气固两相流穿越液池过程颗粒运动及分布特性

吴晅; 梁盼龙; 王丽芳; 李海广; 武文斐

doi:10.11949/j.issn.0438-1157.20141596

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气固两相流穿越液池过程颗粒运动及分布特性

流体力学与传递现象 | 更新时间：2025-12-10

- 气固两相流穿越液池过程颗粒运动及分布特性
- Distribution properties and movement of particles in gas-solids flow passing through liquid bath
- 化工学报 2015年第3期页码：905-914
- 作者机构：
  
  1. 内蒙古科技大学内蒙古自治区白云鄂博矿多金属资源综合利用重点实验室,内蒙古,包头,014010
  2. 内蒙古科技大学能源与环境学院,内蒙古,包头,014010
- 作者简介：
- 基金信息：
- DOI：10.11949/j.issn.0438-1157.20141596
  中图分类号： Q021.1
- 网络首发：2015-03-05，
  
  纸质出版：2015-03-05
- 稿件说明：
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吴晅, 梁盼龙, 王丽芳, 等. 气固两相流穿越液池过程颗粒运动及分布特性[J]. 化工学报, 2015,(3):905-914.

WU Xuan, LIANG Panlong, WANG Lifang, et al. Distribution properties and movement of particles in gas-solids flow passing through liquid bath[J]. CIESC Journal, 2015, (3): 905-914.
吴晅, 梁盼龙, 王丽芳, 等. 气固两相流穿越液池过程颗粒运动及分布特性[J]. 化工学报, 2015,(3):905-914. DOI： 10.11949/j.issn.0438-1157.20141596.

WU Xuan, LIANG Panlong, WANG Lifang, et al. Distribution properties and movement of particles in gas-solids flow passing through liquid bath[J]. CIESC Journal, 2015, (3): 905-914. DOI： 10.11949/j.issn.0438-1157.20141596.

摘要

为了揭示气固两相流穿越液池过程中的气液固三相流动特性

建立了气液固三相实验平台和基于Euler-Lagrange框架下的数值模拟平台

对该过程中的气液固三相流动过程及颗粒运动分布规律进行研究。获得了5～15 μm、80～110 μm和380～530 μm 3种典型粒径颗粒在三相体系中的微观运动过程及其分布规律。实验与数值模拟结果均能反映出一致的客观规律。研究发现

颗粒浓度沿液池高度方向和径向均呈现多峰分布特征;5～15 μm粒径颗粒更易跟随气体一起穿越液池

其在液池内的浓度分布较为均匀;380～530 μm粒径颗粒与气体的跟随性较差

其浓度峰值主要集中在液池底部。随着下降管出口静态浸没深度的增加

液池内颗粒浓度分布趋于平缓。

Abstract

In order to study the flow characteristic of gas-liquid-solids three-phase in the process of gas-solids two-phase flow passing through the liquid bath

an experimental platform and a numerical simulation platform based on the Euler-Lagrange method were established respectively to conduct the studies on three-phase flow and particles movement. The distribution characteristics and the movement of three typical particle sizes were obtained

such as 5—15 μm

80—110 μm and 380—530 μm. The results of experiment were consistent with the results of numerical simulation. A multi-peak distribution of particle concentration existed in the liquid bath along the axial and radial directions. The particles of 5—15 μm in diameter were more easy to follow gas

and their distribution was more uniform. The particles of 380—530 μm in diameter were more difficult to follow gas

and their distribution was mainly concentrated at the bottom of the liquid bath. The increase of static submerged depth of downcomer outlet made the concentration distribution of particles more smoothly in the liquid bath.

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