CFD simulation of isolated bubbles rising in Newtonian or non-Newtonian fluids inside a thin-gap bubble column

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL Chemical Engineering Research & Design Pub Date : 2025-02-01 Epub Date: 2024-12-26 DOI:10.1016/j.cherd.2024.12.030
Sikandar Almani , Walid Blel , Emilie Gadoin , Caroline Gentric
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Abstract

Hydrodynamics of the bubbling process can be complex especially in thin bubble columns, when the gap has the same order of magnitude as the bubble diameter, and with complex fluids. It is then important to understand this phenomenon either by experimental investigation through optical methods such as shadowgraphy and/or Particle Image Velocimetry (PIV) or numerically by Computational Fluid Dynamics (CFD), which, when validated, can allow numerical experimentation in situations which are expensive to implement experimentally or time consuming. In this study, three-dimensional numerical simulations of isolated bubbles rising in Newtonian (water) or non-Newtonian (CarboxyMethyl Cellulose (CMC) and Xanthan Gum (XG) solutions) liquid phases mimicking Chlorella vulgaris cultures at 42 g.L−1 concentration inside a 4 mm gap bubble column are performed using the volume of fluid (VOF) model with the ANSYS FLUENT 17.2 code. Results are validated by comparison with shadowgraphy experiments. Bubble terminal velocity, shape, and trajectory are numerically analysed. Wall shear stress (WSS) induced by the bubble, strain rate, viscosity and flow field around the bubble are also discussed. Numerical results show similar trends as experimental ones despite slightly lower terminal velocity and aspect ratio values are observed in comparison to the experimental results. The trajectory of the bubble is non-rectilinear for water and rectilinear for non-Newtonian fluids as observed experimentally. This numerical study highlights the bubble-liquid and bubble-wall interactions that will help to understand the complex phenomena of bubble rise in non-Newtonian media/microalgae suspensions at high concentrations at the local level in thin-gap bubble columns.
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薄间隙气泡柱内牛顿或非牛顿流体中孤立气泡上升的CFD模拟
当气泡间隙与气泡直径具有相同数量级时,气泡过程的流体力学是复杂的,特别是在薄气泡柱中。因此,通过阴影成像和/或粒子图像测速(PIV)等光学方法的实验研究或计算流体动力学(CFD)的数值研究来理解这一现象是很重要的,这些方法在经过验证后,可以在昂贵的实验或耗时的情况下进行数值实验。在这项研究中,三维数值模拟孤立气泡在牛顿(水)或非牛顿(羧甲基纤维素(CMC)和黄原胶(XG)溶液)液相中上升,模拟普通小球藻培养在42 g。采用流体体积(VOF)模型,利用ANSYS FLUENT 17.2软件对4 mm间隙气泡柱内的L−1浓度进行了计算。通过与阴影实验的对比,验证了结果的正确性。对气泡末端速度、形状和轨迹进行了数值分析。讨论了气泡引起的壁面剪应力、应变速率、黏度和气泡周围的流场。数值结果与实验结果相似,但末速度和展弦比值略低于实验结果。实验观察到,气泡的运动轨迹对水是非直线的,对非牛顿流体是非直线的。该数值研究强调了气泡-液体和气泡-壁的相互作用,这将有助于理解非牛顿介质/微藻悬浮液在薄间隙气泡柱局部高浓度下气泡上升的复杂现象。
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来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
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