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114  FLOW  OF  FLUIDS




                       Bubble                  Slug

                                                                                                     .  .
                                                                                                   .  .
                                                                                                   .  ..
                                                                                                      ..
                        Plug                 Annular                                                 .  ,.
                                                                                                   .  .'
                                                                                                   ..
                                                                                                    .  .
                                                                                                    ..
                                                                                                    .  ..
                      Stratified             Dispersed                                               . ..
                                                                                                      _.
                        Wavy                                     Bubbly                            Annular   Dispersed
                                     (a)




                                                                               lo -   Dispersed  flow  IDB)






                                                                             J
              vi                                                             3
              3z
               d

                                                                                   Stratified
                                                                                   flow LSS)
                                                                                 -
                                                                              .01

                                                                                   .1       1       10       100   500
                                                                                               UG  mls



                Figure 6.7. Flow patterns and correlations of  flow regimes of  liquid-gas  mixtures in pipelines. (a) Patterns in horizontal liquid-gas  flow. (b)
                Patterns in  vertical liquid-gas  flow.  (c)  Correlations of  ranges of  flow  patterns  according to  Baker  [Oil Gas J.  53(12),  185 (1954)], as
                replotted  by  Bell et al.  [Chem. Eng.  Prog. Symp. Ser. 66,  159 (1969)l; u is surface tension of  the liquid, and  ow that  of  water.  (d) Flow
                regimes of water/air at 25°C and 1 atm [Tuitel and Dukler, AIChE J. 22, 47 (1976)l; the fuzzy boundaries are due to Mandhane et al. [Int. J.
                Two-Phase Flow 1, 537 (1974)l.


                SEPARATED FLOW MODELS                               1000  instead  of  the  usual  2000  or  so  because  the  phases  are
                                                                   recognized to disturb each other. Item 1 of  Table 6.8 is a guide to
                Pressure drop in two-phase flow is found in terms of  pressure drops   the  applicability of  the  Lockhart-Martinelli  method,  which  is  the
                of  the  individual  phases  with  empirical  multipliers.  The  basic
                relation is                                        oldest,  and  two  more  recent  methods.  An  indication  of  the
                                                                   attention that has been devoted to experimentation with two phase
                                                                   flow  is  the  fact that  Friedel  (1979)  based  his correlation on some
                                                                   25,000 data points.
                                                                       Example  6.14  compares  the  homogeneous  and  Lockhart-
                                                                    Martinelli models for the flow of  a mixture of  oil and hydrogen.
                The last term is the pressure drop calculated on the assumption that
                the total mass flow has the properties of  the liquid phase.
                   Some  correlations  of  multipliers  are  listed  in  Table  6.8.
                Lockhart  and Martinelli distinguish between the  various combina-   OTHERASPECTS
                tions  of  turbulent  and  laminar  (viscous)  flows  of  the  individual   The pattern of  annular flow tends to form at higher gas velocities;
                phases;  in  this  work  the  transition  Reynolds number  is  taken  as   the  substantial amount of  work  done on this topic is reviewed by
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