Factor 1.22 1.05 1.05 

Dry Molecular Weight, lb/lb-Mole 28.94 28.96 28.96 28.953

Wet Molecular weight, lb/lb-Mole 28.44 28.37 28.41 28.407

Flue Gas Static Pressure, inches of H2O 0.3 0.2 0.2 0.233

Absolute Flue Gas Pressure, inches of Mercury 29.48 29.74 29.67 29.630

Average Stack Gas Temperature, °F 177.25 204.67 206.25 196.057

Average Velocity Head, inches of H2O 0.3143860064

97181

0.326077621

814162

0.3249308960

58

0.322

Average Stack Gas Velocity, feet/second 33.64 34.88 34.88 34.467

Stack Cross-Sectional Area, square feet 57.589 57.589 57.589 57.589

Dry Volumetric Flow Rate, dry scfm 90,528.5 90,082.6 89,922.7 90,177.933

Actual Wet Volumetric Flue Gas Flow Rate, acfm 116,237.6 120,522.3 120,522.3 119,094.067

Percent Isokinetic of Sampling Rate, % 103.9 109.1 106.7 106.567

Percent Excess Air, % 1,744.2 1,879.5 1,879.5 1,834.400

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

Round Duct Diameter, inches 102.756 102.756 102.756 

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

Friday, January 28, 2011 Page 13 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Location Cupola - Method 29

Average

Run Number 1 2 3 

Test Date 10/26/2010 10/26/2010 10/27/2010 

Run Start Time 10:10:00 AM 12:31:00 PM 8:05:00 AM 

Run Finish Time 1:27:00 PM 5:36:00 PM 11:56:00 AM 

Net Traversing Points 48 48 48 

Net Run Time, minutes 192 192 192 

Nozzle Diameter, inches 0.28 0.28 0.28 0.280

Pitot Tube Coefficient 0.805 0.805 0.805 0.805

Dry Gas Meter Calibration Factor 1.013 1.013 1.013 1.013

Barometric Pressure, inches of Mercury 29.6 29.44 29.78 29.607

Average Orifice Meter Differential, inches H2O 1.21 1.24 1.24 1.230

Dry Gas Meter Volume Sampled, cubic feet 134.164 136.270 137.525 135.986

Average Dry Gas Meter Temperature, °F 91.38 94.84 88.31 91.510

Dry Gas Meter Volume Sampled, dscf 129.140 129.657 133.934 130.910

Total Moisture Liquid collected, g 138.3 125.4 149.9 137.867

Volume of Water Vapor, standard cubic feet 6.51 5.90 7.06 6.490

Moisture Content of Stack Gas, % 4.80 4.35 5.01 4.720

Moisture Saturation at Stack Gas Temperature, % 62.97 50.50 82.81 65.427

Dry Mole Fraction 0.952 0.9565 0.9499 0.953

Carbon Dioxide, % 0.96 0.87 1.01 0.947

Oxygen, % 19.78 19.73 19.62 19.710

Carbon Monoxide & Nitrogen, % 79.26 79.4 79.37 79.343

Fuel Factor 1.17 1.34 1.27 

Dry Molecular Weight, lb/lb-Mole 28.94 28.93 28.95 28.940

Wet Molecular weight, lb/lb-Mole 28.41 28.45 28.40 28.420

Flue Gas Static Pressure, inches of H2O 0.3 0.3 0.3 0.300

Absolute Flue Gas Pressure, inches of Mercury 29.62 29.46 29.80 29.627

Average Stack Gas Temperature, °F 189.17 178.85 202.48 190.167

Average Velocity Head, inches of H2O 0.3103517804

72928

0.317414476

562585

0.3217833935

70323

0.317

Average Stack Gas Velocity, feet/second 33.67 33.85 34.54 34.020

Stack Cross-Sectional Area, square feet 57.589 57.589 57.589 57.589

Dry Volumetric Flow Rate, dry scfm 89,180.5 91,041.8 89,992.6 90,071.633

Actual Wet Volumetric Flue Gas Flow Rate, acfm 116,341.3 116,963.3 119,347.4 117,550.667

Percent Isokinetic of Sampling Rate, % 101.6 99.9 104.4 101.967

Percent Excess Air, % 1,728.1 1,602.0 1,471.1 1,600.400

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

Round Duct Diameter, inches 102.756 102.756 102.756 

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

Friday, January 28, 2011 Page 14 of 15
Industrial Insulation Group LLC Phenix City, Alabama Residual Risk Emissions Test

Location Cupola - OTM - 27/28

Average

Run Number 1 2 3 

Test Date 10/26/2010 10/26/2010 10/27/2010 

Run Start Time 10:10:00 AM 2:15:00 PM 8:37:00 AM 

Run Finish Time 1:28:00 PM 5:39:00 PM 11:56:00 AM 

Net Traversing Points 12 12 12 

Net Run Time, minutes 194.8 194.8 191.3 

Nozzle Diameter, inches 0.212 0.212 0.212 0.212

Pitot Tube Coefficient 0.804 0.804 0.804 0.804

Dry Gas Meter Calibration Factor 1.011 1.011 1.011 1.011

Barometric Pressure, inches of Mercury 29.6 29.6 29.78 29.660

Average Orifice Meter Differential, inches H2O 0.40 0.40 0.40 0.400

Dry Gas Meter Volume Sampled, cubic feet 73.960 76.022 73.720 74.567

Average Dry Gas Meter Temperature, °F 81.00 84.88 79.75 81.877

Dry Gas Meter Volume Sampled, dscf 72.268 73.754 72.639 72.887

Total Moisture Liquid collected, g 78.4 74.5 68.7 73.867

Volume of Water Vapor, standard cubic feet 3.69 3.51 3.23 3.477

Moisture Content of Stack Gas, % 4.86 4.54 4.26 4.553

Moisture Saturation at Stack Gas Temperature, % 67.37 64.33 80.63 70.777

Dry Mole Fraction 0.9514 0.9546 0.9574 0.954

Carbon Dioxide, % 0.96 0.87 1.01 0.947

Oxygen, % 19.78 19.73 19.62 19.710

Carbon Monoxide & Nitrogen, % 79.26 79.4 79.37 79.343

Fuel Factor 1.17 1.34 1.27 

Dry Molecular Weight, lb/lb-Mole 28.94 28.93 28.95 28.940

Wet Molecular weight, lb/lb-Mole 28.41 28.43 28.48 28.440

Flue Gas Static Pressure, inches of H2O 0.3 0.3 0.2 0.267

Absolute Flue Gas Pressure, inches of Mercury 29.62 29.62 29.79 29.677

Average Stack Gas Temperature, °F 192.33 190.17 201.17 194.557

Average Velocity Head, inches of H2O 0.3285481472

92702

0.333608843

317495

0.3302379721

66414

0.331

Average Stack Gas Velocity, feet/second 34.69 34.88 34.87 34.813

Stack Cross-Sectional Area, square feet 57.589 57.589 57.589 57.589

Dry Volumetric Flow Rate, dry scfm 91,379.4 92,495.2 91,720.4 91,865.000

Actual Wet Volumetric Flue Gas Flow Rate, acfm 119,865.7 120,522.3 120,487.7 120,291.900

Percent Isokinetic of Sampling Rate, % 95.4 96.2 97.3 96.300

Percent Excess Air, % 1,728.1 1,602.0 1,471.1 1,600.400

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

Round Duct Diameter, inches 102.756 102.756 102.756 

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

Friday, January 28, 2011 Page 15 of 15