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大规模补料分批培养中提高二氧化碳去除率的策略。

Strategies for improved dCO2 removal in large-scale fed-batch cultures.

作者信息

Mostafa Sigma S, Gu Xuejun

机构信息

Lilly Research Laboratories, Indianapolis, Indiana 46285, USA.

出版信息

Biotechnol Prog. 2003 Jan-Feb;19(1):45-51. doi: 10.1021/bp0256263.

Abstract

Carbon dioxide buildup in large-scale reactors can be detrimental to cell growth and productivity. In case of protein X, a therapeutic glycoprotein, when cultures were scaled up from bench scale to the pilot plant, there was a 40% loss of specific productivity. The dissolved CO(2) (dCO(2)) level was 179 +/- 9 mmHg at the pilot plant scale and 68 +/- 13 mmHg at bench scale. The authors proposed a comprehensive approach to maintain dCO(2) levels between 40 and 120 mmHg throughout the 14-day fed-batch process. A cell-free experiment was used to investigate the impact of the following parameters on dCO(2) removal: (1) sparge rate, (2) agitator speed, (3) bubble size, (4) bicarbonate concentration, (5) impeller position, and (6) aeration rate at the headspace of bioreactor. dCO(2) was measured using a fiber optic based probe. dCO(2) removal rate was a strong function of sparge rate and a weak function of agitator speed. Bubble size was modulated by the presence or absence of a sparge stone (10 microm pore size, 1 cm pipe i.d.). Open pipe provided 3- to 4-fold better dCO(2) removal for the same mass transfer coefficient (k(L)a) value. A mathematical model and a bench-scale experiment indicated that the benefit of a lower level of sodium bicarbonate in the culture medium was transient for batch and fed-batch cultures. Thus, this strategy was not used at pilot scale. Decreasing top impeller position improved k(L)a of dCO(2) by 2-fold. Changing headspace aeration rate from 0.02 to 0.04 vvm had no impact on dCO(2) removal. Two pilot runs were conducted using (A) open pipe and (B) antifoam in the presence of sparge stone, both in conjunction with lower impeller position. The presence of antifoam may interfere in product purification; however, demonstration of antifoam removal can be difficult. Open pipe allowed an alternative to using antifoam, as foam level with open pipe was significantly less. Both strategies successfully reduced dCO(2) level by 2.5-fold (179 +/- 9 vs 72 +/- 9 mmHg). Titer at day 10 of culture improved by 1.5-fold. Specific productivity improved by 41%. Historically, cultures were harvested around day 9-11 because of the high amount of foam; both strategies allowed the cultures to be extended up to day 14, resulting in 2-fold higher titer compared to that of the historical control without compromising protein quality.

摘要

大规模反应器中二氧化碳的积累可能对细胞生长和生产力产生不利影响。对于治疗性糖蛋白X而言,当培养规模从实验室规模扩大到中试规模时,比生产率损失了40%。在中试规模下,溶解二氧化碳(dCO₂)水平为179±9 mmHg,在实验室规模下为68±13 mmHg。作者提出了一种综合方法,以在整个14天的补料分批培养过程中将dCO₂水平维持在40至120 mmHg之间。使用无细胞实验来研究以下参数对dCO₂去除的影响:(1)鼓泡速率,(2)搅拌器速度,(3)气泡大小,(4)碳酸氢盐浓度,(5)叶轮位置,以及(6)生物反应器顶部空间的通气速率。使用基于光纤的探头测量dCO₂。dCO₂去除率强烈依赖于鼓泡速率,而对搅拌器速度的依赖较弱。通过有无鼓泡石(孔径10微米,管道内径1厘米)来调节气泡大小。对于相同的传质系数(k(L)a)值,开放管道的dCO₂去除效果要好3至4倍。一个数学模型和实验室规模实验表明,培养基中较低水平的碳酸氢钠对分批培养和补料分批培养的益处是短暂的。因此,该策略未在中试规模上使用。降低顶部叶轮位置可使dCO₂的k(L)a提高2倍。将顶部空间通气速率从0.02 vvm更改为0.04 vvm对dCO₂去除没有影响。进行了两次中试运行,(A)使用开放管道,(B)在有鼓泡石的情况下使用消泡剂,两者均结合较低的叶轮位置。消泡剂的存在可能会干扰产品纯化;然而,证明消泡剂的去除可能很困难。开放管道提供了一种替代使用消泡剂的方法,因为开放管道的泡沫水平明显更低。两种策略均成功将dCO₂水平降低了2.5倍(179±9 mmHg对72±9 mmHg)。培养第10天的滴度提高了1.5倍。比生产率提高了41%。从历史上看,由于大量泡沫,培养物在第9至11天左右收获;两种策略都使培养物能够延长至第14天,与历史对照相比,滴度提高了2倍,同时不影响蛋白质质量。

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