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430  19 Chemoenzymatic Multistep One-Pot Processes

                    with glutaraldehyde) and Pt/C (5%) as heterogeneous catalyst in combination
                    with 20 atm of hydrogen, composition of the reaction mixture showed an amount
                    of 46% each for the products d-mannitol and d-glucitol, while d-glucose (5%)
                    and d-fructose (3%) were found as minor components [8]. Later work addressed
                    process development by varying both immobilized d-glucose isomerase and the
                    metal catalyst component, respectively [9, 10]. Stewart and Ruddlesden [9] applied a
                    ruthenium-loaded zeolite as a catalyst in combination with a d-glucose isomerase,
                    thus obtaining d-mannitol in 29% yield when starting from d-glucose. The van
                    Bekkum group [10] developed a further improved process based on a d-glucose
                    isomerase immobilized on silica in combination with a copper-on-silica catalyst. By
                    means of these catalytic components, this isomerization–hydrogenation process
                    runs efficiently with the formation of d-mannitol in high yields of 62–66%. As
                    substrates, the use of a 1 : 1 d-glucose/d-fructose mixture as well as d-glucose alone
                    was reported to be suitable.
                      After this pioneering work by van Bekkum et al., further breakthroughs were
                    achieved by several groups in the 1990s in the field of combining a chemocatalytic
                    racemization (chosen as a specific type of isomerization) and a hydrolase-catalyzed
                    process toward DKRs. It is noteworthy that a wide variety of different strategies
                    based on different types of chemo- and biocatalysts as well as different reaction
                    media (organic and aqueous solvents) have been realized, all fulfilling the criteria
                    of a DKR.
                      Such a process, which runs in water and is based on a palladium-catalyzed racem-
                    ization of O-acylated allylic alcohols in combination with a hydrolase-catalyzed
                    enantioselective hydrolysis of the ester, was developed in an early pioneering work
                    by Allen and Williams [11]. In this type of DKR process, the resulting allylic
                    alcohols of type, for example, (S)-6, were obtained with satisfactory to high enan-
                    tioselectivities (Scheme 19.3). For example, under these conditions, the hydrolysis
                    of racemic ester rac-5 in the presence of a lipase from Pseudomonas fluorescens gave



                                     Lipase from
                      Ph                              Ph
                                    Pseudomonas
                          O   CH 3   fluorescens         OH
                                          O
                                       + H 2
                            O
                                      − AcOH
                        (S)-5                       (S)-6
                                                 96% conversion
                           PdCl (CH CN) 2           96% ee
                                  3
                              2
                             (5 mol%)
                      Ph
                          O   CH 3
                            O
                        (R)-5

                    Scheme 19.3  Dynamic kinetic resolution of an O-acylated allylic alcohol based on
                    palladium-catalyzed racemization and enzymatic ester hydrolysis.
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