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基于工程化葡萄球菌蛋白A的配体在大肠杆菌中的高水平补料分批发酵表达:纯化与表征

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

作者信息

Kangwa Martin, Yelemane Vikas, Polat Ayse Nur, Gorrepati Kanaka Durga Devi, Grasselli Mariano, Fernández-Lahore Marcelo

机构信息

Downstream Bioprocessing Laboratory, Department of Life Sciences and Chemistry, Jacobs University, Campus Ring 1, 28759, Bremen, Germany.

Laboratorio de Materiales Biotecnológicos (LaMaBio), Universidad Nacional de Quilmes-IMBICE (CONICET), Roque Sáenz Peña 352, B1876BXD, Bernal, Argentina.

出版信息

AMB Express. 2015 Dec;5(1):70. doi: 10.1186/s13568-015-0155-y. Epub 2015 Nov 10.

Abstract

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.

摘要

用于高水平重组蛋白生产的主要平台基于基因改造的微生物,如大肠杆菌(E. coli),这是因为其分裂时间短、能够利用廉价底物,此外,其遗传学相对简单、特征明确且易于操作。在此,我们通过分析不同的培养基样本,研究了寻找高细胞密度发酵最佳培养基的可能性,重点是改进发酵技术和重组蛋白生产。在摇瓶中对大肠杆菌BL21 DE3:pAV01进行的初始发酵表明,与矿物培养基M9、改良基本培养基(MMM)和里森堡矿物培养基(RM)(分别为7、8和7 g/L)相比,使用复合培养基(如Luria-Bertani(LB)和 terrific培养基肉汤(TB))时可实现高细胞密度(分别为10和14 g/L湿重)。然而,在分批补料发酵过程中,当在培养25小时后使用MMM时,在一台30 L TV Techfors-S Infors HT发酵罐中,通过计算机控制的营养供应(以葡萄糖作为碳源)输送系统,有可能产生光密度(OD600)为139,对应于172 g/L湿生物量,这表明几乎是从TB获得的产量的1.5倍。纯化后,每克细胞生物量获得了总共1.65 mg/g的蛋白质,并且纯化后的AviPure显示出对免疫球蛋白的亲和力。通过选择最佳培养基和生长条件,利用许多发酵参数,如培养基、发酵条件、化学浓度、pO2水平、搅拌器速度、pH水平和补料培养基添加量,实现了高细胞密度分批补料发酵。通过提高氧气传递速率和补料,有可能达到比摇瓶和搅拌罐反应器更高的细胞密度。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/cd75/4641145/78aefd5534e8/13568_2015_155_Fig1_HTML.jpg

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