Page 196 - 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








                              6



                               Distillation Trajectories in Infinite Complex

                               Columns and Complexes













                        6.1.   Introduction
                               This chapter extends the geometric description of the distillation process to infinite
                               complex columns and complexes, and then on this basis to develop methods of
                               their calculation.
                                 Here we understand by complex columns a countercurrent cascade without
                               branching of flows, without recycles and bypasses, which, in contrast to simple
                               columns, contains more than two sections. The complex column is a column with
                               several inputs and/or outputs of flows. The column of extractive distillation with
                               two inputs of flows – feed input and entrainer input – is an example of a complex
                               column.
                                 We understand by distillation complex a countercurrent cascade with branch-
                               ing of flows, with recycles or bypasses of flows. Columns with side stripping or
                               side rectifier and columns with completely connected thermal flows (the so-called
                               “Petlyukcolumns”)areexamplesofdistillationcomplexeswithbranchingofflows.
                               A column of extractive distillation, together with a column of entrainer regenera-
                               tion, make an example of a complex with recycle of flows. Columns of this complex
                               work independently of each other; therefore, we do not examine it in this chapter,
                               and the questions of its usage in separation of azeotropic mixtures and questions
                               of determination of entrainer optimal flow rate are discussed in the following
                               chapters.
                                 The fundamental difference between complex columns and complexes and
                               simple columns lies in the availability of intermediate sections (besides the top
                               and the bottom ones). The intermediate sections exchange vapor and liquid flows
                               with other sections or with the decanter.
                                 Therefore, for the intermediate sections, the equations of material balance
                               should be transformed in such a way that the flow rate and composition of a
                               pseudoproduct – that is, the difference between the outgoing and the incoming
                               flows–shouldbesubstitutedtherefortheflowrateandcompositionoftheproduct.
                               Figure 6.1 shows an example of a closed contour for obtaining material balance
                               equations for the intermediate section.

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