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补料分批和批次复性系统中影响蛋白质复性产率的因素。

Factors affecting protein refolding yields in a fed-batch and batch-refolding system.

作者信息

Mannall Gareth J, Titchener-Hooker Nigel J, Dalby Paul A

机构信息

Department of Biochemical, Advanced Center for Biochemical Engineering, Engineering, University College London, Torrington Place, London, WC1E 7JE, United Kingdom.

出版信息

Biotechnol Bioeng. 2007 Aug 15;97(6):1523-34. doi: 10.1002/bit.21377.

Abstract

The refolding of recombinant protein from inclusion bodies expressed in Escherichia coli can present a process bottleneck. Yields at industrially relevant concentrations are restricted by aggregation of protein upon dilution of the denatured form. This article studies the effect of five factors upon the dilution refolding of protein in a twin impeller fed-batch system using refold buffer containing only the oxidized form of the redox reagent. Such a buffer is easier to prepare and more stable than a buffer containing both reduced and oxidized forms. The five factors chosen were: bulk impeller Reynolds number, mini-impeller Reynolds number, injection rate of denatured protein, redox ratio, and guanidine hydrochloride (GdHCl) concentration. A 2(5) factorial experiment was conducted at an industrially relevant protein concentration using lysozyme as the test system. The study identified that in the system used, the guanidine hydrochloride concentration, redox ratio, and injection rate were the most important factors in determining refolding yields. Two interactions were found to be important: redox ratio/guanidine hydrochloride concentration and guanidine hydrochloride concentration/injection rate. Conditions were also found at which high refolding yields could be achieved even with rapid injection and poor mixing efficiency. Therefore, a comparative assessment was carried out with minimal mixing in a simple batch-refolding mode of operation, which revealed different behavior to that of fed-batch. A graphical (windows of operation) analysis of the batch data suggested that optimal yields and productivity are obtained at high guanidine hydrochloride concentrations (1.2 M) and redox ratios of unity or greater.

摘要

从大肠杆菌中表达的包涵体中重折叠重组蛋白可能会成为工艺瓶颈。在工业相关浓度下,产量受到变性形式稀释时蛋白质聚集的限制。本文研究了五个因素对使用仅含氧化形式氧化还原试剂的复性缓冲液在双叶轮补料分批系统中蛋白质稀释复性的影响。这样的缓冲液比同时含有还原型和氧化型的缓冲液更容易制备且更稳定。选择的五个因素是:主叶轮雷诺数、微型叶轮雷诺数、变性蛋白的注入速率、氧化还原比和盐酸胍(GdHCl)浓度。以溶菌酶为测试系统,在工业相关蛋白质浓度下进行了2(5)析因实验。研究发现,在所使用的系统中,盐酸胍浓度、氧化还原比和注入速率是决定复性产量的最重要因素。发现两个相互作用很重要:氧化还原比/盐酸胍浓度和盐酸胍浓度/注入速率。还发现了即使在快速注入和混合效率较差的情况下也能实现高复性产量的条件。因此,在简单的分批复性操作模式下以最小混合进行了比较评估,结果显示其行为与补料分批不同。对分批数据的图形(操作窗口)分析表明,在高盐酸胍浓度(1.2 M)和氧化还原比为1或更高时可获得最佳产量和生产率。

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