Page 377 - Chemical engineering design
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352
                                                                                 correlations
                                                                  Use tabular
                                                                               Use γ i
                                                                    data
                                                                                 Y
                                                                    Y
                                                                   Experimental
                                                                                Experimental
                                                                                      N
                                                                         N
                                                                     data
                                                                                  data
                                                                             γ i
                                     Start
                                                   Hydrocarbon  Special  Use sour  Sour water  case  C 5 water system  Y  Y  N  (polar)  or lighter  N  N  CHEMICAL ENGINEERING P < 4 bar  Use 0 < T < 750K  C T < 150 °  UNIFAC  Y  N  N  Further  N  P < 350 bar experimental  work required  method equilibria  phase  of selection  the  for
                                                                                P < 1 bar
                                                                     present
                                                                          N
                                                                                      N
                                                                   H 2
                                                                                                                      chart
                                                                   Y          Y            Y                Y
                                                   Y                                                                  Flow
                                                                    Use G−S     Use B−K10   P < 200 bar  N            8.4.  Figure
                                                                                           Y                  Use R−K−S
                                              T < 250K   H 2  present  T < 250K
                                       N            Y            N           N
                                               Y                         Y                  Use G−S



                                              Use G−S    Use P−R  or R−K−S  Use B−W−R
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