γ-CT measurement and CFD simulation of cross section gas holdup distribution in a gas-liquid stirred standard Rushton tank

被引:15
|
作者
Liu, Yue-Jin [1 ]
Li, Wei [1 ]
Han, Lu-Chang [1 ]
Cao, Yang [1 ]
Luo, He-an [1 ]
Al-Dahhan, Muthanna [2 ]
Dudukovic, M. P. [2 ]
机构
[1] Xiangtan Univ, Sch Chem Engn, Xiangtan 411105, Peoples R China
[2] Washington Univ, Chem React Engn Lab, St Louis, MO 63130 USA
基金
中国国家自然科学基金; 高等学校博士学科点专项科研基金;
关键词
Gas holdup distribution; gamma-CT measurement; Rushton tank; Larger gas flow; CFD simulation; TRAILING VORTICES; BUBBLE-COLUMNS; FLOW; TOMOGRAPHY; TURBINE; BREAKUP; VESSEL; DROP;
D O I
10.1016/j.ces.2011.03.042
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Cross section gas holdup distributions at 314 dimensionless static liquid height in a gas-liquid stirred standard Rushton tank were measured using Cs-137 gamma-CT scan measuring technology at larger gas flow rates and higher impeller rotating speeds. The obtained CT scan images and digital distribution curves of gas holdup with dimensionless radius based on the CT images could explain the fluctuation changes of gas holdup distribution. The dense area of gas holdup distribution appeared in the upper space of impeller blades. Gas holdup increased both with gas flow rate and impeller rotating speed, but gas flow rate had more influence on gas holdup than impeller rotating speed. The Eulerian-Eulerian two-fluid model coupling with the bubbles' coalescence and break-up models, and the drag coefficient model were established to make CFD simulation of gas holdup distributions for the gas-liquid stirred Rushton tank under different gas flow rates and impeller rotating speeds. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3721 / 3731
页数:11
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