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固定化乳酸乳球菌IO-1产乳酸的优化。

Optimization of lactic acid production by immobilized Lactococcus lactis IO-1.

作者信息

Sirisansaneeyakul Sarote, Luangpipat Tiyaporn, Vanichsriratana Wirat, Srinophakun Thongchai, Chen Henry Ho-Hsien, Chisti Yusuf

机构信息

Department of Biotechnology, Kasetsart University, Bangkok 10900, Thailand.

出版信息

J Ind Microbiol Biotechnol. 2007 May;34(5):381-91. doi: 10.1007/s10295-007-0208-6. Epub 2007 Feb 21.

Abstract

Production of lactic acid from glucose by immobilized cells of Lactococcus lactis IO-1 was investigated using cells that had been immobilized by either entrapment in beads of alginate or encapsulation in microcapsules of alginate membrane. The fermentation process was optimized in shake flasks using the Taguchi method and then further assessed in a production bioreactor. The bioreactor consisted of a packed bed of immobilized cells and its operation involved recycling of the broth through the bed. Both batch and continuous modes of operation of the reactor were investigated. Microencapsulation proved to be the better method of immobilization. For microencapsulated cells at immobilized cell concentration of 5.3 g l(-1), the optimal production medium had the following initial concentrations of nutrients (g l(-1)): glucose 45, yeast extract 10, beef extract 10, peptone 7.5 and calcium chloride 10 at an initial pH of 6.85. Under these conditions, at 37 degrees C, the volumetric productivity of lactic acid in shake flasks was 1.8 g l(-1) h(-1). Use of a packed bed of encapsulated cells with recycle of the broth through the bed, increased the volumetric productivity to 4.5 g l(-1) h(-1). The packed bed could be used in repeated batch runs to produce lactic acid.

摘要

利用乳酸乳球菌IO-1的固定化细胞,研究了由葡萄糖生产乳酸的过程。所用细胞通过包埋在海藻酸钠珠中或包封在海藻酸钠膜微胶囊中进行固定。采用田口方法在摇瓶中对发酵过程进行优化,然后在生产生物反应器中进一步评估。该生物反应器由固定化细胞填充床组成,其操作包括使发酵液循环通过填充床。研究了反应器的分批和连续操作模式。结果表明,微胶囊化是更好的固定化方法。对于固定化细胞浓度为5.3 g l(-1)的微胶囊化细胞,最佳生产培养基的初始营养成分浓度(g l(-1))如下:葡萄糖45、酵母提取物10、牛肉提取物10、蛋白胨7.5和氯化钙10,初始pH值为6.85。在这些条件下,37℃时,摇瓶中乳酸的体积产率为1.8 g l(-1) h(-1)。使用包封细胞填充床并使发酵液循环通过填充床,可将体积产率提高到4.5 g l(-1) h(-1)。该填充床可用于重复分批运行以生产乳酸。

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