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在一个200升塔式发酵罐中使用固定在微珠中的细胞进行青霉素发酵。

Penicillin fermentation in a 200-liter tower fermentor using cells confined to microbeads.

作者信息

Wang D I, Meier J, Yokoyama K

出版信息

Appl Biochem Biotechnol. 1984 Feb;9(1):105-16. doi: 10.1007/BF02798378.

Abstract

The scale-up of the penicillin fermentation through cell confinement in a 200-L tower fermentor is described. P. chrysogenum spores were adsorbed into Celite microbeads having diameters greater than 180 microns. Fed-batch fermentations were performed using both free and confined cells. Cell growth and penicillin concentrations were measured during the fermentation. In addition, the oxygen transfer rate, the aeration rate, and the level of dissolved oxygen were also measured. Significant improvement in the mass transfer coefficient was found when the cells were anchored onto the microbeads. This improved oxygen transfer rate was accompanied by higher production of penicillin at a lower aeration rate. Besides the improved oxygen transfer rate into the mycelial broth, a reduction of the energy input for the oxygen transfer was observed. The confinement of the cells to this microcarrier furthermore allowed the intermittent harvesting of fermentation broth without reducing the cell mass in the fermentor.

摘要

本文描述了通过将细胞限制在200升塔式发酵罐中扩大青霉素发酵规模的过程。产黄青霉孢子吸附到直径大于180微米的硅藻土微珠上。使用游离细胞和固定化细胞进行分批补料发酵。在发酵过程中测量细胞生长和青霉素浓度。此外,还测量了氧传递速率、通气速率和溶解氧水平。当细胞固定在微珠上时,传质系数有显著提高。这种提高的氧传递速率伴随着在较低通气速率下更高的青霉素产量。除了提高进入菌丝体肉汤的氧传递速率外,还观察到氧传递的能量输入减少。将细胞限制在这种微载体上还允许间歇收获发酵液,而不会减少发酵罐中的细胞量。

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