A generic hybrid model development for process analysis of industrial fixed-bed catalytic reactors

被引:48
作者
Azarpour, Abbas [1 ]
Borhani, Tohid N. G. [2 ]
Alwi, Sharifah R. Wan [3 ,4 ]
Manan, Zainuddin A. [3 ,4 ]
Mutalib, Mohamed I. Abdul [1 ]
机构
[1] Univ Teknol Petronas, Dept Chem Engn, Seri Iskandar 32610, Perak, Malaysia
[2] Imperial Coll London, Dept Chem Engn, Ctr Proc Syst Engn, London SW7 2AZ, England
[3] Univ Teknol Malaysia, Res Inst Sustainable Environm, Proc Syst Engn Ctr PROSPECT, Utm Johor Bahru 81310, Johor, Malaysia
[4] Univ Teknol Malaysia, Fac Chem Engn, Utm Johor Bahru 81310, Johor, Malaysia
关键词
Fixed-bed catalytic reactor; First principle model; Catalyst deactivation; Artificial neural network; Dynamic modeling; Catalytic process; TEREPHTHALIC ACID HYDROPURIFICATION; ARTIFICIAL-NEURAL-NETWORK; LIQUID DISTRIBUTION; TRANSPORT LIMITATIONS; PD/C CATALYST; OPTIMIZATION; METHANOL; DEACTIVATION; PERFORMANCE; SYSTEM;
D O I
10.1016/j.cherd.2016.10.024
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Catalyst deactivation is one of the major concerns in industrial catalytic reactors. The capability to perform detailed analysis of the catalytic process and its deactivation phenomenon is therefore vital in maintaining high productivity and product quality. Analysis and prediction of the catalyst deactivation mechanism and the rate of deactivation are among the most challenging endeavors in the area of the catalytic reactor modeling. Hence, the catalyst deactivation phenomenon requires detailed dynamic modeling to enable its performance to be closely scrutinized. In this paper, a hybrid model incorporating first principle model and artificial neural network (ANN) has been used to develop a generic framework to model the industrial fixed-bed catalytic reactors (FBCRs) experiencing catalyst deactivation. The model does not consider the complicated mechanism of catalyst deactivation, and its effect is incorporated employing ANN, which utilizes the catalytic process data. The generic modeling steps have been extensively described, and the developed model has been applied on two industrial case studies. The validation of each model was carried out signifying that the generalized model developed has acceptable accuracy. The model enabled the lifetime of the industrial Pd/C and CuO-ZnO-Al2O3 catalysts and the effects of the operating parameters on the hydropurification process and methanol production reactors to be predicted. The generic strategy presented can be utilized for the performance analysis of any FBCR disregarding the type of catalyst. (C) 2016 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:149 / 167
页数:19
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