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使用无蛋白A的三个色谱步骤对抗体纯化工艺进行析因筛选。

Factorial screening of antibody purification processes using three chromatography steps without protein A.

作者信息

Follman Deborah K, Fahrner Robert L

机构信息

Department of Recovery Sciences, Genentech Inc., 1 DNA Way, South San Francisco, CA 94080, USA.

出版信息

J Chromatogr A. 2004 Jan 23;1024(1-2):79-85. doi: 10.1016/j.chroma.2003.10.060.

Abstract

Protein A affinity chromatography is often employed as a capture step to meet the purity, yield, and throughput requirements for pharmaceutical antibody purification. However, a trade-off exists between step performance and price. Protein A resin removes 99.9% of feed stream impurities; however, its price is significantly greater than those of non-affinity media. With many therapeutic indications for antibodies requiring high doses and/or chronic administration, the consideration of process economics is critical. We have systematically evaluated the purification performance of cation-exchange, anion-exchange, hydroxyapatite, hydrophobic interaction, hydrophobic charge induction, and small-molecule ligand resins in each step of a three-step chromatographic purification process for a CHO-derived monoclonal antibody. Host cell proteins were removed to less-than-detectable for three processes (cation-exchange-anion-exchange-hydrophobic interaction chromatography, cation-exchange-anion-exchange-mixed cation-exchange chromatography, and cation-exchange-mixed cation-exchange-anion-exchange chromatography). The order of the process steps affected purification performance significantly.

摘要

蛋白A亲和色谱法常被用作捕获步骤,以满足制药抗体纯化对纯度、产量和通量的要求。然而,步骤性能和价格之间存在权衡。蛋白A树脂能去除99.9%的进料流杂质;然而,其价格明显高于非亲和介质。由于许多抗体治疗适应症需要高剂量和/或长期给药,因此考虑工艺经济性至关重要。我们系统地评估了阳离子交换、阴离子交换、羟基磷灰石、疏水相互作用、疏水电荷诱导和小分子配体树脂在CHO衍生单克隆抗体三步色谱纯化过程各步骤中的纯化性能。在三个过程(阳离子交换-阴离子交换-疏水相互作用色谱法、阳离子交换-阴离子交换-混合阳离子交换色谱法和阳离子交换-混合阳离子交换-阴离子交换色谱法)中,宿主细胞蛋白被去除至检测不到的水平。工艺步骤的顺序对纯化性能有显著影响。

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