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542                       Applied  Process Design for Chemical  and Petrochemical  Plants

             73. Application,  Selection  and  Specification,  Cat.  7387-1,  1988,   Fishkin,  C.  I.  and  R.  L.  Smith,  "Handling  Flammable  Dusts,"
                Fike Metal Products Co.                            Chern.  Eng.  Prog., Vol. 60, 4,  1964,  p. 45.
             74.  White, R.  E.  and Oswald,  C. ].,  Mitigation of  Explosion Haz-   Flammable Dust Explosion Conference  (Nov.  1988) at St.  Louis,
                ards  of  Marine  Vapor  Control Systems,  Report S\VRI  Project   Missouri,  Plant Operations Progress,  Vol. 8, No.  3,July  1989.
                No.  06-4116 for American Petroleum Institute, Oct.  1992.   "Flanged Steel Safety Relief  Valves for Use in Petroleum Refiner-
             75.  Schneider,  D.  F.,  "How to  Calculate  Purge  Gas Volumes,"   ies," API-Std-526, American Petroleum Institute, New York.
                Hydm Proc.  V.  72., No.  11, Nov.  1993,  p.  89.   Gillis,].  R.,  'Testing for Explosiveness of Dusts," Loss Prevention,
             76. Ebadat,  V.,  "Keep  Dust Cloud  Explosions  at  Bay,"  Chem.   Vol.  2, Amer.  Inst.  Chem. Engr.,  1968,  p.  34.
                Eng., V.  100, No.  12., 1993,  p.  123.         Harmon, G.  W.  and H. A. Marlin,  "Sizing Rupture Discs for Ves-
              77.  Leung,  J.  C.,  "Size  Safety  Relief Valves  for  Flashing  Liq-   sels Containing Monomers," Loss Prevention, Vol. 4, Amer.  Inst.
                uids,"  Chem.  Eng.  Prog., V.  88, No.  2,  1992,  p.  70.   Chem.  Engr.,  1969,  p.  95.
             78.  Niemeyer,  C.  E.  and  Livingston,  G.  N.,  "Chose  the Right   Hattiangadi, V.  S., "Sizing Safety Valves for Heat-Sensitive Mate-
                Flare System Design," Chern.  Eng.  Prog., V.  89, No. 12,  1993,   rials,"  Chern.  Eng., Sept.  7,  1970, P:  96.
                p.  39.                                          Katz,  D.  L.,  "Superheat-Limit Explosions,"  Chem.  Eng.  Progress,
              79.  Bravo,  F.  and Beatty,  B.  D.,  "Decide Whether to Use Ther-   Vol.  68,  (5), 1972,  p.  68.
                mal Relief,"  Chern.  Eng.  Prog., V.  89, No.  12,  1993,  p.  35.   Kayser,  D.  S.,  "Rupture Disc  Selection,"  Chem.  Eng.  Progress,  Vol.
              80.  Cassata,]. R., Dasgupta,  S. and Gandhi, S.  L., "Modeling of   68,  (5), 1972,  p.  61.
                Tower Relief  Dynamics," Hydro.  Proc., Part i, V.  72, No.  10;   LeVine,  R.,  "Electrical  Safety  in  Process  Plants-Classes  and
                Part 2, V.  72, No.  11,  1993.                    Limits of Hazardous Areas,  Chem.  Eng., May  1, 1972, p.  51.
              81. Venart, J.  E.  S.,  Rutledge,  G. A., Sumathipala,  K., and Sol-   National  Fire  Protection Association,  Flammable  Liquid  Code,
                lows,  K., "To  BLEVE or Not to BLEVE, Anatomy of a Boil-   No.  30, Boston, Mass.
                ing  Liquid  Expanding  Vapor  Explosion,"  Process  Safety   Nazario,  F.  N.,  "Rupture  Disks:  A Primer,"  Chem.  Engr., June  20,
                Prog., V.  12, No.  2,  1993,  p.  67.             1988,  p.  86.
              82. Melhem, G. A., Croce, P.A., and Abraham, H., "Data Sum-   Palmer,  K. N., Dust Explosions and Fires,  Chapman and Hall, Lon-
                 mary of the National  Fire Protection Associations BLEVE   don,  1973.
                Tests," Process Safety Prog., V.  12, No.  2,  1993, p.  76.   Schwab, R.  F.,  "Interpretation of Dust Explosion Test Data," Loss
              83. National Electrical Code,  NFPA-70,  National  Fire  Protection   Prevention, Vol.  2, Amer.  Inst.  Chem.  Engr., 1968, p.  37.
                Association.                                     Simon,  H.  and  S.].  Thompson,  "Relief System  Optimization,"
              84. Ahern,  A.  A.,  "Properly  Use  Explosion-Proof  Electrical   Chem.  Eng.  Progress,  Vol.  68,  (5), 1972, p.  52.
                 Equipment,"  Chem.  Eng.  Prog., V.  87, No.  7,  1991, p.  65.   Sonti,  R.  S.,  "Practical  Design and  Operation of Vapor-Depres-
              85.  Papa,  D.  M.,  "Clear Up  Pressure  Relief Sizing  Methods,"   surizing Systems,"  Chem.  Engi:,Jan.  23,  1984,  p.  66.
                 Chem.  Eng.  Prog., V.  87,  No.  8,  1991, p.  81.   "Testing Procedures for Pressure-Relieving Devices Discharging
              86.  Pratt,  T.  H.,  "Electrostatic  Ignition  in  Enriched  Oxygen   Against Variable Back Pressure," API-RP-525, American Petro-
                Atmospheres:  A  Case  History,"  Process  Safety  Prog.,  V.  12,   leum Institute, New York, N.Y
                No.  4,  1993, p.  203.                          VDI  (Association  of German Engineers)  3673, June  1979, VDl-
              87.  Barker,  D. D., Whitney,  M. G., and Waclawczyk,Jr., "Failure   Verlag GmbH, Dusseldorf.
                 and  Design  Limit Criteria  for  Blast Loaded  Structures,"   Whelan, T.  W.  and S.J. Thomson, "Reduce Relief  System Costs,"
                 Process Safety Prog., V.  12, No.  4,  1993,  p.  216.
                                                                   Hydrocarbon Processing, Aug.  1975,  p.  83.
                                                                 Wong,  W.  Y.,  "Safer Relief Valve  Sizing,"  Chem.  Engn,  May  1989,
                               Bibliography                        p.  137.
                                                                 Yowell, R.  L., "Bisphenol-A Dust Explosions," Loss Prevention, Vol.
            Bodurtha,  F.  T.,  et.  al.,  "Discharge  of Heavy  Gases  from  Relief   2, Amer.  Inst.  Chem.  Engr.,  1968,  p.  29.
              Valves,"  Chern.  Eng.  Prog., Vol. 69, 4,  1973,  p.  37.   Banerjee,  K.,  Cherernisinoff,  N.  P.,  and  Cheremisinoff,  P.  N.,
            Boyle, W.]. Jr.,  Sizing Relief Area for Polymerization Reactors,"   Flare  Gas Systems Pocket Handbook,  Gulf Pub.  Co.,  1985.
              Chem.  Eng.  Prog., Vol. 63  (8), 1967, p.  61.     Loss  Prevention  and  Safety  Promotion  in  the  Process  Industries,  4th
            Bright,  G.  F.,  "Halting  Product  Loss  Through  Safety  Relief   International  Symposium,  Vol.  1:  Safety  in  operations  and
              Valves," Chem.  Eng.  Progress,  Vol.  68,  (5), 1972, p.  59.   Processes;  Vol.  2:  Hazardous  Chemicals  and  Liquefied  Gases-Safe
            Center for Chemical  Process Safety,  sponsored by A1ChE.   Transport,  Vol.  3:  Chemical Process  Hazards,  The  Institution  of
            "Commercial Seat Tightness of  Safety Relief  Valves with Metal-to-   Chemical  Engineers,  Symposium Series No.  82,  1983.
              Metal Seats," API-Std-527, American Petroleum Institute, New   Tuve,  R.  L.,  Principles  of  Fire  Protection  Chemistry,  National  Fire
              York.                                                Protection Assoc.,  1976.
            Crozier,  R.  A., Jr.,  "Sizing  Relief Valves  for Fire  Emergencies,"   Lasher,  R.,  Editor,  Control  lillve Handbook,  Fisher Controls  Co.,
              Chem.  Engn,  Oct.  1985, p.  49.                     1965.
            Essenhigh,  R.  H.,  "Dust  Explosion  Research,"  Loss  Prevention,   \Voodward,  J.  L.,  Editor,  International  Symposium  on  Preventing
              Vol.  2, Amer.  Inst.  Chem.  Engr.,  1968,  p.  44.   Major Chemical Accidents,  The Amer.  Institute of Chem.  Engrs.,
            Fauske,  H.  K.,  M.  A.  Grolmes,  and G.  I-I.  Glare,  "Process  Safety   1987.
              Evaluation  Applying  DIERS  Methodology  to  Existing  Plant   Prugh, R. \,V., "Quantify BLEVE Hazards," Chem. Eng.  Prog., V.  87,
              Operations," Plant Operations Progress,  Vol. 8, No.  1, 1989, p. 40.   No.  2,  1991, p.  66.
            Fire  and Explosion,  Dow's  Safety  and Loss Prevention  Guide  Hazard   Englund,  S.  M.,  "Design  and  Operate  Plants for Inherent Safe-
              Classification and Protection,  Amer.  Inst.  Chem.  Engr.,  1973.   ty-Part l," Chem.  Eng.  Prog., V.  87, No. 3, 1991, p. 85 and "Part
            First K.  E. and]. E.  Huff,  "Design Charts for Two-Phase Flashing   2,"  Chem.  Eng.  Prog., No.  5, p. 79.
              Flow  in Emergency  Pressure  Relief Systems," Plant  Operations   Corrigan,  M.  K.,  "Which  Instrumentation  for Hazardous-Area
              Progress,  Vol.  8,  No.  1, 1989,  p.  40.          Plants?"  Chem.  Eng.  Prog., V.  86, No.  9,  1990,  p.  55.
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