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Optimization of ginseng cell culture in airlift bioreactors and developing the large-scale production system

机译:优化气举生物反应器中的人参细胞培养并开发大规模生产系统

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Ginseng cell suspension culture was established in 51 capacity balloon type airlift bioreactors using Murashige and Skoog medium supplemented with 7 mgl(-1) indole butyric acid, 0.5 mgl(-1) kinetin and 30 gl(-1) sucrose. Various parameters such as types of bioreactors (cylinder, balloon, bulb and cone type bioreactors), aeration volume (0.05, 0.1, 0.2, 0.3 vvm constant air supply or the amount air supply was increased from 0.05 to 0.3 vvm at 6-day intervals), and inoculum density (40, 60,80 and 100 gl(-1)) were optimized. Balloon type airlift bioreactors, aeration volume of 0.1 vvm, and inoculum density of 60 gl(-1) were found suitable for accumulation of ginseng cell biomass and ginsenosides. Based on optimized results, 5001 capacity large-scale drum type and balloon type bioreactors were established for the production of ginsenosides. Optimal yield of 187 kg and 400 kg fresh biomass and 6.2 kg and 13.3 kg dry biomass, 7.86 mg g(-1) DW and 7.75 mg g(-1) DW total ginsenosides could be achieved in 5001 capacity drum and balloon type bioreactors respectively. These results are useful for commercial production of ginseng cell biomass and secondary metabolites
机译:人参细胞悬浮培养是在Murashige和Skoog培养基中添加了7 mgl(-1)吲哚丁酸,0.5 mgl(-1)激动素和30 gl(-1)蔗糖的51容量气球型空运生物反应器中建立的。各种参数,例如生物反应器的类型(圆柱,球囊,球泡和锥形生物反应器),通气量(0.05、0.1、0.2、0.3 vvm的恒定供气量或每6天间隔的供气量从0.05增加到0.3 vvm) ),并优化了接种密度(40、60、80和100 gl(-1))。气球型空运生物反应器,通气量为0.1 vvm,接种密度为60 gl(-1),适合人参细胞生物量和人参皂苷的积累。根据优化结果,建立了5001容量的大型鼓式和气囊式生物反应器用于生产人参皂苷。在5001容量的鼓式和气球式生物反应器中,分别可分别获得187 kg和400 kg新鲜生物量以及6.2 kg和13.3 kg干生物量,7.86 mg g(-1)DW和7.75 mg g(-1)DW总人参皂苷的最佳产量。 。这些结果可用于商业生产人参细胞生物量和次生代谢产物

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