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移动床径向反应器中流体力学行为的研究
引用本文:宋续祺,龚美珊.移动床径向反应器中流体力学行为的研究[J].化工学报,1992,43(3):268-274.
作者姓名:宋续祺  龚美珊
作者单位:清华大学化工系,清华大学化工系,清华大学化工系,中国石化总公司北京设计院 北京100084 ,北京100084 ,北京100084 ,北京100029
基金项目:国家自然科学基金资助项目
摘    要:比较了直径500mm移动床径向反应器中向心Z型、向心Π型、离心Z型、离心Π型4种气体流动类型.实验表明,离心Π型流动时,气体轴向分布不均匀度小于5%,为最佳气体流动类型.文中还得到了描述主流道中静压分布的动量交换系数K值.

关 键 词:径向反应器  移动床  反应器  两相流

HYDRODYNAMICS OF RADIAL FLOW MOVING-BED REACTOR
Song Xuqi,Wang Zhanwen and Jin Yong.HYDRODYNAMICS OF RADIAL FLOW MOVING-BED REACTOR[J].Journal of Chemical Industry and Engineering(China),1992,43(3):268-274.
Authors:Song Xuqi  Wang Zhanwen and Jin Yong
Abstract:In a φ500mm cold model of radial flow moving bed reactor, the distributions of pressure and velocity in the main channels were studied under four kinds of gas flow mode: inward Z gas flow; inward gas flow; outward Z gas flow and outward II gas flow. It was found that in the outward n gas flow mode, the axial non-uniformity of gas is minimum (less than 5% under the experiment condition). Correlations about the momentum recovery factor K were proposed. The distribution of pressure in the main channel can be predicted accurately.
Keywords:moving bed  chemical reactor  two phase flow  
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