background report reference ap-42 section number: 10.6€¦ · the file name...
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Background Report Reference
AP-42 Section Number: 10.6.1
Background Report Section: 4
Reference Number: 14
Title: Letter and Emission Summaries For J. M Huber Corporation, From P. McDdonald, JM Huber Corp. To R. Kalagnanam, Commerce, GA
Huber Wood Products
July 1992
' J. .r.
i ' * 'e , ,
2% .I
WOOD PRODUCTS
J.M. Huber Corgoration Wood Products wwon
Route 5, Hi hway 334 P.O. Box 690 Commerce, GA 30529 404 335-7661 Fox 404 335-7647
July 2,1992
Mr. Ramesh S. Kalagnanam Midwest Research Institute 401 Harrison Oaks Blvd., Suite 350 Cary, North Carolina 27513-2412
Dear Mr. Kalagnanam;
This letter and attached documentat in 3 SUDD~ - - 3d in response to your inquiry concerning dryer emissions from our Commerce, Georgia O.S.B. Plant. We appreciate and share your interest in obtaining quality information concerning air emissions from the wood panel industry. It is understood that thuogh the data supplied will be part of a public report , source identification will be anonymous.
Enclosed are the air emission (inlet and outlet) and operational data reports of our most recent compliance and engineering tests for the three WESP-s at Commerce, Georgia. These tests were performed while operating the dryers at maximum through-put and not at the normal lower day to day average rate. The wood used is,comprised of 90% Southern Yellow Pine and 10% soft hard woods. The three rotary kiln dryers each have individual Geoenergy Wet Electrostatic Precipitators controlling emissions.
The emission testing methods used for the test'data supplied are as follows :
DRYER;#1,#3 (APRIL 22,24, 1992)
PARTICULATE - METHOD 5 CONDENSABLE PARTICULATE - METHOD 202 VOC - METHOD '25 NOX - METHOD. 7E CO - METHOD 10 HCHO - BIF 0011 (DNPH)
., : . .
. , .
Mr. Ramesh S. Kalagnanam July 2, 1992 page 2
DRYER tt2 (MARCH 19, 1992)
PARTICULATE - METHOD 5T VOC - METHOD 25 NOX - METHOD 7E CO - METHOD 10B HCHO - SINGLE POINT MIDGET IMPINGER SAMPLING (DNPH) During our last telephone conversation you mentioned that you have dryer emission data from December, 1989. This data is for only one dryer without WESP’s attached. We feel this data is flawed and should not be used since the dryer was not operating at maximum capacity and emission data since that time indicates it is not representative of our actual inlet loading to the WESP-s.
Please accept my sincere apology for the late response to your inquiry concerning dryer emissions. I hope the enclosed information will be useful to you in preparing your report concerning the AP-42 document for the E.P.A.. If you should need further explanation on this data, please do not hesitate to contact me.
/
Sincerely:
f%3.-oJ Peter McDonald Manufacturing Engineer
ENCLOSURE
cc: Billy Martin Dave Wi 1 lis Horst Sturmlinger
HUBER DISK: MRIAP42.LET
i.
L
_. 1
TABLE 2-1 SUMMARY OF EMISSIONS DRYER STACK #1 J. M. HUBER CORPORATION COMMERCE, GEORGIA
PARAMGIFR R U N 1 R U N 2 R U N 3 R U N 4 AVERAGE
Particulate - Front Half Concentration, grldscf Emission Rate, Ibhr
Particulate -Back Half Concentration, grtdscf Emission Rate, Ibhr
Top1 Particulate Concentration, grldscf Emission Rate, Ibhr
Formaldehyde Concentration, ppm Emission Rate, Ibhr
Total Gaseous Nonmethane Organics Inlet
Concentration, ppm (as Carbon) Emission Rate, Ibhr (as Carbon) Total VOCs (1.2~ carbon emission rate)
Concentration, ppm (as Carbon) Emission Rate, lbhr (as Carbon) Total VOCs (1.2~ carbon emission rate)
Outlet
VOC Removal efficiency, 46
Carbon Monoxide Concentration, ppm Emission Rate. Ibhr
___ 0.0141 -_ 3.80
__ 0.0106 ___ 2.85
.__ 0.0247 -_ 6.66
12.9 13.0 2.16 2.00
194 . 756 49.2 45.6 59.04 54.72 '
516 945 38.4 55.6 46.08 66.12
22.0 -21.9
0.0135 3.59
0.0125 3.32
0.0260 6.90
19.6 3.00
812 51.0 61.2
1102 63.8 76.56
-25.1
187 25.3
0.0097 218
0.0105 3.01
0.0202 5.19
-__ ___
_._ -_ ___ ___ ___ ...
._
43.1 6.4
0.0124 3.39
0.0112 3.06
0.0236 6.45
15.2 2.39
807 48.6 58.3
814 52.6 63.1
-8.4
131 18.8
TABLE 3 DRYER #I INLET PARTICUJATE SUMMARY
Meter Box Y Avg Della H. incha H20 Barnmetric P m u r c . i ncha Hg Meter Volume. m.tt
Avg Meter Temp. d q F Slatle P m u r e , lncha HZO Avg Stack Temp, d q F Water Colldcd. ml Cnrbondioxid+ %
0.999
2.M 29.23 49.400 77.9
-17.00 188.7 244.6 3.1
(02) Oxygen.% 17.9 1.411 A q Sqrt Della P, q r t ( ineha HZO)
(0) Sample lime, min 60
(Dn) N d c Diameter. lncha 0.213 @) Slack Diameter, lndm 42
F i l I d , PM
(Mpw) Particulate Collecld (probe wash). g 0.0076 (Mf) PartlNhlc Collded (filler), g 0.3204
Cdmdt4, PM
(Mii) H20 Impinger (inorganic) r a l d u q g 0.0086 (Mio) McCl 1mping.x (organic) realdue, g 0.0667
CALCUUTED DATA
Standard Meter Volume. N.fl Stack P-ure, lneha Hg Moisture, 96 Molscvlar Weight-nt. ibllb-mole Velocity, f lh Slack Ama, q . f t
Volumdtic flow. a d m Volumctrie flow, d d m
Isokinclic Rate, 7%
TO(^ JiItemtfe hd/j PM
Particulate Concentration, plnldd
Particulate Eminion Rate, lWhr O r p d c k k h d J PM
Particulate Concenlmtlon. gralnldsd
Particulate Emiuion Rate, Ibhr ' . I n q p m k k k h d f PM
PadNla le Concentration. p l n l d s d Particulate Emission Rate. lWhr
Train Fractionation: filterable. 96
47.500 27.98 19.5 27.0 93.8 9.62
54,174 33.188 9L9
0.1064
3.23
0.0216 6.15
0.0028
0.79
81
mndcruible, % 19
ERCE, CA RUN4 AVERAQE RUN 2 RUN J
VIWL v w 9 2 4/23/92 R n r W 4 14474SSO 1815497A OUW37
0.999
265 29.23 56.000 85.2
-17.00 184.8 2828
3.1 17.9
1.366
60 0.213
42
0.0254 0.3329
0.02%
0.999
137 29.23 53.377 19.4
-13.00 im.6 326.7 3.5 11.4
1.330
60 0.213
42
0.0092
0.4553
0.0522
0.999
260 7.9.23 48.858 133
-17.00 184.5 2b4.6 29 17.9 1.355 60
0.213 42
0.0952 03781
0.0160
OS99
254 29.23 53.012 793
-17.000 1843 7.91.4
3.2 11.7 1.367 60
' 0.213 42
0.0433 0.3888
0.0326 0.0365 0.0715 . 0.0650 .0.0577
54.022 27.98 19.8 27.0 90.6 9.6i
52,320 32,131 109.0
'51.276 27.98 23.1 26.7 911 9.62
53,139 31,350 106.0
41.499 27.98 m.8 26.9 90.1 9.62
52,019 31,562
97.5
50.933 27.900 21.2 26.8 90.9
. 9.621 52493 31681 104.2
O . I O 2 3 0.1398 0.1537 0.1320 : 23.18 37.55 41.59 35.77
0.0104 0.0215 0.0211 0.0177 2.87 5.78 5.11 4.79
0.0085 0.0157 0.0052 0.0098 2.33 4.n 1.41 265
84 79 85 83 11 16 21 15
!
TAIILE 2.1.1 DRYER #I ourLIs1' PARTICULATE SUMMARY J. M. IlUUEll - CO,
MEASURED DATA Meter Box Y Avg Delta H, inches H20 Barometric Pressure. inches Hg Meter Volume, cu.ft Avg Meter Temp, deg F Slalic Pressure. inches H20 Avg Stack Temp, deg F Water Collected, ml
Carbon dioxide, %
Avg Sqrt Della P, sqrt(inches H20) Samplemme, min N m l e Diameter, inches Stack Diameter, inches
Particulate Collected (probe wash), g Particulate Collected (filter), g
Condendble PM H20 lmpinger (inorganic) residue, g
Oxygen, %
Filterable PM
(Mio) M e a Impingcr (organic) residue, g CALCULATED DATA
(Vmstd) Standard Meter Volume, cu.ft (Ps) Stack Pressure, inches Hg
(%Em) Moisture, % (Ms) Molecular Weight-wet. Ibllb-mole (Vs) Velocity, ft/s (As) Stack Area, sq.ft (Qa) Volumetric flow, acfm (Os) Volumetric flow, dscfm (I) kokinetic Rate.'%
(Cs) Particulate Concentration. grainldxf (En) Particulate Emission Rate, Ibhr
Condensible (back lid f) PM (0) Particulate Concentration, graiddscf (ER) Particulate Emission Rate; Ibhr
Total fmnf and buck I d f PM
(Cs) Particulate Concentration, graiddscl (ER) Particulate Emission Race. Ibhr
Told JiIfera6le (/ran! Id/) PM
1.010 0.99
29.15 31.928
80.1 1.10
142.6 169.2
2.8 17.6
0.708 60
60
30.778 29.23 20.6 26.9 44.5
19.63 52.475 35,671
MERCE, GA .... RUNj2i 4Ii2192 '.
1.010
204 29.15
44.776 88.4 1.10
146.2 279.2
2.8 18.1
0.648 60
0.299 60
1.010 1.98
29.15 44.065
83.6 1.10
147.2 281.1
2.7 17.5 0.640
60 0.299
60
1.010 213
29.18 46.036
88.7 1.10
1422 243.8
2.8 17.6
0.663 60
0.299 60
1.010 2.05
29.16 44.959
a6.9 1.100 145.2 268.0
28 17.7
0.650 60
0.299 60
O.M)(2 0.0067 . 0.0074 ' 0.0068 0.0327 0.0303 0.0202 ' 0.0277
0.01 I8 0.0102 0.0093 0.0104 0.0174 0.0240 ,0.O2CKo6 . O.OZ07
42.622 29.23 23.6 26.5 41.1
19.63 48,461 31,506
90.8
0.0141 3.80
O.OlO6 2.85
0.0247 6.66
42.309 29.23 23.8 26.5 40.7
19.63 47,956 31,022
91.6
0.0135 3.59
0.0125 3.32
0.0260 6.90
43.852 29.26 20.7 26.8 41.7
19.63 49,117 03,368
88.2
0.0097 2.78
0.0105 3.01
0.0202 5.79
42.928 29.241
227 26.6 41.2
19.635 48.5 I 1 31,965
90.2
0.0124 3.39
0.0112 3.06
0.0236 6.45
9 9 9 z z a n n m
. .
minx 2.2.1 DRYER #1 OUI'LLrl' FORMALDEIIYDE TIIW SUMMARY J. M. IIUUER - COMMERCE, GA
MEASURED DATA
Meter Box Y Avg Delta H, inches H 2 0 Barometric Pressure, inches Hg Meter Volume, ct
Avg Mefer Temp, deg F Static Pressure. inches N20 Avg Stack Temp, deg F Water Collected, ml
Carbon dioxide, %
Oxygen, % Avg Sqrt Delta P, (inches HZO)^ 1R Sample lime, min
Nazle Diameter, inches
Stack Diameter, inches Total Formaldehyde, mg
CALCULATED DATA
Standard Meter Volume, dscf Stack Pressure, inches Hg Moisture (from impingem), %
Moisture (af saturation), %
Molecular Weight-wet, Ibflb-mole
Vetocity, rt/s Slack Area, sq I t
Volumetric flow, aclm
Volumetric flow, dscfm Isokinetic Rate. %
Formaldehyde Concentralion, mgldscl
Formnldehyde Conccnfmtlon, ppm
Formoldehydc Emission Rate, lh/hr . .
0.994 1.76
29.15 43.846
82.3 1.10
145.1 216.5
2.8 17.6
0.713 60
0.277 60 19
41.509 29.21 21.1 22.8 26.8 45.0
19.63 5.30E+O4 3.56E + 04
91.2
0.46
12.9
2.16
0.994 1.57
29.15 42.249
92.3 1.10
148.2 249.5
2.8 18.1
0.674 60
0.277 60 18
39.254 29.21 21 .o
' 24.7 26.6 42.8
19.63 5.01E+04 329E+04
93.3
0.46
13.0
2.00
0.994 1.59
29.15 41.595
87.1 1.10
149.0 258.7
2 7 17.5
0.678 6 0 '
0.277 60 27
39.013 29.21 21.8 25.2
26.5 43.2
19.63
0.994 1.64
29.15 42563
87.2 1.10
147.4 248.2
2.8 17.7 0.69
60 0.277 60 21
39.925 29.23 22.1 24.2 26.6 43.7
19.63 5.09E+M 5.14E+04 3.&E+M 3.38E+M
93.0 92.5
0.69 054
19.6 1s.i 3.00 2.39
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SUMMARY OF TEST RESULTS J.M. Huber Corp - Commerce, GA
Number 2 Dryer ESP Inlet) -, . .
Volume @ Meter (Vm): Sqrt Delta P Sampling Time (min): Barometric Pressure (Pb): Delta H (H): Volume in Irnpingers (mls): Static Pressure (in. wc.): Stack Pressure (Ps): Stack Temperature (16): Meter Coefficient (Y): Pitot Coefficient (Cp): Meter Temperature (Tm): Area Stack (As): Area Nozzle (An):
- 9 e r c e n t C02 (%): Percent 0 2 (%): Percent N2 (%): Milligrams, non-cond: Milligrams, cond:
Molecular Weight Dty (Md): Volume Water (Vwstd): VolumeGas Sampled (Vmstd): Stack Gas Moisture (%): Molecular Weight Wet (Ms): Volume Gas Sampled (Vma): Stack Gas Velocity, (Vs): Volumetric Plowrate (Qs):
Volumetric Flowrate (Qa): gr/dscf Non-Condens. (a): gr/dscf Condensables (a):
- Condensables, #/Hour (E): - Non-Condensables, #/Hour (E): -Total Emissions, #/Hour (E):
Percent Isokinetic Sampling:
-~ March 19,1992
Run #l
17.732 1.383 30.0
29.00 1.04
122.7 -17.5 27.71
197 0.993 0.840
68 9.17
0.000187 3.0
79.0 150.7
126
iao
29.20 5.78
17.105 25.2
' 26.37 ' 30.737
94.16 28,830 51,808 0.1359 0.1137 28.09 33.59 61.68 97.05
Run #2
18039 1.392 30.0 2897 1.06
124.1 -17.5 27.68
194 0.993 0.840
70 9.17
0 .0187 3.0
79.0 101.4 143.3
iao
29.20 5.84
17.318 25.2
26.38 31.004 94-61
29,075 s5052 0.0903, 0.1 277 31.82 2252 54.33 97,43
Run #3
17.932 1.397 30.0
28.94 1.07
126.4 -17.5 27.65
199 0.993 0.840
70 9.17
0.000187 3.0
18.0 79.0
111.0 125
29.20 5.95
17.198 25.7
26.32 31.259 95.46
28.8% 55520 0.0996 0.1121 27.78 24.67 5244 fgb. /s' fa"-
97.36
. . . , . . . .
Volume @ Meter (Vm): Sqrt Delta P: Sampling Time (min): Barometric Pressure (Pb): Delta H (H): Volume in lmpingers (mis): Static Pressure (in. wc): Stack Pressure (Ps): Stack Temperature (Ts): Meter Coefficient (Y): Pitot Coefficient (Cp): Meter Temperature (Tm): Area Stack (As): Area Nozzle (An):
. r
&Percent c O 2 (%): Percent 0 2 (%): ' Percent N2 (%): Milligrams, non-cond: Milligrams, cond:
Molecular Weight Dry (Md): Volume Water (Vwstd): Volume Gas Sampled (Vmstd): Stack Gas Moisture (96): Molecular Weight Wet (Ms): 4 Volume Gas Sampled (Vma): Stack Gas Velocity, (Vs): Volumetric Flowrate (Qs): Volumetric Flowrate (Qa): gr/dscl Non-Condens. (a): 51 gr/dscf Condensables (a): Condensables, #/Hour (E):
SUMMARY OF TEST RESULTS J.M. Huber Corp. - Commerce, GA
Number 2 Dlyer EsP@&t, - March 19,1992
Run #1
36.401 0.592 60.0
29.01 1.46
244.5 1.2
29.10 151
1.022 0.840
67 18.35
0.000431 3.5
17.0 79.5 485 90.8
29.24 11.51
36258 24.1
2653 56836 37.82
26,560 41,635 0.0206 0.0386 8.80
Non-Condensables, #kour (E): 4.70 - Total Emissions, #/Hour (E): 13.50 . I
Percent lsokinetic Sampling: 96.93
Run #2
35.422 0.606 60.0 2897 1.57
257.9 1.2
29.06 149
1.022 0.840
68 18.35
0.000431 3.0
17.5 79.5 64.0 686
29.18 1214
35.177 25.7
26.31 56.194 3884
26,765 42,756 0.0281 0.0301
6.90 6.44
13.34 93.32
. . . . . , , . . .~ ---
Run #3
39.420 0.633 60.0
28.94 1.73
295.9 1.2
I 29.03 148
1.022 0.840
74 18.35 ,
0.000431 3.5
17.0
39.5 84.5
79.5
29.24 , 13.93
38.684 26.5
26.26 62444 40.59
27,684 44,688 0.0158 0.0337
8.00 3.74
11.74 /'?I 6G Q"l, 99.22
J.M. Huber Corp. Commerce, GA Dryer #2 ESP March 19,1992 VOC Emissions
29075 788
1578 85.75
. .
Dryer No. 2 ESP Inlet
28896 1387 2779
150.01
Gas Flowrate (DSCFM): VOC Concentration (mgC/cu M): VOC Concentration (PPMC): Total VOC as Carbon (Lb/hr):
26765 147 294
14.73
Dryer No. 2 ESP Outlet
27684 885
1773 91.70
Gas Flowrate (DSCFM): VOC Concentration (mgC/cu M): VOC Concentration (PPMC): Total VOC as Carbon (Lb/hr):
2883C 475 952
51.25
Run 1
26560 681
1364 67.70
I
K a F = 1 95.67
?EMOVAL EFFICIENCY(%): -1
' ' Carbon Monoxlde Calculations J.M. Huber, Cop.
Commerce, Georgla #2 Dryer
March19.1992
I
Run 1 Run 2 Run 3
Gas Fiowrate (DSCFM): 28830 29075 28896 CO Concentratlon (mg/cu M): 548.62 578.91 51 251 CO Concentration (PPM): 471 497 440
CO Emission Rate, (Iblhr): 59.1 9 62.99 55.42
Average CO Emission Rate, (lblhr): 59.20
.- . .
Carbon Monoxlde Calculations J.M. Huber, Cop.
. . . Commerce, Georgla ........................ .. . :.- ........
......... . . . . . . . , . , .
. .
. .
. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . :. . , . ~ + g p : O ~ f , i ;.:;:.::, ;.,::;: :,. . . . . . . . . . . . . . . . . . . . . . . . . . . ... pJ I . . . .
Gas Flowate @SCFM): CO Concentratlon (mg/cu M): CO Concentration (PPM):
CO Emission Rate, (Ibhr):
Run 1
26560 51 9.50
446
51.64
Run 2
26765 489.22
420
49.00
50.56
Run 3
27684 492 71
423
51.05
a b
NOx EMISSION RATE (Whr)
(AS N O 3
J.M. Huber Corporation Commerce, Georgia
SUMMARY OF NOx RESULTS March 19,1992
ALLOWABLE RATE (lbhr) (AS N02)
2658) 0.38 394 1 10581131 2
3 1 el 1-1 el0 15
IAMRAGEGj 8.50
27684
271 22
288
1.68
3.94
3.94
; i
TABULATlON O F TEST RESULTS J.M. Huber Corp. - Commerce, GA
#2 Dtyer ESP Outlet Formaldehyde Testing
March 19,1992
Run 1 Run 2
., . ...... . ..,
Run 3
Volume @ Meter, liters: Barometric Pressure (Pb): Meter Pressure (in. wc) Meter Coefficient (Y): Meter Temperature (Tm): Stack Temperature (Ts): Stack Pressure (Ps): Wet Fraction (Bws): Volume Gas Sampled, std I: Volume Gas Sampled, actual I: Volumetric Flowrate (Qs): Volumetric Flowrate (Qa):
57.38 29.01 1.8
1.012 73 151
29.1 0 0.241 55.99 66.61 26560 41635
60.39 2897 1.8
1.012 79 149
29.06 0.257 58.22 69.14 26765 42756
Formaldehyde
Molecular weight 30.03 Milligrams Analyte: 0.297 Concentration, mgldscm: 5.3048 Concentration, mgacm: 4.4586 Concentration, P P M 4.32
Emission Rate, poundsfiour. 0.53 Emission Rate, gramhour. 239i38
30.03 0.215 3.6929 3.1097 3.01
167. !X3 0.37
59.86 2894 1.8
1.012 72 148
29.03 0.265 58.38 69.28 27684 44688
30.03 0.380 6. 5096 5.4849 5.30
306.18 0.67
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TABLE 2-1 SUMMARY OF EMISSIONS DRYER STACK #3 J. M. HUBER CORPORATION COMMERCE, GEORGIA
PARAMETER RUN1 RUN2 RUN3 AVEIHGB
Particulate -Front Half Concentration, gr/dscf Emission Rate, Ibhr
Particulate . Back Half Concentration. grldscf Emission Rate, Iblhr
Total Particulate Concentration. gr/dscl Emission Rate, lblhr
Formaldehyde Concentration, ppm Emission Rate. Iblhr
Total Gaseous Nonmelhane Organics . Inlet
Concentration, ppm (as Carbon) Emission Rate, Ib/hr (as Carpon) Total VOCs ( 1 . 2 ~ earbqn emission rate)
Concentration, ppm (a Carbon) Emission Rate, Ibhr (as Carbon) Total VOCs (1.2~ carbon emission rate)
Outlet
VOC Removal efficiency, %
VOC Removal efficiency, % Based on the 3 run averages
Carbon Monoxide Concentration, ppm Emission Rate, lblhr
Nitrogen Oxides (as N02) Concentration, ppm Emission Rate, lblhr
O.OUi3 0.0130 7.03 3.70
0.0306 0.0295 8.19 8.41
0.0568 0.0425 15.2 12.1
27.0 26.2 4.21 4.22
822 2837 49.5 118.0 59.4 201.6
517 848 30.2 52.7 36.2 ' 63.2.
39.0 68.6
257 286 35.0 41.4
17.3 16.9 3.9 4.0
0.0289 8.39
0.0189 5.47
0.0478 13.9
33.9 5.36
I134 650 78.0
1178 74.4 89.3
-14.5
284 41.9
16.2 3.9
0.0227 6.37
0.0263 7.36
0.0490 13.7 -_
29.0 4.60
1598 94.2 113.0
848 52.4 62.9
44.3
276 39.4
16.8 3.9
TAIILE 7 DRYER #3 I N L n PARTICULATE SUMMARY J. M. IIUBER -COMMERCE, CA
RUN I RUN 2 RUN 3 IyM8oL PARM&TES uuP2 4 l w p Z 4," AVERAGE
O(LM4OU lls6.13L) 147d-1532 MEASURED DATA
Meler Box Y Avg Della H, incha H2O
Barnmetric P-urc, incha Hg
Mder Volume. cu.11
Avg MelaTemp, d q F Slalic Prruure, incha H2O
Avg Slack Temp, deg F Water Collsted, ml
Carbon d i d d c , %
Oxygen. % Avg Sqrt Della P. q r t ( incha HZO) Sample lime, min NonleDiamdu, inch- Slack Diamcler, Inches
F i l I d * PM Particulalc Collstcd (pmbe wash), g
C a u i d U * PM
H2O lmpinger (inorganic) raidue, g
Particulate collecled (filler), g
1.002
276
29.12
50.280 74.3
.17.3 210.0
239.1
4.0
17.0
1.389
60
0.213
42
0.0569
0.4892
0.0298
1.002
255 29.12
53.694 87.8
-17.3,
209.6
314.3
3.9
17.0
1.419
60
0.213
42
0.0321
0.4624
0.0589
1.002
243
29.12
30.603 89.5
-17.3
203.0
319.8
4.0
17.0
1.389
60
0.213
42
0.1382 0.4714
0.0717
1.002
2.58
29.12
51526
83.9
-17.3
207.5
291.1
4.0
17.0
1.40
60
0.213
42
0.0757
0.4743
O.OS35
(Mio) Mea lmpingu (organic) rsiduc, g o.os26 0.0626 O.OS97 o.osL73 CALCULATED DATA
Standad Meler Volume. cu.11 Slack P-urc, incha Hg
Mohlum, % Molmlar Weight-wet, Ibflb-male velocily. rvs Stack Arca, q . f t
Volumelrie now. adm
Volumeldc flow, d d m lsokinelic Rale, % ' '
T d d ' f i l t e d e (fd half) PM
Particulate Canccnlnlian, grain/dsel Particulate Emission Rale, lblhr
O q m k h u k hal f PM
Particuialc Conccnlralion. grain/d?icl Particulalc Emiuian Rale, lblhr
1 n - d ~ backhalf PM Particulate Concenlralion. grain/dwf Pertieulalc Emiuion Rsle. lbhr
Train Fractionation: fiilcrablc. %
48.774
27.85
18.7
27.2
93.8
9.62
54,156
32,262
98.0
0.1728
47.71
0.0166
4.60
0.0094
2.61
87
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27.8s
22.6
26.8
96.6
9.62 55.767
31.681
103.9
0.1503
40.80
0.0190
517
0.0179
4.86
80
47.690
27.85
24.0
26.6
94.4
9.62
54,470
3.676
100.8
0.1972
51.85
0.0193
5.08
0.0232
6.10
82
49.079
27.85
21.8
26.9
94.9
9.62
54,798
31,540
100.9
0.1734
46.81
0.0183
4.9s
0.0168
4.52
83
mndcnrible. % I 3 20 I8 17
TAllLE 2.1.1
PARTICULATE SUMMARY I)IIYER #3 OUTLET
MEASURED DATA Meter Box Y Avg Delta H, inches H20 Barometric Pressure, inches Hg Meter Volumc, cu.11 Avg Meter Temp, deg F Static Pressure, inches H20 Avg Stack Temp, deg F Water Collected, ml
Carbon dioxide, $6 Oxygen, % Avg Sqrt Delta P. sqn(inches HZO) Sample Time, min N o d e Diameter, inches Suck Diameter, inches
Filterable P M Particulate Collened (probe wash), g Particulate Collected (filter), g
CandemWe P M
1.010 2 16 29.12 46.330 79.9 1.20 148.6 292.2 3.1 17.7 0.644 60
0.299 60
0.0583 0.0179
1.010 2.47 29.12 49.754 86.3 1.20 150.2 319.1 3.1 17.7 0.690 60
0.299 60
0.0135 0.0265
1.010 248 29.12 50.565 94.3 1.20 1.50.6 295.7 3.1 17.7 0.692
60 0.299
' ' 60
0.0582 0.0311
( a i ) HZO Impinger (inorganic) residue, g 0.0267 0.0298 0.0201 (htio) 0.0620 0.0612 0.0381 0.0538 M e a Impinger (organic) residue, g
CALCUWTED DATA Standard Meter Volume, tuft Stack Pressure. inches Hg Moisture, % Molecular Weight-wet, Ibilb-mole Velocity, ftls Stack Area, sq.ft Volumetric flow, acfm Volumetric flow, dscfm Isokinetic Rate. % Told /iltero6le (JmM MJ) P M
Particulate Concentration, grain/dscf Particulate Emission Rate, Ibhr
Condem'ble (back h d f) PM Particulate Concentration, graiddscf Particulate Em'ksion Rate, lblhr
Total fmnIMd buck hnlf PM Particulate Concentration, graintdscl Particulate Emission Rate. Ibhr
1.010 2.37 29.12 48.883 86.8 1.20 149.8 302.3 3. I 17.7 0.68 60
0.299 60
0.0133 0.M52
0.0255
44.763 29.21 21.5 26.6 41.0 19.63
48,247 31,245 96.2
0.0263 7.03
0.0306 8.19
0.0568 15.22
47.545 29.21 24.0 26.5 44.0 19.63 51,817
. 33,249 96.0
0.0 130
3.70
0.0295 8.41
0.0425 12.11
47.624 29.21 22.6 26.7 44.0 19.63
5 1,832 33.845 94.5
0.0~9 8.39
0.0189 5.47
0.0478 13.86
46.644 29.21 23.4 26.6 43.0 19.63
50,632 32.780
9s.5
0.0227 6.37
0.0263 7.36
0.0190 13.73
TAULE 2.2.1 DRYER #3 OUTLEI? FORMALDEIIYDE TEST SUMMAICY J. hl. IIUISER - COMMERCE, CA
RUN I HUN 1 RUN 3
04/24/92 04/24/92 AVEKACE SYMBOL PARAMETER 04/24/92
0857-1013 1153-1311 1424-1534
MEASURED DATA
Meter Box Y Avg Delta H, inches HZO Barometric Pressure, inches Hg Meler Volume, cf Avg Meter Temp, deg F Static Prusure, inches H20 Avg Stack Temp, deg F Water Cnlkned. ml Carbon dioxide, 96
Avg Sqrt Delta P, (inches H20)- In Sample lime, min Nuzzle Diameter. inches Stack Diameter, inches Total Formaldehyde, mg
Oxygen, 96
CALCULATEDDATA
Standard Meter Volume, dscf Slack Pressure, inches Hg Moisture (from impingers), %
Moisture (at saluration), %
Molecular Weight-wet, Ibflb-mole
Velwity, fUs Stack Area, sq f t
Volumetric flow, acfm Volumetric flow, d r f m Isokinelic Rate, %
Fonnaldehydc Concentration, mgldscl Formaldehyde Concentration, ppm Formaldehyde Emission Rate, l bh r
0.994 1.02.
29.12 34.177
79.2 1.20
148.7 220.0
3.1 17.7
0.691 60
0.218 60 31
32.447
29.21 24.2 25.0 26.5 44.0
19.63 s . I ~ E + ~ 3.33E+04
103.3
0.N
27.0 4.21
0.994 0.994 1.03 1.00
29.12 29.12 34.784 34.424
89.7 95.5 1.20 1.20
150.1 151.2
221.6 217.1 3.1 3.1
17.7 17.7 0.718 0.705
60 60 0.218 0.238
60 ' . 60
30 38
32.395 . 29.21 24.4
. 25.9 263 45.8
19.63 5.39E+04
3.45E+04 99.6
0.93
26.2
4.22
31.721
29.21
24.4
26.6 26.5 45.0
19.63 5.30Et04 3 . 3 8 ~ t n 4
99.4
1.20
33.9
5.36
0.994 1.02
29.12 34.462
88.1 1.20
1m.o 219.6
3.1 17.7 0.70
60 0.238
60 33
32.188
29.21 24.3 25.8 26.5
. . 44.9 19.63
5.29E+@4 3.38E+04
100.8
1.0
29.0
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