Austrian Centre of Industrial Biotechnology (ACIB), Muthgasse 11, 1190 Vienna, Austria.
J Chromatogr A. 2013 Dec 6;1319:107-17. doi: 10.1016/j.chroma.2013.10.039. Epub 2013 Oct 17.
An integrated process which combines continuous inclusion body dissolution with NaOH and continuous matrix-assisted refolding based on closed-loop simulated moving bed size exclusion chromatography was designed and experimentally evaluated at laboratory scale. Inclusion bodies from N(pro) fusion pep6His and N(pro) fusion MCP1 from high cell density fermentation were continuously dissolved with NaOH, filtered and mixed with concentrated refolding buffer prior to refolding by size exclusion chromatography (SEC). This process enabled an isocratic operation of the simulated moving bed (SMB) system with a closed-loop set-up with refolding buffer as the desorbent buffer and buffer recycling by concentrating the raffinate using tangential flow filtration. With this continuous refolding process, we increased the refolding and cleavage yield of both model proteins by 10% compared to batch dilution refolding. Furthermore, more than 99% of the refolding buffer of the raffinate could be recycled which reduced the buffer consumption significantly. Based on the actual refolding data, we compared throughput, productivity, and buffer consumption between two batch dilution refolding processes - one using urea for IB dissolution, the other one using NaOH for IB dissolution - and our continuous refolding process. The higher complexity of the continuous refolding process was rewarded with higher throughput and productivity as well as significantly lower buffer consumption compared to the batch dilution refolding processes.
设计并在实验室规模上实验评估了一种集成工艺,该工艺将连续包涵体溶解与 NaOH 结合,并基于闭环模拟移动床分子筛层析连续基质辅助折叠。来自高密度发酵的 N(pro)融合 pep6His 和 N(pro)融合 MCP1 的包涵体用 NaOH 连续溶解,过滤后与浓缩的折叠缓冲液混合,然后通过分子筛层析(SEC)进行折叠。该工艺使模拟移动床(SMB)系统能够以等度操作,闭环设置中以折叠缓冲液作为洗脱缓冲液,并通过切向流过滤浓缩淋洗液来实现缓冲液回收。采用这种连续折叠工艺,与分批稀释折叠相比,两种模型蛋白的折叠和切割收率均提高了 10%。此外,淋洗液中超过 99%的折叠缓冲液可以回收,从而显著减少了缓冲液的消耗。基于实际折叠数据,我们比较了两种分批稀释折叠工艺(一种使用尿素溶解 IB,另一种使用 NaOH 溶解 IB)和我们的连续折叠工艺之间的通量、生产率和缓冲液消耗。与分批稀释折叠工艺相比,连续折叠工艺的复杂性更高,因此通量和生产率更高,缓冲液消耗显著降低。