- Page 1 and 2: dine Series Emission Standards and
- Page 3 and 4: TABLE OF CONTENTS ................
- Page 5 and 6: D.2 THERMAL INCINERATOR VOC EMISSIO
- Page 7 and 8: LIST OF TABLES End Uses of Polyprop
- Page 9 and 10: Typical Inci nerator Parameters for
- Page 11: LIST OF FIGURES Simplified Process
- Page 15 and 16: 2.1 INTRODUCTION 2.0 PROCESS AND PO
- Page 17 and 18: Polypropylene resins are supplied i
- Page 19 and 20: Table 2-2. POLYPROPYLENE (PP) PLANT
- Page 21 and 22: Fxlrus loll l'el lciiz ltlq Methano
- Page 23 and 24: Tab1e 2-3. CHARACTER1 STICS OF VENT
- Page 25 and 26: in addition to C3 and process dilue
- Page 27 and 28: used in maki fig shopping bags. For
- Page 29 and 30: I 2 CTC E%% PCS A wrcc 2 C W P U iZ
- Page 31 and 32: Table '2-6. CHARACTERISTICS OF VENT
- Page 33 and 34: A1 though polymers with molecular w
- Page 35 and 36: A - . STYREL +VACUUH SYSTEM (8) (9)
- Page 37 and 38: Tab1e 2-8. CHARACTERISTICS OF VENT
- Page 42 and 43: industrial boilers, condensers, abs
- Page 44 and 45: Eflisslo~l Swce Gas . + Drain , ''
- Page 46 and 47: The VOC stream enters at the base o
- Page 48 and 49: k Some fuels, a1 so, have chemical
- Page 50 and 51: An excel lent detailed review of th
- Page 52 and 53: m less than 18.3 mlsec (60 ftlsec).
- Page 54 and 55: and burner type but should be kept
- Page 56 and 57: flame burners. Overall, this system
- Page 58 and 59: surface of a solid catalyst. The ca
- Page 60 and 61: 3.1.3.1 Catalytic Incinerator VOC D
- Page 62 and 63: abrasion on the banks of the water
- Page 64 and 65: I gases may consist of a single con
- Page 66 and 67: W I N cn WGIADEW GAS COOLANT "'T f-
- Page 68 and 69: stream downward through a fixed car
- Page 70 and 71: Adsorbers can foul and hence are no
- Page 72 and 73: to the vapors, absorbing the solute
- Page 74 and 75: Reference 1, p. 749. Keller, M. Cmm
- Page 76 and 77: 42. Reference 40, p. 69. 43. Refere
- Page 78 and 79: These RACT recommendations were mad
- Page 80 and 81: C Table 4-2. UNCONTROLLED EMISSION
- Page 82 and 83: design and operating conditions tha
- Page 84 and 85: areas nationwide and provide inform
- Page 86 and 87: A condenser is expected to be the m
- Page 88 and 89: Table 4-6. ADDITIONAL ENERGY REQUIR
- Page 90 and 91:
would be largely, if not entirely,
- Page 92 and 93:
attery-limit costs and do' not incl
- Page 94 and 95:
cn I ;P Tab1e 5-2. INSTALLATION COS
- Page 96 and 97:
Table 5-3. ANNUALIZED COST FACTORS
- Page 98 and 99:
FOOTNOTES FOR Tab1 e 5-3 (Concl ude
- Page 100 and 101:
cmmrci a1 1y available size of .l .
- Page 102 and 103:
periods of continuous flow for stan
- Page 104 and 105:
The catalyst bed size requi red dep
- Page 106 and 107:
steam and by a regression analysis
- Page 108 and 109:
C Table 5-5. HIGH-DENSITY POLYETHYL
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L I I 1 I reductions from uncontrol
- Page 112 and 113:
Table 5-7. COST ANALYSIS FOR POLYPR
- Page 114 and 115:
Table 5-9. COST ANALYSIS FOR POLYPR
- Page 116 and 117:
I N Table 5-10, COST ANALYSIS FOR H
- Page 118 and 119:
elow the 0.12 kg VOC/1000 kg of pro
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Table 5-13. COST ANALYSIS FOR POLYS
- Page 123 and 124:
C Table 5-16. COST EFFECTIVENESS OF
- Page 125 and 126:
REFERENCES FOR CHAPTER 5 Polymer Ma
- Page 127:
Reference 12, pp. Reference 12, pp.
- Page 130 and 131:
APPENDIX A LIST OF COMMENTERS' Comm
- Page 132 and 133:
I I I Monsanto Company 800 N. Lindb
- Page 134 and 135:
Mr. J. R. Farmer Page 3 EPA June 16
- Page 136 and 137:
and removal. Most slurry process wi
- Page 138 and 139:
c.Jnissions factors- However, diffe
- Page 140 and 141:
COMMENTS BY THE TEXAS CHEMICAL COUN
- Page 142 and 143:
If not, we think they should not lw
- Page 144 and 145:
* Includes fugitive and miscell **
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I 1 ov&state both the missions and
- Page 148 and 149:
* W. Ja'dkR. Farmer , June 21, 1982
- Page 150 and 151:
Mv NAME IS RICHARD A. SYMULESKI , I
- Page 153 and 154:
-4- ISSIBNS FROM CONTIMOOUS k8L'IS~
- Page 155 and 156:
1 BACKGiRQUNP RIE UG SHOULD DESCRIB
- Page 157 and 158:
THEREARE A N ER Of ENGINEERING BRAC
- Page 159 and 160:
IS CONCERN IS ?HAT BWE INCINERATOR
- Page 161 and 162:
, P. 0.Box 3766 June 21, 1982 Uoumt
- Page 165 and 166:
Mr. Jack R. Fanner., Chief July 19,
- Page 168 and 169:
OATL4 UNITED STATES ENVIRONMENTAL P
- Page 170 and 171:
APPENDIX C. MAJOR ISSUES AND RESPON
- Page 172 and 173:
are improving and expanding the dat
- Page 174 and 175:
has acknowledged after discussion w
- Page 176 and 177:
the Enviroscience costs. For exampl
- Page 178 and 179:
would be applied to uncontrolled em
- Page 180 and 181:
about the imp1 ication that thermal
- Page 183 and 184:
APPENDIX D EMISSION SOURCE TEST DAT
- Page 185:
on air-assisted flares. The values
- Page 188 and 189:
s 0 E 0 .I- C, C, P e L L 0 0 V) V)
- Page 190 and 191:
Canpany and Lo~catio~n Arco Polymer
- Page 192:
I I b) spent catalyst, c) waste pol
- Page 195 and 196:
Table D-4. TYPICAL INCINERATOR PARA
- Page 197 and 198:
The principle underlying the Byron
- Page 199 and 200:
D.2.2 Environmental Protection Agen
- Page 201 and 202:
two to three hours for each sample.
- Page 203 and 204:
Table D-6. AIR OXIDATION UNIT THERM
- Page 205 and 206:
fuel value of the streams fed to it
- Page 207 and 208:
utadiene unit at Houston, Texas, an
- Page 209 and 210:
2. Sampling and Analytical Techniqu
- Page 211:
subsequent survey in September 1978
- Page 214 and 215:
. The thermal oxidizer is provided
- Page 216 and 217:
he results of the Union Carbide wor
- Page 218 and 219:
eing undertaken to determine the ef
- Page 221 and 222:
esuIts are for a butadiene plant, a
- Page 223 and 224:
weve large enough to mask the effec
- Page 225:
13. Letter and attachments f~om Bow
- Page 228 and 229:
APPENDIX E: DETAILED DESIGN AND COS
- Page 230 and 231:
Table E-I. PROCEDURE TO DESIGN 98 P
- Page 232 and 233:
FOlOTNOTES FOR TABLE E-1 (continued
- Page 234 and 235:
-- - - --- - --- Table E-2. FLARE B
- Page 237 and 238:
auxi 1i ary fuel, considering requi
- Page 239 and 240:
Table E-3. CAPITAL AND ANNUAL OPERA
- Page 241 and 242:
I Foot notes for Tab 1e E-3 (Conclu
- Page 243 and 244:
01 0 - 0 r m o D,?? 92%
- Page 245 and 246:
Tab1e E-5. GENERALIZED WASTE GAS CO
- Page 247 and 248:
Footnotes for Table E-6 a Haste gas
- Page 251 and 252:
TABLE E-7. CAPITAL AND ANNUAL OPERA
- Page 253:
E.4.1 Catalytic Incinerator Design
- Page 256 and 257:
Itefia - - I I I Tahl~F-R, OPERATIN
- Page 259 and 260:
Catalytic Incinerator Equipment Pur
- Page 261 and 262:
,000 - Key : 10 $ 3 0.5 1 10 100 I
- Page 263 and 264:
-___P___P_5-==-=- Table E-11. CAPIT
- Page 265 and 266:
(1) styrene in steam and .(2) sytre
- Page 267 and 268:
Table E-12. PROCEDURE TO CALCULATE
- Page 269 and 270:
characteristics given primarily in
- Page 271 and 272:
Table E-14. PROCEDURES TO CALCULATE
- Page 273 and 274:
FOOTNOTES FOR Table E-14 (concluded
- Page 275 and 276:
Table E-16. CAPITAL AND ANNUAL OPER
- Page 277 and 278:
Footnotes for Table E-16 (Concluded
- Page 279 and 280:
- 10 I00 1,OOC Refrigeration Capaci
- Page 281 and 282:
Table E-17.: PIPING AND DUCTING DES
- Page 283 and 284:
Table E-19. INSTALLED PIPING COSTS~
- Page 285 and 286:
REFERENCES FOR APPENDIX E Kalcevic,
- Page 287:
Reference 26, pp. 3-191, 3-212 thro
- Page 290 and 291:
APPENDIX F. CALCULATION OF UNCONTRO
- Page 292 and 293:
Table F-2 summarizes these costs fo
- Page 294 and 295:
C Table F-3. BASIC MINIMUM COSTS AT
- Page 297 and 298:
Polymer Table F-5. SUMMARY OF COST
- Page 299 and 300:
I ~ Inserting the above information
- Page 301 and 302:
I A W Tab1 e F-6. CONTROL COSTS FOR
- Page 303 and 304:
condenser sizes are not necessarily
- Page 305 and 306:
(15,770 - 1,080) ER (3.09 ' (2,875
- Page 307:
TECHNJCAL REPORT DATA {Please read