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Modeling the dynamics of E-coli populations in the three-dimensional turbulent field of a stirred-tank bioreactor - A structured-segregated approach

机译:在搅拌槽生物反应器的三维湍流场中模拟大肠杆菌种群的动力学-一种结构分离的方法

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In the present work, an Euler-Lagrange approach has been applied to characterize the behavior of a heterogeneous cell population in a stirred-tank bioreactor with non-ideal mixing. It allows one to describe population behavior as the outcome of the interaction between the intracellular state of its individual cell and the turbulent flow field in the reactor. The modeling approach and the numerical method employed are based on an Euler-Lagrange formulation of the system combined with a fractional-step method to allow for a stable, accurate, and numerically efficient solution of the underlying equations. This strategy permits one to account for the heterogeneity present in real reactors in both the abiotic and biotic phases. The example of sugar uptake (phosphotransferase system, PTS) of E. coli cells growing in a fed-batch culture is used to illustrate the application of the approach. The activity of the uptake system depends on the local concentration of glucose as well as the ratio of the intracellular concentrations of phosphoenolpyruvate and pyruvate, which in turn is a function of the history of the individual cell. The simulation results point to distinct differences in the viability of the cells at different scale of operation. (c) 2006 Published by Elsevier Ltd.
机译:在目前的工作中,欧拉-拉格朗日方法已被应用于表征非理想混合的搅拌罐式生物反应器中异质细胞群体的行为。它使人们能够将种群行为描述为其单个细胞的细胞内状态与反应堆中湍流场之间相互作用的结果。所采用的建模方法和数值方法是基于系统的Euler-Lagrange公式与分数步法相结合的,从而可以对基础方程式进行稳定,准确和数值高效的求解。这种策略允许人们考虑非生物和生物相中真实反应堆中存在的异质性。以分批补料培养法生长的大肠杆菌细胞的糖摄取(磷酸转移酶系统,PTS)为例来说明该方法的应用。摄取系统的活性取决于葡萄糖的局部浓度以及磷酸烯醇丙酮酸和丙酮酸的细胞内浓度之比,这又取决于单个细胞的历史。仿真结果表明,在不同的操作规模下,细胞活力存在明显差异。 (c)2006年由Elsevier Ltd.发布。

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