Multiphase CFD modeling - scale-up of Fluidized-Bed Crystallizer

被引：0

作者：

Al-Rashed, Mohsen ^{[2
]}

Wojcik, Janusz ^{[1
]}

Plewik, Roch ^{[1
]}

Synowiec, Piotr ^{[1
,3
]}

Kus, Agata ^{[1
]}

机构：

[1] Silesian Tech Univ, Dept Chem & Proc Engng, Ks M Strzody 7, PL-44101 Gliwice, Poland

[2] Coll Technol Studies, Publ Author Appl Educ & Training, Kuwait, Kuwait

[3] Inst Inorgan Chem, PL-44100 Gliwice, Poland

来源：

19TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING | 2009年 / 26卷

关键词：

scale-up; fluidized bed; crystallizer; multiphase flow; CFD; SEGREGATION;

D O I：

暂无

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The main goal of this study was to obtain a closer look to scale up problem of the Fluidized-Bed crystallizer operation, in particular for solids concentration larger than 10 vol.%. To achieve that a multi-phase CFD code was used. Such an approach to this problem has not been investigated until now. Data collected using CFD technique, impossible to obtain in any other way, especially for an industrial apparatus, provides the information about the suspension flow behaviour in such crystallizers.

引用

页码：695 / 700

页数：6

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