Page 169 - Chiral Separation Techniques
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5.4 Concluding remarks  147

                                             Fig. 5-20. Enantiomer separation in a cascaded ultrafil-
                                             tration (UF) system of 60 stages [77]















               Although the basic principles underlying this MEUF process for chiral separa-
             tions have been established, no optimization has yet been performed. Based on the
             ability of UF to treat large streams relatively inexpensively, this process will poten-
             tially become an extension to the rather limited range of large-scale commercial sep-
             aration processes. In addition, to facilitate further purification (e.g. by diastere-
             omeric salt crystallization) a single-stage MEUF process can potentially serve as an
             effective low-grade separation method.




             5.4 Concluding remarks



             In this chapter, we have discussed the potential of membrane technology for chiral
             separations. As the focus of this chapter has been on large-scale separations, the var-
             ious developments have been discussed from an engineering point of view. A signif-
             icant effort is being put into the development of chiral polymer membranes by a
             number of research groups. Nevertheless, these membranes still are in an early stage
             of development, and for industrial use significant improvements on flux and/or enan-
             tioselectivity are required. Once these limitations have been overcome, the applica-
             tion of chiral membranes will be similar to reverse osmosis and ultrafiltration, which
             will allow a relatively rapid implementation. Similarly, a large number of chiral
             selectors have been developed for application in liquid membranes. A major issue
             for the application of liquid membranes on an industrial scale lies in the problem of
             staging. As a result of the many recycles in the process, selective liquid membranes
             will require a large number of storage vessels, which is undesirable from a process
             economics standpoint.
               In the short term, we do not expect chiral membranes to find large-scale applica-
             tion. Therefore, membrane-assisted enantioselective processes are more likely to be
             applied. The two processes described in more detail (liquid–membrane fractionation
             and micellar-enhanced ultrafiltration) rely on established membrane processes and
             make use of chiral interactions outside the membrane. The major advantages of these
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