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利用重复分批发酵生产短乳杆菌 CASD 生产 D-乳酸的动力学。

Kinetics of D-lactic acid production by Sporolactobacillus sp. strain CASD using repeated batch fermentation.

机构信息

Institute of Microbiology, Chinese Academy of Sciences, Beijing, People's Republic of China.

出版信息

Bioresour Technol. 2010 Aug;101(16):6499-505. doi: 10.1016/j.biortech.2010.03.069. Epub 2010 Apr 5.

Abstract

D-lactic acid was produced by Sporolactobacillus sp. strain CASD in repeated batch fermentation with one- and two-reactor systems. The strain showed relatively high energy consumption in its growth-related metabolism in comparison with other lactic acid producers. When the fermentation was repeated with 10% (v/v) of previous culture to start a new batch, D-lactic acid production shifted from being cell-maintenance-dependent to cell-growth-dependent. In comparison with the one-reactor system, D-lactic acid production increased approximately 9% in the fourth batch of the two-reactor system. Strain CASD is an efficient D-lactic acid producer with increased growth rate at the early stage of repeated cycles, which explains the strain's physiological adaptation to repeated batch culture and improved performance in the two-reactor fermentation system. From a kinetic point of view, two-reactor fermentation system was shown to be an alternative for conventional one-reactor repeated batch operation.

摘要

D-乳酸是由 Sporolactobacillus sp. 菌株 CASD 在单反应器和双反应器系统的分批补料发酵中产生的。与其他乳酸生产菌相比,该菌株在与其生长相关的代谢中表现出相对较高的能量消耗。当以 10%(v/v)的前培养物重复发酵开始新批次时,D-乳酸的生产从细胞维持依赖性转变为细胞生长依赖性。与单反应器系统相比,双反应器系统在第四批发酵中,D-乳酸的产量增加了约 9%。菌株 CASD 是一种高效的 D-乳酸生产菌,在重复循环的早期阶段具有较高的生长速率,这解释了该菌株对重复分批培养的生理适应以及在双反应器发酵系统中性能的提高。从动力学角度来看,双反应器发酵系统是传统单反应器重复分批操作的替代方案。

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