Liquid flow pattern transition, droplet diameter and size distribution in the cavity zone of a rotating packed bed: A visual study

被引:118
|
作者
Sang, Le [1 ,2 ]
Luo, Yong [1 ,2 ]
Chu, Guang-Wen [1 ,2 ]
Zhang, Jing-Peng [1 ,2 ]
Xiang, Yang [2 ]
Chen, Jian-Feng [1 ,2 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Organ Inorgan Composites, Beijing 100029, Peoples R China
[2] Beijing Univ Chem Technol, Res Ctr, Minist Educ High Grav Engn & Technol, Beijing 100029, Peoples R China
基金
中国国家自然科学基金;
关键词
Rotating packed bed; Cavity zone; Liquid flow pattern transition; Average droplet diameter; Droplet size distribution; MASS-TRANSFER; PROCESS INTENSIFICATION; LIGAMENT FORMATION; SLAG GRANULATION; SPINNING WHEEL; ABSORPTION; REACTOR; DISINTEGRATION; HYDRODYNAMICS; ATOMIZATION;
D O I
10.1016/j.ces.2016.10.044
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A rotating packed bed (RPB) is one of the typical process intensification equipment. Its zone between the packing and the casing (cavity zone) is an important mass transfer zone. However, the liquid flow pattern, droplet diameter and size distribution in the cavity zone of a RPB, which is essential for the mass transfer modeling and performance, are still unclear. In this work, the liquid flow in the cavity zone of a RPB was studied under different experimental conditions using photographs taken by a high- speed camera. Two typical liquid flow patterns and liquid disintegrating modes were observed. A flow pattern transition criterion for the transition of ligament flow to droplet flow was presented. Effects of rotational speed, liquid initial velocity, outer packing radius, liquid viscosity, and liquid surface tension on the average droplet diameter and droplet size distribution were investigated. Furthermore, a correlation of the average droplet diameter was proposed. The predicted values of the average droplet diameter were found to be in agreement with the experimental values with deviations generally within +/- 15%.
引用
收藏
页码:429 / 438
页数:10
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