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Growth and anthraquinone production of Morinda elliptica cell suspension cultures in a stirred-tank bioreactor

机译:搅拌罐生物反应器中巴戟天细胞悬浮培养的生长和蒽醌的产生

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摘要

The effects of medium strategy, number of impellers, aeration mode, and mode of operation on Morinda elliptica cell suspension cultures in a stirred-tank bioreactor are described. A lower number of impellers and continuous aeration contributed toward high cell growth rate, whereas a higher number of impellers reduced cell growth rate, although not anthraquinone yield. The semicontinuous mode could indirectly imitate the larger scale version of production medium strategy and improved anthraquinone production even with 0.012% (v/v) antifoam addition. Production medium promoted both growth (maximum dry cell weight of 24.6 g/L) and anthraquinone formation (maximum content of 19.5 mg/g of dry cell weight), without any necessity for antifoam addition. Cultures in production medium or with higher growth rate and anthraquinone production were less acidic than cultures in growth medium or with lower growth rate and anthraquinone production. Using the best operating variables, growth of M. elliptica cells (24.6 g/L) and anthraquinone yield (0.25 g/L) were 45% and 140%, respectively, lower than those using a shake flask culture after 12 days of cultivation. [References: 27]
机译:描述了培养基策略,叶轮数量,曝气模式和操作模式对搅拌罐式生物反应器中巴戟天椭圆形细胞悬浮培养的影响。较少数量的叶轮和连续通气有助于提高细胞生长速度,而较高数量的叶轮则降低了细胞生长速度,尽管蒽醌的产量不高。即使添加0.012%(v / v)消泡剂,半连续模式也可以间接模仿大规模生产培养基策略,并提高蒽醌的产量。生产培养基既促进生长(最大干细胞重量为24.6 g / L)又促进蒽醌的形成(最大含量为19.5 mg / g干细胞重量),而无需添加消泡剂。生产培养基中或具有较高生长速度和蒽醌产量的培养物的酸性低于生长培养基中或具有较低生长速度和蒽醌产量的培养物。使用最佳操作变量,椭圆形支原体细胞的生长(24.6 g / L)和蒽醌产率(0.25 g / L)分别比培养12天后使用摇瓶培养的细胞低45%和140%。 [参考:27]

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