Modelling, optimization and control of batch polymerization reactor of styrene

被引:0
|
作者
Karagoz, AR [1 ]
Ozkan, G [1 ]
Erdogan, S [1 ]
Alpbaz, M [1 ]
机构
[1] GAZI UNIV,DEPT CHEM ENGN,TR-06570 ANKARA,TURKEY
来源
CONTROL AND COMPUTERS | 1997年 / 25卷 / 01期
关键词
styrene; polymerization; batch reactor; mathematical modelling; optimization; control;
D O I
暂无
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
The authors investigate the modelling, optimization, and control of a batch polymerization reactor in which polymerization of styrene initiated by benzoyl peroxide takes place, at different operating conditions. The polymerization kinetics and physical properties of the polymer obtained are determined and the mathematical model of this system is solved by using the data obtained from experimental-studies. The optimization of the batch polymerization reader is then carried out, and the performances of IMC and PID controller are compared. The performance of IMC was found to be better than that of PID.
引用
收藏
页码:21 / 26
页数:6
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