Page 271 - Distillation theory
P. 271

P1: JPJ/FFX  P2: JMT/FFX  QC: FCH/FFX  T1: FCH
            0521820928c07  CB644-Petlyuk-v1                                                      June 11, 2004  20:18





                                7.4 Design Calculation of Extractive Distillation Columns         245


                                      x D
                                                                x  '
                                                                 D
                                x E
                                x F
                                                     −
                                                   N
                                                     m  2
                                      x B                   x E
                                                x F+E


                                               +
                                           x e  ≡ N m  x min  x    m S
                                                   f − 1  f − 1       s S
                                         ∞   +                       max
                                        x  ≡ N                      x  f  − 1
                                         f  s                  min
                                       x  −          x  f     x  f
                                        e  1
                                         1                              3
                                               13
                                                    x F
                                           x D
                                Figure 7.12. Calculated section trajectories for acetone
                                (1)-water(2)-methanol(3) extractive distillation. E/F =
                                2.03, R r = 7, x F (0.6, 0.0, 0.4), the region of intermediate
                                                3
                                                 R
                                section trajectories Reg w,e  is shaded.
                                                1,2
                        7.4.1. Three-Component Azeotropic Mixtures
                                In Fig. 7.12, x ∞  = N s +  and coordinates of point x min  tied with it by the con-
                                            f
                                                                            f −1
                                ditions of material balance in the feed cross-section are determined with the
                                                                                      1
                                help of Eq. (5.18). Point x min  is located at line S s − N (Reg qsh,R ), and point
                                                                                 +
                                                        f                        s    sep,s
                                                              3                       2,3
                                x max  is located at line S m − N (Reg qsh,R ). This determines coordinates of points
                                                         +
                                 f −1                    m     sep,e
                                                              1,2
                                (x max sh   min sh                              sh  can be located out-
                                               ) . Along with that segment, [x f −1 ]
                                    ) and (x
                                  f −1 lin   f  lin                             lin
                                side the working trajectory bundle of the intermediate section N − S m − N +
                                                                                          −
                                                                                                    m
                                                                                         m
                                in Reg att  of point N . The same way as for two-section columns at segments
                                                  +
                                                 m
                                     sh
                                              sh
                                [x f −1 ] and [x f ] , there are points x opt  and x opt  interconnected by conditions of
                                     lin      lin               f −1   f
                                material balance for which summary number of trays in the bottom and interme-
                                diate sections is minimum.
                                  As far as the joining of trajectories of the top and the intermediate sections
                                is concerned, the composition point at the first tray below the cross-section of
                                the entrainer input x e should be located quite close to the boundary element
                                of the concentration simplex that contains components of the top product and
                                of the entrainer (in Fig. 7.12 – to side 1-2). Allowable concentration of impurity
                                components in point x e is determined by the requirements to the purity of the top
                                product. Therefore, the composition in point x e is not an optimized parameter and
                                the composition in point x e−1 at the first tray above the cross-section of entrainer
                                input is determined by the conditions of material balance in this cross-section.
   266   267   268   269   270   271   272   273   274   275   276