Page 239 - 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





                                References                                                        213

                                set flow rate of entrainer – to determine the modes of minimum and maximum
                                reflux number (R min and R max ).


                        6.11.   Questions

                            1.  Let at sides 1-2 and 2-3 of the concentration triangle be a region of order of
                                components Reg 132 . Is it possible to use extractive distillation to separate this
                                              ord
                                ternary mixture? Which component can be the entrainer? The top product?
                            2.  Let at sides 1-2 and 2-3 of the concentration triangle be a region of order of
                                components Reg 231 . Which process can be used to separate this mixture? How
                                              ord
                                should the components be distributed among the products? Which component
                                should be the entrainer?
                            3.  In the concentration tetrahedron and its faces, there is a region of order of com-
                                ponents Reg 1234 . Which sharp extractive splits are feasible for this mixture?
                                          ord
                            4.  In the concentration tetrahedron and at its edges 1-2 and 3-4, there is a region of
                                order of components Reg 1234 . Is it possible to use a “Petlyuk column” to separate
                                                     ord
                                this mixture into components? What minimum number of sections should this
                                column have?

                            5.  Write the trajectory of an extractive distillation column at separation of a four-
                                component mixture at minimum reflux, bottom feeding being the control one.
                            6.  Write the trajectories of heteroazeotropic and heteroextractive distillation; indi-
                                cate the components present and absent in the product points and in trajectory
                                tear-off points.


                                References

                                Agrawal, R. (1996). Synthesis of Distillation Column Configurations for a Multi-
                                  component Separation. Ind. Eng. Chem. Res., 35, 1059–71.
                                Agrawal, R. (1999). More Operable Fully Thermally Coupled Distillation Column
                                  Configurations for Multicomponent Distillation. Trans IChemE., 77, Part A,
                                  543–53.
                                Agrawal, R., & Fidkowski, Z. T. (1998). More Operable Arrangements of Fully
                                  Thermally Coupled Distillation Columns. AIChE J., 44, 2565–81.
                                Agrawal, R., Woodward, D. W., & Modi, A. K. (1997). Coproduction of High Pu-
                                  rity Products Using Thermally-Linked Columns. In Distillation and Absorption
                                  Conference. Maastricht, pp. 511–520.
                                Amminudin, K. A., Smith, R., Thong, D. Y.-C., & Towler, G. P. (2001). Design
                                  and Optimization of Fully Thermally Coupled Distillation Columns. Part 1:
                                  Preliminary Design and Optimization Methodology. Trans. IChemE., 79, Part
                                  A, 701–15.
                                Barnes, F. G., Hanson, D. N., & King, C. J. (1972). Calculation of Minimum Reflux
                                  for Distillation Columns with Multiple Feeds. Ind. Eng. Chem. Process Des.
                                  Dev., 11, 136–47.
                                Bauer, M. H., & Stichlmair, J. (1995). Synthesis and Optimization of Distillation
                                  Sequences for the Separation of Azeotropic Mixtures. Comput. Chem. Eng., 19,
                                  515–20.
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