Group of Complex Systems and Statistical Physics, Department of Theoretical Physics, Physics Faculty, University of Havana, Havana, Cuba.
Systems Biology Department, Center of Molecular Immunology, Havana, Cuba.
Biotechnol Bioeng. 2021 May;118(5):1884-1897. doi: 10.1002/bit.27704. Epub 2021 Mar 1.
The cell culture is the central piece of a biotechnological industrial process. It includes upstream (e.g. media preparation, fixed costs, etc.) and downstream steps (e.g. product purification, waste disposal, etc.). In the continuous mode of cell culture, a constant flow of fresh media replaces culture fluid until the system reaches a steady state. This steady state is the standard operation mode which, under very general conditions, is a function of the ratio between the cell density and the dilution rate and depends on the media supplied to the culture. To optimize the production process it is widely accepted that the concentration of the metabolites in this media should be carefully tuned. A poor media may not provide enough nutrients to the culture, while a media too rich in nutrients may be a waste of resources because, either the cells do not use all of the available nutrients, or worse, they over-consume them producing toxic byproducts. In this study, we show how an in-silico study of a genome scale metabolic network coupled to the dynamics of a chemostat could guide the strategy to optimize the media to be used in a continuous process. Given a known media we model the concentrations of the cells in a chemostat as a function of the dilution rate. Then, we cast the problem of optimizing the production process within a linear programming framework in which the goal is to minimize the cost of the media keeping fixed the cell concentration for a given dilution rate in the chemostat. We evaluate our results in two metabolic models: first a simplified model of mammalian cell metabolism, and then in a realistic genome-scale metabolic network of mammalian cells, the Chinese hamster ovary cell line. We explore the latter in more detail given specific meaning to the predictions of the concentrations of several metabolites.
细胞培养是生物技术工业过程的核心部分。它包括上游(例如培养基准备、固定成本等)和下游步骤(例如产物纯化、废物处理等)。在细胞培养的连续模式中,新鲜培养基的恒定流量取代培养物,直到系统达到稳定状态。这个稳定状态是标准操作模式,在非常一般的条件下,它是细胞密度与稀释率之比的函数,并取决于提供给培养物的培养基。为了优化生产过程,人们普遍认为应该仔细调整这种培养基中代谢物的浓度。较差的培养基可能无法为培养物提供足够的营养,而营养过于丰富的培养基可能是资源的浪费,因为细胞要么无法利用所有可用的营养物质,要么更糟糕的是,它们过度消耗它们产生有毒的副产物。在这项研究中,我们展示了如何通过将基因组规模代谢网络与恒化器动力学相结合的计算机模拟研究,指导优化连续过程中使用的培养基的策略。给定已知的培养基,我们将恒化器中细胞的浓度建模为稀释率的函数。然后,我们将优化生产过程的问题纳入线性规划框架中,目标是在保持恒化器中给定稀释率的细胞浓度固定的情况下,最小化培养基的成本。我们在两个代谢模型中评估我们的结果:首先是哺乳动物细胞代谢的简化模型,然后是哺乳动物细胞的真实基因组规模代谢网络,中国仓鼠卵巢细胞系。我们详细探讨了后者,赋予了几种代谢物浓度的预测特定的含义。