Whole-cell biocatalysis in organic media

被引:249
作者
León, R [1 ]
Fernandes, P [1 ]
Pinheiro, HM [1 ]
Cabral, JMS [1 ]
机构
[1] Univ Tecn Lisboa, Ctr Engn Biol & Quim, Engn Bioquim Lab, Inst Super Tecn, P-1096 Lisbon, Portugal
关键词
whole cells; biocatalysis; bioconversions; organic media;
D O I
10.1016/S0141-0229(98)00078-7
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The use of water-immiscible organic solvents in whole-cell biocatalysis has been exploited for biotransformations involving sparingly water-soluble or toxic compounds. These systems can overcome the problem of low productivity levels in conventional media due to poor substrate solubility, integrate bioconversion and product recovery in a single reactor, and shift chemical equilibria enhancing yields and selectivities; nevertheless, the selection of a solvent combining adequate physicochemical properties with biocompatibility is a difficult task. The cell membrane seems to be the primary target of solvent action and the modification of its characteristics the more relevant cellular adaptation mechanism to organic solvent-caused stress. Correlations between the cellular tonicity or the extractive capacities of different solvents and some of their physical properties have-been proposed in order to minimize preliminary, solvent-selection experimental work but also to help in the understanding of the molecular mechanisms of toxicity and extraction. The use of whole cells in organic-media biocatalysis provides a way to regenerate cofactors and carry out bioconversions or fermentations requiring multi-step metabolic pathways; some processes already are commercially exploited;Immobilization can further protect cells from solvent toxicity, and has thus been effectively used in organic solvent-based systems. Several examples of extractive fermentations and other whole-cell bioconversions in organic media are presented. (C) 1998 Elsevier Science Inc.
引用
收藏
页码:483 / 500
页数:18
相关论文
共 167 条
[21]   NEW MODE OF DUNALIELLA BIOTECHNOLOGY - 2-PHASE GROWTH FOR BETA-CAROTENE PRODUCTION [J].
BENAMOTZ, A .
JOURNAL OF APPLIED PHYCOLOGY, 1995, 7 (01) :65-68
[22]  
BOEREN S, 1987, BIOCATALYSIS ORGANIC, P303
[23]  
BRINK LES, 1987, J CHEM TECHNOL BIOT, V37, P21
[24]   OPTIMIZATION OF ORGANIC-SOLVENT IN MULTIPHASE BIOCATALYSIS [J].
BRINK, LES ;
TRAMPER, J .
BIOTECHNOLOGY AND BIOENGINEERING, 1985, 27 (08) :1258-1269
[25]   BIOCATALYSIS IN ORGANIC MEDIA [J].
BRINK, LES ;
TRAMPER, J ;
LUYBEN, KCAM ;
VANTRIET, K .
ENZYME AND MICROBIAL TECHNOLOGY, 1988, 10 (12) :736-743
[26]   SOLVENT SELECTION-STRATEGIES FOR EXTRACTIVE BIOCATALYSIS [J].
BRUCE, LJ ;
DAUGULIS, AJ .
BIOTECHNOLOGY PROGRESS, 1991, 7 (02) :116-124
[27]  
BUITELAAR R M, 1990, Biotechnology Techniques, V4, P415, DOI 10.1007/BF00159388
[28]   EXTRACTIVE FERMENTATION OF ACETIC-ACID - ECONOMIC TRADEOFF BETWEEN YIELD OF CLOSTRIDIUM AND CONCENTRATION OF ACETOBACTER [J].
BUSCHE, RM .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 1991, 28-9 :605-621
[29]   2-PHASE AIRLIFT FERMENTER OPERATION WITH ELICITATION FOR THE ENHANCED PRODUCTION OF BENZOPHENANTHRIDINE ALKALOIDS IN CELL-SUSPENSIONS OF ESCHERICHIA-CALIFORNICA [J].
BYUN, SY ;
PEDERSEN, H .
BIOTECHNOLOGY AND BIOENGINEERING, 1994, 44 (01) :14-20
[30]  
Cabral J. M. S., 1991, EXTRACTIVE BIOCONVER, P207