文献类型：期刊文献

中文题名：内部部分润湿催化剂的动力学行为

英文题名：Global kinetics of reaction accompanied by partial internal wetting of catalysts

作者：周志明[1];程振民[1];李卓[1];袁渭康[1]

机构：[1]华东理工大学反应工程国家重点实验室,上海200237

年份：2005

卷号：56

期号：4

起止页码：637

中文期刊名：化工学报

外文期刊名：CIESC Journal

收录：CSTPCD;;EI(收录号：2005229136627);Scopus;北大核心:【北大核心2004】；CSCD:【CSCD2011_2012】；

基金：国家自然科学基金项目 (20106005);中国石化总公司项目 (201085)~~

语种：中文

中文关键词：部分润湿;毛细冷凝;反应动力学;苯加氢

外文关键词：Adsorption;Benzene;Capillary tubes;Catalysts;Condensation;Evaporation;Hydrogenation;Mathematical models;Pore size;Reaction kinetics;Wetting

摘要：The global reaction rate of benzene hydrogenation to cyclohexane accompanied by partial internal wetting of catalyst pellets was measured by a new method, which investigated both adsorption and chemical reaction.The adsorption investigation was used to establish a relationship between the extent of liquid filling of the catalyst and the bulk conditions while the chemical reaction investigation was to study the effect of partial internal wetting of the catalyst on the global reaction rate.It was shown that the extent of liquid filling in the catalyst interior showed a significant effect on the global rate, and the current state of the catalyst depended on the history, i.e. whether it was a liquid evaporation process or a vapor condensation process, and two steady states were found under certain circumstances.A mathematical model was developed, which took multicomponent diffusion, chemical reaction, pore size distribution of the catalyst and capillary condensation of condensable components in the catalyst pellet into consideration.The predicted values were in good agreement with the experimental data.
The global reaction rate of benzene hydrogenation to cyclohexane accompanied by partial internal wetting of catalyst pellets was measured by a new method, which investigated both adsorption and chemical reaction. The adsorption investigation was used to establish a relationship between the extent of liquid filling of the catalyst and the bulk conditions while the chemical reaction investigation was to study the effect of partial internal wetting of the catalyst on the global reaction rate. It was shown that the extent of liquid filling in the catalyst interior showed a significant effect on the global rate, and the current state of the catalyst depended on the history, i.e. whether it was a liquid evaporation process or a vapor condensation process, and two steady states were found under certain circumstances. A mathematical model was developed, which took multicomponent diffusion, chemical reaction, pore size distribution of the catalyst and capillary condensation of condensable components in the catalyst pellet into consideration. The predicted values were in good agreement with the experimental data.