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大肠杆菌的细胞工程可实现高细胞密度积累,而无需补料分批过程控制。

Cell engineering of Escherichia coli allows high cell density accumulation without fed-batch process control.

作者信息

Bäcklund Emma, Markland Katrin, Larsson Gen

机构信息

School of Biotechnology, AlbaNova University Center, KTH, 106 91 Stockholm, Sweden.

出版信息

Bioprocess Biosyst Eng. 2008 Jan;31(1):11-20. doi: 10.1007/s00449-007-0144-x. Epub 2007 Sep 27.

Abstract

A set of mutations in the phosphoenolpyruvate:carbohydrate phosphotransferase system (PTS) was used to create Escherichia coli strains with a reduced uptake rate of glucose. This allows a growth restriction, which is controlled on cellular rather than reactor level, which is typical of the fed-batch cultivation concept. Batch growth of the engineered strains resulted in cell accumulation profiles corresponding to a growth rate of 0.78, 0.38 and 0.25 h(-1), respectively. The performance of the mutants in batch cultivation was compared to fed-batch cultivation of the wild type cell using restricted glucose feed to arrive at the corresponding growth profiles. Results show that the acetate production, oxygen consumption and product formation were similar, when a recombinant product was induced from the lacUV5 promoter. Ten times more cells could be produced in batch cultivation using the mutants without the growth detrimental production of acetic acid. This allows high cell density production without the establishment of elaborate fed-batch control equipment. The technique is suggested as a versatile tool in high throughput multiparallel protein production but also for increasing the number of experiments performed during process development while keeping conditions similar to the large-scale fed-batch performance.

摘要

利用磷酸烯醇式丙酮酸

碳水化合物磷酸转移酶系统(PTS)中的一组突变来创建葡萄糖摄取速率降低的大肠杆菌菌株。这使得生长受到限制,这种限制是在细胞水平而非反应器水平上进行控制的,这是分批补料培养概念的典型特征。工程菌株的分批培养导致细胞积累曲线分别对应于0.78、0.38和0.25 h⁻¹的生长速率。将突变体在分批培养中的性能与野生型细胞在使用受限葡萄糖进料的分批补料培养中的性能进行比较,以得出相应的生长曲线。结果表明,当从lacUV5启动子诱导重组产物时,乙酸盐产生、氧气消耗和产物形成是相似的。使用突变体进行分批培养时,可以产生多十倍的细胞,且不会产生对生长有害的乙酸。这使得在不建立复杂的分批补料控制设备的情况下实现高密度生产成为可能。该技术被认为是高通量多平行蛋白质生产中的一种通用工具,同时也可用于在工艺开发过程中增加实验次数,同时保持与大规模分批补料性能相似的条件。

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