Laboratory of Separation and Reaction Engineering - LSRE, Associate Laboratory LSRE/LCM, Department of Chemical Engineering, Faculty of Engineering, University of Porto, Rua Dr. Roberto Frias s/n, 4200-465 Porto, Portugal.
Enzyme Microb Technol. 2011 Jul 10;49(2):183-91. doi: 10.1016/j.enzmictec.2011.04.017. Epub 2011 Apr 30.
In this work, we have investigated the kinetics of the biotechnological production of lactobionic acid (LBA) and sorbitol by the catalytic action of glucose-fructose oxidoreductase (GFOR) and glucono-δ-lactonase (GL) enzymes. The cells of bacterium Zymomonas mobilis ATCC 29191 containing this enzymatic complex were submitted to permeabilization and reticulation procedures. The effect of the concentration of substrates on the rate of product formation using a mobilized cell system was investigated. The application of higher fructose concentration seems to not affect the initial rate of formation of the bionic acid. Under conditions of low initial concentration of lactose, the experimental kinetic data of the bi-substrate reaction were modelled by assuming a rate equation of the classical ping-pong mechanism. The found kinetic parameters displayed a low affinity of the GFOR enzyme for both substrates. The enzymatic system did not exhibit normal Michaelis-Menten kinetics in response to a change of concentration of lactose, when fructose was held constant, presenting a sigmoid relationship between initial velocity and substrate concentration. A rate equation based on Hill kinetics was used to describe the kinetic behaviour of this enzyme-substituted reaction at higher lactose concentrations. The results from batch experiments using immobilized cells within Ca-alginate beads revealed that there is no pronounced occurrence of mass transfer limitations on LBA production for beads with 1.2 mm in average diameter. This discussion aids for defining the best operating conditions to maximize the productivity for LBA and sorbitol in this bioconversion and also for reducing the complexity of downstream separation processes.
在这项工作中,我们研究了通过葡萄糖-果糖氧化还原酶(GFOR)和葡萄糖酸-δ-内酯酶(GL)的催化作用生物技术生产乳糖酸(LBA)和山梨醇的动力学。含有这种酶复合物的运动发酵单胞菌(Zymomonas mobilis)ATCC 29191 细胞经历了渗透和交联过程。研究了在流动细胞体系中使用不同底物浓度对产物形成速率的影响。使用较高的果糖浓度似乎不会影响仿生酸的初始形成速率。在初始乳糖浓度较低的条件下,通过假设经典乒乓机制的速率方程对双底物反应的实验动力学数据进行了建模。发现的动力学参数显示 GFOR 酶对两种底物的亲和力较低。当果糖保持恒定时,该酶系统对乳糖浓度的变化没有表现出正常的米氏-门坦动力学,初始速度与底物浓度之间呈现出 S 形关系。基于 Hill 动力学的速率方程用于描述在较高乳糖浓度下该酶替代反应的动力学行为。在 Ca-藻酸盐珠内使用固定化细胞进行分批实验的结果表明,对于平均直径为 1.2 毫米的珠,LBA 生产过程中没有明显的传质限制。该讨论有助于确定最佳操作条件以最大程度地提高生物转化中 LBA 和山梨醇的生产力,并降低下游分离过程的复杂性。