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208  9 Stereoselective Hydrolase-Catalyzed Processes in Continuous-Flow Mode

                      A porous vessel filled with the biocatalyst and immersed in recirculating toluene
                    was applied for the preparation of methyl trans-(2R,3S)-(4-methoxyphenyl)glycidate
                    (an intermediate of Diltiazem) from its racemic methyl ester [88]. In this system,
                    hydrolysis of the ester with Lecitase ® Ultra (a commercially available phospholi-
                    pase) immobilized in macroporous gelatin organo-gel (gelozyme) gave the desired
                    product in 47% yield and >99% ee.
                      A recirculated PBR filled with lactonase from Fusarium proliferatum adsorbed
                    onto cotton cloth and cross-linked with glutaraldehyde was applied for enantiomer
                    selective hydrolysis of racemic 2-hydroxy-γ-butyrolactone (HBL) [89]. The system
                    was operated for 60 cycles with an average productivity of 2.48 g l −1  h −1  and
                    90.0–96.4% ee.
                      Hydrolytic reactions in real flow-through systems are summarized in Figure 9.3
                    and Table 9.4.
                      Hydrolysis in a PBR filled with CrL adsorbed on silica gel was evaluated for the
                    influence of flow rate, height to diameter ratio (H/D) and substrate concentration to
                    yield (S)-ketoprofen [(S)-13] from its racemic 2-chloroethyl ester (Figure 9.4, entry 1)
                    [90]. By using a semicontinuously operated PBR, enantiopure (S)-13 (>99% ee) was
                                                                                 −1
                    produced with a conversion of 30% and productivity of 1.5 mg g −1  biocatalyst h .
                      The hollow fiber MBR (Figure 9.4) proved to be a versatile tool to perform
                    continuous-flow KRs by lipase-catalyzed hydrolysis of racemic esters. The system
                    consists of an organic phase containing the racemic ester, a lipase-loaded
                    membrane, and an aqueous phase that extracts the product. A full-scale plant
                    was built for the chiral separation of the above mentioned Diltiazem intermediate
                                   2
                    containing 1440 m of hollow fiber in a MBR and producing 75 tons/year of
                    resolved product [96].
                      (S)-Ibuprofen [(S)-14] was produced from its racemic 2-ethoxyethyl ester by using
                    lipase-catalyzed hydrolysis in hollow fiber MBR (Table 9.4, entries 2 and 3) [91,
                    92]. The operating temperatures, organic phase and aqueous phase flow rates, and
                    enzyme loadings were varied leading to a KR with enantiomeric ratio (E)of13and
                    85–90% ee of (S)-14 [91, 92]. On the other hand, hydrolysis of racemic ibuprofen
                    heptyl ester under the same conditions gave only an E value of 1–4 [92].


                                                               MeO
                                   O                    O                      O
                                     OH                   OH                     OH
                          O
                    (S)-Ketoprofen: (S)-13  (S)-Ibuprofen: (S)-14  (S)-Naproxen: (S)-15
                    Alcohol in parent ester:  Alcohol in parent ester:  Alcohol in parent ester:
                    HOCH CH CI [90],       HOCH CH OEt [91, 92],  HOMe [93, 94]
                                                  2
                                               2
                         2
                            2
                                               H
                    HOCH 2 CH OEt [87],    HOC 7 15  [92]
                            2
                    HOEt [95]
                    Figure 9.3  Products of kinetic resolutions of the esters indicated by enzyme-catalyzed
                    hydrolysis in continuous-flow mode [87, 90–95].
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