Development of a monolith based immobilized lipase micro-reactor for biocatalytic reactions in a biphasic mobile system

被引:29
作者
He, Ping [1 ]
Greenway, Gillian [1 ]
Haswell, Stephen J. [1 ]
机构
[1] Univ Hull, Dept Chem, Kingston Upon Hull HU6 7RX, N Humberside, England
关键词
Micro-reactor; Immobilized lipase; Monolith; Biphasic system; Hydrolysis reaction; Enzyme kinetics; ENANTIOSELECTIVE ACYLATION; TRYPSIN; SILICA; PURIFICATION; ADSORPTION; RESOLUTION; KINETICS; SUPPORTS;
D O I
10.1016/j.procbio.2009.12.008
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
This paper reports a simple method for producing macroporous silica-monoliths with controllable porosity that can be used for the immobilization of lipases to generate an active and stable micro-reactor for biocatalysis. A range of commercially available lipases has been examined using the hydrolysis reactions of 4-nitrophenyl butyrate in water-decane media. The kinetic studies performed have identified that a similar value for k(cat) is obtained for the immobilized Candida antarctica lipase A (0.13 min(-1)) and the free lipase in solution (0.12 min(-1)) whilst the immobilized apparent Michaelis constant K-m (3.1 mM) is 12 times lower than the free lipase in solution (38 mM). A 96% conversion was obtained for the immobilized C. antarctica lipase A compared to only 23% conversion for the free lipase. The significant higher conversions obtained with the immobilized lipases were mainly attributed to the formation of a favourable biphasic system in the continuous flowing micro-reactor system, where a significant increase in the interfacial activation occurred. The immobilized C. antarctica lipase A on the monolith also exhibited improved stability, showing 64% conversion at 80 degrees C and 70% conversion after continuous running for 480 h, compared to 40 and 20% conversions under the same temperature and reaction time for the free lipase. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:593 / 597
页数:5
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