Bifurcation analysis for MTBE synthesis in a suspension catalytic distillation column

被引:0
|
作者
Wang, J. [1 ]
Chang, Y. [2 ]
Wang, E. Q. [1 ]
Li, C. Y. [1 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Chem Resource Engn, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, Sch Sci, Beijing 100029, Peoples R China
关键词
methyl tert-butyl ether synthesis; suspension catalytic distillation; mathematical model; bifurcation analysis; multiple steady states;
D O I
暂无
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
A rigorous bifurcation study is presented of methyl tert-butyl ether synthesis by suspension catalytic distillation (SCD). SCD is anew development of catalytic distillation (CD) in which fine catalyst particles are suspended in liquid, not only inherits advantages of CD but overcomes transfer limitations in catalyst bed. A complete equilibrium stage model is developed. Analysis results show that this system is sensitive to the operating parameters: the reflux ratio, the bottom flowrate, the methanol feed, the n-butane feed and the operation pressure, and the characteristic parameter for SCID: the solid/liquid separator ratio. The bifurcation diagram displays very intricate and highly nonlinear steady-state behavior, which can results in as many as seven steady-state solutions for identical column specifications. Especially, the results reveal that the superior column performance can be reached under practical operating conditions because the upper bound of the multiplicity range for the solid/liquid separation ratio is very small. (C) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1316 / 1324
页数:9
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