Page 328 - Distillation theory
P. 328

P1: JPJ/FFX  P2: FCH/FFX  QC: FCH/FFX  T1: FCH
            0521820928c08  CB644-Petlyuk-v1                                                      June 11, 2004  20:20





                        302    Synthesis of Separation Flowsheets

                               exist. This rule excludes, as far as possible, the necessity of expensive methods of
                               separation with application of entrainers and two levels of pressure. The third rule:
                               sequences with recycle flows are less preferable than sequences without them. For
                               example, if it is possible to manage without columns of autoextractive distillation,
                               splits in columns with two feedings have to be excluded.
                                 The rest of heuristic rules are less obvious. The fourth rule: sequences with
                               minimum number of columns are preferable. Hence, it follows that splits with
                               distributed components have to be excluded if there are ones without them. Cap-
                               ital costs at minimum number of columns are the smallest. However, energy ex-
                               penditures in this case are not always the smallest. For zeotropic mixtures, the
                               situation is the same as for azeotropic: flowsheets with prefractionator are more
                               profitable sometimes than without it (see Section 8.2). Therefore, the designer has
                               to decide him- or herself if he or she should use this rule at the stage of automatic
                               sequences.
                                 The fifth rule: sharp splits with a preliminary recycle for change of feed compo-
                               sition are more preferable than semisharp splits without preliminary recycle. Fig-
                               ure 8.22 shows two possible separation flowsheets of mixture acetone(1)-benzene
                               (2)-chloroform(3) into pure components in the case of the bottom product point

                                           2  x B  ) 2 (
                               a)
                                                                               x  ) 2 (
                                                                         1      D        3
                                     ) 0 (
                                   x               x  ) 1 (  =  x  ) 2 (
                                    F               B   F
                                 x  ) 1 (                          x  ) 1 (  x  ) 2 (  x  ) 3 (
                                  F                           x  F  ) 0 (  F  F     F
                                                                        x  ) 1 (
                                                                        B
                                                                                 2     x  ) 3 (
                                                                                        B
                               1                       3
                                               13
                                  x D  ) 1 (  x B  ) 3 (  x  D  ) 2 (  = x F  ) 3 (  x D  ) 3 (
                                           2  x  ) 2 (
                               b)              B                        1       3
                                                   x  B  ) 1 (  =  x  F  ) 2 (
                                      ) 1 (
                                     x
                                      F                             ) 1 (   ) 2 (
                                     ) 0 (                        x       x
                                   x                          x  ) 0 (  F  F
                                    F                          F
                                                                       x  ) 1 (
                                                                        B
                                                                                2
                               1                       3
                                              13
                                  x D  ) 1 (            x  D  ) 2 (
                               Figure 8.22. Sequences for distillation of the acetone(1)-benzene(2)-chloro-
                               form(3) mixture: (a) with best semisharp distillation in the first column, (b) with
                               primary recycle in order that bottom of first column belong to possible bottom
                                             1
                                              (2)
                               product segment Reg  (thick line).
                                              B
                                             2,3
   323   324   325   326   327   328   329   330   331   332   333