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148  Chapter 5 Process Simplification and Intensification Techniques
                 5.3.1
                 Reaction

                This combination is exploited in mixed ion-exchange beds for water treatment.
                 Another application is in the ethylbenzene dehydrogenation reaction, which is
                 endothermal. In this process ± which is an equilibrium reaction ± the conversion
                 can be increased by the removal of hydrogen, with such removal being achieved by
                 selective oxidation between the reaction stages. In this case, the oxidation step
                 simultaneously generates heat which is used for heating between the stages.

                 5.3.1.1  Reactive distillation
                 Reactive distillation has been in use for quite some time in batch processes, al-
                 though initially it was not known by this name. Esterifications are exothermic equi-
                 librium reactions that produce reaction water. By removing this water in a rectifica-
                 tion column or dephlegmator on top of the reactor, see Figure 5.9, it is possible to
                 shift the reaction to completion if the water is the lightest component (an example
                 is the preparation of butyl acetate). The application of an esterification and an ether-
                 ification in both continuous processes are shown in Figure 5.1. The combination of
                 reaction with the removal of components by distillation is called ªreactive distilla-
                 tionº. The reaction might be endothermal or exothermal, homogeneous in the liquid
                 phase, or heterogeneous at a solid catalyst kept under liquid while the liquid is at
                 bubble point.
                  The most well-known industrial applications of continuous processes are the
                 preparation of the octane boosters ETBE (ethyl-tert-butyl ether), MTBE (methyl-tert-
                 butyl ether) and TAME (tert-amyl-methyl ether) (DeGarmo et al., 1992; Doherty and
                 Buzad, 1992). Other applications, next to etherification, include de-etherifications,
                 esterification (as mentioned above), and alkylation of aromatics.



                       Methyl Acetate            MTBE
                     homogeneous catalyzed   heterogeneous catalyzed
                                              C4’s Methanol
                                               ISO butylene
                                Methyl acetate
                 Acetic
                 acid                                           C4’s and
                                                                 excess
                                                                methanol
                 Sulfuric             Pre reactor
                  acid
                 catalyst
                 Methanol


                                                             MTBE
                               Water
                 Fig. 5.1. Reactive distillation examples; Methyl acetate and MTBE production.
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