Simulation and optimization of the molecular weight distribution in a non-ideal polymerization reactor

被引:0
作者
Zhang, Chi [1 ]
Chen, Xi [1 ]
Shao, Zhijiang [1 ]
Xu, Chaozhong [2 ]
Wang, Jiajun [2 ]
机构
[1] Zhejiang Univ, Coll Control Sci & Engn, State Key Lab Ind Control Technol, Hangzhou 310027, Zhejiang, Peoples R China
[2] Zhejiang Univ, Coll Chem & Biol Engn, State Key Lab Chem Engn, Hangzhou 310027, Zhejiang, Peoples R China
来源
26TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING (ESCAPE), PT A | 2016年 / 38A卷
基金
中国国家自然科学基金;
关键词
computational fluid dynamics; free radical polymerization; molecular weight distribution; process optimization; CFD;
D O I
10.1016/B978-0-444-63428-3.50099-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Molecular weight distribution (MWD) is essential for describing the microstructural quality of a polymer. In the past decade, the simulation and optimization of the MWD of a polymerization process have received considerable attention. However, most studies are limited to ideal reactors, such as CSTRs. However, in large-scale industrial reactors, imperfect mixing often leads to a non-uniform distribution. The commercial software Fluent is used in this study to simulate free radical polymerization by the method of moments and computational fluid dynamics (CFD). An interface is designed in-house to extend the simulation to MWD calculation. Given a specific MWD curve as the target, process optimization is performed by combining CFD and MWD calculations in the in-house developed interface between C language and Fluent. A non-ideal tubular reactor is demonstrated for the low-density polyethylene process.
引用
收藏
页码:565 / 570
页数:6
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