Page 93 - Distillation theory
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P1: JPJ/FFX  P2: FCH/FFX  QC: VINOD/IYP  T1: FCH
            0521820928c03  CB644-Petlyuk-v1                                                      June 11, 2004  20:12





                                3.5 Feasible Splits at R =∞ and N =∞                               67

                                              123                           123
                                     x D ≡  N  +   N −
                                a)       D         B           b)
                                                                     12
                                       12

                                    1                             1                  +
                                                                                    N
                                                                                     D
                                                    134
                                                                                  134
                                           13                             13  x ≡  N  −
                                                                               B   B

                                              123                           123
                                                    +
                                                                                 +
                                c)                N D          d)               N ≡  N  −
                                                                     12          D  B
                                       12

                                    1                             1

                                                    134                           134
                                                       −
                                                      N B
                                           13                             13
                                                               123

                                                       12


                                                    1

                                                                    134

                                                                     +
                                                            13      N D ≡  N B −
                                Figure 3.19. Example of determination whether the feed point (Fig. 3.14a)
                                                                                   ∞
                                belongs to the product simplex Reg simp (only the distillation region Reg ≡
                                12 ⇒ 13 is shown). Material balance lines and distillation trajectories at R =
                                ∞, N =∞ (shown schematically on linear boundary elements of the dis-
                                              simp
                                tillation region Reg  , not on curvilinear ones of the distillation region
                                              bound
                                Reg ∞  ). The visible faces of the simplex are shaded (one darker, one
                                   bound
                                lighter).

                                  1.  1 : 234,23,38,568,58,78,89,8
                                  2.  1,234 : 23,38,568,58,78,89,8
                                  3.  1,234,23 : 38,568,58,78,89,8
                                  4.  1,234,23,38 : 568,58,78,89,8
                                  5.  1,234,23,38,568 : 58,78,89,8
                                  6.  1,234,23,38,568,58 : 78,89,8
                                  7.  1,234,23,38,568,58,78 : 89,8
                                  8.  1,234,23,38,568,58,78,89 : 8
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