Hoffman B J, Broadwater J A, Johnson P, Harper J, Fox B G, Kenealy W R
Institute for Enzyme Research, Graduate School, University of Wisconsin, Madison 53705, USA.
Protein Expr Purif. 1995 Oct;6(5):646-54. doi: 10.1006/prep.1995.1085.
A method for producing recombinant proteins in pilot scale fermentation equipment using a glucose fed-batch initial growth, followed by a midlog phase feeding of a glucose and lactose mixture is described. Using the host strain Escherichia coli BL21(DE3), the diiron protein stearoyl-acyl carrier protein delta 9 desaturase has been overexpressed at a biomass level of up to 12 g x liter-1 dry cell weight, representing a 12-fold increase in volumetric productivity relative to that obtained from batch fermentations. Under these conditions, a maximum of 36% of the total cellular protein accumulates as the desaturase polypeptide. A correlation between the slowed growth rate of the fed-batch culture, a continued, albeit slower, exponential growth under inducing conditions, and a favorable partitioning between formation of the soluble holoprotein and inclusion bodies is reported. This correlation suggests that fed-batch techniques can be used to beneficially influence rate-limiting processes in the maturation of overexpressed proteins, such as metal uptake and incorporation proposed here. By using cells produced from the fed-batch method, the iron-containing, soluble desaturase can be purified in a yield of up to 66 mg x g-1 dry cell weight (approximately 500 mg x liter-1 culture), representing a three to fivefold increase in the yield relative to that obtained from batch fermentations. In addition, these methods are suitable for the production of the Anabena 7120 vegetative [2Fe 2S] ferredoxin in E. coli BL21(DE3) pLysS, a host strain used for the overexpression of toxic proteins.
描述了一种在中试规模发酵设备中生产重组蛋白的方法,该方法采用葡萄糖补料分批培养进行初始生长,随后在对数中期阶段补料葡萄糖和乳糖混合物。使用宿主菌株大肠杆菌BL21(DE3),二铁蛋白硬脂酰-酰基载体蛋白Δ9去饱和酶已在高达12 g·L⁻¹干细胞重量的生物量水平上过量表达,相对于分批发酵获得的产量,体积生产力提高了12倍。在这些条件下,最多36%的总细胞蛋白以去饱和酶多肽的形式积累。报道了补料分批培养生长速率减慢、诱导条件下持续(尽管较慢)的指数生长以及可溶性全蛋白和包涵体形成之间有利分配的相关性。这种相关性表明,补料分批技术可用于有益地影响过表达蛋白成熟过程中的限速过程,例如此处提出的金属摄取和掺入。通过使用补料分批法生产的细胞,含铁的可溶性去饱和酶可以以高达66 mg·g⁻¹干细胞重量(约500 mg·L⁻¹培养物)的产量纯化,相对于分批发酵获得的产量提高了三到五倍。此外,这些方法适用于在大肠杆菌BL21(DE3)pLysS中生产鱼腥藻7120营养型[2Fe 2S]铁氧化还原蛋白,该宿主菌株用于有毒蛋白的过表达。