Liquid saturation in concurrent gas-liquid downflow through packed beds

被引：3
|
作者：
Sai, PST
机构：
[1] Department of Chemical Engineering, Indian Institute of Technology
来源：
BIOPROCESS ENGINEERING | 1997年 / 16卷 / 05期
关键词：
Foam; Packing Size; Liquid Saturation; Column Diameter; Newtonian Liquid;
D O I：
10.1007/s004490050323
中图分类号：
Q81 [生物工程学（生物技术）]; Q93 [微生物学];
学科分类号：
071005 ; 0836 ; 090102 ; 100705 ;
摘要：
The total and dynamic liquid saturation under concurrent gas-liquid downflow through packed beds were experimentally measured for non-foaming, foaming New tonian and non-Newtonian liquids. The variables include the column diameter, packing size and shape, flow rate of the phases, and physical properties. Correlations were presented in terms of Lockhart-Martinelli parameter, chi for non-foaming Newtonian and non-Newtonian liquids and in terms of modified Lockhart-Martinelli parameter, chi' for foaming Newtonian liquids.
引用
收藏
页码：283 / 287
页数：5
相关论文
共 50 条
12345