Studies on paired packed-bed electrode reactor: Modeling and experiments

被引:4
|
作者
Zhang, XS [1 ]
Wu, GB [1 ]
Ding, P [1 ]
Zhou, XG [1 ]
Yuan, WK [1 ]
机构
[1] E China Univ Sci & Technol, UNILAB Res Ctr Chem React Engn, Shanghai 200237, Peoples R China
基金
中国国家自然科学基金;
关键词
paired packed-bed electrode reactor; electrode reactor model; potassium ferricyanide; potassium ferrocyanide; electrochemical reaction;
D O I
10.1016/S0009-2509(98)00320-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Experiments are carried out in a paired packed-bed electrode reactor with the cathodic reduction of potassium ferricyanide coupled with the anodic oxidation of potassium ferrocyanide as the working system. Eight probes are used to determine the potential distribution. A two-dimensional model is developed and solved by the finite element method. Good agreement is observed between the experimental data and the model predictions for reactors of different sizes and operating conditions. The effect of the operating variables (cell voltage, electrolyte velocity, reactant inlet concentration and electrolyte conductivity) and the Sizes of the electrodes on the potential and concentration distributions are investigated by simulation. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:2969 / 2977
页数:9
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