Qian Zhi-Gang, Zhao Zhen-Jiang, Xu Yufang, Qian Xuhong, Zhong Jian-Jiang
State Key Laboratory of Bioreactor Engineering, East China University of Science and Technology, Shanghai 200237, China.
Biotechnol Bioeng. 2005 May 20;90(4):516-21. doi: 10.1002/bit.20460.
A highly efficient bioprocessing strategy was developed for enhancing the production of plant secondary metabolites by repeatedly eliciting a fed-batch culture with a newly synthesized powerful jasmonate analog, 2,3-dihydroxypropyl jasmonate (DHPJA). In suspension cultures of a high taxuyunnanine C (Tc)-producing cell line of Taxus chinensis, 100 microM DHPJA was added on day 7 to fed-batch cultures with feeding of 20 g L(-1) sucrose on the same day. The synergistic effect of elicitation and substrate feeding on Tc biosynthesis was observed, which resulted in higher Tc accumulation than that by elicitation or sucrose feeding alone. More interestingly, both specific Tc yield (i.e., Tc content) and volumetric yield was further improved by a second addition of 100 microM DHPJA (on day 12) to the fed-batch cultures. In particular, with repeated elicitation and sucrose feeding the Tc volumetric yield was increased to 827 +/- 29 mg L(-1), which was 5.4-fold higher than that of the nonelicited batch culture. Furthermore, the above novel strategy was successfully applied from shake flask to a 1-L airlift bioreactor. A high Tc production and productivity of 738 +/- 41 mg L(-1) and 33.2 +/- 1.9 mg L(-1) d(-1), respectively, was achieved, which is higher than previous reports on Tc production in bioreactors. The results suggest that the aforementioned bioprocessing strategy may potentially be applied to other cell culture systems for efficient production of plant secondary metabolites.
开发了一种高效的生物加工策略,通过用新合成的强效茉莉酸酯类似物2,3-二羟基丙基茉莉酸酯(DHPJA)反复诱导补料分批培养来提高植物次生代谢产物的产量。在高产紫杉醇C(Tc)的中国红豆杉细胞系的悬浮培养中,在第7天向补料分批培养物中添加100μM DHPJA,同时在同一天补加20 g L(-1)蔗糖。观察到诱导和底物补加对Tc生物合成的协同作用,这导致Tc积累量高于单独诱导或蔗糖补加。更有趣的是,通过向补料分批培养物中第二次添加100μM DHPJA(在第12天),特定Tc产量(即Tc含量)和体积产量都进一步提高。特别是,通过反复诱导和蔗糖补加,Tc体积产量提高到827±29 mg L(-1),比未诱导的分批培养高5.4倍。此外,上述新策略成功地从摇瓶应用到1-L气升式生物反应器。分别实现了738±41 mg L(-1)和33.2±1.9 mg L(-1) d(-1)的高Tc产量和生产率,高于以前关于生物反应器中Tc生产的报道。结果表明,上述生物加工策略可能潜在地应用于其他细胞培养系统,以高效生产植物次生代谢产物。