PREDICTION OF MEAN DROP SIZE IN BATCH AGITATED VESSELS

被引：19

作者：

GNANASUNDARAM, S

DEGALEESAN, TE

LADDHA, GS

机构：

[1] Alagappa Chettiar College of Technology, Madras

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 1979年 / 57卷 / 02期

关键词：

D O I：

10.1002/cjce.5450570203

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

A correlation is proposed for prediction of mean drop size in agitated vessels in the two major hydrodynamic regimes of importance as observed in this study covering a wide range of holdup from 0.01 to 0.5 and impeller Weber numbers from 35–200,000. Copyright © 1979 Canadian Society for Chemical Engineering

引用

页码：141 / 144

页数：4

共 17 条

[1]

BALAKRISHNAN LM, 1973, THESIS MADRAS U

[2] DROP SIZE DISTRIBUTION OF STIRRED NON-COALESCING LIQUID-LIQUID SYSTEM [J].