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纤维床生物反应器中固定化 Lactococcus lactis 细胞从菊芋水解液中高效生产 L-乳酸。

Efficient production of l-lactic acid from hydrolysate of Jerusalem artichoke with immobilized cells of Lactococcus lactis in fibrous bed bioreactors.

机构信息

The Key Laboratory of Biomass Chemical Engineering, Ministry of Education, Zhejiang University, Hangzhou 310027, China.

出版信息

Enzyme Microb Technol. 2012 Oct 10;51(5):263-8. doi: 10.1016/j.enzmictec.2012.07.007. Epub 2012 Jul 25.

Abstract

Hydrolysate of Jerusalem artichoke was applied for the production of l-lactic acid by immobilized Lactococcus lactis cells in a fibrous bed bioreactor system. Preliminary experiments had indicated that the high quality hydrolysate, which was derived from the 40 min acid treatment at 95 °C and pH 1.8, was sufficient to support the cell growth and synthesis of l-lactic acid. With the addition of 5 g/l yeast extract, the fermentative performance of free cell system was evidently improved. After the basal settlement of hydrolysate based fermentation, the batch mode and the fed-batch mode fermentation were carried out in the free cell system and the fibrous bed bioreactor system, respectively. In all cases the immobilized cells presented the superior ability to produce l-lactic acid. The comparison of batch mode and fed-batch mode also indicated that the growth-limiting feeding strategy could reduce the lag phase of fermentation process and enhance the production of l-lactic acid. The achieved maximum concentration of l-lactic acid was 142 g/l in the fed-batch mode. Subsequent repeated-batch fermentation of the fibrous bed bioreactor system had further exhibited the persistence and stability of this system for the high production of l-lactic acid in a long term. Our work suggested the great potential of the fibrous bed bioreactor system and hydrolysate of J. artichoke in the economical production of l-lactic acid at industrial scale.

摘要

以固定化乳球菌细胞为催化剂,在纤维床生物反应器系统中利用菊芋酸解液生产 L-乳酸。初步实验表明,高质量的酸解液(在 95°C 和 pH 值 1.8 的条件下酸解 40 分钟得到)足以支持细胞生长和 L-乳酸的合成。添加 5 g/L 酵母提取物后,游离细胞体系的发酵性能明显提高。在基于水解物的发酵基础阶段完成后,分别在游离细胞体系和纤维床生物反应器体系中进行分批和补料分批发酵。在所有情况下,固定化细胞都表现出生产 L-乳酸的优越能力。分批模式和补料分批模式的比较也表明,生长限制型进料策略可以减少发酵过程的迟滞期,提高 L-乳酸的产量。在补料分批模式下,L-乳酸的最高浓度达到 142 g/L。随后对纤维床生物反应器系统的重复分批发酵进一步表明,该系统在长期、经济地工业化生产 L-乳酸方面具有巨大的潜力。我们的工作表明,纤维床生物反应器系统和菊芋酸解液在经济生产 L-乳酸方面具有巨大的潜力。

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