Control of Volatile Organic Compounds Emissions from Manufacturing

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Reference 12, p. 6-3 and 6-4. Reference 10, Fig. V-15, curve 3, p. V-18. I Neverill, R.B. Capital and Operating Costs of Selected Air Po1 lution Control Systems. U.S. Envi ronmental Protection Agency, Research Triangle Park, N.C. Publication No. EPA-45015-80-002. December 1978. I Richardson Engineering Services. Process Plant Construction Cos Estimating Standards, 1980-1981. 1980. Tel econ. Katari , Vi shnu, Pacif ic Envi ronmental Services, Inc. with Tucker, Larry, Met-Pro Systems Division. October 19, 1982. Catalytic incinerator system cost estimates. Telecon. Katari , Vishnu, Pacific Environmental Services, Inc., with Kroehling, John, DuPont, Torvex Catalytic Reactor Company. October 19, 1982. Catalytic incinerator system cost estimates. Key, J.A. Control Device Evaluation: Catalytic Oxidation. In: Chemical Manufacturi ng Volume 4: Combustior\ Control Devices. U.S. Envi ronmental Protect ion Agency. Research Tri angle Park, N.C. Pub1ication No. EPA-45013-80-026. December 1980. Telecon. Siebert, Paul, Pacific Environmen1;al Services, ~nc., Steam: Its Generation and Use. New York, 1975. p. 6-10. - h Reference 10, Fig. V-15, curve 3, p. V-18. Perry, R.H. and C.H. Chilton, eds. Chemical Engineers' Handbook, fifth edition. New York, McGraw-Hill Book Company. 1973. p. 3-59 Rossini, F.D. et al. Selected Values of Physical and ~hermod~nahic Properties of Hydrocarbons and Re1 ated Compounds, Compri sing the Tables of API Research Project 44. Pittsburg, Carnegie Press, 1953. pp. 652 and 682. Reference 26, pp. 10-25 through 10-28. Reference 26, pp. 10-12 through 10-15. Reference 26, pp. 11-1 through 11-18. I I I I I 1 I I I I E-60 I l l I I I
Reference 26, pp. 3-191, 3-212 through 3-214, and 12-46 through 12-48. Weast, R.C., ed. Handbook of Chemistry and Physics, fifty-thi rd edition. Cleveland, The Chemical Rubber Company. 1972. p. E-26. Erikson, D.G. Control Device Evaluation: Condensation. In: Organic Chemical Manufacturi ng Volume 5: Adsorpi ton, Condensation and Absorption Devices. US. Envi ronmental Protect ion Agency, Research Triangle Park, N.C. Publication No. EPA-450/3-80-027. December 1980. p. A-3. Reference 26, pp. 3-71, 3-206, 3-213, and 3-214. Kern, D.Q. Process Heat Transfer. New York, McGraw-Hill Book Company, 1950. p. 306. Tel econ. Katari , Vi shnu, Paci fic Envi ronmental Services, Inc., with Mr. Ruck, Graham Company. September 29, 1982. Heat exchanger system cost estimates. Telecon. Katari , V i shnu, Pacific Envi ronmental Services, Inc., with Clower, Dove, Adams Brothers, a representative of Graham Company. September 30, 1982. Heat exchanger system cost estimates. Telecon. Katari , Vishnu, Pacific Environmental Services, Inc., with Mahan, Randy, Brown Fi ntube Company. October 7, 1982. Heat exchanger system cost estimates. Reference 33, pp. A-4 and A-5. Reference 26, p. 6-3. Reference 26, p. 5-31. Chontos, L.W. Find Economic Pipe Diameter via Improvec d Formula. Chemical Engineering. -87(12) :139-142. June 16, 1980. Memo from Desai, Tarun, EEA, to EB/S Files. March 16,' 1982. Procedure to estimate piping costs. Memo from Kawecki , Tom, EEA, to SOCMI Distil lation File. November; 13, 1981. Distil lation pipeline costi ng model documentation. EEA. SOCMI Distil lation NSPS Pipe1 ine Costing Computer Program (DMPIPE) , 1981. Reference 17, Section 4.2, p. 4-15 through 4-28.
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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
Page 11:
LIST OF FIGURES Simplified Process
Page 15 and 16:
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
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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 282 and 283: m Equi p ent Type Check Valves Gate
Page 284 and 285: - 1/8 - - Table E-20. INSTALLED DUC
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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