Page 204 - Distillation theory
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P1: FCH/FFX  P2: FCH/FFX  QC: FCH/FFX  T1: FCH
            0521820928c06  CB644-Petlyuk-v1                                                      June 11, 2004  20:17





                        178    Distillation Trajectories in Infinite Complex Columns and Complexes

                                       D                                                 x  '
                                                                                          D


                                                                     2
                               F 1
                               F 2


                                                           S m
                                       B
                                                         +
                                                        N m









                                                 1                                       3
                               Figure 6.5. Intermediate section trajectories of ideal ternary mixtures (K 1 > K 2 >
                                                                            +

                               K 3 ) for two-feed column. x , pseudoproduct point, S m and N , stationary points of
                                                   D
                                                                           m
                               intermediate section regions Reg R  .
                                                       int
                               tie-lines liquid-vapor) and the points of top x D or bottom product x B , along with
                               that, in accordance with Eq. (6.3) can be located only in the vicinity of sides 1-2 or
                               2-3 in Fig. 6.3 or facets 1-2-3 or 2-3-4 in Fig. 6.4. Hence, it follows that feasible splits
                               for columns with one or two feeds are the same (i.e., if the flows of several feeds
                               are mixed before separation, we can only get the same products as in a column
                               with several feeds, but the energy consumption for separation will be bigger).
                                 Figure 6.5 shows stationary points S m and N of trajectory bundles of inter-
                                                                        +
                                                                        m
                               mediate section Reg R  and separatrixes of saddle stationary point S m obtained by
                                                int
                               means of calculation for ideal mixture pentane(1)-hexane(2)-heptane(3) at the
                               composition of pseudoproduct x    =−1.0; x     = 1.5; x    = 0.5 and at the value
                                                          D,1        D,2       D,3
                               of L/V = 1.2.
                                 In contrast to nonsharp separation in the top and bottom sections, the interme-
                               diate section has at reversible distillation trajectory not just one node stationary
                               point, but there are saddle point S m and node point N m . Separatrixes of the saddle
                               points S m divide concentration triangle into four regions Reg R  filled trajectory
                                                                                    int
                               bundles of intermediate section, one of which is the working one Reg R  .
                                                                                          w,int
                        6.3.3. Control Feed at Minimum Reflux Mode

                               The trajectory of the intermediate section in a three-section column connects
                               the trajectories of the top and bottom sections, and should join them in the cross-
                               sections of the top and the bottom feeds (i.e., at trays above and below these cross-
                               sections, the material balance should be valid). In the mode of minimum reflux,
                               only two of three sections adjacent to one of the feeds x F1 or x F2 , called “control”
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