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在大肠杆菌中表达的人白细胞介素-8的生产:从用于体外测试的实验室规模,到用于动物研究的技术规模,再到符合GMP标准生产的工艺规模。

Production of human interleukin-8 expressed in Escherichia coli: from a laboratory scale for in vitro tests via a technical scale for animal studies to a process scale for a GMP-compatible production.

作者信息

Koltermann A, Boidol W, Daum J, Scholz P, Donner P

机构信息

Max-Planck-Institute of Biochemical Chemistry, Department of Biochemical Kinetics, Göttingen, Germany.

出版信息

J Biotechnol. 1997 Apr 4;54(1):29-42. doi: 10.1016/s0168-1656(97)01689-1.

DOI:10.1016/s0168-1656(97)01689-1
PMID:9188199
Abstract

An Escherichia coli K 12 strain has been constructed for efficient expression of recombinant biologically active human IL-8 (Interleukin-8). The development of a fermentation and purification process from the laboratory scale (cells from 15 l fermentation broth) to a production scale (cells from 200 l fermentation broth) is described. Material obtained from the laboratory scale was used for initial in vitro studies and for the development of a biological assay. An upscale purification process starting from 80 l fermentation broth resulted in larger amounts of IL-8 needed for preclinical studies. This process includes a fully automated control of the initial affinity chromatography step. Finally, a production process which differed markedly from the small-scale processes was tailor-made for GMP conformity and economic considerations. It consists of a cell disruption step followed by two crossflow diafiltrations with different molecular weight cut offs and filtration rates, one cation exchange chromatography and a final dialysis step. In order to enhance the overall yield of biologically active IL-8, conditions for a resolubilisation of insoluble IL-8 present in the remaining pellet after cell disruption were worked out.

摘要

构建了一种大肠杆菌K12菌株,用于高效表达重组生物活性人白细胞介素8(IL-8)。本文描述了从实验室规模(15升发酵液中的细胞)到生产规模(200升发酵液中的细胞)的发酵和纯化工艺的开发过程。从实验室规模获得的材料用于初步体外研究和生物测定的开发。从80升发酵液开始的放大纯化工艺产生了临床前研究所需的大量IL-8。该工艺包括对初始亲和色谱步骤的全自动控制。最后,针对GMP合规性和经济考虑因素,量身定制了一种与小规模工艺明显不同的生产工艺。它包括细胞破碎步骤,随后是两个具有不同截留分子量和过滤速率的错流渗滤步骤、一次阳离子交换色谱和一个最终透析步骤。为了提高生物活性IL-8的总收率,研究了细胞破碎后剩余沉淀中存在的不溶性IL-8的复溶条件。

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