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在大肠杆菌自控补料分批发酵中降低代谢和蛋白质生产速率,减少 N-端甲硫氨酸化,同时提高产量。

Reduction of N-terminal methionylation while increasing titer by lowering metabolic and protein production rates in E. coli auto-induced fed-batch fermentation.

机构信息

Biologics Process Science, Global Manufacturing and Supply, Bristol-Myers Squibb, Syracuse, NY 13057, USA.

出版信息

J Ind Microbiol Biotechnol. 2012 Aug;39(8):1199-208. doi: 10.1007/s10295-012-1127-8. Epub 2012 Apr 20.

Abstract

A standard fed-batch fermentation process using 1 mM isopropyl-β-D: -thiogalactopyranoside (IPTG) induction at 37 °C in complex batch and feed media had been developed for manufacturing of a therapeutic protein (TP) expressed in inclusion bodies (IBs) by E. coli BL21 (DE3) driven by T7 promoter. Six unauthentic TP N-terminal variants were identified, of which methionylated TP (Met-TP) ratio was predominant. We hypothesized that lowering metabolic and protein production rates would reduce the Met-TP ratio while improving TP titer. The standard process was surprisingly auto-induced without added IPTG due to galactose in the complex media. Without changing either the clone or the batch medium, a new process was developed using lower feed rates and auto-induction at 29 °C after glucose depletion while increasing induction duration. In comparison to the standard process, the new process reduced the unauthentic Met-TP ratio from 23.6 to 9.6 %, increased the TP titer by 85 %, and the specific production yield from 210 to 330 mg TP per gram of dry cell weight. Furthermore, the TP recovery yield in the purified IBs was improved by ~20 %. Adding together, ~105 % more TP recovered in the purified IBs from per liter of fermentation broth for the new process than the standard process. The basic principles of lowering metabolic and production rates should be applicable to other recombinant protein production in IBs by fed-batch fermentations.

摘要

已开发出一种使用 1mM异丙基-β-D:-硫代半乳糖吡喃糖苷(IPTG)在 37°C 下进行标准补料分批发酵的方法,适用于在复杂分批和补料培养基中通过 T7 启动子表达的包含体(IBs)中的治疗性蛋白(TP)的生产。鉴定了六个非天然的 TP N 端变体,其中甲硫氨酸化 TP(Met-TP)的比例占主导地位。我们假设降低代谢和蛋白质产率会降低 Met-TP 比例,同时提高 TP 滴度。由于复杂培养基中的半乳糖,标准工艺出人意料地在没有添加 IPTG 的情况下自动诱导。在不改变克隆或分批培养基的情况下,开发了一种新的工艺,使用较低的补料率,在葡萄糖耗尽后在 29°C 下自动诱导,同时延长诱导时间。与标准工艺相比,新工艺将非天然的 Met-TP 比例从 23.6%降低到 9.6%,提高了 85%的 TP 滴度,以及从 210mg TP/克干细胞重量提高到 330mg TP/克干细胞重量的比生产产率。此外,在纯化的 IBs 中,TP 的回收率提高了约 20%。总的来说,新工艺从每升发酵液中回收的纯化 IBs 中的 TP 比标准工艺多约 105%。降低代谢和生产速率的基本原则应适用于其他通过补料分批发酵在 IBs 中生产的重组蛋白。

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