Constantinides A, Mehta N
Department of Chemical and Biochemical Engineering, Rutgers, The State University of New Jersey, Piscataway, New Jersey 08854, USA.
Biotechnol Bioeng. 1991 May;37(11):1010-20. doi: 10.1002/bit.260371105.
A lumped model for cell growth and secondary metabolite production in an immobilized live cell bioreactor has been developed. This model is applied here to simulate the performance of an immobilized bioreactor under steady-state conditions and under conditions of periodically varying concentration of a growth-limiting substrate. The results of the simulation study were experimentally verified in the case of the production of the antibiotic candicidin by Streptomyces griseus in an immobilized bioreactor with forced periodic operation. The results of the studies suggest that periodically operated immobilized live cell bioreactors can provide a potent alternative for the production of non-growth-associated biochemicals, as compared to free cell fermentations, pulsed fermentations with process cycle regeneration, and nonregenerated bioreactors. This work has demonstrated that by frequent pulsing of the growth limiting nutrient, stable extended production can be obtained at high specific cellular productivities.
已开发出一种用于固定化活细胞生物反应器中细胞生长和次级代谢产物生产的集总模型。在此应用该模型来模拟固定化生物反应器在稳态条件下以及生长限制底物浓度周期性变化条件下的性能。在链霉菌在强制周期性操作的固定化生物反应器中生产抗生素杀假丝菌素的情况下,对模拟研究结果进行了实验验证。研究结果表明,与游离细胞发酵、具有过程循环再生的脉冲发酵和非再生生物反应器相比,周期性操作的固定化活细胞生物反应器可为非生长相关生化物质的生产提供有力的替代方案。这项工作表明,通过频繁脉冲添加生长限制营养素,可以在高比细胞生产率下获得稳定的延长生产。