气升式内循环反应器内的气含率与液体循环(英文)  

Gas Holdup and Liquid Circulation in an Internal Airlift Loop Reactor

作　　者：任源[1] 韦朝海[1] 吴超飞[1] 谢波[1] 肖宏亮[1] 

机构地区：[1]华南理工大学化工学院,广东广州510640

出　　处：《华南理工大学学报（自然科学版）》2002年第3期72-77,共6页Journal of South China University of Technology(Natural Science Edition)

基　　金：教育部跨世纪优秀人才培养计划基金资助项目 (教技函 0 0 2号 );广东省科技厅科技计划项目 (2KB0 6 6 0 4C)~~

摘　　要：研究了气升式内循环反应器内的气含率与液体循环 .反应器包含一个传统的导流筒和三段缩放型导流筒 .通过实验分别对气 -水、气 -CMC(羧甲基纤维素 )溶液两相系统和气 -水 -树脂颗粒三相系统进行了研究 .用两相漂移通量模型对三相牛顿流体和两相非牛顿流体进行了评价 .结果表明 ,三段缩放型导流筒内的气含率高于传统的导流筒 ,且随表观气速而提高 .在两相和三相系统中 ,导流筒结构参数的变化对气含率的影响很小 .Gas holdup and liquid circulation in an internal airlift loop reactor were investigated. The reactor consists of one conventional draft tube and three convergence_divergence draft tubes. Experiments were carried out in two_phase systems with air_water and air_CMC (carboxyl methyl cellulose) solutions and in three_phase system with air_water_resin particles, respectively. The two_phase drift_flux model was used to estimate gas holdup for three_phase Newtonian and two_phase non_Newtonian systems. It is shown that gas holdup in convergence_divergence draft tube is higher than that in conventional draft tube and increases with superficial gas velocity. The variation of structural parameters of draft tubes has little effect on gas holdup in the two_phase system and the three_phase system. The mathematical model, which is based on drift_flux model, can describe the liquid circulation in reactor satisfactorily.

关 键 词：气升式内循环反应器 缩放型导流筒 气含率 液体循环 漂移通量模型 表观气速 

分 类 号：X505[环境科学与工程—环境工程]