Page 114 - Distillation theory
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P1: FCH/FFX  P2: FCH/FFX  QC: FCH/FFX  T1: FCH
            0521832772c04  CB644-Petlyuk-v1                                                      June 11, 2004  17:49





                        88     Trajectories of Thermodynamically Reversible Distillation

                                 In Fig. 4.9a, there are two trajectories tear-off points x t  of the reversible
                                                                                   rev
                                                                                                  (2)
                               distillation trajectory for any points x D of the possible product segment Reg
                                                                                                  D
                               at side 1-2. For point x D located at the end of the possible product composition
                               segment, both these trajectories tear-off points x t  coincide with each other, but
                                                                         rev
                               the length of the trajectory inside the concentration triangle becomes equal to
                               zero. The segment from vertex 1 to point α 23 is trajectory tear-off segment Reg t(2)  .
                                                                                                rev,r
                               At the same figure at side 1-3 from point α 23 to vertex 3, there is a segment of
                               trajectories tear-off Reg t(2)  and possible product composition segment Reg (2)
                                                    rev,r                                         D
                               coincides with side 1-3. Along with that, for any point x D there is one trajectory
                                            t
                               tear-off point x .
                                            rev

                        4.3.4. Necessary Condition of Sharp Reversible Distillation

                               It follows from the aforesaid that sharp separation in a reversible distillation
                               column is feasible only if the liquid–vapor tie-line of feeding is directed to the
                                                                   (n−1)
                               possible product composition region Reg  at the boundary element C n−1 of
                                                                   D
                                                                        (n−1)
                               the concentration simplex and from region Reg  at other boundary element
                                                                        B
                               C n−1 .
                                 In other words, for sharp separation in a two-section column it is necessary that
                               the feed point belongs to the intersection of true bundles of reversible distillation
                               trajectories of the two sections x F ∈ (Reg rev,r • Reg rev,s ) (Fig. 4.10). The reversible


                                           2                         2
                                               x                        x
                               a)      α 23    B        b)      α 23    B
                                                                     x F
                                       x F                                  α
                                                  α 13                       13

                                 x D
                                 1       α 23  13     3   1  x D  α 23  13      3
                                                        2

                                                           x
                                            c)      α 23    B

                                                       x F     α 13

                                              x D
                                              1       α 23  13     3
                               Figure 4.10. Sharp reversible section trajectories of acetone(1)-
                               benzene(2)-chloroform(3) mixture for two-section columns: (a) split
                               1,2 : 2,3, x F ∈ (Reg 3 rev,r  • Reg 1 rev,s ); (b) split 1,3 : 2,3, x F ∈ (Reg 2 rev,r  •
                               Reg 1 rev,s ); and (c) split 1 : 2,3, x F ∈ (Reg 2=3  • Reg 1 rev,s ) and x F ∈ α 23 .
                                                           rev,r
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