Control of Volatile Organic Compounds Emissions from Manufacturing

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m Equi p ent Type Check Valves Gate Valves Control Valves Strainers El bows I ~n Tees ~ Flanges Drip Leg Valves Expansion Fittings Bolt and Gasket Sets Hangers Field Welds n:-- C-L--I A n I=+\ r I ye, xrieulr .1 1i3 ru [I b1 a~rom Reference 44. Table E-18. PIPING CO~MPOW!ENTS~ Number of Equipment Type in Pipe Leg Type Source compressor Pipe1 ine (500) Pipe1 ine (2,000)
Table E-19. INSTALLED PIPING COSTS~ Cost in August 1978 Dollars for Pipe Leg Type Pipe Diameter (ft) (TO') Source Leg (20' ) Compressor Leg 500' Pipeline 2,000' Pipeline 0.0411 2,200 1,050 2,275 4,360 0.0518 2,262 1,085 2,555 4,955 0.0647 2,330 1,120 2,660 5,255 0.0874 2,470 1,170 2,870 5,800 0.1342 2,725 1,375 3,485 7,235 0.1722 3,340 1,490 3,990 8,190 0.2057 5,644 2,725 5,765 10,690 6,045 2,900 6,640 12,500 7,428 3,465 7,925 14,825 7.786 3,830 9,000 16,870 a~rom SOCMI-Di still ation NSPS Computer Program "DM Pipe" (Reference 45 ) based on component costs from Reference 18.
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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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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
Page 231 and 232: Footnotes for Table E-1 astandad co
Page 233 and 234: sources to the flare header were as
Page 235: Flare Tip Diameter (in.) Figure E-1
Page 238 and 239: Table E-3. CAPITAL AND ANNUAL OPERA
Page 240 and 241: Footnotes for Table E-3 aFluidic se
Page 242 and 243: Tab1e E-4. WtORKSHEET FOR CALCULATI
Page 244 and 245: excess air for oxygen in the waste
Page 246 and 247: Table E-6. PROCEDURE TO DESIGN THER
Page 248: I I a plant had a use for it, heat
Page 252 and 253: Footnotes for Table E-7 Wpdated usi
Page 255 and 256: Table E-8. OPERATING PARAMETERS AND
Page 257: TABLE E-9. GAS PARAMETERS USED FOR
Page 260 and 261: ~ 1 1 I I l 1 I I represent June 19
Page 262 and 263: Tabl e -11 CAPITAL AND . IERATIONG
Page 264 and 265: $0.335/scfm for units with no heat
Page 266 and 267: Table E-12. PROCEDURE TO CALCULATE
Page 268 and 269: Footnotes for Table E-12 (Concluded
Page 270 and 271: i m- Table E-13. PROCEDURE TO CALCU
Page 272 and 273: I - I - 1 A nnnrrn~~nrc rn rnl PIII
Page 274 and 275: Table E-15. CAPITAL AND ANNUAL OPER
Page 276 and 277: aUpdated using Chemical ~ I nneiri
Page 278 and 279: Condenser ~y2 ! ;tern Area (ftL) Fi
Page 280 and 281: ased on an equation in the Chemical
Page 284 and 285: - 1/8 - - Table E-20. INSTALLED DUC
Page 286 and 287: Reference 12, p. 6-3 and 6-4. Refer
Page 289 and 290: APPENDIX F CALCULATION OF UNCONTROL
Page 291 and 292: Table F-1 . INITIAL EMISSION CHARAC
Page 293 and 294: Table F12. SUMMARY OF ANNUAL COSTS,
Page 295: = the difference between the operat
Page 298 and 299: I 8 - a F.Z. 1 Sty rene-i n-Steam m
Page 300 and 301: (9 CE = AC - (0.9 ~ CDnA ~ x eRC) d
Page 302 and 303: Substituting the values from Table
Page 304 and 305: Table 7. EXPONENTS USED FOR CONDENS
Page 306 and 307: Within Line Table F-8. STYRENE'-IN-
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Control of Volatile Organic Compounds Emissions from Manufacturing

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