# 0 OWENS CORNING WAXAHACHIE, TEXAS EMISSIONS TESTING 

# V-1 Line, V-2 Line, and V-3 Line MACT Sampling October

1 through 5, 2002 / 

# \ File Number 02-1057 

# ( Prepared For: 

# Mr. Gary Chastain Owens Corning 3700 N. Interstate 35 East Waxahachie, Texas 75165-0837 Voice (972) 923-4360



# W ESTERN E NVIRONMENTAL S ERVICES AND T ESTING, INC. 913 Foster Road Casper, Wyoming 82601 Phone: (307) 234-5511 ToO-Free: (800) 545-5711 Fax: (307) 234-8324 E-mail: WEST@testair.com 

## James E . Meador, Jr. President( EXECUTIVE SUMMARY

Owens Corning Waxahachie, Texas Western Environmental Services and Testing, Inc. (Western Environmental)
of Casper, Wyoming, conducted

a Stack Emissions Survey at the Owens Coming's Glass Wool Insulation Manufacturing facility in Waxahachie, Texas October

1 through 5, 2002. The emissions of formaldehyde from 8 sources and the emissions of particulate matter (PM) from 5 sources were determined during this sampling program. The sampling program was to show compliance with the "National Emission Standards for Hazardous Air Pollutants for Wool Fiberglass Manufacturing", Subpart NNN of Title 40, Part 63 of the Code of Federal Regulations (CFR). Summaries of the average test results are presented on the following pages.c

- me V lL" F orma ld h d s e 1y1 e ources Stack Air Source Number Contaminant V -1 Mixing Chamber EPNlO Formaldehyde, V -1 Cooling_ Section EPN13 Formaldehyde - me V2L"
F orma ld h d s e ay1 e ources Stack Air Source Number Contaminant V -2 Mixing Chamber EPN22 Formaldehyde V-2 Cooling Section EPN23 Formaldehyde V -2 Smoke Stripper EPN55 Formaldehyde - me V3L"
F orma ld h d s e IYI e ources Stack Air Source Number Contaminant V -3 Mixing Chamber EPN40 Formaldehy_de V -3 Cooling Section EPN41 Formaldehyde V-3 Smoke Stripper EPN56 Formaldehyde I

Owens Corning Waxahachie, Texas EPA Emission Test Methods Rate lbslhr 1-4, 316 2.533 1-4, 316 0.066 Line Total 2.599 Allowable 6.00 EPA Emission Test Methods Rate lbs/hr 1-4, 316 2.822 1-4,316 0.761 1-4, 316 0.038 Line Total 3.621 Allowable 7.50 EPA Emission Test Methods Rate lbslhr 1-4, 316 3.783 1-4, 316 0.097 1-4,316 0.210 Line Total 4.090 Allowable 7.49

II

# c

V -1 Line Particulate Source Stack Air EPA Source Number Contaminant Test Methods V-1 DEP EPN03 PM
1-5 Allowable V-2 Line Particulate Sources Stack Air EPA Source Number Contaminant Test Methods V-2 #1 Furnace Stack EPN19 PM
1-5 (East) V- 2 #2 Furnace Stack EPN20 PM
1-5 (West)

Line Total Allowable V -3 Line Particulate Sources Stack Air EPA Source Number Contaminant Test Methods V -3 #l Furnace Stack EPN38 PM
1-5 (East) V -3 #2 Furnace Stack EPN39 PM
1-5 (West)

Line Total Allowable Owens Coming Waxahachie, Texas Emission Rate lbslhr 0.323 2.49 Emission Rate lbslhr 1.518 1.171 2.689 3.12 Emission Rate lbslhr 0.295 0.464 0.759 3.13

i iic c-·· TABLE OF CONTENTS I. INTRODUCTION AND RESULTS SUMMARY II. TEST RESULTS III. TEST PROCEDURES IV. PROCESS DESCRIPTION V. PROCESS AND CONTROL MONITORING VI. METHOD DEVIATIONS AND STACK ANOMALIES VII. SOURCE EMISSIONS CALCULATIONS LIST OF TABLES Table
1: Sources Tested Table 2: Program Coordination Table 3: V -1 Mixing Chamber Method 316 Formaldehyde, Runs 1, 3, & 4 Table 4: V -1 Mixing Chamber Method 316 Formaldehyde, Run 2 Table 5: V -1 Cooling Section Method 316 Formaldehyde Table 6: V-2 Mixing Chamber Method 316 Formaldehyde, Runs 1, 3, & 4 Table 7: V-2 Cooling Section Method 316 Formaldehyde Table 8: V-2 Smoke Stripper Method 316 Formaldehyde Table 9: V-3 Mixing Chamber Method 316 Formaldehyde, Runs 1, 3, & 4 Table 10: V-3 Cooling Section Method 316 Formaldehyde, Run 2 Table 11: V -3 Smoke Stripper Method 316 Formaldehyde Table 12: V-1 DEP Method
5 Particulate Table 13: V-2 #1 Furnace (East) Method
5 Particulate Table 14: V-2 #2 Furnace (West) Method
5 Particulate Table 15: V-3 #1 Furnace (East) Method
5 Particulate Table 16: V-3 #2 Furnace (West) Method
5 Particulate Table 17: V -1 Sampling Locations Table 18: V -2 Sampling Locations Table 19: V-3 Sampling Locations

1 3 17 39 41 44 45 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 18 22 28

I VcLISTOFFIGURESFigure1:V-1MixingChamber19Figure2:V-1CoolingSection20Figure3:V-1DEP21Figure4:V-2MixingChamber23Figure5:V-2CoolingSection24Figure6:V-2SmokeStripper25Figure7:V-2#1FurnaceStack(East)26Figure8:V-2#2FurnaceStack(West)27Figure9:V-3MixingChamber29Figure10:V-3CoolingSection30Figure11:V-3SmokeStripper31Figure12:V-3#1FurnaceStack(East)32Figure13:V-3#2FurnaceStack(West)33Figure14:ParticulateSamplingTrain36Figure15:FormaldehydeSamplingTrain38(v

# ( LIST OF APPENDICES Appendix
A Sampling Locations 

# ( Appendix
B Cyclonic Flow Detenninations Appendix
C Field Testing Data Appendix
D Computer Data Entry Appendix
E Analytical Data Appendix

F Calibration of Equipment Appendix
G Chain of Custody Appendix
H Resumes of Test Personnel Appendix

I Test Protocol Appendix

J Confidential Process Data

vic(_.'I.INTRODUCTIONANDRESULTSSUMMARYOwensComingWaxahachie,TexasOwensCorningofWaxahachie,TexascontractedWesternEnvironmentalServicesandTesting,Inc.(WesternEnvironmental)toprovidepointsourceemissionssurveys,analysis,andreportingontheirbehalf.Theemissionsofformaldehydeandparticulatematter(PM)fromvariousstacksweredeterminedOctober1through5,2002.Thesourcesarelistedbelow.SourceV-1MixingChamberV-1CoolingSectionV-2MixingChamberV-2CoolingSectionV-2SmokeStripperV-3MixingChamberV-3CoolingSectionV-3SmokeStripperV-1DEPV-2#1Furnace(East)V-2#2Furnace(West)V-3#1Furnace(East)V-3#2Furnace(West)WesternEnvironmentalServicesandTesting,Inc.Table1SourcesTestedAirStackNumberContaminantEPN10FormaldehydeEPN13FormaldehydeEPN22FormaldehydeEPN23FormaldehydeEPN55FormaldehydeEPN40FormaldehydeEPN41FormaldehydeEPN56FormaldehydeEPN03PMEPN19PMEPN20PMEPN38PMEPN39PM02-1057EPATestMethods1-4,3161-4,3161-4,3161-4,3161-4,3161-4,3161-4,3161-4,3161-51-51-51-51-5Table 2 p rogram 

### c d"
f oor ma Jon Plant Project Manaeer Mr. Gary Chastain
Mr. Jerry Moore Owens Coming Owens Coming 3700 N. Interstate 35 East 2790 Columbus Road, Route 16 Waxahachie, Texas 75165-0837 Granville, Ohio 43023 (972) 923-4360 (phone) (740) 321-7675 (phone) (972) 937-7360 (fax) (740) 321-7567 (fax) gary .chastain @owenscorning.com jerry .l.moore @owenscorning.com
Owens Coming Waxahachie, Texas Sampline Companv Mr. Alan D. Roxlance Western Environmental Services and Testing 913 Foster Road Casper, WY 82601 (307) 234-5511 (phone) (307) 234-8324 (fax) aroylance@testair.com The sampling was witnessed by Mr. Gary Mokry with the Environmental Protection Agency, Region 6; and Mr. Gary Goldman and Mr. Bill Petersen with the Texas Commission on Environmental Quality. Summaries of the average test results are presented on the following pages

. Individual and average emissions and test parameters from each run conducted on the stacks are shown on the following pages. The sampling followed the procedures set forth in the Appendix to the Code of Federal Regulations, Title 40, Part 60. Western Environmental Services and Testing, Inc. 02-1057

2OwensComingWaxahachie,TexasII.TestResultsTable3c·V-1MixingFormaldehyde,Runs1,3,and4RunNumber:1l!StartDate/Time10/1/20029:1510/1/200213:0010/1/200214:39StopDate/Time10/11200210:5210/1/200214:3010/11200216:10TestParameleraYDI!IPbar(BarometricPressure,absolute)ln.Hg29.7029.7029.7029.70Y(DryGasMeterCalibrationFactor)dimensionless0.99100.99100.99100.9910Cp(PilottubeCoefficient)dimensionless0.6310.6310.6370.631Dn(DiameterofNozzle)Inches0.2420.2420.2410.2428(TotalSamplingTimeofTest)Minutes87.5087.5087.5087.50.6H(OrificePressureDrop)ln.H200.890.800.730.84Vm(VolumeofDryGasSampled·asmeasured)113(dry)47.70945.63244.10046.n1T m(GasMeterTemperature,avg.)Degr.Fn909263v,.(Condensate-impingersandsilicagel)mlorg87.988.985.588.4MassofFormaldehydecollectedmg6.5876.7506.7306.669l.!!1£ltiRD!fll!BJII!Imm-sA.(Cross-sectionalAreaofStack)If82.9382.9382.9382.93Pg(StaticPressureofStackGas)ln.H20-o.30-Q.30-o.30-o.30T1(TemperatureofStackGas)Deg.F228237228232v·.dp(Sq.rootofvelocityheadofgas){"ln.H200.58820.56340.53740.5758C02(CarbonDioxide)%0.40.40.40.402(Oxygen)%20.420.420.420.4N2(Nitrogen)%79.279.279.279.2Calcyllti!!DIv.....,(GasSampled,standardconditions(std))It"46.23443.38441.58544.809v_(WaterVaporinGasSampled,std)II"4.144.184.024.16B,.(WaterVaporinGas,ProportionbyVol.)%8.218.808.828.51G0(ProportionofDryGasinstack)%91.891.291.291.5M0(MolecularWeightofDryStackGas)lbllb-mole28.8828.8828.8828.88M.(MolecularWeightofWetStackGas)lbllb-rnole27.9927.9227.9227.95P1(PressureofStackGas,Absolute)ln.Hg29.6829.6829.6829.68lso(PercentoflsokinetlcSampling)%103.8102.9102.8103.4FIC!WRnylll!V1(AverageStackGasVelocity)ftlm(fpm)2282220221022242a.,.(DryVolumetricFlowRate,std.)113/m(dscfm)132186125132121000128659a.,.(WetVolumetricFlowRate,std.)tt"lm(wscfm)144015137201132710140608a.(MeasuredVolumetricFlowRate,Actual)ll"lm(elm)189254182652174340185953FRnn•lc!ehvc!eRuulllFormaldehydeConcentrationsgr/dscf0.00220.00240.00250.0023FormaldehydeConcentrationsppm4.02n4.39854.57524.2131E!!nn•IS!!Ibvc!eEmilll!!DBllllFormaldehydeEmissionRatelb/hr2.4912.5752.5902.533StandardConditions=6ffF,29.92"HgWesternEnvironmentalServicesandTesting,Inc.02-10573OwensCorning..Waxahachie,TexasTable4V-1Mixing0Formaldehyde,Run2RunNumber:aStartDate!Time10/1/200211:10StopDate/Time10/1/200212:42TeatParameflrsUnitsPbor(BarometricPressure,absolute)ln.Hg29.7029.70Y(DryGasMetarCsllbretlonFactor)dimensionless0.99100.9910c;,(PitottubeCoefficient)dimensionless0.8370.837D.(DiameterofNoule)Inches0.2410.2418(TotalSamplingTimeofTest)Minutes87.5087.50(OrificePressureDrop)ln.H200.770.77Vm(VolumeofDryGasSampled-asmeasured)If{dry)44.81344.813T m(GasMeterTemperature,avg.)Degr.F8585v.,(Condensate-impingersandsilicagel)mlorg87.587.5MassofFormaldehydecollectedmg13.27413.274fl[lmelllrsA.(Cross-sectionalAreaofStack)If82.9382.93Pg(StaticPressureofSteckGas)ln.H20-0.30.0.30T,(TemperatureofStackGas)Deg.F234234(Sq.rootofvelocityheadofgas)rln.H200.53670.5367C02(CsrbonDioxide)%0.40.4(02(Oxygen)%20.420.4N2(Nitrogen)%79.279.2Ca!culat!S!Mv.....,(GasSampled,standardconditions(std))fe42.79642.796v_(WaterVaporinGasSampled,std)If4.124.12S...(WaterVaporInGas,ProportionbyVol.)%8.788.78Gd(ProportionofDryGasInstack)%91.291.2Md(MolecularWeightofDryStackGas)lbllb-mole28.8828.88M.{MolecularWeightofWetStackGas)lbllb-mole27.9227.92P,(PressureofStackGas,Absolute)ln.Hg29.6829.68Iso(PercentoflsokineticSampling)%106.4106.4FinRgu!tav.{AverageStackGasVelocity)lt/m(fpm)21092109Qltd(DryVolumetricFlowRate,std.)rftm{dschn)120321120321Qltd(WetVolumetricFlowRate,std.)fftm(wscfm)131900131900a.(MeasuredVolumetricFlowRate,Actual)113/m(elm)174917174917E!!rmald!hvdeRnunaFormaldehydeConcentrationsgr/dscf0.00480.0048FormaldehydeConcentrationsppm8.76868.7686Egrml!ldehv!!lEmi!lli2DBlllUFormaldehydeEmissionRatelblhr4.9364.936StandardConditions=6ff'F,29.92"HgWesternEnvironmentalServicesandTesting,Inc.02-10574

## Owens Corning TableS 

## oiNaxahachie, Texas V-1 Cooling 

## Formaldehyde Run Number:



## 1



# a

i 

# AX!riBI Start Date/Time 10/1/02 9:14 10/1/0211:10 10/1/02 13:00 Stop Date/Time

1 0/1/02
1 0:28 10/1/02 12:24 10/1/02 14:15 Teat Parameters

Units Pbar (Barometric Pressure, absolute)

ln. Hg 29.70 29.70

29

. 70 29.70 

### Y (Dry Gas Meter Calibration Factor) dimensionless 0.990 0.990 0.990

0
. 990 Cp (Pitot tube Coefficient) dimensionless 0.850 0.843 0.842 0.845 Dn (Diameter of Nozzle)
Inches 

### 0244 0.247 0242 0.244 

# e (Total Sampling Time of Test) Minutes 72.00 72.00 72.00 72.00 AH (Orifice Pressure Drop)

ln. H20 0.74 0.78 0.65 0.72 Vm (Volume 

### of Dry Gas Sampled- as measured)

ff (dry) 35.211 37.432 35.229 35.957 T m (Gas Meter Temperature, avg.) Degr. F
87

94 104

95 

# v ... (Condensate- implngers and slice 

### gel) mlorg 33.8 33.1 31.4 32.8 Mass of Fonnaldehyde 

### collected

mg 1.711 1.715 1.n8

1 . 735 Locat!s!Dreroceaa Parameters 

## A. (Cross-sectional Area of Stack)



## ff 6.80 6.80 6.80 6.80 P 

### u (Static Pressure of Stack Gas)

ln. H20 0.07 0.07 0.07 0.07 T. (Temperature
of Stack Gas)

Deg

. F 140 153 162 152 

# v·Ap (Sq. root 

### of velocity head of gas)



# Y ln. H20 0.4708 0.4897 0.4445 0.4684 C0 2 (Carbon Dioxide)

%



### 0

0

0 0.0 02 (Oxygen)

% 

### 20.8 20.8 20.8

20

. 8 N2 (Nitrogen)

% 

### 79.2 79.2 

### 792 792 

# (~. Calculations Vmold (Gas Sampled, standard conditions (std))



### ft3 33.483 35.100



### 32

. 484 33.689 VWIId (Water Vapor in Gas Sampled, std)

ff 1.59 1.56 1.48 1.54 

# e,.. (Water Vapor in 

### Gas, Proportion by Vol.)

% 

### 4.54 4.25

4
. 35 4.38 

### Saturated Molstu/"9 in stack 

### gss, by volume

% 

### 19.11 26.49

32

. 82
26

. 14 Gd (Proportion of Dry Gas in stack)

% 

### 95.5 95.7 95.6 95.6 Md (Molecular Weight of Dry Stack Gas) lb/lb-mole 28.83 28.83 28.83 28.83 M, (Molecular Weight 

### of Wet Stack Gas) lb/lb-mole 28.34 28.37 28.36 28.36 P, (Pressure of Stack Gas, Absolute)

ln. Hg 29.71 29.71 29.71 29.71 lso (Percent 

### of lsoklnetlc Sampling)

%



### 99

. 1
99

. 1 106.2 101.5 Flow Result! 

# v, (Average Stack Gas Velocity)

ft/m (fpm) 1733 1806 1649 1729 

### Qllld (Dry Volumetric Flow Rate, std.) fftm (dscfm) 9826 10054 9044 9641 

### Qllld (Wet Volumetric Flow Rate, std.)



### ft 3 /m (wscfm) 10293 10501 

### 9455 10083 

# a. (Measured Volumetric Flow Rate, Actual)



### ft 3 /m (cfm) 11786 12282 11217 11762 Formaldehyde Resuha Formaldehyde Concentrations, ppm
ppm 1.4446 1.3813 1.5474

1 . 4578 Formaldehyde Concentrations
gr/dscf 0.0008 0.0008 0.0008 0.0008 FormaldebYSI!! Emission R!!l.! Fonnaldehyde Emission Rate

lbhlr 0.066 0.065 0.065 0.066 

### Standard Conditions= 68° F, 29.92

" Hg



## 5 Western Environmental Services and Testing, Inc. 02-1057

## Owens Coming 

## Table6 Waxahachie, Texas V-2 Mixing 

## Formaldehyde Run Number:



# a

**~**



## ! Average Start Dateffime

1 0/2/02
1 0:37

1 0/2/02 12:25 10/2/02 14:05 Stop Dateffime

1 0/2/02 11 :59 10/2/02 13:52 10/2/02 15:24 Test Parameters

Units Pbar (Barometric Pressure, absolute)

ln. Hg 29.55 29.55 29.55 29.55 Y (Dry Gas Meter Calibration Factor) dimensionless 1.0160 1.0160 1.0160 1.0160 Cp (Pilot tube Coefficient) dimensionless 0.831 0.837 0.831

0
. 833 Dn (Diameter of Nozzle)
Inches 0.242 0.241 0.242 0.242 9 (Total Sampling Time of Test) Minutes 72.00

72

. 00
72

. 00 72.00 AH (Orifice Pressure Drop)

ln. H20 1.37 1.30 1.30 1.32 V m 

### (Volume of Dry Gas Sampled

- as measured)

fe (dry) 50.577 49.856 50.496 50.310 T m 

### (Gas Meter Temperature, avg.) Degr. F
87

93

97

92 **V~c** 

### (Condensate- impingers and silica gel)

ml org 78.2

79

. 2 78.8 78.7 Mass 

### of Fonnaldehyde collected

mg

5 . 576 6.167 5.987 5.910 Location/Proce!s Parameters 

## A. (Cross-sectional Area of Stack)



## If 84.88 84.88 84.88 84.88 Pg (Static Pressure of Stack Gas)

ln. H20 0.32 0.32 0.32 0.32 Ta (Temperature
of Stack Gas) Deg.F 190 179 186 185 1/flp (Sq. root of velocity head of gas)


# v';;., H20 0.7421 0.7218 0.7203 0.7281 C0 2 (Carbon Dioxide)

%


### 0.6
0.4
0.4
0.5 02 (Oxygen)

% 

### 19.4 19.6 19.8 19.6 N 2 (Nitrogen)

%



### 80
80 79.8 79.9 

# c

Calculations **Vms~d** 

### (Gas Sampled, standard conditions (std))



## te 49.173 47.920 48.161 48.418 Vwstd (Water Vapor in Gas Sampled, std)



## te 3.68 3.73

3
. 71 3.71 B.,. (Water Vapor in Gas, Proportion by Vol.)

% 

### 6.96 7.22 7.15 7.11 Saturated Moisture in stack gas, 

### by volume

% 

### 63.50 49.81 58.10 57.14 Gd (Proportion
of Dry Gas in stack)

% 

### 93.0 92.8 92.8 92.9 Md (Molecular Weight of Dry Stack Gas) lb/lb-mole 28.87 28.85 28.86 28.86 M. (Molecular Weight of Wet Stack Gas) lbllb-mole 28.11 28.06 28.08 28.09 P 0 

### (Pressure of Stack Gas, Absolute)

ln. Hg 29.57 29.57 29.57

29

. 57 lso (Percent of lsokinetic Sampling)

% 

### 102.4 102

. 0 103.2 102.5 Flow Results 

# v. (Average Stack Gas Velocity)

film (fpm) 2797 2720 2709 2742 Qstd 

### (Dry Volumetric Flow Rate, std.) 

### fetm (dsctm) 177226 174790 172336 174784 Qstd 

### (Wet Volumetric Flow Rate, std.)

11 3 

### /m (wscfm) 190492 188388 185608 188163 Q 8 

### (Measured Volumetric Flow Rate, Actual)

11 3 

### /m (elm) 237426 230861 229900 232729 Formaldehyde Results Formaldehyde Concentrations, ppm
ppm 3.2057 3.6383 3.5143 3.4528 Formaldehyde Concentrations
gr/dscf 0.0017 0.0020 0.0019 0.0019 Formaldehyde Emission Rates Formaldehyde Emission Rate

lblhr 2.658 2.975 2.833 2.822 Standard Conditions


# = 68° F, 29.92 "Hg 

### Western Environmental Services and Testing, Inc

. 02-1057



## 6

## Owens Coming Table?



## Waxahachie, Texas 

# ( V-2Cooling Formaldehyde Run Number:



## 1



# a

**~** 

## &!!!'.lSI Start Date/Time 10/2/02 9:03 1012/02 10:37 10/2/02 12:25 Stop Date/Time 10/2102 10:17 1012/02 11:51 1012/02 15:39 Teat Parameter!



## Y!lbl P.,.. (Barometric Pressure, absolute) ln.Hg 29.55 29.55 29.55 29.55 Y (Dry Gas Meter Calibration Factor) dimensionless 0.994 0.994 0.994 0.994 Cp (Pitot tube Coefficient) dimensionless 0.850 0.843 0.850 0.848 Dn (Diameter of Nozzle)
Inches 0.190 0.184 0.190 0.188 

# e (Total Sampling Time of Test) Minutes 72.00 72.00 72.00 72.00 AH (Orifice Pressure Drop)

ln. H20 0.84 0.75 0.78 0.79 Vm (Volume of Dry Gas Sampled- as measured)



### ft 3 (dry) 38.613 37.141 37.909

37

. 888 T m (Gas Meter Temperature, avg.) Degr. F 80
88
92
87 Vtc (Condensate

- impingers and silica 

### gel) mlorg 53.3 50.3 56.8 53.5 Mass of Formaldehyde 

### collected



### rng 9.418 9.168 7.853 8.813 **Locatlon!Pm~sa** Parameters 

## A. (Cross-sectional Area of Stack)



## ff 9.62 9.62 9.62 9.62 Pg (Static Pressure of Stack Gas)

ln. H20 -o.10 -o.10 -o.10 -o.10 T 8 (Temperature
of Stack Gas) Deg.F
111 113 113 112 

# v-Ap (Sq. root of velocity head of gas) {"ln. H20 0.7998 0.8105 

## o.n36 0.7946 C0 2 (Cerbon Dioxide)



## ' ·

%

0

0

0 0.0 0 2 (Oxygen)



### % 20.8 20.8 20.8 20.8 

# c: **~** (Nitrogen)

% 79.2 79.2 79.2 79.2 Calculation• 

# vmatd (Gas Sampled, standard conditions (std))



### ft3 37.133 35.193 

### 35.680 36.002 Vwatd (Water Vapor in Gas Sampled, std)



### ft3 2.51 2.37 2.67 2.52 

## a_ (Water Vapor in Gas, Proportion by Vol.)



### % 6.33 6.30 6.97 6.53 

### Saturated Moisture in stack gas, 

### by volume

% 8.64 9.07 9.08 8.93 Gd (Proportion of Dry 

### Gas in stack)



### % 93.7 93.7 93.0 93.5 Md (Molecular Weight of Dry Stack Gas) lbllb-mole 28.83 28.83 28.83 28.83 M. (Molecular Weight of Wet Stack Gas) lbllb-mole 28.15 28.15

28

. 08 28.12 P. (Pressure of Stack Gas, Absolute) in.Hg 29.54 29.54 29.54 29.54 lso (Percent of lsokinetic Sampling)



### % 106.1 106.8 106.1 106.3 Flow 

### Rgulta 

# v. (Average Stack Gas Velocity)

ftlm (fpm) 2890 2908 2803 2887 

### Cold (Dry Volumetric Flow Rate, std.)



### ft 3 /m (dscfm) 23767 23856 22824 23483 

### Cold (Wet Volumetric Flow Rate, std.)



### ft 3 /m (wscfm) 25372 25461 24535 25123 

### Ca (Measured Volumetric Flow Rate, Actual)



### ft 3 /m (cfm) 27802 27981 26965 27583 **for!!!!l~hJt£11** Reaylta Formaldehyde Concentrations, ppm
ppm 7.1701 7.3646 6.2221 6.9189 Formaldehyde Concentrations
gr/dscf 0.0039 0.0040 0.0034 0.0036 **Forrnaldeh~** Emission RIJI! Formaldehyde Emission Rate

iblhr 0.797 0.822 0.664 0.761 

### Standard Conditions= 68° F, 29.92 "Hg



## 7 Western Environmental Services and Testing, Inc

. 02-1057Owens Corning TableS W!'Xahachie, Texas c

V -2 Smoke Stripper Formaldehyde Run Number:

1
**~** Start Date/Time

1 012102 9:04 1012102 10:37 10/2/02 12:25 Stop Date/Time 10/2102 10:18 1012102 11:51 1012102 13:39 Test Pararnetenl

Y.!.!b! **P~~or** (Barometric Pressure, absolute) ln.Hg 29.55 29.55 29.55 29.55 Y (Dry Gas Meter Calibration Factor) dimensionless 0.990

0
. 990 0.990 0.990 Cp (Pitot tube Coefficient) dimensionless 0.842 0.827 0.842 0.837 Dn (Diameter of Nozzle)
Inches 0.315 0.305 0.315 0.312 e (Total Sampling Time of Test) Minutes 72.00 72.00 72.00 72.00 aH (Orifice Pressure Drop)

ln. H20 0.97 0.80 0.99 0.92 Vm (Volume of Dry Gas Sampled ·as measured)

ft 3 (dry) 40.856 37.491 41.323 39.890 T m (Gas Meter Temperature, avg.) Degr. F
92

95
97

95 v., (Condensate· impingers and silica gel) mlorg 52.4 44.1 50.6 49.0 Mass of Formaldehyde collected

mg 8.303 6.750 9.498 8.184 Locatlon/Proceu P!rametera A. (Cross-sectional Area of Stack)

If 1.35 1.35 1.35 1.35 Pg (Static Pressure of Stack Gas)

ln. H20 0.05 0.05 0.05 0.05 T, (Temperature
of Stack Gas) Deg.F
171 166 169 169 lr&p (Sq. root of velocity head of gas)

.r ln. H20 0.3381 0.3209 0.3385 0.3325 **C~** (Carbon Dioxide)

%

0

0

0 0.0 0 2 (Oxygen)

% 20.8 20.8 20.8 20.8 N2 (Nitrogen)

% 79.2 79.2 79.2 79.2 **c.·~** Calculation! Vffflld (Gas Sampled, standard conditions (std))

ft3 38.325 34.980 38.383 37.223 v_ (Water Vapor in Gas Sampled, std)

ft3 2.47 2.08 2.38

2
. 31 e... (Water Vapor in Gas, Proportion by Vol.)

o/o 6.05 5.60 5.84 5.83 Saturated Moisture in stack gas, by volume

% 41.12 36.81 39.24 39.05 Gd (Proportion of Dry Gas in stack)

% 94.0 94.4 94.2 94.2 Md (Molecular Weight of Dry Stack Gas) lbllb-mole 28.83 28.83 28.83 28.83 M, (Molecular Weight of Wet Steck Gas) lbllb-mole 28.18 28.22 28.20 28.20 P. (Pressure of Stack Gas, Absolute) ln.Hg 29.55 29.55 29.55 29.55 lso (Percent of lsokinetic Sampling)

% 99.7 103.3 99.4 100.8 Flow R!!Uit! v. (Average Stack Gas Velocity)

ftJm (fpm) 1271 1179 1270 1240 **Oo~~~** (Dry Volumetric Flow Rate, std.)

ft 3 /m (dscfm) 1335 1254 1341 1310 **Oo~~~** (Wet Volumetric Flow Rate, std.)

ft 3 /m (wscfm) 1421 1328 1424 1391 a. (Measured Volumetric Flow Rate, Actual) **~/m** (cfm) 1720 1596 1718 1678 formaldehyde Rt!UII! Formaldehyde Concentrations, ppm
ppm 6.1246 5.4583 6.9957 6.1929 Formaldehyde Concentrations
gr/dscf 0.0033 0.0030 0.0038 0.0034 Form!ld.!hvd.! Emission R!ll! Formaldehyde Emission Rate

lblhr 0.038 0.032 0.044 0.038 Standard Conditions= 68° F, 29.92 "Hg

8 Western Environmental Services and Testing, Inc. 02-1057Table9OwensCorningV-3MixingWaxahachie,TexasFonnadlebyde(RunNumber:1!lAveraaeStartDatemme10131028:05101310210:42"101310213:15StopDatemme101310210:32101310213:08101310215:41T!ftParametlr!Y!!lllPbor(BarometricPressure,absolute}ln.Hg29.5029.5029.5029.50Y(DryGasMetarC&llbratlonFactor}dimensionless0.99100.99100.99100.9910Cp(PltottubeCoefficient}dimensionless0.8310.8500.8310.837Dn(DiameterofNozzle}Inches0.2420.2410.2420.242e(TotalSamplingTimeofTest}Minutes140.00140.00140.00140.00AH(OrificePressureDrop)ln.H200.400.390.380.39Vm(VolumeofDryGasSampled-asmeasured}ft"{dry}53.16553.19153.56153.306Tm(GasMeterTemperature,avg.)Degr.F879710696v..{Condensate-lmpingersandsHicagel}mlorg88.894.191.691.5MassofFormaldehydecoHectedmg8.5509.7387.4598.582PgrametersA.(Cross-sectionalAreaofStack}tt2147.16147.16147.16147.18Pg(StaticPressureofStackGas}ln.H20-o.31-o.30-o.30-o.30T.(TemperatureofStackGas}Deg.F1n1791n178lrAp(Sq.rootofvelocityheadofgas}.rln.H200.40010.39570.39040.3954C02{C&rbonDioxide}%0.40.60.80.502(Oxygen}%20.620.420.620.5Nz(Nitrogen}%797978.878.9Calcul!!t!ontV.-(GasSampled,standardconditions(std}}ft"5021449.30849.90949.4nv_(WaterVaporInGasSampled,std}ft"4.184.434.314.31e_(WaterVaporInGas,ProportionbyVol.}%7.688.248.108.01(.!uratedMoistureInstackgas,byvolume%472349.6147.3749.07"""d(ProportionofDryGasInstack}%92.391.891.992.0Md(MolecularWeightofDryStackGas}lbllb-mole28.8928.9128.9228.91M.(MolecularWeightofWetStackGas}lbllb-mole28.0528.0128.0428.03P.(PressureofStackGas,Absolute}ln.Hg29.4929.4929.4929.49lso(PercentoflsoklnetlcSampling}%99.598.199.899.2FlowRnult!v.(AverageStackGasVelocity}ft/m(fpm)1497151814611492(DryVolumetricFlowRate,std.}ft"im(dscfm}166039100n1161296164702(WetVolumetricFlowRate,std.)ft"/m(wscfm}179880181752175515179042a.(MeasuredVolumetricFlowRate,Actual}ft3/m(cfm}220274223339214990219534FormaldehVdtRnult!tFormaldehydeConcentrationppm4.81375.58334.31154.9028FormaldehydeConcentrationgr/dscf0.00260.00300.00240.0027Formals!!hl!sllEmlui2nBill!FormaldehydeEmissionRatelblhr3.7394.3563.2533.783StandardConditions=68°F,29.92"HgWesternEnvironmentalServicesandTesting,Inc.02-10579

## Owens Corning Table 10 

## W1l'Jt.ahachie, Texas V-3 Cooling 

## Formaldehyde Run Number:



## !

i

i 

## Auwl! Start Date/Time 1013102
8 : 15 1013/02 10:10 10/3102 11:45 Stop Datefrlme 10/3102 9:29

1 013/02 11 :24

1 013/02 12:59 Test Pa!Jmeters



## Ynb! P""' (Barometric Pressure, absolute) ln.Hg 29.50 29.50 29.50 29.50 Y (Dry Gas Meter Calibration Factor) dimensionless 0.994 0.994 0.994 0.994 

## Cp (Pitot tube Coefficient) dimensionless 0.843 0.842 0.843 0.843 Dn (Diameter of 

### Noule)
Inches 0.299 0.302 0.299

0
. 300 9 (Total Sampling Time of Test) Minutes 72.00 72.00 72.00 72.00 AH (Orifice Pressure Drop)

ln. H20 1.08 1.05 1.00 1.04 Vm (Volume 

### of Dry Ges Sampled- as measured)


# w (dry) 43.556 43.06 42.744 43.120 T m (Gas Meter Temperature, avg.) Degr. F
78

87
93
86 **V~c** 

### (Condensate- impingers and silica 

### gel) mlorg 24.3 28.9

31

. 0 28.1 Mass of Formaldehyde 

### collected

mg 2.587 2.675 2.863 2.708 **Locatlo~roceaa** 

### Parametara 

## A. (Cross-sectional Area of Stack)



## ff 9.45 9.45 9.45 9.45 P 8 

### (Static Pressure of Stack Gas)

ln. H20 -0.07 -0.07 -0.07 -0.07 T. (Temperature
of Stack Gas) Deg.F
119 122 127 123 

# lrAp (Sq. 

### root of velocity head 

### of gas)



# .r ln. H20 0.3833 0.3730 0.3703 0.3755 C0 2 (Carbon Dioxide)

%



### 0

0

0 0.0 02 (Oxygen)

% 

### 20.8 20.8 20.8 20.8 

# c_· **~** 

### (Nitrogen)

% 

### 79.2 79.2 79.2 79.2 Calculatlont 

# vmald (Gas Sampled, standard conditions (std))



# w 41.974 40.866

40

. 063 

### 40.968 

# v_ (Water Vapor in Gas Sampled, std)

fe 1.14 1.36 1.46 1.32 

# e... (Water Vapor in Gas, Proportion by Vol.)

% 

### 2.65 3.22 3.51 3.13 Saturated Moisture in stack gas, by volume



### % 

### 10.95 11.86

13

. 43 12.08 

## G.. (Proportion


### of Dry 

### Gas in stack)

% 

### 97.3 96.8 96.5 96.9 

## Met (Molecular Weight of Dry Stack Gas) lbl1b-mole 28.83 28.83 28.83 28.83 M, (Molecular Weight of Wet Stack Gas) lbl1b-mole 28.54 28.48 28.45 28.49 P, (Pressure of Stack Gas, Absolute) ln.Hg 29.49 29.49 29.49 29.49 lso (Percent of lsokinetic Sampling)

% 

### 99.5

98

. 4 99.6 99.2 FlowRe!ult! V, (Average Stack Gas Velocity)

ftlm (fpm) 1375 1341 1339 1352 0 1111 

### (Dry Volumetric Flow Rate, std.) W/m (dscfm) 11361 10961 10828 11050 Q 111 

### (Wet Volumetric Flow Rate, std.) fe/m (wsctm) 11670 11326 11222 11406 

### Oa (Measured Volumetric Flow Rate, Actual) fe/m (cfm) 12993 12671 12652 12772 Formaldehyde Reault! Formaldehyde Concentrations, ppm
ppm 1.7424 1.8505 2.0203 1.8711 Formaldehyde Concentrations
gr/dscf 0.0010 0.0010 0.0011 0.0010 **Formal~v!B** 

### Emission RISU Formaldehyde Emission Rate

lblhr 0.093 0.095 0.102 0.097 

### Standard Conditions= 68° F, 29.92 "Hg



## 10 Western Environmental Services and 

### Testing, Inc

. 

### 02-1057OwensCorningTable11Waxahachie,TexasV-3SmokeStripperFormaldehydeRunNumber:1AverageStartDate/Time10/31028:231013/0210:101013/0211:45StopDateffime10/3/029:3810/310211:241013/0212:59TestParametersY.!lB!Pbar(BarometricPressure,absolute)ln.Hg29.5029.5029.5029.50Y(DryGasMeterCalibrationFactor)dimensionless0.9900.9900.9900.990Cp(PitottubeCoefficient)dimensionless0.8420.8260.8420.837Dn(DiameterofNozzle)Inches0.1800.1760.1800.179a(TotalSamplingTimeofTest)Minutes72.0072.0072.0072.00&H(OrificePressureDrop)ln.H201.441.211.221.29Vm(VolumeofDryGasSampled-asmeasured)tf(dry)48.85244.96245.77648.530Tm(GasMeterTemperature,avg.)Degr.F90959995v..,(Condensate-irnpingersandsilicagel)mlorg56.850.631.046.1MassofFormaldehydecollectedmg20.49418.32719.64919.490Location/ProcessParametersA.(Cross-sectionalAreaofStack)ff1.031.031.031.03Pg(StaticPressureofStackGas)ln.H200.600.600.600.60T.(TemperatureofStackGas)Deg.F162158156158lr&p(Sq.rootofvelocityheadofgas).(ln.H201.21481.14171.1212(CarbonDioxide)%0000.002(Oxygen)%20.820.820.820.8N2(Nitrogen)%79.279.279.279.2CalculationsVrnlld(GasSampled,standardconditions(std))fl345.95541.90742.32643.396Vwald(WaterVaporInGasSampled,std)fl32.672.381.462.17B,(WatarVaporinGas,ProportionbyVol.)%5.505.383.334.74SaturatedMoistureinstackgas,byvolume%33.2329.9128.4530.53Gd(ProportionofDryGasinstack)%94.594.696.795.3Md(MolecularWeightofDryStackGas)lbllb-mole28.8328.8328.8328.83M.(MolecularWeightofWetStackGas)lbllb-mole28.2428.2528.4728.32P.(PressureofStackGas,Absolute)ln.Hg29.5429.5429.5429.54lso(PercentoflsokineticSampling)%100.7103.798.1100.8FlowResult!v.(AverageStackGasVelocity)film(fpm)4530416141434278Q1111(DryVolumetricFlowRate,std.)tftm(dscfm)3699342634963541Qlld(WetVolumetricFlowRate,std.)tt3/m(wscfm)3914362136173717Q8(MeasuredVolumetricFlowRate,Actual)ft3/m(cfm)4671429142724411FormaldehydeResuhsFormaldehydeConcentrations,ppmppm12.607312.363513.123912.6982FormaldehydeConcentrationsgr/dscf0.00690.00670.00720.0069FormaldehydeEmlaalonR!!!sFormaldehydeEmissionRatelb/hr0.2180.1980.2150.210StandardConditions=68°F,29.92"HgItWesternEnvironmentalServicesandTesting,Inc.02-1057

## Owens Coming Table 12



## Waxahachie, Texas V-1 DEP 

# c METHODS PARTICULATE Run Number:



## 1

!



## 1 Start Date/Time 10/4102 8:43 10/4/02 11 :00 10/4/02 13:15 Stop Date/Time 10/4102 10:45 10/4/0213:02 10/4/02 15:17 Test Paramettra



## !J.nbl P.,., (Barometric Pressure

, absolute)

ln

. Hg

29

. 50
29

. 50
29

. 50
29

. 50 Y (Dry Gas Meter Calibration Factor) dimensionless 0.9900

0
. 9900 0.9900 0.9900 

# c;, (Pitot tube Coefficient) dimensionless

0
. 850 0.831

0
. 850 0.844 Dn (Diameter 

### of Nozzle)

Inches 0.241 0.242

0
. 241

0
. 241 

# e (Total Sampling Time 

### of Test) Minutes
120

. 00 120.00 120.00 120.00 aH (Orifice Prassure Drop)

ln . H20 0.90

1 . 02 1.10 1.00 Vm (Volume 

### of Dry Gas Sampled -as measured)



## If (dry) 65.025 67.086 67.841 66.651 T m (Gas Meter Temperature, avg

. )
Degr. F


### 90
97 109
99 **v~** (Condensate -lmplngers and slUes gel) mlorg 115.0 108.2 103.7 109.0 Mass 

### of Particulate collected, Filter

mg

3
. 100 3.000 5.300 3.800 Mass of Partk:ulate 

### collected

, Probe

- Acetone rinse
mg 3.964

14

. 464

8
. 736

9 . 055 Mass 

### of Particulate collected, Probe- D.l. rinse

mg

0
. 396

1 . 358 0.000 0.585 Mass of Particulate collected, Front-hall

mg 7.460 18.822

14

. 036
13

. 440 L221!!tlg!.!lf£2Sllll Pgmmllhlrfl 

### A. (Cross-sectional Area 

### of Stack)



## If 6.97 6.97 6.97

6
. 97 P g (Static Pressure 

### of Stack Gas)

ln . H20

-0

. 39 -0.39 -0.39

-0

. 39 

### I. (Temperature



### of 

### Stack Gas)
Deg.F
401 407 413 407 

### I;Ep (Sq. root 

### of velocity head of gas)



# v ln . H20

0
. 6394 0.6642 0.6767 0.6601 

### CO:! (Carbon Dioxide)

%

4 3.8

4 3.9 02 (Oxygen)

%

20
20

20 20.0 

# ( N2 (Nitrogen)



### %

76
76

. 2
76

76

. 1 Ctl!culat!ooa 

## vlfiiOl (Gas Sampled, standard conditions (std))



## If 61.110 62.212 61.587 61.636 

## v_ (Water Vapor In Gas Sampled, std)



### 113 5.41 5.09 4.88 5.13 

## a,.. (Water Vapor In Gas, Proportion by Vol.)



### %

8
. 14 7.57 7.34 7.68 Gd (Proportion


### of Dry Gas In stack)



### %

91

. 86
92

. 43
92

. 66
92

. 3 **~** (Molecular Weight 

### of Dry Stack Gas) lbllb-mole

29

. 44 29.41 29.44 29.43 M. (Molecular Weight of Wet Stack Gas) lbllb-mole 28.51 28.54 28.60 28.55 P. (Pressure of Stack Gas, Absolute)

ln . Hg 29.47 29.47

29

. 47 29.47 lso (Percent oflsoklnetlc Sampling)

% 102.7 101.9 97.8 100.8 F!()w 

## RttuHa 

## v. (Average Steck 

### Gas Velocity)

film (fpm) 2822 2874 3002 2899 **On~** (Dry Volumetric Flow Rate, std.)



### 11 3 /m (dsclm) 10912 11105 11552 11190 **Oot~~** (Wet Volumetric Flow Rate, std.)



### 11 3 /m (wsclm) 11878 12015 12467 12120 

# a. (Measured Volumetric Flow Rate, Actual)



### 11 3 /m (elm) 19671 20031 20928 20210 Pgrtlcu!gtl 

### Rt1ultl Particulate Concentrations, Filer
gr/dscl

0
. 0008 0.0007 0.0013 0.0010 Particulate Concantratlons, Probe

- Acetone rinse gr/dscl 0.0010 0.0036 0.0022 0.0023 Partk:ulate Concentrations, Probe- D.l. rinse gr/dscl

0
. 0001

0
. 0003 0.0000 0.0001 Particulate 

### Concentrations, Front-hall Total gr/dscl 0.0019 0.0047 0.0035

0
. 0034 

### f!!::ll!ll:!llll l;miHiszn 

### Ratea Particulate Emission Rate, Filter

lblhr 0.073

0
. 071

0
. 131 0.092 Particulate Emission Rate, Probe

- Acetone rinse lblhr 0.094 0.341 0.217 0.217 Particulate Emission Rate, Probe-
D . I. rinse
lblhr

0
. 009 0.032

0
. 000 0.014 

# c_·_ Particulate Emission Rate, Front-hall Total
lblhr 0.176 0.444 0.348

0
. 323 Standard Conditions


## = 68u F, 29.92 "Hg Western Environmental Services and Testing, Inc. 02 - 1057



### 12

## Owens Coming Table 13

Waxahachie, Texas V -2 #1 Furnace (East) 

## METHODS PARTICULATE Run Number:



## 1

&



## 1 Start Date/Time 10/5102 7:50 10/510210:10

1 0/5102 12:25 Stop Date/Time

1 0/5102 9:52 10/5102 12:12

1 0/5102 14:27 Test Parametera



## Yl!l!! Pbor (Barometric Pressure

, absolute)

ln . Hg 29.65 29.65 29.65 29.65 Y (Dry Gas Meter Calibration Factor) dimensionless

0 . 9940

0 . 9940 0.9940

0
. 9940 

### Cp (Pitot tube Coefficient) dimensionless

0 . 837

0
. 831 0.837 0.835 Dn (Diameter 

### of Nozzle)

Inches 0.432 0.432 0.432 0.432 9 (Total SampMng Time 

### of Test) Minutes 120.00 120.00 120

. 00 120.00 

### Mi (Orifice Pressure Drop)

ln . H20 1.00

1 . 07 1.07

1 . 05 Vm (Volume of Dry Gas Sampled- as measured)



## If (dry) 

### 68.68

74

. 129 74.256

72

. 355 T m (Gas Meter Temperature, avg

. )
Degr

. F 100 115 122 112 **V~c** 

### (Condensate

- lmplngers and silica gel) mlorg 52.3

73

. 3 69.8 65.1 Mass of Particulate collected, Filter



### mg

65

. 500 96.900 87.000 83.133 Mass 

### of Particulate 

### colected, Probe

- Acetone rinse

mg 26.436 34.104

29

. 224 29.921 Mass 

### of Particulate collected, Probe

- D.l
. rinse

mg

1 . 583 1.324 2.186 1.698 Mass of Particulate collected, Front-half

mg

93

. 519 132.328 118.410 114.752 b!l!!<!!tlo!!lf[2!1!11 Parl!metera 

## A. (Cross-sectional Area 

### of Stack)



## If

12

. 70

12

. 70
12

. 70 12.70 P 0 

### (Static Pressure 

### of Stack Gas)

ln. H20 ..Q.01 ..().01 ..().01

..()

. 01 T, (Temperature

of Stack Gas)

Deg. F 137 148 150 145 

### l.,tAp (Sq. root of velocity head of gas)



# v ln . H20 0.1691 0.1754 0.1754

0 . 1733 

### 00 2 

### (Carbon Dioxide)



### %

0

0

0
0.0 **~(Oxygen)**



### %

20

. 8 20.8 20.8 20.8 

# (
N 2 

### (Nitrogen)



### % 79.2 79.2

79

. 2
79

. 2 CalculetJont 

## v ms!d 

### (Gas Sampled, standard conditions (std))



## If

63

. 916 67.282

66

. 491
65

. 896 

## v- (Water Vapor

In Gas Sampled, std)



## If 2.46 3.45 3.29 3.07 

# a.. (Water Vapor

In 

### Gas, Proportion by Vol.)



### %

3 . 71 4.88 4.71

4 . 43 Saturated 

### Moisture In stsclc 

### gas, by volume



### %

17

. 64 23.51

24

. 44 21.86 Gd (Proportion 

### of Dry Gas In stack)



### % 96.29 95.12

95

. 29
95

. 6 Md (Molecular Weight of 

### Dry Stack Gas) lb/lb-mole 28.83 28.83 28.83 28.83 

### M. (Molecular Weight 

### of Wet Stack Gas) lbllb-mole 28.43 28.30 28.32 28.35 P, (Pressure 

### of Stack Gas, Absolute)

ln . Hg 29.65

29

. 65 29.65 29.65 lso (Percent 

### of lsoldnetlc Sampling)



### %
101

. 5 105.8 103.8 103

. 7 FlowRnuHI V, (Average Stack Gas Velocity)

ftlm (fpm)
611 636 642 630 Qotd 

### (Dry Volumetric Flow Rate, std.)


### tflm (dscfm) 6545 6611 6662 6606 

### On, (Wet Volumetric Flow Rate, std.)
W/m (wscfm) 6797 6950 6991 6912 

# a. (Measured Volumetric Flow Rate

, Actual) W/m(cfm) 

### n57 8080 8148 7995 Partlculatl Rgunt Particulate Concentrations, Alter
gr/dscf 0.0158

0 . 0222 0.0202 0.0194 Particulate Concentrations, Probe

- Acetone rinse gr/dscf 0.0064

0
. 0078 0.0068

0
. 0070 Particulate Concentrations, Probe· D. I. rinse gr/dscf 0.0004 0.0003

0
. 0005 0.0004 Particulate Concentrations

, Front-half Total gr/dscf 0.0226 0.0303 0.0275 0.0268 P!!rti£UI1!!! **~miiii5!D** 

## !31111 Particulate Emission Rate, Filter

lblhr

0 . 887 1.259 1.153 1.100 Particulate Emission Rate, Probe

- Acetone rinse
lblhr 0.358

0
. 443 0.387 0.396 Particulate Emission Rate, Probe· D. I. rinse
lblhr 0.021 0.017

0
. 029

0
. 023 Particulate Emission Rate, Front-half Total

lblhr

1 . 267 1.720

1 . 569 1.518 Standard Conditions= 

### 68u F, 29.92 "Hg Western Environmental Services and Testing, Inc. 

### 02-1057



## 13

## Owens Coming Table 14

""Waxahachie, Texas V-2 #2 

## Furnace (West) 

## METHODS PARTICULATE Run Number:



## 1

g



## 1 Start Date/Time 10/5102 7:50 10/5102 10:10 10/5102 12:25 Stop Date/Time 10/5102 9:52 10/510212:12

1 0/5102 14:27 Teet Paramltlf!



## .u.nJil Pbar (Barometric Pressure, absolute)

ln. Hg

29

. 65
29

. 65
· 29.65 29.65 Y (Dry Gas Meter catlbretion Factor) dimensionless 1.0160 1.0160 1.0160 1.0160 Cp (Pitot tube Coefficient) dimensionless

0 . 835 0.843 0.835 0.838 Dn (Diameter


### of Nozzle)

Inches 0.492 0.499 0.492 0.494 

# e (Total SampMng Time of Test) Minutes 120.00 120.00 120

. 00 120.00 AH (Orifice Pressure Drop)

ln. H20

1 . 13 1.15 1.06 1.11 Vm (Volume 

### of Dry Gas Sampled -as measured)



### ft 3 (dry) n.186 79.068 76.906 77.720 Tm (Gas Meter Temperature, avg.)
Degr. F

99 112 119 110 

# v.., (Condensate

- lmplngers and silica gel) mlorg 79.7 90.8 77.2 82.6 Mass 

### of Particulate collected, Alter

mg 69.100

94

. 800 93.900 85.933 Mass of Particulate collected

, PIObe

- Acetone rinse

mg 22.192 17.972



### 32

. 548
24

. 237 Mess of Particulate collected, PIObe- D.l. 

### rtnse

mg 1.862 1.262 2.831 1.985 Mess 

### of Particulate collected, Front-half

mg 93.154 114.034 129.279 112.156 **bS!!<!tlo!!lf~H!!** Pa[!mettlnl 

## A. (Cross-sectional Area 

### of Steck)



## ff 12.70 12.70 12.70 12.70 P 8 (Sialic Pressure 

### of Stack 

### Gas)

ln . H20

-o

. 01 -o.01 -o.01 -o.01 T, (Temperature



### of Stack Gas)
Deg.F
143 149 149 147 

### 11Ap (Sq. root 

### of velocity head of gas)



# v ln. H20 0.1525 0.1525 0.1483 0.1511 **~** (Carbon Dioxide)



### %

0

0

0 0.0 0 2 (Oxygen)



### % 20.8 20.8 20.8 20.8 N 2 (Nitrogen)



### % 79.2 79.2 79.2

79

. 2 Calcyll!t!ont 

# v"'* (Gas Sampled, standard conditions (std))



### fta 73.570 73.709 70.771 72.683 

# v- (Water Vapor In Gas Sampled, std)



### ff 3.75 4.27 3.63 3.89 

### Bw. (Water Vapor In 

### Gas, Proportion by Vol.)

o/o 4.85

5
. 48 4.88 5.07 Saturated Moisture In stack 

### gas, by volume

% 20.85 24.16 23.94 

### 22.98 Gd (Proportion


### of Dry 

### Gas In stack)

o/o 95.15 94.52 95.12 94.9 Md (Molecular Weight 

### of Dry Stack Gas) lbllb-mole 28.83 28.83 28.83

28

, 83 M, (Molecular Weight of Wet Stack Gas) lbllb-mole 28.31 28.24 28.30 28.28 P, (Pressure of Stack Gas, Absolute)

ln . Hg 29.65 29.65 29.65 29.65 lso (Percent ollsoklnetlc Sampling)

o/o 101.6

99

. 1 101

. 1 100.6 FlowRuyltt 

# v. (Average Stack Gas Velocity)

film (fpm) 554 563 541 553 

## Cot.! (Dry Volumetric Flow Rate, 

### std.)


### fflm (dscfm) 5602 5798 5613 5738 

## Cot.! (Wet Volumetric Flow Rete, 

### std.)


### fftm (wscfm) 6098 6134 5901 6045 

## 0. (Measured Volumetric Flow Rete

, Actual)


### fftm (elm) 7034 7144 6869 7016 PtrtfcUiate 

## BUu!tt Particulate Concentrations, Filter
gr/dscf 0.0145 0.0198 0.0205

0 . 0183 Particulate Concentrations, Probe

- Acetone rinse gr/dscf 0.0047 0.0038 0.0071 0.0052 Particulate Concentrations, Probe

- D.l. rinse gr/dscf 0.0004

0 . 0003 0.0006 0.0004 Particulate Concentrations, Front-hall Total gr/dscf 0.0195 0.0239 0.0282 0.0239 

## E!ld!!a!!!tl l;mtaaiS!!l 

## Bltll Particulate Emission Rate, Alter

lblhr 0.721 0.986 0.985 0.897 Particulate Emission Rete, Probe

- Acetone rinse
lblhr 0.231 0.187 0.341 0.253 Particulate Emission Rate, Probe

- D.l. rinse
lblhr 0.019

0
. 013 0.030 0.021 Particulate Emission 

### Rete, Front-half Total
lblhr 0.972 1.186 1.356 1.171 Standard Conditions= 

### 68u F, 29.92 "Hg Western Environmental Services and Testing, Inc
. 

### 02-1057



### 14

## Owens Coming Table 15

Waxahachie, Texas V-3 #1 Furnace (East) 

# c METHODS PARTICULATE Run Number:



## 1



## 2.



## 1 Start Date/Tlme 10/4102 9:30 10/4102 12:25 10/410214:57 Stop DatefTime 10/4102 11:33 10/410214:28 10/410217:00 

### Test Parametm



## Y.nU! Pt.er (Barometric Pressure, absolute)

ln . Hg

29

. 50 29.50 29.50 29.50 Y (Dry Gas Meter C&Ubration Factor) dimensionless 0.9940 0.9940

0
. 9940 0.9940 

### Cp (Pilot tube Coefficient) dimensionless 0.837

0
. 837 0.837

0
. 837 Dn (Diameter 

### of Nozzle)

Inches 0.499 0.499 0.499 0.499 

# e (Total Sampling Time 

### of Test) Minutes 120.00 120.00 120

. 00 120.00 

### Mi (Orifice Pressure Drop)

ln. H20

0
. 92 1.01

0
. 90 0.95 Vm (Volume 

### of Dry Gas Sampled- as measured)



## tf (dry)

68

. 9 72.357 68.599 69.952 T m (Gas Meter Temperature, avg

. )
Degr

. F
97 107 105 103 **V~e** (Condensate

- lmplngers and silica gel) mlorg 48.2 50.8 47.4 48.8 Mass 

### of Particulate collected, Filter



### mg 11.400 13.900 18.600 14.633 Mess 

### of Particulate collected

, Probe

- Acetone rinse

mg

10

. 148
10

. 372
20

. 260
13

. 593 Mess 

### of PartlcuJate coJJected, Probe

• D.l. rinse

mg 1.997 1.765 1.579 1.781 Mass 

### of ParticUlate collected, Front-half

mg 23.545 26.037

40

. 439 30.007 LS!9!112!!lf!l!SCUI **P!rl!meten~** 

### A. (Cross-sectional Area 

### of Stack)



## ff 12.70 12.70

12

. 70 12.70 Pv (Static Pressure of Stack Gas)

ln . H20 ..().01 ..0.01 ..().01 ..0.01 

### T, (Temperature


### of Stack Gas)
Deg.F

95 109 117 107 

### I;Kp (Sq

. root of velocity head 

### of gas)



# -r ln . H20 0.1197 0.1247 0.1178 0.1207 

### CO:! (Csrbon Dioxide)



### 'Yo

0

0

0 0.0 02 (Oxygen)



### 'Yo 20.8 20.8 20.8 20.8 

# c **~** (Nitrogen)

% 79.2

79

. 2
79

. 2
79

. 2 Ce!cullt!ona 

# vrnCJ (Gas Sampled, standard conditions (std))

n3 64.142 66.158 62.997 64.432 

# v- (Water Vapor In Gas Sampled, std)



## tf 2.27 2.39 2.23 2.30 

## e,. (Water Vapor In Gas, Proportion 

### by Vol.)



### 'Yo

3
. 42 3.49 3.42

3
. 44 Saturated Moisture In 

### stsc1c 

### gas , by volume

%

5
. 32

8
. 11 10.13 7.85 Gd (Proportion


### of Dry Gas In stack)



### 'Yo 96.58 96.51

96

. 58 96.6 Md (Molecular Weight of Dry Stack Gas) lbllb-mole 28.83

28

. 83
28

. 83 28.83 M, (Molecular Weight 

### of Wet Stack Gas) lbllb-mole 28.46 28.45 28.46 28.46 P, (Pressure of Stack Gas, Absolute)

ln . Hg 29.50 29.50 29.50

29

. 50 lso (Percent 

### of lsokinetlc Sampling)

% 104.1 104

. 4 105

. 8 104.7 FlowRny!ta V, (Average Stack Gas Velocity) Wm(fpm)
418 441 419 426 Qotd (Dry Volumetric Flow Rate, std

. )



### ft 3 /m (dscfm) 4803 4941 4639 4794 Qotd (Wet Volumetric Flow Rate, std.)


### fflm (wscfm) 4973 5119 4803 4965 O, (Measured Volumetric Flow Rate, Actual)


### fflm (elm) 

### 5304 5596 5321 5407 P!rtlcullt! 

## Buultt Particulate Concentrations, Filter
gr/dscf 0.0027 0.0032 0.0046 0.0035 Particulate Concentrations, Probe

• Acetone rinse gr/dscf

0
. 0024 0.0024 0.0050 0.0033 Particulate Concentrations, Probe

- D
. l . rinse gr/dscf 0.0005 0.0004 0.0004 0.0004 PartJcuJate Concentrations

, Front-half Total gr/dscf 0.0057

0
. 0061

0
. 0099 0.0072 e!!:!I!<Y!!I! E!DI1112n 

## BI!SI! Particulate Emission Rate, Filter

lblhr 0.113 0.137 0.181 0.144 Particulate Emission Rate, Probe

- Acetone rinse
lblhr 0.101 0.102 0.197

0
. 133 Particulate Emission Rate

, Probe

- D.l
. rinse
lblhr

0
. 020

0
. 017 0.015 0.018 Particulate Emission Rate, Front-half Total
lblhr 0.233 0.257 0.394 0.295 Standard Conditions= 

### 68u F, 29.92 "Hg Western Environmental Services and Testing, Inc. 

### 02-1057



## 15Owens Corning Table 16 **~axahachie,** Texas V-3 #2 Furnace (West) c
METHOD

5 PARTICULATE Run Number:

1

2.

l Start Date/Time 10/4102 9:30 10/4102 12:25

1 0/4102 14:57 Stop Date/Time 10/4102 11:33 10/4102 14:28 10/4102 17:00 Test Parameters

Ynl!! P.., (Barometric Pressure, absolute)

ln. Hg 29.50

29

. 50
29

. 50 29.50 Y (Dry Gas Meter Csibratlon Factor) dimensionless 1.0160 1.0160 1.0160 1.0160 Cp {Pilot tube Coefficient) dimensionless 0.835 0.843 0.835 0.838 Dn (Diameter of Nozzle)

inches 0.492 0.499 0.492 0.494 9 (Total Sampling Time of Test) Minutes 120.00 120.00 120.00 120.00 4H (Orifice Pressure Drop)

ln. H20

0
. 94

0
. 95 0.94

0
. 94 Vm (Volume of Dry Ges Sampled- as measured)

ft' {dry) 69.939 71.53 71.231 70.900 T m (Gas Meter Temperature, avg.)
Degr. F

91 104 104 100 V1c (Condensate

- impingers and silica gel) mlorg 92.5 94.8 75.3 87.5 Mass ol Particulate collected, Filter

mg 18.900 29.000 24.900 24.267 Mass ol Particulate collected, Probe

- Acetone rinse

mg 7.600 18.385 16.780 14.255 Mass of Particulate colected, Probe

- D.i
. rinse

mg 0.171 19.301 4.605 8.026 Mass of Particulate collected, Front-hall

mg 26.671 66.687 46.285 46.548 L5!!0!ti2!!lftsS!!I Paramet•• A. (Cross-sectional Area of Stack)

If 12.70 12.70 12.70 12.70 Pg (Static Pressure of Stack Gas)

ln . H20 {).01 {).01 {).01 {).01 T, (Temperature
of Stack Gas)
Deg.F
103 114 116 111 I,IEp (Sq. root of velocity head of gas)

v ln. H20 0.1312 0.1304 0.1302 0.1306 **~** (Carbon Dtoxide)

%

0

0

0 0.0 **~(Oxygen)**

% 20.8 20.8 20.8 20.8 N2 (Nitrogen)

% 79.2 79.2 79.2

79

. 2 CtJcuflllont vmold (Gas Sampled, standard conditions (std))

ft' 67.349 67.209 66.926 67.162 v- (Water Vapor In Gas Sampled, std)

ft' 4.35 4.46 3.54 4.12 Bw. (Water Vapor in Gas, Proportion by Vol.)

% 6.07 6.23 5.03 5.78 Saturated Moisture In stack gas, by volume

% 6.88 9.31 9.86 8.68 Gd (Proportion
of Dry Gas in stack)

%

93

. 93
93

. n 94.97 94.2 **~** (Molecular Weight of Dry Stack Gas) lbllb-moie 28.83 28.83 28.83 28.83 M. (Molecular Weight of Wet Stack Gas) lbllb-mole 28.17 28.16 28.29 28.21 P, (Pressure of Stack Gas, Absolute)

ln. Hg 29.50 29.50 29.50 29.50 lso (Percent of lsoklnetiC Sampling)

% . 106.0 103.5 106.2 105.2 F!owRnuna V, (Average Stack Gas Velocity)

!tim {lpm) 462 468 463 465 Oct.t (Dry Volumetric Flow Rate, std.)
ft'!m {dsclm) 5096 5060 5050 5069 Qlld (Wet Volumetric Flow Rate, std.)
ft'!m (wsclm) 5425 5396 5318 5380 a. (Measured Volumetric Flow Rate, Actual)
ft'!m {elm) 5872 5948 5882 5901 Partlculll! Rttu!tt Particulate Concentrations, Filter
gr/dscl 0.0043 0.0067 0.0057 0.0056 Particulate Concentrations, Probe

- Acetone rinse gr/dscl 0.0017 0.0042 0.0039 0.0033 Particulate Concentrations, Probe

- D.i. rinse gr/dscl

0
. 0000 0.0044 0.0011 0.0018 Particulate Concentrations, Front-hall Total gr/dscl 0.0061 0.0153 0.0107 0.0107 Particulate Emlg!on R111t Particulate Emission Rate, Filter

lblhr 0.189 0.289 0.249 0.242 Particulate Emission Rate, Probe

- Acetone rinse
!blhr 0.076 0.183 0.167 0.142 Particulate Emission Rate, Probe- D. I. rinse
lblhr 0.002 0.192 0.046 0.080 Particulate Emission Rate, Front-hall Total
lblhr 0.267 0.664 0.462 0.464 Standard Conditions= 68v F, 29.92 "Hg Western Environmental Services and Testing, Inc. 02-1057

16