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己烷中酶催化反应热力学水活度的实时测量与控制

Real time measurement and control of thermodynamic water activities for enzymatic catalysis in hexane.

作者信息

Kang I J, Pfromm P H, Rezac M E

机构信息

Kansas State University, Department of Chemical Engineering, 105 Durland Hall, Manhattan, KS 66506-5102, USA.

出版信息

J Biotechnol. 2005 Sep 23;119(2):147-54. doi: 10.1016/j.jbiotec.2005.04.002.

Abstract

The esterification reaction of geraniol with acetic acid catalyzed by immobilized Candida antarctica lipase B was studied in hexane using a pervaporation-assisted batch reactor. The effect of thermodynamic water activity (a(w)) on the initial reaction rate was investigated at a(w) ranging from 0.02 to 1.0. The a(w) was monitored on-line in real time. a(w) was actively controlled throughout the reaction by using highly water-selective membrane pervaporation. This novel combination of a(w) sensing and control eliminates changes in a(w) during the reaction even in the initial phase of relatively rapid water release during an esterification. No chemicals are introduced for a(w) control, and no purge gases or liquids are needed. A maximum in the initial reaction rate was found approximately at a(w)=0.1. The initial reaction rate declined quickly at higher a(w), and dropped precipitously at lower a(w).

摘要

使用渗透蒸发辅助间歇式反应器,在己烷中研究了固定化南极假丝酵母脂肪酶B催化香叶醇与乙酸的酯化反应。在热力学水活度(a(w))范围为0.02至1.0的条件下,研究了其对初始反应速率的影响。实时在线监测a(w)。在整个反应过程中,通过使用高水选择性膜渗透蒸发来主动控制a(w)。这种a(w)传感与控制的新组合消除了反应过程中a(w)的变化,即使在酯化反应中相对快速释放水的初始阶段也是如此。无需引入化学物质来控制a(w),也无需吹扫气体或液体。在a(w)约为0.1时发现初始反应速率出现最大值。在较高的a(w)下,初始反应速率迅速下降,而在较低的a(w)下则急剧下降。

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