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30  2 New Trends in the In Situ Enzymatic Recycling of NAD(P)(H) Cofactors

                              O                               OH
                                             ADH
                            R    R′                         R  *  R′
                                      NADPH       NADP +



                                            G6PDH

                                 Gluconolactone-6P  G6P

                                            Sf-Pho

                    Gluconolactone       PP i                 Glucose

                                                   P i
                       Gluconic
                        acid             Phosphorylated
                                            Sf-Pho
                    Scheme 2.4  Regeneration of NADPH by glucose-6-phosphate dehydrogenase (G6PDH)
                    with the in situ generation of glucose 6-phosphate (G6P) catalyzed by an acid phosphatase
                    (Sf -Pho) in the presence of glucose and pyrophosphate (PP ).
                                                             i
                    catalyzed by the same ADH at the expense of a sacrificial co-substrate. A high
                    co-substrate concentration (up to 50% (v/v) in the case of 2-propanol (also called
                    isopropyl alcohol (IPA)) [41]) can be used to drive the equilibrium of the system
                    toward the desired direction. However, this solution has several limitations, for
                    example, incomplete (<99%) degree of conversion, expensive and complicate
                    product purification, and detrimental effects on the enzyme stability.
                      A possible solution to overcome these thermodynamic limitations is the use
                    of an ‘‘in situ product removal’’ (ISPR) technique [42]. This approach can be
                    easily applied when the co-substrate and the co-product have significantly different
                    physical properties. For example, in the case of the IPA/acetone system used
                    in several ADH-catalyzed ketone reductions, the co-product acetone is the most
                    volatile compound in the reaction mixture. Therefore, it can be removed by a simple
                    stripping process, such as by passing a continuous air stream (previously saturated
                    with water and IPA) through the reaction mixture (Figure 2.1).
                      The general applicability and easy scale-up of this approach has been recently
                    demonstrated in the synthesis of chirally pure (S)-2-bromo-2-cyclohexen-1-ol, a
                    key intermediate for the preparation of different natural products and drugs [43].
                    During the process optimization, it was further shown that the concentration of IPA
                    (20% (v/v)) must be maintained constant by either using an IPA/H O saturated
                                                                          2
                    air sparge or replenishing appropriate amounts of the co-substrate during the
                    conversion. The reduction reaction, catalyzed by a selected ketoreductase, was
                    eventually performed on 100 g of the starting ketone and the desired product was
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