Page 184 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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Fluid  Flow                                          157

           32.  Coker,  A.  K.,  "Determine  Process  Pipe  Sizes,"  Chem.  Eng.   55. Tube  Turns,  Division  of Chemetron  Corporation,  Bulletin
              Prog.,  1991, Vol.  87,  No.  3.                      No.TT 725, Flow  of  Fluids,  Chemetron  Corporation,  1952,
                                                                    and Tube Turn Technologies,  Inc.
           33. Baker,  0.,  "Multiphase Flow in  Pipe Lines," Oil and Gas  joun,
              Nov.  lO,  1958,  p.  155.                         56.  Walworth Co.,  Valve  Catalog No.  57,  Section on Flow of  Fluids in
                                                                    Pipes,  1957, Walworth Co.
           34.  Beij,  K.  H.,  "Pressure  Loss of Fluid Flow  in  90°  Bends," ]our.
              P.es.  Nat.  Bur:  Stds., �?I, RP  1110,July  1938.   57. 'Weymouth,  T.  R.,  Problems in  Natural-Gas Engineering,  Trans.
                                                                    A.S.M.E.  34,  1912,  pp.  197-203.
           35.  Brigham,  W.  E.,  E.  D.  Holstein,  R.  L.  Huntington,  "How
              Uphill  and  Downhill  Flow  Affect  Pressure  Drop  in  Two-   58.  Chen,  H:J,  "An  Exact.  Solution  to  the Colebrook Equation,"
              Phase  Pipelines,"  Oil and Gas  [oun, No.  11, 1957,  p.  145.   Chem. Eng.,  1987, Vol. 94, No.  2,  p.  196.
           35.  Brooke, M.,  Chem.  Eng  .. 54  (l), 26,  1957.   59.  Hook-up Designs  for Steam and Fluid Systems,  1968, 7th printing,
                                                                    1981, Spirax Sarco,  Inc. Allentown, Pa.
           37. Chenoweth,  ].  M.  and  M.  \V.  Martin,  Turbulent  Two-Phase
              fww,  Pet.  Ref.,  Oct.,  1955,  p.  151.
                                                                                    Bibliography
           38.  Church, A.  H.,  editor,  and  H.  Gartman,  Del.aoal Handbook,
              2nd ed., DeLaval  Steam Turbine Co., Trenton, N, J.,  1955.
                                                                 DeGrance, A.  E.  and R.  W.  Atherton,  Horizontal-Flow  Correla-
           39.  Crane  Company,  Engineering  Division,  Technical  Paper  No.   tions,  Chern.  Eng.,July  13,  1970,  p.  95.
              409,  1942,  Crane Co.
                                                                 DeGrance,  A.  E.  and  R.  W.  Atherton,  "Pressure-Drop  Sample
           40.  Dunning,  A.  R.  Ill, Trans.  A.S.M.E., .'l4,  No.  17 (32).   Calculations,"  Chem.  Eng.,  no.  2,  1970,  p.  I 01.
           41. Flanigan,  0.,  "Effect  of Uphill  Flow  on  Pressure  Drop  in   Dukler,  A.  E.  et al., "Frictional  Pressure  Drop in Two-Phase Flow:
              Design  of Two-Phase  Gathering  Systems,"  Oil and  Gas [ouc,   A  Comparison of Existing  Correlations  for  Process  Loss  and
              Mar,  10,  1958,  p.  132.                           Holdup,"  A.I.Ch.EJ.;  10,  1964,  p.  38-43.
           42.  Hook-up Designs for Steam and Fluid Systems,  3rd ed., 1971  and   Dukler,  A.  E.  et al., "Frictional Pressure Drop in Two-Phase Flow:
              7th ed.  1981, Spirax  Sarco Co. Inc., Allentown, Pa.   B-An Approach Through Similarity  Analysis,"  A.I.Ch.Ej.; 10,
           43. Johnson,  T.  W.  and  W.  B.  Berwald,  Flow  of Natural  Gas   1964,  pp.  44-51.
              Through  High  Pressure  Transmission Lines,  Monograph  No.  6,   Dukler,  A.  E.,  Gas-Liquid Flow in Pipelines,  Am.  Petrol.  Inst.  Proc.,
              U.S.  Department of the Interior,  Bureau of Mines, Washing-   Sept.  1967.
              ton,  D.C.
                                                                 Eaton,  Ben A.,  el  al.,  'The  Prediction  of Flow  Patterns,  Liquid
           44.  Kern,  Robert,  "How  to  Size  Piping and Components  as Gas   Holdup  and  Pressure  Losses  Occurring  During  Continuous
              Expands  al Flow  Conditions,"  Chem.  Eng.,  Oct.  13,  1975,  p.   Two-Phase  Flow  in  Horizontal  Pipelines," J.  Petrol.  Technol.,
              125.                                                June 1967,  pp.  315-328.
           45.  Lapple,  C.  E., Trans.  A.l.Ch.E., 39,  1943,  pp.  385-432.   Gould, T.  L., el.  al.,  Engi.neering  Methods and Computer Applications
                                                                   For Design  and Operation of  Ttoo-Phase Pipeline Systems,  The Uni-
           46.  Lockhart,  R.  W.  and  R.  C.  Martinelli,  Proposed  Correlation  of   versity of Michigan, Ann Arbor,  Mich.,  1973.
              Data  For  Isothermal  Two-Phase,  Two  Component  Flow  in  Pipe
              Lines,  C. E.  P.  45,  1949,  39.                 Covier,  G.  \Al.  et al., "The Upward Vertical Flow of Air Water Mix-
                                                                   tures,"  Canadian journal of Chem.  Eng,  Pan I,  Aug.  1957,  pp.
           47.  Loeb.  M.  B.,  "New  Graphs  for  Solving  Compressible  Flow   58-70;  Part  II.  Oct.  1958,  pp.  195-202,  and  Part  Ill,  April
              Problems,"  Chem.  Eng., May  19,  1969, p.  179.    1960,  pp.  62-66.
           48.  O'Brien and Hickox, Applied Fluids Mechanics,  1937, McGraw-   Creskovich, A.  L.,  et.  al.,  "Five  Gas  Content for Horizontal  Gas-
              Hill Book Co.  Inc., New York,  New York,  p.  211.   Liquid  Flow,"  Ind.  Eng.  Chem.  Fundamentals,  Aug.  1969,  pp.
           49.  O'Neill,  F.  W.,  editor,  Compressed  Air Data,  5th  ed.,  1939,   591-593.
              Compressed Air Magazine.  Bowling Green  Building,  New York,   Haberstroh,  R.  E.  and  P.  Griffith,  The  Slug-Annular  Two-Phase
              N.Y                                                  Flow Regime  Transition, Am. Soc.  Mech. Engr., Paper 65-HT-52.
           50.  Pollard, R.  S.,  "Sizing Return Lines," Industry  and Power;  Feb.   1965.
              1954,  p.  83.                                     Hughmark,  G.  A.,  "Holdup  and  Heat  Transfer  in  Horizontal
                                                                   Slug Gas-Liquid Flow,"  Chem.  Eng.  ss; 20,  1964,  p.  1007.
           51. Powell,  \,1 .. 'rn.,  Vctlve  Catalog  No.  11,  Wm.  Powell  Valve  Co.,
              Cincinnati, Ohio.                                  Hughmark,  G.  A.,  "Holdup  in  Gas-Liquid  Flow,"  Chem.  Eng.
                                                                   Prog.,  58,  1962,  pp.  62-65.
           52.  Schneider,  F.  N.,  P.  D.  White,  R.  L.  Huntington,  PijJe  Line
              Industry,  Oci.,  1954.                            Kern, Robert,  "How to Size Process Piping for Two-Phase Flow,"
                                                                   Hsdrocarboa Processing,  Oct.  1969,  p.  i05.
           53.  Shaw,  G.  V ..  editor,  and  A.  W.  Loomis,  Cameron  Hydraulic
              Data,  Ingersoll-Rand  Co.,  Eleventh  Edition,  1942  and  16th   Kern,  Robert,  "How  to  Size  Piping  and  Components  as  Gas
              ed,  1979,  Ed.  C.  R.  Westaway  and A.  W.  Loomis,  Ingersoll-   Expands at Flow Conditions,"  Chern.  Eng., Oct.  13,  1975, p.  125.
              Rand Co.,  Woodcliff Lake, NJ.                     Kern, Robert,  "Piping Design  For Two-Phase Flow,"  Chem.  Eng.,
           54.  Standards for Steam Jet  Ejectors,  3rd  ed.,  Heat Exchange  Insti-   June 23,  1975, p.  145.
              tute,  1956, and  Stnndards for Steam]et Vacuum System�;.  4th ed.,   Meador,  L.  and A. Shah, "Steam Lines Designed for Two-Phase,"
              1988,  Cleveland, Ohio.                              Hydrocarbon Processing,  48,  1,  l 969,  p.  143.
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