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Industrial control of recombinant E. coli fed-batch culture: new perspectives on traditional controlled variables

机译:重组大肠杆菌补料分批培养的工业控制:传统控制变量的新观点

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摘要

Three industrially relevant fed-batch algorithms were applied to the production of recombinant proteins in Escherichia coli BL21 DE3. Starvation dissolved-oxygen (DO)-transient control sustained growth rates greater than those in pH-stat (0.16 h~(-1) versus 0.11-0.13 h~(-1)) while feed-up DO-transient control better tracked the measured threshold for acetate production (μ~ 0.2 h~(-1)). All controllers supported growth without acetate production, resulting in end concentrations of recombinant protein up to 20 times greater than in batch culture. Both DO-transient control systems were judged superior to pH-stat for their ability to detect and track the acetate threshold. Results also showed that although high cell density at the stationary phase is desirable, this parameter may be dictated by the choice of media and reactor design as opposed to controller type. Controller selection, however, has a great impact on the capacity to track the acetate threshold and therefore to enhance productivity without concomitant acetate production.
机译:将三种与工业相关的补料分批算法应用于大肠杆菌BL21 DE3中重组蛋白的生产。饥饿溶解氧(DO)瞬态控制的持续生长速度高于pH值(0.16 h〜(-1)对0.11-0.13 h〜(-1)),而补料DO瞬变控制更好地跟踪了测得的乙酸盐生产阈值(μ〜0.2 h〜(-1))。所有控制器均支持无乙酸盐生长的生长,从而使重组蛋白的终浓度比分批培养高出20倍。两种DO瞬态控制系统均具有检测和跟踪乙酸盐阈值的能力,因此被认为优于pH-stat。结果还表明,尽管在固定相中需要较高的细胞密度,但该参数可能由介质的选择和反应器设计(与控制器类型相反)决定。但是,选择控制器对跟踪乙酸盐阈值的能力有很大影响,因此在不伴随乙酸盐生产的情况下提高了生产率。

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