Modeling and simulation for an industrial reactor on hydroisomerization of C8-aromatics

被引：0
|
作者：
Xu O. [1 ]
Fu Y. [1 ]
Chen X. [1 ]
机构：
[1] Zhijiang College, Zhejiang University of Technology, Hangzhou 310024, Zhejiang
来源：
Huagong Xuebao/CIESC Journal | 2011年 / 62卷 / 08期
关键词：
Hydroisomerization process; Industrial reactor; Simulation; Triangular reaction network;
D O I：
10.3969/j.issn.0438-1157.2011.08.037
中图分类号：
学科分类号：
摘要：
A triangular reaction network lumping three xylene isomers into a species is proposed for hydroisomerization of C8-aromatics and the corresponding kinetic model for an industrial reactor is also developed. The kinetic parameters are estimated by the traditional optimization method based on several sets of balanced plant data. Meanwhile, the model is simulated by large number of plant data at different operating conditions and a good agreement is obtained between the estimated and observed values. When compared with other models, the good performance of the proposed model is demonstrated in detail in terms of the indexes such as relative error, relative mean square error and parameter estimation time. © All Rights Reserved.
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页码：2298 / 2302
页数：4
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