Hong J
Department of Chemical and Nuclear Engineering, University of Maryland, College Park, Maryland 20742.
Biotechnol Bioeng. 1986 Sep;28(9):1421-31. doi: 10.1002/bit.260280916.
The optimal substrate feeding policy for the fed batch fermentation which is governed by product and substrate inhibited kinetics is presented. The conjunction point between nonsingular and singular arcs and the feeding policy along the singular arc are derived analytically in terms of the concentrations of substrate and product and the liquid volume. Thus, it is possible to determine the feeding rate by monitoring the state variables (i.e., closed loop control). As a specific example, an optimization study of the fed batch fermentation for ethanol production by Saccharomyces cerevisiae is presented. It is shown that the optimal feeding patterns are heavily dependent upon the initial conditions. The point selectivity provides the guideline for predicting the optimal feeding patterns and explaining the results of rigorous mathematical analysis.
提出了由产物和底物抑制动力学控制的分批补料发酵的最优底物补料策略。根据底物和产物的浓度以及液体体积,通过解析方法推导出非奇异弧和奇异弧之间的连接点以及沿奇异弧的补料策略。因此,可以通过监测状态变量(即闭环控制)来确定补料速率。作为一个具体例子,给出了酿酒酵母生产乙醇的分批补料发酵的优化研究。结果表明,最优补料模式强烈依赖于初始条件。点选择性为预测最优补料模式和解释严格数学分析结果提供了指导。