Plantwide control system design of the benchmark vinyl acetate monomer production plant

被引：17

作者：

Seki, Hiroya ^{[1
]}

Ogawa, Morimasa ^{[2
]}

Itoh, Toshiaki

Ootakara, Shigeki ^{[3
]}

Murata, Hisashi ^{[4
]}

Hashimoto, Yoshihiro ^{[5
]}

Kano, Manabu ^{[6
]}

机构：

[1] Tokyo Inst Technol, Chem Resources Lab, Midori Ku, Tokyo 2268503, Japan

[2] Yamatake Corp, Okayama 7128061, Japan

[3] Mitsui Chem Inc, Osaka 5928501, Japan

[4] Toyo Engn Corp, Chiba 2750024, Japan

[5] Nagoya Inst Technol, Dept Civil Engn & Syst Management, Showa Ku, Nagoya, Aichi 4668555, Japan

[6] Kyoto Univ, Dept Chem Engn, Nishikyo Ku, Kyoto 6158510, Japan

来源：

COMPUTERS & CHEMICAL ENGINEERING | 2010年 / 34卷 / 08期

关键词：

Process control; Plantwide control; Benchmark problem; Vinyl acetate process; Recycle system; OPTIMIZING CONTROL; RECYCLE; SEPARATOR; REACTOR;

D O I：

10.1016/j.compchemeng.2009.11.022

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

This paper addresses control system design of the vinyl acetate monomer production plant that has been introduced as a plantwide control benchmark problem by Luyben et al. Nonlinear analysis of a simplified model, which includes detailed reactor behavior and ideal separation with gas and liquid recycle, is performed to identify the optimal operating condition and to develop intuition for control system design. Control system is hierarchically constructed to realize the optimal operating condition, which is verified through simulation on a rigorous nonlinear model. (C) 2009 Elsevier Ltd. All rights reserved.

引用

页码：1282 / 1295

页数：14

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