环隙气升式反应器的开发III．高浓度山梨糖流加过程的动力学及控制策略  

Development of Annulus Airlift Reactor III.Kinetics and Control Strategy for Fed-Batch Fermentation of High Concentration Sorbose

作　　者：魏明旺[1] 章学钦[1] 

机构地区：[1]华东理工大学生物化工研究开发中心

出　　处：《华东理工大学学报（自然科学版）》1994年第5期615-620,共6页Journal of East China University of Science and Technology

摘　　要：在全容积１６Ｌ的环隙气升式反应器内，进行了高浓度山梨糖流加发酵过程的研究。根据其发酵过程的特征，建立了流加过程的动力学模型。在此基础上，获得适合该过程的流加控制策略。实验结果表明，采用该控制策略，可使底物浓度的波动范围小于２ｇ／Ｌ。Experimental studies were carried out on the fed-batch fermentation process of sorbose in a 16L airlift reactor.According to the characteristics of the fermentation process, a kinetic model of fed-batch fermentation was established.On the basis of the kinetic model, a control strategy which was used to control fed-batch fermentatin process of sorbose was obtained.The experiments showed that using the control strategy,the fluctuation range of substrate concentration is less than 2 g/L.

关 键 词：反应器 发酵 山梨糖 环隙气升式 

分 类 号：TQ920.5[轻工技术与工程—发酵工程]