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固定化青霉素酰化酶生产6-APA的流程设计
引用本文:曲红波,丛威,王贞,欧阳藩.固定化青霉素酰化酶生产6-APA的流程设计[J].过程工程学报,1999,20(2):155-161.
作者姓名:曲红波  丛威  王贞  欧阳藩
作者单位:中国科学院化工冶金研究所生化工程国家重点实验室,北京,100080
基金项目:国家“九五”科技攻关项目
摘    要:针对本组研制的一种新型固定化青霉素酰化酶,以动力学方程为基础,分别进行了批式反应和连续反应的计算.对于批式反应,计算了不同浓度底物的水解过程和各种抑制因子对反应过程的影响;对于连续反应,计算了不同级数下的需酶量、转化率和成本消耗。结果表明,三、四级连续反应是可行的,有工业应用的前景。

关 键 词:固定化青霉素酰化酶  连续反应  动力学方程

CALCULATION ON REACTION PROCESS USING IMMOBILIZED PENICILLIN AMIDASE WITH THE KINETIC EQUATION
QU Hongbo,CONG Wei,WANG Zhen,OUYANG Fan.CALCULATION ON REACTION PROCESS USING IMMOBILIZED PENICILLIN AMIDASE WITH THE KINETIC EQUATION[J].Chinese Journal of Process Engineering,1999,20(2):155-161.
Authors:QU Hongbo  CONG Wei  WANG Zhen  OUYANG Fan
Abstract:Reaction of a novel immobilized penicillin amidase developed in the authors' group was calculated with the kinetic equation. The effect of substrate and products on the enzymatic reaction in batch mode was also analyzed. Although batch reaction is usually adopted in the industrial production of 6-APA, continuous reaction is more attractive. In the case of continuous operation, the consumption of enzyme, conversion and cost with different number of reaction stages were examined. The results suggest that three- or four-stage continuous reaction has greater potential.
Keywords:Immobilized penicillin amidase  Continuous reaction  Kinetic equation
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