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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
- 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 41 and 42: 3.0 EMISSION CONTROL TECHNIQUES Vol
- Page 43 and 44: that they require for complete comb
- Page 45 and 46: PILOT AND CENTER mAlri JET ELNATION
- Page 47 and 48: Ground flares are usually enclosed
- Page 49 and 50: flare was operated with from 130 t
- Page 51 and 52: w Table 3-1 . FLARE EMISSIONS STUDI
- Page 53 and 54: has become less common during the p
- Page 55 and 56: Waste Gas- Stack Section Figure 3-3
- Page 57 and 58: chamber temperatures ranging from 7
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- Page 61 and 62: control can be used. Any breakdown
- Page 63 and 64: and, in some cases, reused in the p
- Page 65: are immiscible with the coolant. Th
- Page 69 and 70: VOC -*, VENT TO VcntS~ AmOSPnERE Fi
- Page 71 and 72: ABSORBlHG UQUlD WITH VOC OUT To Dis
- Page 73 and 74: REFERENCES FOR CHAPTER 3 Lee, K.C.,
- Page 75 and 76: Reference 24, p. 34. Key, J . A. Or
- Page 77 and 78: 4.1 INTRODUCTION 4.0 ENVIRONME NTAL
- Page 79 and 80: Table 4-1. UNCONTROLLED EMISSION RA
- Page 81 and 82: C Table 4-3. UNCONTROLLED EMISSION
- Page 83 and 84: the results and an analysis of cost
- Page 85 and 86: Tab1e 4-4. MODEL PLANT ENVIRONMENTA
- Page 87 and 88: Tab1e 4-5. ADDITIONAL ENERGY REQUIR
- Page 89 and 90: -- Table 4-7. ADDITIONAL ENERGY REQ
- Page 91 and 92: 5.0 CONTROL COST ANALYSIS OF RACT T
- Page 93 and 94: m I W 1. Simple. continuous uanuall
- Page 95 and 96: Tab1e 5-2, INSTALLATION COST FACTOR
- Page 97 and 98: FOOTNOTES FOR Tab1 e 5-3 a Incl ude
- Page 99 and 100: In order to prevent an explosion ha
- Page 101 and 102: analysis of the Distil 1 ation NSPS
- Page 103 and 104: Install ed piping and ducting costs
- Page 105 and 106: estimated by the same procedure as
- Page 107 and 108: .ble 5-4. POLYPROPYLENE MODEL PLANT
- Page 109 and 110: Table 5-6. POLYSTYRENE MODEL PLANT
- Page 111 and 112: emitters, while other dryers, e.g.,
- Page 113 and 114: Table 5-8. COST ANALYSIS FOR POLYPR
- Page 115 and 116: 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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APPENDIX B COMMENTS OW MAY 1982 DRA
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Mr. J. R. Famet Page 2 EPA June 16,
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October 19, 1981 Attachment to June
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Be The mocial plant does nst incEud
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1000 BRAZOS, SUITE 200, AUSTIN, TEX
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our previous comments the TCC quest
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. . . . " . . 5. Emission Reduction
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REFERENCES Texas Chemical Council t
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' Y !. Jack R. Faner o The A~ency h
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NATION& AIR POLLUTION CONTROL Y COM
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" DEFINITION OF INCINERATION AS MCT
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-5- IN SUWRYj THE AGENCY, BY RELYIN
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STRUMS WITH RELATIVELY STABLE FLOW
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1 I CoHPlTIONS OF 10 TIMES NORMAL S
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I 1 I - gU - I I n G PROPO.SED INCI
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The use of data from the CTG for ai
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Mr. Jack R. Farmer, Chief July 19,
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APPENDIX C MAJOR ISSUES AND RESPONS
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generally for large volume, variabl
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control devices, such as thermal an
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modification or rep1 acement, based
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epresent excellent agreement for su
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Response: The following responses a
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processes (e.g ., polypropylene and
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I I I I The purpose of this appendi
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Data collection continued for each
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Test . Number ~104Velocity (scfm) (
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found for tests of incinerators at
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7' Tab1e 0-4. TYPICAL INCINERATOR P
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I I I I I l l I averages for the mo
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Table D-5. ARC0 POLYMERS INCINERATO
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Thempies Spaced Evenly Across the T
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probe for the temperature while a w
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The total installed capital cost of
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3. Test Results - VOC destruction e
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Figure D-4. Petro-Tex 0x0 unit inci
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air to reduce the air flow through
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HEAT EXCHANGE1 NOTE: From Exchanger
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' organic carbon. chromatography. T
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D.3 VAPOR RECOVERY SYSTEM VOC EMISS
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However, the calculations assume pe
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The 20 pprn level was judged to be
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REFERENCES FOR APPENDIX D McDaniel,
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APPENDIX E: DETAILED DESIGN AND COS
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characteristics: volumetric flow ra
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Footnotes for Table E-1 astandad co
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sources to the flare header were as
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Flare Tip Diameter (in.) Figure E-1
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Table E-3. CAPITAL AND ANNUAL OPERA
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Footnotes for Table E-3 aFluidic se
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Tab1e E-4. WtORKSHEET FOR CALCULATI
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excess air for oxygen in the waste
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Table E-6. PROCEDURE TO DESIGN THER
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I I a plant had a use for it, heat
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Footnotes for Table E-7 Wpdated usi
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Table E-8. OPERATING PARAMETERS AND
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TABLE E-9. GAS PARAMETERS USED FOR
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~ 1 1 I I l 1 I I represent June 19
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Tabl e -11 CAPITAL AND . IERATIONG
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$0.335/scfm for units with no heat
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Table E-12. PROCEDURE TO CALCULATE
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Footnotes for Table E-12 (Concluded
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i m- Table E-13. PROCEDURE TO CALCU
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I - I - 1 A nnnrrn~~nrc rn rnl PIII
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Table E-15. CAPITAL AND ANNUAL OPER
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aUpdated using Chemical ~ I nneiri
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Condenser ~y2 ! ;tern Area (ftL) Fi
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ased on an equation in the Chemical
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m Equi p ent Type Check Valves Gate
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- 1/8 - - Table E-20. INSTALLED DUC
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Reference 12, p. 6-3 and 6-4. Refer
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APPENDIX F CALCULATION OF UNCONTROL
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Table F-1 . INITIAL EMISSION CHARAC
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Table F12. SUMMARY OF ANNUAL COSTS,
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= the difference between the operat
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I 8 - a F.Z. 1 Sty rene-i n-Steam m
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(9 CE = AC - (0.9 ~ CDnA ~ x eRC) d
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Substituting the values from Table
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Table 7. EXPONENTS USED FOR CONDENS
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Within Line Table F-8. STYRENE'-IN-