Estimation of catalyst deactivation parameters of ethyl tert-butyl ether (ETBE) reactors based on industrial plant data

被引：0

作者：

Domingues, Luis ^{[1
]}

Pinheiro, Carla C. ^{[1
]}

Oliveira, Nuno M. C. ^{[2
]}

Vilelas, Andre ^{[3
]}

Fernandes, Jorge ^{[3
]}

Ribeiro, Fernando Ramoa ^{[1
]}

机构：

[1] Univ Tecn Lisboa, Inst Super Tecn, Inst Biotechnol & Bioengn, Av Rovisco Pais 1, P-1049001 Lisbon, Portugal

[2] Univ Coimbra, Dept Chem Engn, P-3030790 Coimbra, Portugal

[3] Repsol Polmeros, P-7520954 Sines, SA, Portugal

来源：

22 EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING | 2012年 / 30卷

关键词：

Dynamic modeling; Parameter estimation; Catalyst deactivation; ETBE; Industrial data; ION-EXCHANGE-RESINS; DISTILLATION;

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：

This work considers the catalyst deactivation phenomena in ethyl tert-butyl ether (ETBE) reactors, and the estimation of the corresponding kinetic parameters from industrial plant data. For this purpose a simulation model of these units is developed, and used to build a parameter estimation problem constrained by partial differential equations. Good agreement between the model predictions and the available industrial data is achieved, enabling the use of the resulting model in several process related tasks.

引用

页码：1002 / 1006

页数：5

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