Austrian Centre of Industrial Biotechnology (ACIB), Muthgasse 11, 1190 Vienna, Austria.
Austrian Centre of Industrial Biotechnology (ACIB), Muthgasse 11, 1190 Vienna, Austria; Department of Biotechnology, University of Natural Resources and Life Sciences, Vienna, Muthgasse 18, 1190 Vienna, Austria.
J Chromatogr A. 2014 Apr 11;1337:48-56. doi: 10.1016/j.chroma.2014.02.016. Epub 2014 Feb 22.
Continuous processing of recombinant proteins was accomplished by combining continuous matrix-assisted refolding and purification by tandem simulated moving bed (SMB) size-exclusion chromatography (SEC). Recombinant proteins, N(pro) fusion proteins from inclusion bodies were dissolved with NaOH and refolded in the SMB system with a closed-loop set-up with refolding buffer as the desorbent buffer and buffer recycling of the refolding buffer of the raffinate by tangential flow filtration. For further purification of the refolded proteins, a second SMB operation also based on SEC was added. The whole system could be operated isocratically with refolding buffer as the desorbent buffer, and buffer recycling could also be applied in the purification step. Thus, a significant reduction in buffer consumption was achieved. The system was evaluated with two proteins, the N(pro) fusion pep6His and N(pro) fusion MCP-1. Refolding solution, which contained residual N(pro) fusion peptide, the cleaved autoprotease N(pro), and the cleaved target peptide was used as feed solution. Full separation of the cleaved target peptide from residual proteins was achieved at a purity and recovery in the raffinate and extract, respectively, of approximately 100%. In addition, more than 99% of the refolding buffer of the raffinate was recycled. A comparison of throughput, productivity, and buffer consumption of the integrated continuous process with two batch processes demonstrated that up to 60-fold higher throughput, up to 180-fold higher productivity, and at least 28-fold lower buffer consumption can be obtained by the integrated continuous process, which compensates for the higher complexity.
通过连续基质辅助折叠和串联模拟移动床 (SMB) 尺寸排阻色谱 (SEC) 连续纯化来实现重组蛋白的连续处理。将包含体中的 N(pro) 融合蛋白用 NaOH 溶解,并在 SMB 系统中进行折叠,该系统采用闭环设置,以折叠缓冲液作为解吸缓冲液,并通过切向流过滤回收洗脱液中的折叠缓冲液。为了进一步纯化折叠后的蛋白质,还添加了第二个基于 SEC 的 SMB 操作。整个系统可以用折叠缓冲液作为解吸缓冲液等度操作,也可以在纯化步骤中回收缓冲液。因此,显著减少了缓冲液的消耗。该系统用两种蛋白质,N(pro) 融合肽 pep6His 和 N(pro) 融合 MCP-1 进行了评估。含有残留 N(pro) 融合肽、切割自蛋白酶 N(pro) 和切割靶肽的折叠溶液被用作进料溶液。在纯度和回收率方面,切割靶肽从残留蛋白质中得到了完全分离,在洗脱液和提取液中的纯度和回收率分别约为 100%。此外,超过 99%的洗脱液中的折叠缓冲液被回收。连续集成工艺与两个批处理工艺的通量、生产率和缓冲液消耗的比较表明,连续集成工艺的通量可提高 60 倍以上,生产率可提高 180 倍以上,缓冲液消耗可降低至少 28 倍,从而弥补了更高的复杂性。