文献类型：期刊文献

中文题名：水力旋流冷氢箱的流体力学

英文题名：Hydrodynamic principles of hydrocyclone quench box

作者：赖朝荣[1];程振民[1];黄子宾[1];方向晨[2];刘忠信[2];彭德强[2]

机构：[1]华东理工大学化学工程联合国家重点实验室,上海200237;[2]抚顺石油化工研究院,辽宁抚顺113001

年份：2007

卷号：58

期号：8

起止页码：1955

中文期刊名：化工学报

外文期刊名：CIESC Journal

收录：CSTPCD;;EI(收录号：20073610802240);Scopus;北大核心:【北大核心2004】；CSCD:【CSCD2011_2012】；

基金：中国石油化工股份有限公司项目(105033);教育部新世纪优秀人才支持计划项目(NCET-04-0412)~~

语种：中文

中文关键词：水力旋流;Froude数;冷氢箱

外文关键词：hydrospiral flow;Froude number; quench box

摘要：A hydrocyclone quench box was designed according to the fluid dynamics of spiral flow.The quench box size, the drainage tube diameter, and the inlet tube diameter were designed based on Froude number and conservation of mechanical energy.The pressure drop of the hydrocyclone quench box was measured, and the liquid volumetric mass transfer coefficient was determined by oxygen absorption.The hydrocyclone quench box was compared with the horizontal flow quench box.The streamline of hydrocyclone quench box was simulated by computational fluid dynamics software.It was found that the pressure-drop and liquid volumetric mass transfer coefficient of the hydrocyclone quench box was better than the horizontal flow quench box .The pressure drop was less than 20 kPa and the liquid volumetric mass transfer coefficient was 0.0256 s -1 at 10 m 3·h -1 liquid flow rate and 60 m 3·h -1 gas flow rate.Simulation indicated that the average length of streamline under spiralling was 4 times of that under non-spiralling condition, which enhanced mixing for gas and liquid.
A hydrocyclone quench box was designed according to the fluid dynamics of spiral flow. The quench box size, the drainage tube diameter, and the inlet tube diameter were designed based on Froude number and conservation of mechanical energy. The pressure drop of the hydrocyclone quench box was measured, and the liquid volumetric mass transfer coefficient was determined by oxygen absorption. The hydrocyclone quench box was compared with the horizontal flow quench box. The streamline of hydrocyclone quench box was simulated by computational fluid dynamic pressure-drop and liquid volumetric mass transfer coefficient of the hyd than the horizontal flow quench box . The pressure drop was less than mass transfer coefficient was 0. 0256 s 1 at 10 m^3·h^-1 liquid flow rate. Simulation indicated that the average length of streamline under spi non-spiralling condition, which enhanced mixing for gas and liquid. s software. It was found that the rocyclone quench box was better 20 kPa and the liquid volumetric rate and 60m^3·h^-1 gas flow ralling was 4 times of that under