A theoretical model for bubble coalescence by coupling film drainage with approach processes

被引:12
作者
Gong, Shenggao [1 ,2 ]
Gao, Ningning [1 ]
Han, Luchang [2 ]
Luo, He'an [2 ]
机构
[1] Hunan Inst Technol, Sch Mat & Chem Engn, Hengyang 421002, Hunan, Peoples R China
[2] Xiangtan Univ, Sch Chem Engn, Xiangtan 411105, Hunan, Peoples R China
基金
中国国家自然科学基金;
关键词
Bubble coalescence; Critical coalescence velocity; Film drainage; Approach; Turbulence; INTERFACIAL AREA TRANSPORT; POPULATION BALANCE MODEL; MASS-TRANSFER; STABILITY CONDITION; REGIME TRANSITION; APPROACH VELOCITY; DROPLET BREAKAGE; ENERGY-SPECTRUM; TURBULENCE; FLOW;
D O I
10.1016/j.ces.2019.115387
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An improved theoretical model for simulating bubble coalescence caused by turbulence was developed. Unlike the previous models, this improved model simulated the film drainage and approach processes between two bubbles simultaneously in the condition of fully mobile interfaces, considering the influence of the variation of approach velocity, film thickness, film area/radius and interaction forces etc. with time on the bubble coalescence. The lubrication form drag force caused by flattening of colliding surface was introduced to model the approach process. The initial film thickness and radius required for film drainage process were estimated by the expressions validated by experimental data. The critical coalescence velocities for determining coalescence predicted by the improved model were consistent with available experimental data. Moreover, the proposed improved model was used to predict the size distribution in a bubble column, and a good agreement between simulated and experimental results was obtained. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页数:20
相关论文
共 73 条
[1]   A comprehensive CFD study on the effect of dense vertical internals on the hydrodynamics and population balance model in bubble columns [J].
Agahzamin, Siamak ;
Pakzad, Leila .
CHEMICAL ENGINEERING SCIENCE, 2019, 193 :421-435
[2]   Numerical modeling of drop coalescence in the presence of soluble surfactants [J].
Bazhlekov, I. ;
Vasileva, D. .
JOURNAL OF COMPUTATIONAL AND APPLIED MATHEMATICS, 2016, 293 :7-19
[3]   A new model for estimation of drag force in the flow of Newtonian fluids around rigid or deformable particles [J].
Ceylan, K ;
Altunbas, A ;
Kelbaliyev, G .
POWDER TECHNOLOGY, 2001, 119 (2-3) :250-256
[4]   Mesoscale modeling of emulsification in rotor-stator devices Part I: A population balance model based on EMMS concept [J].
Chen, Chao ;
Guan, Xiaoping ;
Ren, Ying ;
Yang, Ning ;
Li, Jinghai ;
Kunkelmann, Christian ;
Schreiner, Eduard ;
Holtze, Christian ;
Muelheims, Kerstin ;
Sachweh, Bernd .
CHEMICAL ENGINEERING SCIENCE, 2019, 193 :171-183
[5]   COALESCENCE TIME FOR A SMALL DROP OR BUBBLE AT A FLUID-FLUID INTERFACE [J].
CHEN, JD ;
HAHN, PS ;
SLATTERY, JC .
AICHE JOURNAL, 1984, 30 (04) :622-630
[6]   Three-dimensional simulation of bubble column flows with bubble coalescence and breakup [J].
Chen, P ;
Dudukovic, MP ;
Sanyal, J .
AICHE JOURNAL, 2005, 51 (03) :696-712
[7]  
Chesters A. K., 1975, International Journal of Multiphase Flow, V2, P191, DOI 10.1016/0301-9322(75)90008-7
[8]   Effect of insoluble surfactants on drainage and rupture of a film between drops interacting under a constant force [J].
Chesters, AK ;
Bazhlekov, IB .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2000, 230 (02) :229-243
[9]   BUBBLE COALESCENCE IN PURE LIQUIDS [J].
CHESTERS, AK ;
HOFMAN, G .
APPLIED SCIENTIFIC RESEARCH, 1982, 38 :353-361
[10]   Modeling of bubble size distribution in isothermal gas-liquid flows: Numerical assessment of population balance approaches [J].
Cheung, S. C. P. ;
Deju, L. ;
Yeoh, G. H. ;
Tu, J. Y. .
NUCLEAR ENGINEERING AND DESIGN, 2013, 265 :120-136