Department of Chemical and Biochemical Engineering, Rutgers, The State University of New Jersey, Piscataway, New Jersey 08855-0909, USA.
Biotechnol Bioeng. 1991 Aug 5;38(4):331-9. doi: 10.1002/bit.260380403.
Airlift bioreactor operations have been studied for the growth-associated production of secondary metabolites from plant cell suspension cultures. The model system used in this work was Thalictrum rugosum producing berberine, an isoquinoline alkaloid. The airlift system was well suited for growth of Thalictrum cell suspension cultures unless the cell density was high. At high cell density, the airlift system with a draught tube was not adequate due to large aggregates clogging the recirculation paths. This was overcome by use of a cell scraper in the reactor. For berberine production, gas-stripping also played a significant role and it was discovered that CO(2) and ethylene were important for product formation. By supplying a mixture of CO(2) and ethylene into the airlift system, the specific berberine content was increased twofold. It is evident that continuous gas sparging was harmful for the production of berberine without supplementation with other gases.
气升式生物反应器的操作已被研究用于从植物细胞悬浮培养物中生长相关地生产次生代谢物。在这项工作中使用的模型系统是产生小檗碱的唐松草,一种异喹啉生物碱。气升式系统非常适合唐松草细胞悬浮培养物的生长,除非细胞密度很高。在高细胞密度下,带有通风管的气升式系统由于大的聚集体堵塞了再循环路径而不足够。通过在反应器中使用细胞刮板克服了这一问题。对于小檗碱的生产,气提也起着重要的作用,并且发现 CO(2)和乙烯对于产物形成很重要。通过将 CO(2)和乙烯的混合物供应到气升式系统中,小檗碱的比含量增加了两倍。显然,没有其他气体的补充,连续气体鼓泡对小檗碱的生产是有害的。