Page 142 - Distillation theory
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P1: JPJ/FFX  P2: FCH/FFX  QC: FCH/FFX  T1: FCH
            0521820928c05  CB644-Petlyuk-v1                                                      June 11, 2004  20:15





                        116    Distillation Trajectories and Conditions of Mixture Separability


                                 At further increase of R (the second class of fractioning), the product point x D
                               moves alongside 1-2 to vertex 1, the stationary point disappears in feeding, and
                               the composition in the stationary point S is changed (Fig. 5.2c). At the second
                                                                    2
                               limit (boundary) value of reflux number R , the product point x D approaches
                                                                    lim
                               vertex 1 (the third class of fractioning; Fig. 5.2d). At this mode, the second zone
                               of constant concentrations (vertex 1 is the unstable node N ) appears again in
                                                                                   −
                               the column. At further increase of R (the third class of fractioning), the product
                               point stays in vertex 1 and the stationary point S moves to vertex 2 (Fig. 5.2e). At
                               R =∞, the stationary points of trajectory bundle coincide with the vertexes of
                                                                           ∞
                               concentration triangle (Fig. 5.2f) and Reg R  = Reg .
                                                                  w,r
                                 It is seen from Fig. 5.2 that the distillation trajectory bundle of the one-section
                                                             R
                               column fills up some triangle Reg w,r , the vertexes of which are the stationary
                               points. Some of these stationary points are located inside the concentration tri-
                               angle C (3)  and the rest of them outside it (i.e., they are of theoretical nature).
                               The triangle Reg R(3)  filled up with trajectory bundle is called distillation triangle.
                                             w,r
                               At a greater number of components, the trajectory bundle fills up some distil-
                               lation simplex Reg R(n) . In two-section columns, each section has its distillation
                                               w,r
                               simplex Reg R  or Reg R  , and the availability of the common roots of the equa-
                                         w,r      w,s
                               tions of Underwood for two sections means that these simplexes in the mode of
                               minimum reflux adjoin to each other by their vertexes, edges, faces, or hyper-
                               faces.


                                      x D
                                                               2

                               x
                                F

                                      x B
                                                 2
                                                R  = 16.17
                                                 lim                      x
                                                                           B
                                                             R=10.0
                                              x
                                               D                              R  = 11.47
                                                                               2
                                                                  R=5.0        lim
                                                                              D/F=0.2
                                                                                  1
                                                                                 R  = 7.7
                                                                                  lim
                                                                                 (D/F) =0.26
                                          1                           x             pr
                                         R lim  = 7.7    D/F=0.4 D/F=0.5  F
                                          =0.26   D/F=0.3
                                      (D/F) pr                                           x B
                                    x
                                                                                       2
                                    D
                                                                                      R  = 16.17
                                                                                       lim
                                                                                      D/F ≥ 0.26
                                        1
                                           2
                                          R  = 11.47                                   3
                                           lim
                                          D/F ≤ 0.2
                               Figure 5.3. Product compositions x D and x B for an ideal mixture with α 1 = 1.5, α 2 =
                               1.1, α 3 = 1.0, x F1 = 0.2, x F2 = 0.3, and x F3 = 0.5 at minimum reflux for different R min
                               and D/F. Thick lines with arrows − D/F = const, thin lines − R = const.
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