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dine Series Emission Standards and
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TABLE OF CONTENTS ................
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D.2 THERMAL INCINERATOR VOC EMISSIO
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LIST OF TABLES End Uses of Polyprop
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Typical Inci nerator Parameters for
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LIST OF FIGURES Simplified Process
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2.1 INTRODUCTION 2.0 PROCESS AND PO
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Polypropylene resins are supplied i
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Table 2-2. POLYPROPYLENE (PP) PLANT
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Fxlrus loll l'el lciiz ltlq Methano
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Tab1e 2-3. CHARACTER1 STICS OF VENT
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in addition to C3 and process dilue
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used in maki fig shopping bags. For
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I 2 CTC E%% PCS A wrcc 2 C W P U iZ
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Table '2-6. CHARACTERISTICS OF VENT
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A1 though polymers with molecular w
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A - . STYREL +VACUUH SYSTEM (8) (9)
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Tab1e 2-8. CHARACTERISTICS OF VENT
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3.0 EMISSION CONTROL TECHNIQUES Vol
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that they require for complete comb
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PILOT AND CENTER mAlri JET ELNATION
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Ground flares are usually enclosed
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flare was operated with from 130 t
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w Table 3-1 . FLARE EMISSIONS STUDI
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has become less common during the p
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Waste Gas- Stack Section Figure 3-3
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chamber temperatures ranging from 7
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= alti-
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control can be used. Any breakdown
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and, in some cases, reused in the p
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are immiscible with the coolant. Th
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3.2 .I .1 Condenser Control Efficie
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VOC -*, VENT TO VcntS~ AmOSPnERE Fi
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ABSORBlHG UQUlD WITH VOC OUT To Dis
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REFERENCES FOR CHAPTER 3 Lee, K.C.,
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Reference 24, p. 34. Key, J . A. Or
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4.1 INTRODUCTION 4.0 ENVIRONME NTAL
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Table 4-1. UNCONTROLLED EMISSION RA
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C Table 4-3. UNCONTROLLED EMISSION
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the results and an analysis of cost
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Tab1e 4-4. MODEL PLANT ENVIRONMENTA
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Tab1e 4-5. ADDITIONAL ENERGY REQUIR
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-- Table 4-7. ADDITIONAL ENERGY REQ
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5.0 CONTROL COST ANALYSIS OF RACT T
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m I W 1. Simple. continuous uanuall
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Tab1e 5-2, INSTALLATION COST FACTOR
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FOOTNOTES FOR Tab1 e 5-3 a Incl ude
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In order to prevent an explosion ha
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analysis of the Distil 1 ation NSPS
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Install ed piping and ducting costs
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estimated by the same procedure as
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.ble 5-4. POLYPROPYLENE MODEL PLANT
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Table 5-6. POLYSTYRENE MODEL PLANT
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emitters, while other dryers, e.g.,
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Table 5-8. COST ANALYSIS FOR POLYPR
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other dryers may have higher or low
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Table 5-11. COST ANALYSIS FOR HIGH
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Table 5-12. COST ANALYSIS FOR POLYS
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Polymer Table 5-15. COST EFFECTIVEN
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effectiveness of polystyrene contro
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EEA. Distil lation NSPS Pi peline C
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APPENDIX A LIST OF COMFIENJERS
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- Page 133 and 134: Mr. J. R. Famet Page 2 EPA June 16,
- Page 135 and 136: October 19, 1981 Attachment to June
- Page 137 and 138: Be The mocial plant does nst incEud
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- Page 145 and 146: REFERENCES Texas Chemical Council t
- Page 147 and 148: ' Y !. Jack R. Faner o The A~ency h
- Page 149 and 150: NATION& AIR POLLUTION CONTROL Y COM
- Page 151: " DEFINITION OF INCINERATION AS MCT
- Page 154 and 155: -5- IN SUWRYj THE AGENCY, BY RELYIN
- Page 156 and 157: STRUMS WITH RELATIVELY STABLE FLOW
- Page 158 and 159: 1 I CoHPlTIONS OF 10 TIMES NORMAL S
- Page 160 and 161: I 1 I - gU - I I n G PROPO.SED INCI
- Page 162: The use of data from the CTG for ai
- Page 166: Mr. Jack R. Farmer, Chief July 19,
- Page 169 and 170: APPENDIX C MAJOR ISSUES AND RESPONS
- Page 171 and 172: generally for large volume, variabl
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- Page 181: processes (e.g ., polypropylene and
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FOlOTNOTES FOR TABLE E-1 (continued
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-- - - --- - --- Table E-2. FLARE B
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auxi 1i ary fuel, considering requi
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Table E-3. CAPITAL AND ANNUAL OPERA
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I Foot notes for Tab 1e E-3 (Conclu
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01 0 - 0 r m o D,?? 92%
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Tab1e E-5. GENERALIZED WASTE GAS CO
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Footnotes for Table E-6 a Haste gas
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TABLE E-7. CAPITAL AND ANNUAL OPERA
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E.4.1 Catalytic Incinerator Design
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Itefia - - I I I Tahl~F-R, OPERATIN
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Catalytic Incinerator Equipment Pur
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,000 - Key : 10 $ 3 0.5 1 10 100 I
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-___P___P_5-==-=- Table E-11. CAPIT
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(1) styrene in steam and .(2) sytre
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Table E-12. PROCEDURE TO CALCULATE
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characteristics given primarily in
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Table E-14. PROCEDURES TO CALCULATE
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FOOTNOTES FOR Table E-14 (concluded
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Table E-16. CAPITAL AND ANNUAL OPER
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Footnotes for Table E-16 (Concluded
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- 10 I00 1,OOC Refrigeration Capaci
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Table E-17.: PIPING AND DUCTING DES
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Table E-19. INSTALLED PIPING COSTS~
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REFERENCES FOR APPENDIX E Kalcevic,
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Reference 26, pp. 3-191, 3-212 thro
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APPENDIX F. CALCULATION OF UNCONTRO
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Table F-2 summarizes these costs fo
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C Table F-3. BASIC MINIMUM COSTS AT
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Polymer Table F-5. SUMMARY OF COST
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I ~ Inserting the above information
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I A W Tab1 e F-6. CONTROL COSTS FOR
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condenser sizes are not necessarily
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(15,770 - 1,080) ER (3.09 ' (2,875
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TECHNJCAL REPORT DATA {Please read