Zhao Ben, Li Yafei, Mbifile Martha Daniel, Li Changling, Yang Hailin, Wang Wu
The Key Laboratory of Industrial Biotechnology Ministry of Education Jiangnan University Wuxi China.
College of Biological and Food Engineering Huaihua University Huaihua China.
Eng Life Sci. 2017 Apr 18;17(9):981-988. doi: 10.1002/elsc.201600249. eCollection 2017 Sep.
sp. AB-610 accumulates relatively higher amount of DHA-rich lipid in the cells, and it was found that DHA yield was closely related to the cell morphology and pH value during fermentation period. DHA production from sp. AB-610 in fed-batch fermentation was investigated and four growth stages were clarified as lag stage, balanced growth stage, lipid accumulation stage, and lipid turnover stage, based on the morphologic observation and key parameters changes. Then a simple strategy of two-stage pH control was developed, in which pH 7.0 was kept until 12 h after the end of balanced growth stage, and then shifted to 5.0 for the rest period in fermentation. A maximal DHA production of 11.44g/L was achieved. This approach has advantage of easy scaling up for industrial DHA fermentation from sp. cells.
菌株AB-610在细胞内积累了相对较高含量的富含DHA的脂质,并且发现发酵期间DHA产量与细胞形态和pH值密切相关。研究了分批补料发酵中菌株AB-610的DHA生产情况,并根据形态学观察和关键参数变化,明确了四个生长阶段,即延迟期、平衡生长期、脂质积累期和脂质周转期。然后制定了一种简单的两阶段pH控制策略,即在平衡生长期结束后12小时内保持pH 7.0,然后在发酵剩余时间将pH值调至5.0。实现了11.44g/L的最大DHA产量。这种方法具有易于扩大规模用于该菌株细胞的工业DHA发酵的优点。