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P1: FCH/FFX  P2: FCH/FFX  QC: FCH/FFX  T1: FCH
            0521820928c06  CB644-Petlyuk-v1                                                      June 11, 2004  20:17





                        188    Distillation Trajectories in Infinite Complex Columns and Complexes

                                 Conditions 1 ÷ 3 are necessary for the fact that at big enough values of param-
                               eters (L/V) r ,(L/V) m , and (L/V) s , in each of the three sections, trajectory bundles
                               of these sections arise. Condition 4 maintains the potential feasibility of joining of
                               these trajectory bundles. Therefore, the conditions (1 ÷ 4) are necessary ones of
                               mixture separability in a three-section column. These conditions not valid; sharp
                               separation with obtaining set products is unfeasible.




                        6.5.2. Three-Component Mixtures
                               For the mixture acetone(1)-water(2)-methanol(3) (the entrainer is water, see Fig.
                               6.8) these four conditions are valid: (1) at side 1-2 there is intermediate section
                                                       3
                                                         t
                               trajectory tear-off region Reg , where K 1 > K 3 > K 2 (the segment [α 13 , 2]); (2)
                                                         e
                                                      1,2
                               vertex 1 is the unstable node N at side 1-2 (region Reg 1:2  ) (i.e., it can be the top
                                                         −
                                                                              sh,r
                                                         r
                                                       2
                                                 −
                               product point x D = N ≡ Reg at separation of the mixture 1,2 [K 1 > K 2 ]); (3) the
                                                 r
                                                         D
                                                       1             1
                               whole side 2-3 is bottom product segment Reg for the mixture 1,2,3 (K 1 > K 3 >
                                                                       B
                                                                    2,3         1,2:3
                               K 2 ); and (4) intermediate section sharp split region Reg  (region K 1 > K 3 >
                                                                                sh,e
                                                                                  1:3,2
                               K 2 ) coincides with the bottom section sharp split region Reg  and intersects the
                                                                                  sh,s
                               top section sharp split region Reg 1:2  at side 1-2 (the whole side 1-2).
                                                            sh,r
                                 We now examine the conditions of joining of sections trajectories at a set flow
                               rate of entrainer (i.e., at set value of the parameter E/D) for a three-component
                               mixture in the mode of minimum reflux. Each of two feeds can be the control
                               one, and the intermediate section trajectory in the mode of minimum reflux in
                               both cases should pass through the saddle point S m because this trajectory passes
                               through the node point N not only in the mode of minimum reflux, but also
                                                      +
                                                      m
                               at reflux bigger than minimum (point N arises at the boundary element of the
                                                                  +
                                                                 m
                               concentration simplex because the extractive distillation under consideration is
                               sharp).
                                 Therefore, point x f −1 (composition at the tray of the intermediate section that is
                               higher than the feed cross-section) in the mode of minimum reflux should lie on the
                                         −
                               separatrix N − S m (Fig. 6.10). If it turns out that point x f −1 is outside the working
                                         m
                                                                         3
                               trajectory bundle of the intermediate section Reg R  [(L/V) m < (L/V) min ] then,
                                                                          w,e               m
                                                                        1,2
                               as this figure shows, the trajectory of the intermediate sections deviates into the
                               side opposite to point N .Atareflux bigger than minimum [(L/V) m > (L/V) min ],
                                                   +
                                                                                                m
                                                   m
                               point x f −1 gets inside the working trajectory bundle of the intermediate section
                               and the trajectory of this section does not pass through point S m . Figure 6.10 shows
                               the case when the bottom feed is the control one. In this case, point x f (composition
                               at the tray of the bottom section that is lower than the feed cross-section) should
                               coincide with point N . Along with that, the condition of material balance should
                                                 +
                                                 s
                               be valid in the feed cross-section:
                                    L m x f −1 + L F x F = L s x f ,  where                     (6.4)
                                    L m + L F = L s                                             (6.5)
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