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Applied  Process Design                                    543

            Coffee, R. D., "Cool Flames and Autoignition," presented AIChE   Hilado, C.J., "How to Predict if  Materials Will Burn," Chem.  Eng.,
              Loss Prevention Symposium,  Houston, Texas, April  2,  1979.   Dec.  14,  1970,  p.  174.
            Affens,  W.  A.  and  Sheinson,  R.  S.,  "Autoignition-A  Two  Stage   Grote,  S.  H.,  "Calculating  Pressure  Release Times,"  Chem.  Eng.,
              Process,"  presented  AIChE  Loss  Prevention  Symposium,   July  17,  1967,  p.  203.
              Houston, Texas, April  2,  1979.                    Sengupta, M.  and Staats, F. Y, "Calculations Improved for Relief-
            D'Onofrio,  E. J.,  "Cool Flames  and Autoignition  Studies of Sev-   Valve Load," Oil & Gas  joun,  May  22,  1978,  p.  74.
              eral  Glyols,"  Presented  AIChE  Loss  Prevention  Symposium,   Leung, J.  C.  and Fauske,  H.  K,  "Runaway System  Characteriza-
              Houston, Texas, April  2,  1979.                      tion  and  Vent Sizing  Based  on  DIERS  Methodology,"  Plant
            Hoppe, T.  and Grob, B., "Heat Flow Calorimetry for Preventing   Operations Progress,  V.  6, :'-lo.  2,  1987,  p.  77.
              Runaway Reactions,"  Chem.  Eng.  Prog.,  V.  89, No.  1, 1990.   Swift,  I.  and Epstein,  M.,  "Performance of Low Pressure  Explo-
            Creed, M. J. and Fauske, H.K.,  "An  Easy Inexpensive Approach   sion Vents," Plant Operations Progress,  V.  6,  No.  2,  1987,  p. 98.
              to The DIERS Procedure," Chem. Eng.  Prog., V.  86, No,  3,  1990.   Brown, D. M. and Nolan, P.  F.,  'The Interaction of Shock Waves
            Friedman,  K.  A.,  "CCPS:  Setting  the  Standard  for  Industrial   on  Cylindrical  Structures,"  Plant  Operations  Progress,  V.  6,  No.
              Safety,"  Chem.  Eng.  Prog., V.  86, No.  3,  1990.   1, 1987,  p.  52.
            Trambouze,  P.,  "Reactor  Scaleup  Methodology,"  Chem.  Eng.   "A  Guide  to  the  Safe  Handling  of Hazardous  Materials  Acci-
              Prog., V.  Sc, No.  2,  1990.                         dents," ASTM-STP 825.
            Gygax,  R.  W.,  "Scaleup  Principles  for Assessing Thermal  Run-   Cashdollar,  K.  L.  and  Hertzberg,  M.,  Editors,  Industrial  Dust
              away Risks,"  Chem.  Eng.  Prog., V.  86,  No.  2,  1990.   Explosions,  Symposium  on  Industrial  Dust Explosions,  ASTl'vl
            Heitnerr,  I., Trautmanis, T.  and Morrissey,  M.,  "When Gas-filled   Technical Publication  No. 958,  1986.
              Vessels Are Exposed to Fire," Hydro.  Proc.,\!.  62,  No.  11, 1983.   North American Combustion Handbook,  Second Ed., North  Ameri-
            O'Keefe, W., "Benefit from Systems Approach with Today's Safe-   can  Mfg.  Co., 1978.
              ty Valves," Powe1.:Jan.  1984,  p.  17.             Simisky,  P.  L.  and Faulkner,  C. R., "Better Relief  Systems Design,"
            Liebman, I., Perlee, I-I.  E., and Corry.]., "Investigation of Flame   Hydro.  Proc., V.  68, No.  5,  1989,  p.  63.
              Propagation  Characteristics  in  Layered  Gas  Mixtures,"  R  f   Narasimhan, N. D., "Predict Flare Noise," Hsdro.  Proc., V.  65, No.
              # 7078,  U.S. Bureau of Mines,  1968.                 4,  I 986,  p.  133.            .
            Kletz, T.  A.,  "Consider Vapor Cloud Dangers When You Build a   Oen  bring,  P.  R.  and Sifferrnan, T.  R., "Flare Design  ...  Are Cur-
              Plant," Hydro Proc., V.  59,  No.  10,  1979,  p.  205.   rent Methods Too  Conservative>,"  Hydro.  Proc.,  V.  59,  No.  5,
            Paruit,  B.  and  Kimmel,  W.,  "Control  Blowdown  to  the  Flare,"   1980,  p.  124.
              Hydro.  Proc., V.  59,  No.  10,  1979,  p.  117.   De  Faveri,  D.  i'vL,  Zonato,  C.,  Fumarola,  G.  and  Ferraiolo,  G.,
            Mak,  H.  Y,  "New  Method  Speeds  Pressure-Relief  Manifold   "Estimate Flare Radiation Intensity," Hydro.  Proc., V.  64,  No. 5,
                                                                    1985,  p.  89.
              Design,"  Oil U Cas  joun,  Nov.  20,  1978,  p.  166.   McMurray,  R.,  "Flare  Radiation  Estimated,"  Hydro.  Proc., V.  61,
            Constance, J.  D.,  "Control  of Explosive  or Toxic  Air-Gas  Mix-   No.  11, 1982,p.  175.
              tures,"  Chem.  Eng., April  19,  1971, p.  121.
            Le  Vine,  R.  Y.,  "Electrical  Safety  in  Process  Plants,"  Chem.  Eng.,   Van Boskirk,  B.  A.,  "Sensitivity  of Relief Valves  to Inlet and Out-
                                                                    let Line Lengths,"  Chem.  Eng.,\!.  19, No.  17,  1982,  p.  77.
              May  1,  1972,  p.  30.                             Papa,  D.  M.,  "How  Back  Pressure  Affects  Safety  Relief Valves,"
            Cocks,  R.  E.,  "Dust Explosions:  Prevention and Control,"  Chem.   Hydro.  Proc., V.  62, No.  5, 1983,  p.  79.
              Eng., Nov.  5,  1979, p.  94.                       Davenport,]. A., "Prevent Vapor Cloud Explosions," Hydro.  Proc.,
            Pratt,  T.  H.,  "Electrostatic  Initiation  of  Explosions  in  Dusts,"   V.  56,  No.  3,  1977,  p.  205.
              Cereal Foods  World,  V.  23, No.  10,  1978.       Harris, L.  R., "Select the Right Rupture Disk," Hydro.  Proc., \I.  62,
            Frydenlund,  M.  1-"1., "Protecting a Plant from  Lightning," Specijj'-   No.  5,  1983, p.  75.
              ing Engi:neer,  May  1984,  p.  79.                 Brown, L.  £., Wesson, H.  R.  and Welker,].  R.,  "Predict LNG Fire
            Saletan, D.  L., "The Theory Behind Static Electricity Hazards in   Radiation," Hydro.  Proc., V.  53, No.  5,  1974,  p.  141.
              Process Plants,".June l,  1959,  p.  99.            Ogiso,  C., Takagi,  N., and Kitagawa,  T.,  "On  the  Mechanism  of
            Eichel, F.  G.,  "Electrostatics,"  Chem.  Eng.,  Mar.  13,  1967,  p.  153.   Vapor Explosion," Yokohama National  University,  Yokahama,
            Gibson,  R.  0.  and  Yinson,  D.  J.,  "Design  and  Installation  of   Japan.
              Smokeless  Flare  Systems  for Gasoline  Plants,"  ASME,  Paper   Katz,  D.  L.,  "Superheat-Limit Explosions,"  Chem.  E11g.  Prog.,  V.
              No.  72-Pet-12,  1972.                                68, No.  5,  1972,  p.  63.
            Brzustowski,  T.  A.,  "Flaring:  the  State  of the Art," Loss  Preven-   Reid, R.  C., "Superheated Liquids," American Scientist.N, 64, Mar-
              tion  Symposium,  AIChE  National  Meeting,  Mar.  20,  1977,   Apr.  1976,  p.  146.
              Houston, Texas.                                     Zabetakis,  M.  G.,  "Flammability  Characteristics  of Combustible
            Constance,].  D.,  "Solve  Gas  Purging  Problems  Graphically,"   Gases and Vapors,"  U.S.  Bureau of Mines, R.  I.  No 627, NTIS
              Chem.  Eng.,  Dec.  29,  1980,  p.  65.               No. AD-701-576.
            Nagy,J., Conn,.J. \.\.'.  and Verakis, 1-1. C., "Explosion Development   "Static  Electricity:  Rules  for  Plant  Safety,"  Expert  Commission
              in a  Spherical  Vessel," R.J.  #7279,  U.S.  Bureau of Mines.   for Safety  in the Swiss Chemical Industry (ESCIS), Plant/Oper-
            Burgess,  D.  S.,  Murphy,  J.  N.,  and  Zabetakis,  M.  G.,  "Hazards   ations Prog.  V.  7, No.  1, 1988,  p.  1.
              Associated  with  the  Spillage  of  Liquefied  Natural  Gas  on   "Guidelines for Risk Evaluation  and  Loss Prevention in  Chemi-
              Water," R.J.  #7448,  U.S.  Bureau of Mines,  1970.   cal  Plants," Manufacturing Chemists Assoc.,  1970.
            Witte,  L.  C.  and  Cox,  J.  E.,  'The  Vapor  Explosion-A  Second   Fauske,  H. K and Epstein,  M.,  "Source Term  Considerations  in
              Look,"].  Metals,  Oct.  1978,  p.  29.               Connection with  Chemical Accidents  and Vapor Cloud Mod-
            Perteous,  W.  M,  and  Reid,  R.  C.,  "Light Hydrocarbon  Vapor   eling,"]. Loss Preti  Process Ind., V.  1, April  1988,  p.  75.
              Explosions,"  Chem.  Eng.  Prog., V.  72,  May,  I 976.   Martinsen,  W.  E., Johnson,  D.  W.,  and  Terrell,  W.  F.,  "Bleves:
            Apfel,  R.  E.,  "Vapor Nucleation  at a Liquid-Liquid  Interface,"].   Their Causes, Effects and Prevention," Hydro.  Proc., V.  65,  No.
              Chemical Physics,  V.  54,  No.  l, 1971, p.  62.     11, 1986,  p.  141.
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