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High-level fed-batch fermentative expression of an engineered Staphylococcal protein A based ligand in E. coli: purification and characterization

机译:基于大肠杆菌的工程葡萄球菌蛋白A配体的高水平补料发酵表达:纯化和鉴定

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摘要

The major platform for high level recombinant protein production is based on genetically modified microorganisms like Escherichia coli (E. coli) due to its short dividing time, ability to use inexpensive substrates and additionally, its genetics is comparatively simple, well characterized and can be manipulated easily. Here, we investigated the possibilities of finding the best media for high cell density fermentation, by analyzing different media samples, focusing on improving fermentation techniques and recombinant protein production. Initial fermentation of E. coli BL21 DE3:pAV01 in baffled flasks showed that high cell density was achieved when using complex media, Luria–Bertani (LB) and Terrific medium broth (TB) (10 and 14 g/L wet weight, respectively), as compared to mineral media M9, modified minimal medium (MMM) and Riesenberg mineral medium (RM) (7, 8 and 7 g/L, respectively). However, in fed-batch fermentation processes when using MMM after 25 h cultivation, it was possible to yield an optical density (OD600) of 139 corresponding to 172 g/L of wet biomass was produced in a 30 L TV Techfors-S Infors HT fermenter, with a computer controlled nutrient supply (glucose as a carbon source) delivery system, indicating nearly 1.5 times that obtained from TB. Upon purification, a total of 1.65 mg/g of protein per gram cell biomass was obtained and the purified AviPure showed affinity for immunoglobulin. High cell density fed batch fermentation was achieved by selecting the best media and growth conditions, by utilizing a number of fermentation parameters like media, fermentation conditions, chemical concentrations, pO2 level, stirrer speed, pH level and feed media addition. It is possible to reach cell densities higher than shake flasks and stirred tank reactors with the improved oxygen transfer rate and feed.Electronic supplementary materialThe online version of this article (doi:10.1186/s13568-015-0155-y) contains supplementary material, which is available to authorized users.
机译:高水平重组蛋白生产的主要平台是基于转基因微生物,例如大肠埃希氏菌(E. coli),这是因为其分离时间短,使用廉价底物的能力,此外,其遗传学相对简单,特征明确并且可以操纵容易。在这里,我们通过分析不同的培养基样品,着重于改进发酵技术和重组蛋白质的生产,研究了寻找用于高细胞密度发酵的最佳培养基的可能性。大肠杆菌BL21 DE3:pAV01在带挡板的烧瓶中的初步发酵表明,使用复杂培养基Luria-Bertani(LB)和Terrific培养基肉汤(TB)(分别为10和14 g / L湿重)可实现高细胞密度,与M9矿物培养基,改良的基本培养基(MMM)和Riesenberg矿物培养基(RM)相比(分别为7、8和7 g / L)。但是,在25小时培养后使用MMM的分批分批发酵过程中,有可能产生139的光密度(OD600),相当于在30 L TV Techfors-S Infors HT中产生了172 g / L的湿生物质发酵罐,具有计算机控制的养分供应(葡萄糖作为碳源)输送系统,是结核病的近1.5倍。纯化后,每克细胞生物质共获得1.65 mg / g蛋白质,纯化的AviPure对免疫球蛋白显示出亲和力。通过选择最佳培养基和生长条件,并利用许多发酵参数(例如培养基,发酵条件,化学浓度,pO2水平,搅拌器速度,pH值和进料培养基添加)来实现高细胞密度补料分批发酵。通过提高氧气传输速率和进料,可以达到比摇瓶和搅拌釜反应器更高的细胞密度。电子补充材料本文的在线版本(doi:10.1186 / s13568-015-0155-y)包含补充材料,其中适用于授权用户。

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