Bubble's rise characteristics in shear-thinning xanthan gum solution: a numerical analysis

被引:10
|
作者
Islam, Md. Tariqul [1 ,2 ]
Nguyen, Anh V. [1 ,2 ]
Afzal, Asif [3 ,4 ]
机构
[1] Univ Queensland, Sch Chem Engn, Brisbane, Qld 4072, Australia
[2] Univ Newcastle, ARC Ctr Excellence Enabling Ecoefficient Benefici, Sch Engn, Callaghan, NSW 2308, Australia
[3] Visvesvaraya Technol Univ, PA Coll Engn, Dept Mech Engn, Mangalore 574153, India
[4] Glocal Univ, Sch Technol, Dept Mech Engn, Delhi Yamunotri Marg,SH 57,Mirzapur Pole, Saharanpur 247121, Uttar Pradesh, India
基金
澳大利亚研究理事会;
关键词
Bubble; Terminal velocity; Xanthan gum; Liquid velocity; Viscosity; LEVEL SET APPROACH; RHEOLOGICAL PROPERTIES; RISING BEHAVIOR; SIMULATION; FLUID; FLOW; COALESCENCE; DYNAMICS; MOTION; VOLUME;
D O I
10.1016/j.jtice.2022.104219
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Background: The rise of gaseous bubbles in shear-thinning liquid is a fundamental issue in fluid physics, particularly the bubbles rise dynamics in water-soluble xanthan gum concentration have a strong link for enhancing the stability of foams that have been encountered extensively in oil recovery, methane hydrate formation processing, froth flotation, and food and beverage industries.Methods: Here, air bubble rise behavior in xanthan gum solution (XGs) was investigated by using a coupled volume of fluid with the level set approach in CFD (computational fluid dynamics) modelling. The CarreauYasuda rheological model was adopted to define the viscous properties of the XGs and the continuum surface force model was used to track the interface between bubble and XGs. Additionally, ANN (artificial neural network) modeling was demonstrated for estimating the outputs of CFD. Our estimated CFD results for different bubble terminal velocities in water and experimental data obtained from the literature showed that there was a maximum relative error of 4.51%. Then, the CFD setup was utilized to investigate the effect of different concentrations of XGs and liquid flow index (N) on bubble rise dynamics within the bubble Reynolds number (Reb) range up to 10.05 and Eotvos number (Eo) range up to 3.47.Significant findings: For a fixed bubble size, the dimensionless bubble terminal velocity decreased in increased flow index and concentration of XGs, which led to decrease Reb and increase Eo. For a given XGs, the dimensionless bubble terminal velocity significantly depends on Reb and Eo. It was found that XGs and flow index significantly affect the distribution of dimensionless liquid viscosity than that of the dimensionless liquid velocity close to the bubble's underneath region. In a comparison with the rheological power-law model, the Carreau-Yasuda model showed to predict more accurate results. The estimated drag coefficient showed a deviation from the empirical equation reported in the literature, in contrast, a more accurate estimation in drag coefficient was obtained based on modified Reynolds number and Archimedes number. ANN modelling outputs agreed with CFD results and indicated that the training and testing of ANN have great efficiency to predict unknown values. (c) 2022 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
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页数:14
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