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开发一个高产且可扩展的质粒DNA生产平台。

Development of a highly productive and scalable plasmid DNA production platform.

作者信息

Listner K, Bentley L, Okonkowski J, Kistler C, Wnek R, Caparoni A, Junker B, Robinson D, Salmon P, Chartrain M

机构信息

Bioprocess R&D, Merck Research Laboratories, Rahway, New Jersey 07065, USA.

出版信息

Biotechnol Prog. 2006 Sep-Oct;22(5):1335-45. doi: 10.1021/bp060046h.

Abstract

With the applications of DNA vaccines extending from infectious diseases to cancer, achieving the most efficient, reproducible, robust, scalable, and economical production of clinical grade plasmid DNA is paramount to the medical and commercial success of this novel vaccination paradigm. A first generation production process based on the cultivation of Escherichia coli in a chemically defined medium, employing a fed-batch strategy, delivered reasonable volumetric productivities (500-750 mg/L) and proved to perform very well across a wide range of E. coli constructs upon scale-up at industrial scale. However, the presence of monosodium glutamate (MSG) in the formulation of the cultivation and feed solution was found to be a potential cause of process variability. The development of a second generation process, based on a defined cultivation medium and feed solution excluding MSG, was undertaken. Optimization studies, employing a plasmid coding for the HIV gag protein, resulted in cultivation conditions that supported volumetric plasmid titers in excess of 1.2 g/L, while achieving specific yields ranging from 25 to 32 microg plasmid DNA/mg of dry cell weight. When used for the production of clinical supplies, this novel process demonstrated applicability to two other constructs upon scale-up in 2,000-L bioreactors. This second generation process proved to be scalable, robust, and highly productive.

摘要

随着DNA疫苗的应用从传染病扩展到癌症,实现临床级质粒DNA的最高效、可重复、稳健、可扩展且经济的生产对于这种新型疫苗接种模式的医学和商业成功至关重要。第一代生产工艺基于在化学限定培养基中培养大肠杆菌,采用补料分批策略,可实现合理的体积生产力(500 - 750毫克/升),并在工业规模放大时,在广泛的大肠杆菌构建体中表现良好。然而,在培养和补料溶液配方中发现味精(MSG)的存在是工艺变异性的潜在原因。因此开展了基于不含味精的限定培养基和补料溶液的第二代工艺开发。使用编码HIV gag蛋白的质粒进行优化研究,得到的培养条件可支持体积质粒滴度超过1.2克/升,同时实现25至32微克质粒DNA/毫克干细胞重量的特定产量。当用于临床用品生产时,这种新工艺在2000升生物反应器中放大时,证明适用于另外两种构建体。第二代工艺被证明是可扩展、稳健且高产的。

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