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多管环流反应器的流动和传质特性

刘永民 刘铮 袁乃驹

化工学报2001,Vol.52Issue(3):222-226,5.
化工学报2001,Vol.52Issue(3):222-226,5.

多管环流反应器的流动和传质特性

LIQUID CIRCULATION RATE AND VOLUMETRIC MASS TRANSFER COEFFICIENT IN MULTI-TUBE AIRLIFT LOOP REACTOR

刘永民 1刘铮 2袁乃驹2

作者信息

  • 1. 抚顺石油学院石油化工系,
  • 2. 清华大学化学工程系,
  • 折叠

摘要

Abstract

A correlation of liquid circulation rate in a multi-tube air-lift loop reactor(MALR) was established on the basis of the momentum balance, in which a new method for the determination of the overall frictional-loss coefficient in air-water system was developed. The method for determining the exposure time of liquid particle in the gas-liquid interphase was proposed, which formed the basis for the calculation of volumetric mass transfer coefficient of gas component according to Higbie's penetration theory. The validity of these two correlations was demonstrated by the fairly good agreements between the calculated liquid rate and mass transfer coefficients with the experimental data.

关键词

环流反应器/气升式/循环液速/阻力损失系数/体积传质系数

分类

化学化工

引用本文复制引用

刘永民,刘铮,袁乃驹..多管环流反应器的流动和传质特性[J].化工学报,2001,52(3):222-226,5.

基金项目

辽宁省自然科学基金资助项目 ()

化工学报

OA北大核心CSCD

0438-1157

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