Hydrodynamic correlations for bubble columns from complementary UXCT and RPT measurements in identical geometries and conditions

被引:11
作者
Azizi, S. [1 ]
Yaday, A. [2 ]
Lau, Y. M. [1 ]
Hampel, U. [1 ,3 ]
Roy, S. [2 ]
Schubert, M. [1 ]
机构
[1] Helmholtz Zentrum Dresden Rossendorf, Inst Fluid Dynam, Bautzner Landstr 400, D-01328 Dresden, Germany
[2] Indian Inst Technol Delhi, Dept Chem Engn, Delhi 110016, India
[3] Tech Univ Dresden, Chair Imaging Tech Energy & Proc Engn, D-01062 Dresden, Germany
基金
欧洲研究理事会;
关键词
Bubble columns; Hydrodynamic correlations; Ultrafast X-ray computed tomography; Radioactive particle tracking; GAS HOLD-UP; MASS-TRANSFER COEFFICIENT; 2-PHASE FLOW; REACTORS; SIZE; PREDICTION; PRESSURE; PATTERNS; VELOCITY; DENSITY;
D O I
10.1016/j.ces.2019.07.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Many correlations have been developed to predict the hydrodynamics of bubble columns. Often, these studies are performed for incomparable systems in terms of column and sparger dimensions as well as physical fluid properties. In this work, a different approach is proposed comprising interrelated correlations for liquid velocity, gas holdup and bubble size. The correlations are developed on the basis of complementary experiments with non-invasive measurement techniques, namely, Ultrafast X-ray Computed Tomography (UXCT) and Radioactive Particle Tracking (RPT). The experimental setup consists of a bubble column equipped with a needle sparger. The developed correlations consider sparger dimensions, operating conditions and bubble size. The bubble size is applied as the characteristic length in the Reynolds and the Eotvos numbers, which are utilized for the gas holdup and liquid velocity correlations. In comparison with previous approaches, the developed correlations show better agreement with experimental data from this study as well as from the literature. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页数:19
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