洗脱
色谱法
超滤(肾)
膜
化学
蛋白质纯化
体积热力学
生物化学
量子力学
物理
作者
Gaoya Yuan,Meng Qu,Xu Dong Zhang,Yifeng Li
出处
期刊:Journal of biological methods
[Journal of Biological Methods]
日期:2025-04-10
卷期号:: e99010050-e99010050
标识
DOI:10.14440/jbm.2025.0109
摘要
Background: Protein A chromatography is widely used for antibody purification. With conventional packed-bed columns, mass transfer within resin beads is diffusion-limited, entailing long residence time to achieve high binding capacities. Recently, several vendors have introduced Protein A membranes as alternatives to traditional Protein A resins/columns. These membranes feature open pore structures that facilitate the convective transport of protein molecules, enabling high binding capacities within significantly shorter residence time. The use of Protein A membranes can improve throughput, eliminate the need for column packing, and reduce cost. These advantages notwithstanding, Protein A membranes present certain drawbacks. A major limitation is their high dead volume-to-stationary phase ratio, which leads to larger elution volumes compared to their conventional counterparts. This results in significant eluate dilution and increased buffer consumption. Objective: In the current study, we aimed to demonstrate that ultrafiltration (UF), when used in combination with Protein A membrane chromatography, can address these limitations by allowing eluate concentration and buffer reuse. Methods: A laboratory model of UF integrated Protein A membrane was set up to test the feasibility and effectiveness of the proposed strategy. Results: Integrated UF effectively concentrated Protein A membrane eluate to a concentration comparable to that of Protein A column eluate. In addition, reuse of pH-adjusted UF filtrate as elution buffer reduces buffer consumption by 50%. Conclusion: UF integration is an effective solution for addressing the problem of increased elution volume and buffer consumption associated with Protein A membrane.
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