Modeling for the catalytic coupling reaction of carbon monoxide to diethyl oxalate in fixed-bed reactors: Reactor model and its applications

被引:12
|
作者
Zhu, Ya-Ping [1 ]
Tu, Song [1 ]
Luo, Zheng-Hong [1 ]
机构
[1] Xiamen Univ, Coll Chem & Chem Engn, Dept Chem & Biochem Engn, Xiamen 361005, Peoples R China
基金
中国国家自然科学基金;
关键词
Multiphase reactors; Mathematical modeling; Kinetics; Fixed-bed reactor; Catalytic coupling reaction; PD-FE/ALPHA-AL2O3; CATALYST; MECHANISM; FLOW;
D O I
10.1016/j.cherd.2011.12.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A two-dimensional (2D) pseudo-homogeneous reactor model was developed to simulate the performance of fixed-bed reactors for catalytic coupling reaction of carbon monoxide to diethyl oxalate. Reactor modeling was performed using a comprehensive numerical model consisting of two-dimensional coupled material and energy balance equations. A power law kinetic model was applied for simulating the catalytic coupling reaction with considering one main-reaction and two side-reactions. The validity of the reactor model was tested against the measured data from different-scale demonstration processes and satisfactory agreements between the model prediction and measured results were obtained. Furthermore, detailed numerical simulations were performed to investigate the effect of major operation parameters on the reactor behavior of fixed bed for catalytic coupling reaction of carbon monoxide to diethyl oxalate, and the result shows that the coolant temperature is the most sensitive parameter. (C) 2011 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1361 / 1371
页数:11
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