糖基化
核苷酸糖
糖蛋白
单克隆抗体
功能(生物学)
生物反应器
吞吐量
中国仓鼠卵巢细胞
合理设计
生物系统
细胞培养
化学
细胞外
细胞内
计算生物学
计算机科学
生物化学
生物
细胞生物学
核苷酸
抗体
遗传学
受体
基因
有机化学
电信
无线
作者
Thomas K. Villiger,Ernesto Scibona,Matthieu Stettler,Hervé Broly,Massimo Morbidelli,Miroslav Šoóš
摘要
N‐linked glycosylation is known to be a crucial factor for the therapeutic efficacy and safety of monoclonal antibodies (mAbs) and many other glycoproteins. The nontemplate process of glycosylation is influenced by external factors which have to be tightly controlled during the manufacturing process. In order to describe and predict mAb N‐linked glycosylation patterns in a CHO‐S cell fed‐batch process, an existing dynamic mathematical model has been refined and coupled to an unstructured metabolic model. High‐throughput cell culture experiments carried out in miniaturized bioreactors in combination with intracellular measurements of nucleotide sugars were used to tune the parameter configuration of the coupled models as a function of extracellular pH, manganese and galactose addition. The proposed modeling framework is able to predict the time evolution of N‐linked glycosylation patterns during a fed‐batch process as a function of time as well as the manipulated variables. A constant and varying mAb N‐linked glycosylation pattern throughout the culture were chosen to demonstrate the predictive capability of the modeling framework, which is able to quantify the interconnected influence of media components and cell culture conditions. Such a model‐based evaluation of feeding regimes using high‐throughput tools and mathematical models gives rise to a more rational way to control and design cell culture processes with defined glycosylation patterns. © 2016 American Institute of Chemical Engineers Biotechnol. Prog ., 32:1135–1148, 2016
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