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 

SERVICES AND 

TESTING, 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 
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. 
V -1 Cooling_ Section EPN13 Formaldehyde 

V2L" - me F orma ld e h d ay1 e s ources 

Stack Air 

Source Number Contaminant 

V -2 Mixing Chamber EPN22 Formaldehyde 

V-2 Cooling Section EPN23 Formaldehyde 

V -2 Smoke Stripper EPN55 Formaldehyde 

V3L" - me F orma ld e h d IYI e s 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 

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 
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 

Emission Rate 

lbslhr 

1.518 

1.171 

2.689 

3.12 

Emission Rate 

lbslhr 

0.295 

0.464 

0.759 

3.13 

iii 
c-·· 

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 

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 

IV 
g

g 

Figure 6: V -2 Smoke Stripper 25 

Figure 7: V-2 #1 Furnace Stack (East) 26 

Figure 8: V-2 #2 Furnace Stack (West) 27 

Figure 9: V -3 Mixing Chamber 29 

Figure 10: V-3 Cooling Section 30 

Figure 11: V -3 Smoke Stripper 31 Figure 12: V -3 #1 Furnace Stack (East) 32 Figure 13: V-3 #2 Furnace Stack (West) 33 

Figure 14: Particulate Sampling Train 36 

Figure 15: Formaldehyde Sampling Train 38 

( 

v 
( 

pp

y

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 

vi 
(_.' 

(Western Environmental) to provide point source emissions surveys, analysis, and reporting on their 

behalf. The emissions of formaldehyde and particulate matter (PM) from various stacks were determined 

October 1 through 5, 2002. The sources are listed below. 

Source 

V -1 Mixing Chamber 

V -1 Cooling Section 

V-2 Mixing Chamber 

V-2 Cooling Section 

V-2 Smoke Stripper 

V -3 Mixing Chamber 

V -3 Cooling Section 

V -3 Smoke Stripper 

V-1 DEP 

V-2 #1 Furnace (East) 

V-2 #2 Furnace (West) 

V -3 #1 Furnace (East) 

V-3 #2 Furnace (West) 

Western Environmental Services and Testing, Inc. 

Table 1 

Sources Tested 

Air 

Stack Number Contaminant 

EPN10 Formaldehyde 

EPN13 Formaldehyde EPN22 Formaldehyde 

EPN23 Formaldehyde 

EPN55 Formaldehyde EPN40 Formaldehyde 

EPN41 Formaldehyde 

EPN56 Formaldehyde 

EPN03 PM EPN19 PM 

EPN20 PM 

EPN38 PM 

EPN39 PM 

02-1057 

EPA 

Test Methods 

1-4,316 1-4, 316 

1-4, 316 

1-4,316 

1-4, 316 

1-4, 316 

1-4,316 

1-4, 316 

1-5 

1-5 

1-5 

1-5 

1-5 
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 

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 2 
Y (Dry Gas Meter Calibration Factor) dimensionless 0.9910 0.9910 0.9910 0.9910 

Cp (Pilot tube Coefficient) dimensionless 0.631 0.631 0.637 0.631 

Dn (Diameter of Nozzle) Inches 0.242 0.242 0.241 0.242 

8 (Total Sampling Time of Test) Minutes 87.50 87.50 87.50 87.50 

.6H (Orifice Pressure Drop) ln. H20 0.89 0.80 0.73 0.84 

Vm (Volume of Dry Gas Sampled· as measured) 113 (dry) 47.709 45.632 44.100 46.n1 

T m (Gas Meter Temperature, avg.) Degr. F n 90 92 63 

v,. (Condensate- impingers and silica gel) mlorg 87.9 88.9 85.5 88.4 

Mass of Formaldehyde collected mg 6.587 6.750 6.730 6.669 

l.!!1£ltiRD!fll!BJII!Imm-s 

A. (Cross-sectional Area of Stack) If 82.93 82.93 82.93 82.93 

P g (Static Pressure of Stack Gas) ln. H20 -o.30 -Q.30 -o.30 -o.30 

T1 (Temperature of Stack Gas) Deg.F 228 237 228 232 

v·.dp (Sq. root of velocity head of gas) {"ln. H20 0.5882 0.5634 0.5374 0.5758 

C02 (Carbon Dioxide) % 0.4 0.4 0.4 0.4 

0 2 (Oxygen) % 20.4 20.4 20.4 20.4 

N2 (Nitrogen) % 79.2 79.2 79.2 79.2 

Calcyllti!!DI 

v....., (Gas Sampled, standard conditions (std)) It" 46.234 43.384 41.585 44.809 

v_ (Water Vapor in Gas Sampled, std) II" 4.14 4.18 4.02 4.16 

B,. (Water Vapor in Gas, Proportion by Vol.) % 8.21 8.80 8.82 8.51 

G0 (Proportion of Dry Gas in stack) % 91.8 91.2 91.2 91.5 

M0 (Molecular Weight of Dry Stack Gas) lbllb-mole 28.88 28.88 28.88 28.88 

M. (Molecular Weight of Wet Stack Gas) lbllb-rnole 27.99 27.92 27.92 27.95 

P 1 (Pressure of Stack Gas, Absolute) ln. Hg 29.68 29.68 29.68 29.68 

lso (Percent of lsokinetlc Sampling) % 103.8 102.9 102.8 103.4 

FIC!WRnylll! 

V1 (Average Stack Gas Velocity) ftlm (fpm) 2282 2202 2102 2242 

a.,. (Dry Volumetric Flow Rate, std.) 113/m (dscfm) 132186 125132 121000 128659 a.,. (Wet Volumetric Flow Rate, std.) tt"lm (wscfm) 144015 137201 132710 140608 

a. (Measured Volumetric Flow Rate, Actual) ll"lm (elm) 189254 182652 174340 185953 

FRnn•lc!ehvc!e Ruulll 

Formaldehyde Concentrations gr/dscf 0.0022 0.0024 0.0025 0.0023 Formaldehyde Concentrations ppm 4.02n 4.3985 4.5752 4.2131 

E!!nn•IS!!Ibvc!e Emilll!!D Bllll 

Formaldehyde Emission Rate lb/hr 2.491 2.575 2.590 2.533 

Standard Conditions = 6ff F, 29.92 "Hg 

Western Environmental Services and Testing, Inc. 02-1057 3 
Y (Dry Gas Metar Csllbretlon Factor) dimensionless 0.9910 0.9910 

c;, (Pitot tube Coefficient) dimensionless 0.837 0.837 

D. (Diameter of Noule) Inches 0.241 0.241 

8 (Total Sampling Time of Test) Minutes 87.50 87.50 

(Orifice Pressure Drop) ln. H20 0.77 0.77 

Vm (Volume of Dry Gas Sampled- as measured) If {dry) 44.813 44.813 

T m (Gas Meter Temperature, avg.) Degr. F 85 85 

v., (Condensate- impingers and silica gel) mlorg 87.5 87.5 

Mass of Formaldehyde collected mg 13.274 13.274 

fl[lmelllrs 

A. (Cross-sectional Area of Stack) If 82.93 82.93 

P g (Static Pressure of Steck Gas) ln. H20 -0.30 .0.30 

T, (Temperature of Stack Gas) Deg.F 234 234 

(Sq. root of velocity head of gas) rln.H20 0.5367 0.5367 

C02 (Csrbon Dioxide) % 0.4 0.4 

( 02 (Oxygen) % 20.4 20.4 

N2 (Nitrogen) % 79.2 79.2 

Ca!culat!S!M 

v....., (Gas Sampled, standard conditions (std)) fe 42.796 42.796 

v_ (Water Vapor in Gas Sampled, std) If 4.12 4.12 

S... (Water Vapor In Gas, Proportion by Vol.) % 8.78 8.78 

Gd (Proportion of Dry Gas In stack) % 91.2 91.2 

Md (Molecular Weight of Dry Stack Gas) lbllb-mole 28.88 28.88 

M. {Molecular Weight of Wet Stack Gas) lbllb-mole 27.92 27.92 

P, (Pressure of Stack Gas, Absolute) ln. Hg 29.68 29.68 

I so (Percent of lsokinetic Sampling) % 106.4 106.4 

Fin Rgu!ta 

v. {Average Stack Gas Velocity) lt/m(fpm) 2109 2109 

Qltd (Dry Volumetric Flow Rate, std.) rftm {dschn) 120321 120321 Qltd (Wet Volumetric Flow Rate, std.) fftm (wscfm) 131900 131900 

a. (Measured Volumetric Flow Rate, Actual) 113/m (elm) 174917 174917 

E!!rmald!hvde Rnuna 

Formaldehyde Concentrations gr/dscf 0.0048 0.0048 

Formaldehyde Concentrations ppm 8.7686 8.7686 

Egrml!ldehv!!l Emi!lli2D BlllU 

Formaldehyde Emission Rate lblhr 4.936 4.936 

Standard Conditions= 6ff' F, 29.92 "Hg 

Western Environmental Services and Testing, Inc. 02-1057 4 
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 

C02 (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.) ft3/m (wscfm) 10293 10501 9455 10083 

a. (Measured Volumetric Flow Rate, Actual) ft3/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 
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 

C02 (Carbon Dioxide) % 0.6 0.4 0.4 0.5 

02 (Oxygen) % 19.4 19.6 19.8 19.6 

N2 (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 

P0 (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.) 113/m (wscfm) 190492 188388 185608 188163 

Q 8 (Measured Volumetric Flow Rate, Actual) 113/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 
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) ft3 (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 

T8 (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 

C02 (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.) ft3/m (dscfm) 23767 23856 22824 23483 

Cold (Wet Volumetric Flow Rate, std.) ft3/m (wscfm) 25372 25461 24535 25123 

Ca (Measured Volumetric Flow Rate, Actual) ft3/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. 02-1057 
(

y 

) 

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) ft3 (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.) ft3/m (dscfm) 1335 1254 1341 1310 Oo~~~ (Wet Volumetric Flow Rate, std.) ft3/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. 02-1057 
e (Total Sampling Time of Test} Minutes 140.00 140.00 140.00 140.00 

AH (Orifice Pressure Drop) ln. H20 0.40 0.39 0.38 0.39 

V m (Volume of Dry Gas Sampled- as measured} ft" {dry} 53.165 53.191 53.561 53.306 

T m (Gas Meter Temperature, avg.) Degr. F 87 97 106 96 

v .. {Condensate -lmpingers and sHica gel} mlorg 88.8 94.1 91.6 91.5 

Mass of Formaldehyde coHected mg 8.550 9.738 7.459 8.582 

Pgrameters 

A. (Cross-sectional Area of Stack} tt2 147.16 147.16 147.16 147.18 

Pg (Static Pressure of Stack Gas} ln. H20 -o.31 -o.30 -o.30 -o.30 

T. (Temperature of Stack Gas} Deg. F 1n 179 1n 178 

lrAp (Sq. root of velocity head of gas} .r ln. H20 0.4001 0.3957 0.3904 0.3954 

C02 {C&rbon Dioxide} % 0.4 0.6 0.8 0.5 

0 2 (Oxygen} % 20.6 20.4 20.6 20.5 

Nz (Nitrogen} % 79 79 78.8 78.9 

Calcul!!t!ont 

V.- (Gas Sampled, standard conditions (std}} ft" 50214 49.308 49.909 49.4n 

v_ (Water Vapor In Gas Sampled, std} ft" 4.18 4.43 4.31 4.31 

e_ (Water Vapor In Gas, Proportion by Vol.} % 7.68 8.24 8.10 8.01 

( . !urated Moisture In stack gas, by volume % 4723 49.61 47.37 49.07 

"""d (Proportion of Dry Gas In stack} % 92.3 91.8 91.9 92.0 

Md (Molecular Weight of Dry Stack Gas} lbllb-mole 28.89 28.91 28.92 28.91 

M. (Molecular Weight of Wet Stack Gas} lbllb-mole 28.05 28.01 28.04 28.03 

P. (Pressure of Stack Gas, Absolute} ln.Hg 29.49 29.49 29.49 29.49 

lso (Percent of lsoklnetlc Sampling} % 99.5 98.1 99.8 99.2 

FlowRnult! 

v. (Average Stack Gas Velocity} ft/m (fpm) 1497 1518 1461 1492 

(Dry Volumetric Flow Rate, std.} ft"im (dscfm} 166039 100n1 161296 164702 

(Wet Volumetric Flow Rate, std.) ft"/m(wscfm} 179880 181752 175515 179042 

a. (Measured Volumetric Flow Rate, Actual} ft3/m (cfm} 220274 223339 214990 219534 

FormaldehVdt Rnult!t Formaldehyde Concentration ppm 4.8137 5.5833 4.3115 4.9028 

Formaldehyde Concentration gr/dscf 0.0026 0.0030 0.0024 0.0027 Formals!!hl!sll Emlui2n Bill! 

Formaldehyde Emission Rate lblhr 3.739 4.356 3.253 3.783 

Standard Conditions= 68° F, 29.92 "Hg 

Western Environmental Services and Testing, Inc. 02-1057 9 
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 

P8 (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 

C02 (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 

Q111 (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. 02-1057 
Cp (Pitot tube Coefficient) dimensionless 0.842 0.826 0.842 0.837 

Dn (Diameter of Nozzle) Inches 0.180 0.176 0.180 0.179 

a (Total Sampling Time of Test) Minutes 72.00 72.00 72.00 72.00 

&H (Orifice Pressure Drop) ln. H20 1.44 1.21 1.22 1.29 

Vm (Volume of Dry Gas Sampled- as measured) tf (dry) 48.852 44.962 45.776 48.530 

T m (Gas Meter Temperature, avg.) Degr. F 90 95 99 95 

v.., (Condensate- irnpingers and silica gel) mlorg 56.8 50.6 31.0 46.1 

Mass of Formaldehyde collected mg 20.494 18.327 19.649 19.490 

Location/Process Parameters 

A. (Cross-sectional Area of Stack) ff 1.03 1.03 1.03 1.03 

P g (Static Pressure of Stack Gas) ln. H20 0.60 0.60 0.60 0.60 

T. (Temperature of Stack Gas) Deg.F 162 158 156 158 

lr&p (Sq. root of velocity head of gas) .(ln. H20 1.2148 1.1417 1.1212 

(Carbon Dioxide) % 0 0 0 0.0 

02 (Oxygen) % 20.8 20.8 20.8 20.8 

N2 (Nitrogen) % 79.2 79.2 79.2 79.2 

Calculations 

Vrnlld (Gas Sampled, standard conditions (std)) fl3 45.955 41.907 42.326 43.396 Vwald (Water Vapor In Gas Sampled, std) fl3 2.67 2.38 1.46 2.17 

B, (Watar Vapor in Gas, Proportion by Vol.) % 5.50 5.38 3.33 4.74 

Saturated Moisture in stack gas, by volume % 33.23 29.91 28.45 30.53 

Gd (Proportion of Dry Gas in stack) % 94.5 94.6 96.7 95.3 

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 28.24 28.25 28.47 28.32 P. (Pressure of Stack Gas, Absolute) ln. Hg 29.54 29.54 29.54 29.54 

lso (Percent of lsokinetic Sampling) % 100.7 103.7 98.1 100.8 

Flow Result! 

v. (Average Stack Gas Velocity) film (fpm) 4530 4161 4143 4278 

Q1111 (Dry Volumetric Flow Rate, std.) tftm (dscfm) 3699 3426 3496 3541 Qlld (Wet Volumetric Flow Rate, std.) tt3/m (wscfm) 3914 3621 3617 3717 Q8 (Measured Volumetric Flow Rate, Actual) ft3/m (cfm) 4671 4291 4272 4411 

Formaldehyde Resuhs 

Formaldehyde Concentrations, ppm ppm 12.6073 12.3635 13.1239 12.6982 

Formaldehyde Concentrations gr/dscf 0.0069 0.0067 0.0072 0.0069 

Formaldehyde Emlaalon R!!!s 

Formaldehyde Emission Rate lb/hr 0.218 0.198 0.215 0.210 

Standard Conditions= 68° F, 29.92 "Hg 

It 

Western Environmental Services and Testing, Inc. 02-1057 
c;, (Pitot tube Coefficient) d

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.) 113/m (dsclm) 10912 11105 11552 11190 Oot~~ (Wet Volumetric Flow Rate, std.) 113/m (wsclm) 11878 12015 12467 12120 

a. (Measured Volumetric Flow Rate, Actual) 113/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 
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 

002 (Carbon Dioxide) % 0 0 0 0.0 

~(Oxygen) 

% 20.8 20.8 20.8 20.8 

( N2 (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 
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) ft3 (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 

P8 (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 

N2 (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 
p (

) 

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.) ft3/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 15 
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