Sizes of Maximum Stable Drops with Different Flow Behavior in Liquid-Liquid Agitation

被引：1

作者：

Tokanai, Hideki ^{[1
]}

Kuriyama, Masafumi ^{[1
]}

机构：

[1] Yamagata Univ, Dept Chem & Chem Engn, Yonezawa, Yamagata 9928510, Japan

来源：

JOURNAL OF CHEMICAL ENGINEERING OF JAPAN | 2015年 / 48卷 / 04期

关键词：

Agitation; Drop Breakup; Drop Size; Herschel-Bulkley Model; Yield Stress; DISPERSED-PHASE VISCOSITY; BREAKUP; VESSEL; TANK;

D O I：

10.1252/jcej.14we251

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The drop breakup model in liquid-liquid agitation, which has been proposed by the authors, is extended theoretically and experimentally. The extended model provides a new correlation equation for the maximum stable drop size. The equation is shown to be useful in prediction of sizes of the maximum stable drops with various flow behavior.

引用

页码：257 / 261

页数：5

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