Page 334 - Distillation theory
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            0521820928c08  CB644-Petlyuk-v1                                                      June 11, 2004  20:20





                        308    Synthesis of Separation Flowsheets

                                                                         x
                                                                          E
                                       ) 1 (
                                     x                                       2
                                      D
                                         2
                                                                                      ) 2 (      ) 3 (
                                                                                    x           x
                            a)                                    b)                 D          D
                                  x  ) 0 (    x  ) 1 (
                                  F            F
                                        321
                                              23   ) 3 (
                                  α 23           x
                                                  D
                                                   x D  ) 2 (  =  x F  ) 3 (              ) 3 (
                                          231                        x  ) 1 (  x  ) 2 (  x  F
                             ) 1 (                                 ) 0 (  F     F
                           x F +  E                               x F
                        x  B  ) 1 (  = x F  ) 2 (   α 13
                                                  213   x  ) 3 (          x  ) 1 (
                                                         B
                                                                           B          1
                           1                                                                     3
                                              13       3
                              ) 2 (
                            x  =  x
                             B   E
                               Figure 8.25. Phase equilibria map (a) and sequence for distillation of a ternary mixture with
                               two binary azeotropes in three columns (with semisharp autoextractive distillation in the first
                               column) (b).
                                                2
                               product segment Reg , and binary mixture 1,2 is zeotropic and component 2 is
                                                  B
                                               1,3
                                             1
                               light in it (2 ≡ Reg ).
                                               D
                                             2
                                 However, sharp extractive distillation is not expedient because bottom product
                               x B is a binary mixture with azeotrope 13. Split of extractive semisharp distillation
                                        (1)
                               2 : 1,2,3 (x ) is preferable. Indirect split 2,3 : 1, at which the top product point
                                        B
                                                                                        1
                                                (2)
                               of second column x  gets to the possible top product segment Reg , has to be
                                                D                                         D
                                                                                        2,3
                               applied in the second column. Split 23 : 3 is applied in the third column, and top
                                       (3)
                               product x  = 23(Az) is used as recycle flow into the first column. The search for
                                       D
                               such a sequence can hardly be automated because analysis of possible sharp splits
                               in the first column does not give any preferable split. It is necessary to analyze
                               possible splits simultaneously in several columns.
                        8.6.2. Application of Pressure Change
                               In some cases, change of pressure very much influences the location of azeotrope
                               points and sometimes even leads to transformation of azeotropic mixture into
                               zeotropic. That uses change of pressure for separation of azeotropic mixtures
                               without entrainers. The example is separation of mixture acetic acid(1)-water(2)-
                               formic acid(3) at two pressures: at atmospheric pressure and at 200 mm Hg pres-
                               sure (Kuschner et al., 1969).
                                 Figure 8.26a shows the location of azeotropes and separatrix lines at these two
                               pressures. Such location separatrix lines use flowsheet, shown in Fig. 8.26b (in the
                               first and the third columns, there is atmospheric pressure; in the second one, there
                               is pressure 200 mm Hg). The same figure shows lines of material balance and
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