Page 250 - Cascade_Biocatalysis_Integrating_Stereoselective_and_Environmentally_Friendly_Reactions
P. 250

226  9 Stereoselective Hydrolase-Catalyzed Processes in Continuous-Flow Mode

                     59. Yamaguchi, H. and Miyazaki, M.  operation modes. Biotechnol. Prog., 20,
                        (2013) Enzyme-immobilized reac-  1044–1052. doi: 10.1021/bp034314c
                        tors for rapid and efficient sample  67. Al-Zuhair, S. (2005) Production of
                        preparation in MS-based proteomic  biodiesel by lipase-catalyzed transes-
                        studies. Proteomics, 13, 457–466. doi:  terification of vegetable oils: a kinetics
                        10.1002/pmic.201200272           study. Biotechnol. Prog., 21, 1442–1448.
                     60. Liese, A., Seelbach, K., and Wandrey,  doi: 10.1021/bp050195k
                        C. (eds) (2006) Industrial Biotransfor-  68. Royon, D., Daz, M., Ellenrieder, G.,
                        mations, 2nd edn, Wiley-VCH Verlag  and Locatelli, S. (2007) Enzymatic
                        GmbH, Weinheim, New York. doi:   production of biodiesel from cotton
                        10.1002/3527608184
                                                         seed oil using t-butanol as a solvent.
                     61. Panke, S., Held, M., and Wubbolts,  Bioresour. Technol., 98, 648–653. doi:
                        M. (2004) Trends and innovations
                                                         10.1016/j.biortech.2006.02.021
                        in industrial biocatalysis for the
                                                      69. Chen, H.C., Ju, H.Y., Wu, T.T., Liu,
                        production of fine chemicals. Curr.
                                                         Y.C., Lee, C.C., Chang, C., Chung,
                        Opin. Biotechnol., 15, 272–279. doi:
                                                         Y.L., and Shieh, C.J. (2011) Continuous
                        10.1016/j.copbio.2004.06.011
                                                         production of lipase-catalyzed biodiesel
                     62. Costa, I.C.R., Itabaiana, I.J., Flores,
                                                         in a packed-bed reactor: optimization
                                 ¸
                        M.C., Lourenco, A.C., Leite, S.G.F.,
                        Miranda, L.S.M., Leal, I.C.R., and de  and enzyme reuse study. J. Biomed.
                        Souza, R.O.M.A. (2013) Biocatalyzed  Biotechnol., Article ID 950725, 6 pp.
                        acetins production under continuous-  doi: 10.1155/2011/950725
                        flow conditions: valorization of glycerol  70. Dossat, V., Combes, D., and Marty,
                        derived from biodiesel industry. J. Flow  A. (2002) Efficient lipase catalysed
                        Chem. doi: 10.1556/JFC-D-13-00001  production of a lubricant and surfac-
                     63. Arcos, J.A., Garcia, H.S., and Hill,  tant formulation using a continuous
                        C.G. (2000) Continuous enzy-     solvent-free process. J. Biotechnol.,
                        matic esterification of glycerol with  97, 117–124. doi: 10.1016/S0168-
                        (poly)unsaturated fatty acids in a  1656(02)00021-4
                        packed-bed reactor. Biotechnol. Bioeng.,  71. Yang, T., Rebsdorf, M., Engelrud, U.,
                        68, 563–670. doi: 10.1002/(SICI)1097-  and Xu, X. (2005) Enzymatic produc-
                        0290(20000605)68:5<563::AID-     tion of monoacylglycerols containing
                        BIT11>3.0.CO;2-H                 polyunsaturated fatty acids through
                     64. Rønne, T.H., Yang, T., Mu, H.,  an efficient glycerolysis system. J.
                        Jacobsen, C., and Xu, X. (2005)
                                                         Agric. Food Chem., 53, 1475–1481. doi:
                        Enzymatic interesterification of
                                                         10.1021/jf048405g
                        butterfat with rapeseed oil in a con-
                                                      72. Jeganathan, J., Nakhla, G., and Bassi,
                        tinuous packed bed reactor. J. Agric.
                                                         A. (2007) Hydrolytic pretreatment of
                        Food Chem., 53, 5617–5624. doi:  oily wastewater by immobilized lipase.
                        10.1021/jf050646g
                     65. Kim, B.H. and Akoh, C.C. (2006)  J. Hazard. Mater., 145, 127–135. doi:
                                                         10.1016/j.jhazmat.2006.11.004
                        Characteristics of structured lipid pre-
                        pared by lipase-catalyzed acidolysis of  73. Vasic-Racki, D. (2006) in Industrial
                        roasted sesame oil and caprylic acid  Biotransformations, 2nd edn (eds A.
                                                         Liese, K. Seelbach, and C. Wandrey),
                        in a bench-scale continuous packed
                        bed reactor. J. Agric. Food Chem., 54,  Wiley-VCH Verlag GmbH, Wein-
                        5132–5141. doi: 10.1021/jf060607k  heim, New York, pp. 1–36. doi:
                     66. Gonz´ alez Moreno, P.A.,        10.1002/3527608184.ch1
                        Robles Medina, A., Camacho Rubio, F.,  74. Sotolongo, V., Johnson, D.V., Wahnon,
                        Camacho P´ aez, B., and Molina Grima,  D., and Wainer, I.W. (1999) Immobi-
                        E. (2004) Production of structured  lized horse liver alcohol dehydrogenase
                        lipids by acidolysis of an EPA-enriched  as an on-line high-performance liquid
                        fish oil and caprylic acid in a packed  chromatographic enzyme reactor for
                        bed reactor: analysis of three different  stereoselective synthesis. Chirality,
   245   246   247   248   249   250   251   252   253   254   255