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在热诱导补料分批培养中,对重组 HuGM-CSF 生产的缩小模型中的葡萄糖和氧气梯度进行全面研究。

A comprehensive study of glucose and oxygen gradients in a scaled-down model of recombinant HuGM-CSF production in thermoinduced fed-batch cultures.

机构信息

Departamento de Biología Molecular y Biotecnología, Instituto de Investigaciones Biomédicas, Universidad Nacional Autónoma de México, Cd. Universitaria, Coyoacán, Ciudad de México, México.

Posgrado en Ciencias Biomédicas, Universidad Nacional Autónoma de México, México. Unidad de Posgrado, CDMX, México.

出版信息

Prep Biochem Biotechnol. 2024 Nov;54(10):1263-1274. doi: 10.1080/10826068.2024.2347403. Epub 2024 May 3.

DOI:10.1080/10826068.2024.2347403
PMID:38701182
Abstract

The effect of gradients of elevated glucose and low dissolved oxygen in the addition zone of fed-batch thermoinduced recombinant high cell density cultures can be evaluated through two-compartment scale-down models. Here, glucose was fed in the inlet of a plug flow bioreactor (PFB) connected to a stirred tank bioreactor (STB). cells diminished growth from 48.2 ± 2.2 g/L in the stage of RP production if compared to control (STB) with STB-PFB experiments, when residence time inside the PFB was 25 s (34.1 ± 3.5 g/L) and 40 s (25.6 ± 5.1 g/L), respectively. The recombinant granulocyte-macrophage colony-stimulating factor (rHuGM-CSF) production decreased from 34 ± 7% of RP in inclusion bodies (IB) in control cultures to 21 ± 8%, and 7 ± 4% during the thermoinduction production phase when increasing residence time inside the PFB to 25 s and 40 s, respectively. This, along with the accumulation of acetic and formic acid (up to 4 g/L), indicates metabolic redirection of central carbon routes through metabolic flow and mixed acid fermentation. Special care must be taken when producing a recombinant protein in heat-induced , because the yield and productivity of the protein decreases as the size of the bioreactors increases, especially if they are carried at high cell density.

摘要

在补料分批热诱导重组高密度培养物的添加区中,升高的葡萄糖和低溶解氧梯度的影响可以通过两室比例缩小模型来评估。在这里,葡萄糖在与搅拌釜生物反应器(STB)相连的推流式生物反应器(PFB)的入口处进料。如果与 STB-PFB 实验相比,在 PFB 内的停留时间分别为 25 s(34.1±3.5 g/L)和 40 s(25.6±5.1 g/L)时,细胞的生长从 RP 生产的 48.2±2.2 g/L 减少。重组粒细胞-巨噬细胞集落刺激因子(rHuGM-CSF)的产量从对照培养物中包含体(IB)中 RP 的 34±7%下降到 21±8%,和 7±4%,当在 PFB 内的停留时间分别增加到 25 s 和 40 s 时,在热诱导生产阶段。这与乙酸和甲酸(高达 4 g/L)的积累一起表明,通过代谢流和混合酸发酵,中心碳途径的代谢重新定向。在热诱导的情况下生产重组蛋白时必须特别小心,因为随着生物反应器尺寸的增加,特别是在高细胞密度下进行时,蛋白质的产率和生产力会降低。

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