Page 217 - Separation process principles 2
P. 217

Table 5.4  (Continued)
                                                                                            Variable Specificationa
                                                                                       Case I,            Case 11,
                                                                                      Component          Number of
                                                                                      Recoveries        Equilibrium
                 Unit Operation                                          ND           Specified        Stages Specified
                 (f)  Reboiled                                      2N + C + 3    1. Recovery of     1. Number of
                    stripping                                                       one key           stages
                    (one inlet                                                      component        2. Bottoms flow
                    stream)                                                       2. Reboiler heat    rate
                                                                                    dutyd







                 (g)  Distillation                                  2N+C+9        1. Ratio of vapor   1. Ratio of vapor
                    (one inlet                                                      distillate to liquid   distillate to
                    stream,                                                         distillate        liquid distillate
                    partial                                                       2. Recovery of     2. Number of
                    condenser,                           Liquid                     light key         stages above
                    partial                                                         component         feed stage
                    reboiler,                                                     3. Recovery of     3. Number of
                    both                                                            heavy key         stages below
                    liquid and                                                      component         feed stage
                    vapor                                                         4. Reflux ratio    4. Reflux ratio
                    distillates)                                                    (> minimum)      5. Liquid distillate
                                                                                  5. Optimal feed stageb   flow rate
                 (h) Extractive                                     2N + 2C + 12   1. Condensate at   1. Condensate at
                    distillation                                                    saturation         saturation
                    (two inlet                                                      temperature       temperature
                    streams, total                                                2. Recovery of     2. Number of
                    condenser,                                                      light key          stages above
                    partial                                                         component         MSA stage
                    reboiler,                                                     3. Recovery of     3. Number of
                    single-phase                                                    heavy key          stages between
                    condensate)                                                     component         MSA and feed
                                                                                  4. Reflux ratio      stages
                                                                                    (> minimum)      4. Number of
                                                                                  5. Optimal          ' stages below
                                                                                    feed stageb       feed stage
                                                                                  6. Optimal         5. Reflux ratio
                                                                                    MSA stageb       6. Distillate flow rate
                 (i) Liquid-liquid                                  2N + 2C + 5   1. Recovery of     1. Number of
                   extraction                                                       one key            stages
                   (two inlet                                                       component
                   streams)





                 (j) Stripping (two                                 2N + 2C + 5   1. Recovery of     1. Number of
                   inlet streams)                                                   one key           stages
                                                                                    component







                 ODoes not include the following variables, which are also assumed specified: all inlet stream variables (C + 2 for each stream); all element and unit
                 pressures; all element and unit heat transfer rates except for condensers and reboilers.
                 b~ptimal stage for introduction of inlet stream corresponds to minimization of total stages.
                 'For  case I variable specifications, MSA flow rates must be greater than minimum values for specified recoveries.
                 d~or case I variable specifications, reboiler heat duty must be greater than minimum value for specified recovery.
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