ECVT imaging of 3D spiral bubble plume structures in gas-liquid bubble columns

2014 ◽  
Vol 92 (12) ◽  
pp. 2078-2087 ◽  
Author(s):  
Aining Wang ◽  
Qussai Marashdeh ◽  
Liang-Shih Fan
2020 ◽  
Vol 13 (2) ◽  
pp. 737-751
Author(s):  
T. Matiazzo ◽  
R. K. Decker ◽  
J. C. S. C. Bastos ◽  
M. K. Silva ◽  
H. Meier ◽  
...  
Keyword(s):  

Computation ◽  
2019 ◽  
Vol 7 (1) ◽  
pp. 17 ◽  
Author(s):  
Giorgio Besagni ◽  
Fabio Inzoli

A precise estimation of the bubble size distribution (BSD) is required to understand the fluid dynamics in gas-liquid bubble columns at the “bubble scale,” evaluate the heat and mass transfer rate, and support scale-up approaches. In this paper, we have formulated a population balance model, and we have validated it against a previously published experimental dataset. The experimental dataset consists of BSDs obtained in the “pseudo-homogeneous” flow regime, in a large-diameter and large-scale bubble column. The aim of the population balance model is to predict the BSD in the developed region of the bubble column using as input the BSD at the sparger. The proposed approach has been able to estimate the BSD correctly and is a promising approach for future studies and to estimate bubble size in large-scale gas–liquid bubble columns.


2020 ◽  
Vol 4 (2) ◽  
pp. 23 ◽  
Author(s):  
Son Ich Ngo ◽  
Young-Il Lim

This review covers the scope of multiscale computational fluid dynamics (CFD), laying the framework for studying hydrodynamics with and without chemical reactions in single and multiple phases regarded as continuum fluids. The molecular, coarse-grained particle, and meso-scale dynamics at the individual scale are excluded in this review. Scoping single-scale Eulerian CFD approaches, the necessity of multiscale CFD is highlighted. First, the Eulerian CFD theory, including the governing and turbulence equations, is described for single and multiple phases. The Reynolds-averaged Navier–Stokes (RANS)-based turbulence model such as the standard k-ε equation is briefly presented, which is commonly used for industrial flow conditions. Following the general CFD theories based on the first-principle laws, a multiscale CFD strategy interacting between micro- and macroscale domains is introduced. Next, the applications of single-scale CFD are presented for chemical and biological processes such as gas distributors, combustors, gas storage tanks, bioreactors, fuel cells, random- and structured-packing columns, gas-liquid bubble columns, and gas-solid and gas-liquid-solid fluidized beds. Several multiscale simulations coupled with Eulerian CFD are reported, focusing on the coupling strategy between two scales. Finally, challenges to multiscale CFD simulations are discussed. The need for experimental validation of CFD results is also presented to lay the groundwork for digital twins supported by CFD. This review culminates in conclusions and perspectives of multiscale CFD.


Processes ◽  
2020 ◽  
Vol 8 (7) ◽  
pp. 795 ◽  
Author(s):  
Yixuan Cheng ◽  
Qiong Zhang ◽  
Pan Jiang ◽  
Kaidi Zhang ◽  
Wei Wei

Based on low-cost and easy to enlarge, the bubble column device has been widely concerned in chemical industry. This paper focuses on bubble plumes in laboratory-scale three-dimensional rectangular air-water columns. Static behavior has been investigated in many experiments and simulations, and our present investigations consider the dynamic behavior of bubble plume offset in three dimensions. The investigations are conducted with a set of closure models by the Euler–Euler approach, and subsequently, literature data for rectangular bubble columns are analyzed for comparison purposes. Moreover, the transient evolution characteristics of the bubble plume in the bubble column and the gas phase distribution in sections are introduced, and the offset characteristics and the oscillation period of the plume are analyzed. In addition, the distributions of the vector diagram of velocity and vortex intensity in the domain are given. The effects of different fluxes and column aspect ratios on bubble plumes are studied, and the offset and plume oscillation period (POP) characteristics of bubbles are examined. The investigations reveal quantitative correlations of operating conditions (gas volume flux) and aspect ratios that have not been reported so far, and the simulated and experimental POP results agree well. An interesting phenomenon is that POP does not occur under conditions of a high flux and aspect ratio, and the corresponding prediction values for the conditions with and without POP are given as well. The results reported in this paper may open up a new way for further study of the mass transfer of bubble plumes and development of chemical equipment.


2019 ◽  
Vol 372 ◽  
pp. 352-362 ◽  
Author(s):  
Liu Liu ◽  
Hongjie Yan ◽  
Thomas Ziegenhein ◽  
Hendrik Hessenkemper ◽  
Qing Li ◽  
...  

2017 ◽  
Vol 94 ◽  
pp. 53-78 ◽  
Author(s):  
Giorgio Besagni ◽  
Alessandro Di Pasquali ◽  
Lorenzo Gallazzini ◽  
Elia Gottardi ◽  
Luigi Pietro Maria Colombo ◽  
...  

2014 ◽  
Vol 92 (11) ◽  
pp. 2352-2360 ◽  
Author(s):  
Sergio A. Baz-Rodríguez ◽  
José E. Botello-Alvarez ◽  
Alejandro Estrada-Baltazar ◽  
Luis E. Vilchiz-Bravo ◽  
José A. Padilla-Medina ◽  
...  

2004 ◽  
Vol 191 (8) ◽  
pp. 1003-1016 ◽  
Author(s):  
MING-YAN LIU ◽  
ZHONG-DING HU ◽  
JING-HAI LI

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