Department of Experimental Medicine, Section of Biotechnology and Molecular Biology, Second University of Naples, via de Crecchio 7, 80138, Naples, Italy.
Appl Microbiol Biotechnol. 2010 Feb;85(6):1779-87. doi: 10.1007/s00253-009-2261-8. Epub 2009 Oct 1.
The production of industrially relevant microbial polysaccharides has recently gained much interest. The capsular polysaccharide of Escherichia coli K4 is almost identical to chondroitin, a commercially valuable biopolymer that is so far obtained from animal tissues entailing complex and expensive extraction procedures. In the present study, the production of capsular polysaccharide by E. coli K4 was investigated taking into consideration a potential industrial application. Strain physiology was first characterized in shake flask experiments to determine the optimal culture conditions for the growth of the microorganism and correlate it to polysaccharide production. Results show that the concentration of carbon source greatly affects polysaccharide production, while the complex nitrogen source is mainly responsible for the build up of biomass. Small-scale batch processes were performed to further evaluate the effect of the initial carbon source concentration and of growth temperatures on polysaccharide production, finally leading to the establishment of the medium to use in following fermentation experiments on a bigger scale. The fed-batch strategy next developed on a 2-L reactor resulted in a maximum cell density of 56 g(cww)/L and a titre of capsular polysaccharide equal to 1.4 g/L, approximately ten- and fivefold higher than results obtained in shake flask and 2-L batch experiments, respectively. The release kinetics of K4 polysaccharide into the medium were also explored to gain insight into the mechanisms underlying a complex aspect of the strain physiology.
最近,工业相关微生物多糖的生产引起了广泛关注。大肠杆菌 K4 的荚膜多糖与商业价值极高的生物聚合物软骨素几乎完全相同,而软骨素目前是从动物组织中提取得到的,这需要复杂且昂贵的提取过程。在本研究中,考虑到潜在的工业应用,研究了大肠杆菌 K4 荚膜多糖的生产。首先通过摇瓶实验对菌株生理学进行了表征,以确定微生物生长的最佳培养条件,并将其与多糖生产相关联。结果表明,碳源浓度对多糖生产有很大影响,而复杂的氮源主要负责生物量的积累。进行了小规模分批过程以进一步评估初始碳源浓度和生长温度对多糖生产的影响,最终确定了在更大规模发酵实验中使用的培养基。随后在 2-L 反应器上开发的补料分批策略使细胞密度达到 56 g(cww)/L 的最大值,荚膜多糖的产量达到 1.4 g/L,分别比摇瓶和 2-L 分批实验中的结果高出约十倍和五倍。还探索了 K4 多糖向培养基中的释放动力学,以深入了解该菌株生理学复杂方面的机制。