Computational Fluid Dynamics Simulation of Multiscale Mixing in Anionic Polymerization Tubular Reactors

被引:20
|
作者
Xie, Le [1 ]
Zhu, Li-Tao [1 ]
Luo, Zheng-Hong [1 ]
机构
[1] Shanghai Jiao Tong Univ, Coll Chem & Chem Engn, Dept Chem Engn, Shanghai 200240, Peoples R China
基金
中国国家自然科学基金;
关键词
Computational fluid dynamics; Kinetics; Multiscale mixing; Polymerization; Tubular reactor; RADICAL POLYMERIZATION; AUTOCLAVE REACTORS; MODEL; CFD; ACRYLATE; DESIGN;
D O I
10.1002/ceat.201500628
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The molecular properties of polymers are greatly influenced by operation parameters during polymerization in reactors. Since operation parameter distributions in reactors also result in molecular property distributions, polymerization bridges the gap between molecular properties and operation parameters. The combination of the computational fluid dynamics technology with the method of moments to form a uniquely coupled model was used to describe multiscale mixing fields in the reactor. The coupled model was validated by open experimental data, and the effects of polymerization kinetics on macroscopic and microscopic fields were investigated numerically. Also, the coupled model was applied to numerically predict the impacts of some key operation conditions on the main macroscopic flow field parameters and polymer molecular properties.
引用
收藏
页码:857 / 864
页数:8
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