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新型多模态阳离子交换膜用于从毕赤酵母上清液中纯化单链可变片段。

Novel multimodal cation-exchange membrane for the purification of a single-chain variable fragment from Pichia pastoris supernatant.

机构信息

Department of Chemical and Biochemical Engineering, Technical University of Denmark, 2800 Kgs. Lyngby, Denmark.

Department of Chemical and Biomolecular Engineering, North Carolina State University, Raleigh, NC 27695-7905, USA.

出版信息

J Chromatogr A. 2024 Mar 15;1718:464682. doi: 10.1016/j.chroma.2024.464682. Epub 2024 Feb 1.

Abstract

A novel salt-tolerant cation-exchange membrane, prepared with a multimodal ligand, 2-mercaptopyridine-3-carboxylic acid (MMC-MPCA), was examined for its purification properties in a bind-and-elute mode from the high conductivity supernatant of a Pichia pastoris fermentation producing and secreting a single-chain variable fragment (scFv). If successful, this approach would eliminate the need for a buffer exchange prior to product capture by ion-exchange. Two fed-batch fermentations of Pichia pastoris resulted in fermentation supernatants reaching an scFv titer of 395.0 mg/L and 555.7 mg/L, both with a purity of approximately 83 %. The MMC-MPCA membrane performance was characterized in terms of pH, residence time (RT), scFv load, and scFv concentration to identify the resulting dynamic binding capacity (DBC), yield, and purity achieved under optimal conditions. The MMC-MPCA membrane exhibited the highest DBC of 39.06 mg/mL at pH 5.5, with a residence time of 1 min, while reducing the pH below 5.0 resulted in a significant decrease of the DBC to around 2.5 mg/mL. With almost no diffusional limitations, reducing the RT from 2 to 0.2 min did not negatively impact the DBC of the MMC-MPCA membrane, resulting in a significant improvement in productivity of up to 180 mg/mL/min at 0.2 min RT. Membrane fouling was observed when reusing the membranes at 0.2 and 0.5 min RT, likely due to the enhanced adsorption of impurities on the membrane. Changing the amount of scFv loaded onto the membrane column did not show any changes in yield, instead a 10-20 % loss of scFv was observed, which suggested that some of the produced scFv were fragmented or had aggregated. When performing the purification under the optimized conditions, the resulting purity of the product improved from 83 % to approximately 92-95 %.

摘要

一种新型耐盐阳离子交换膜,采用多模态配体 2-巯基吡啶-3-羧酸(MMC-MPCA)制备,用于从毕赤酵母发酵生产和分泌单链可变片段(scFv)的高电导率上清液中以绑定-洗脱模式进行纯化。如果成功,这种方法将消除在离子交换产品捕获之前进行缓冲液交换的需要。毕赤酵母的两次分批发酵使发酵上清液达到 395.0 mg/L 和 555.7 mg/L 的 scFv 滴度,纯度均约为 83%。根据 pH 值、停留时间(RT)、scFv 负载量和 scFv 浓度来表征 MMC-MPCA 膜的性能,以确定在最佳条件下获得的动态结合容量(DBC)、产率和纯度。MMC-MPCA 膜在 pH 值为 5.5 时表现出最高的 DBC 为 39.06 mg/mL,停留时间为 1 分钟,而将 pH 值降低到 5.0 以下会导致 DBC 显著下降到约 2.5 mg/mL。由于几乎没有扩散限制,将 RT 从 2 分钟减少到 0.2 分钟不会对 MMC-MPCA 膜的 DBC 产生负面影响,从而使生产率提高了高达 180 mg/mL/min,RT 为 0.2 分钟。当在 0.2 和 0.5 分钟 RT 下重复使用膜时观察到膜污染,这可能是由于杂质在膜上的吸附增强所致。改变加载到膜柱上的 scFv 量不会对产率产生任何影响,而是观察到 scFv 的 10-20%损失,这表明部分产生的 scFv 已被片段化或聚集。在优化条件下进行纯化时,产物的纯度从 83%提高到约 92-95%。

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