Numerical Simulation of Mass-Transfer Characteristics of a Bubble Rising in Yield Stress Fluids

被引:12
|
作者
Cao, Baixu [1 ]
Fan, Jungeng [2 ]
Sun, Xuelin [1 ]
Li, Shaobai [1 ]
机构
[1] Shenyang Aerosp Univ, Coll Energy & Environm, Shenyang 110136, Liaoning, Peoples R China
[2] Northeastern Univ, Key Lab Natl Educ, Minist Electromagnet Proc Mat, Shenyang 110819, Liaoning, Peoples R China
来源
ACS OMEGA | 2020年 / 5卷 / 23期
基金
中国国家自然科学基金;
关键词
CARBON-DIOXIDE; TRANSFER COEFFICIENT; ABSORPTION; VISCOSITY; COLUMN; FLOW; HYDRODYNAMICS; MOTION; SIZE;
D O I
10.1021/acsomega.0c01265
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The mass-transfer characteristics of bubbles rising in yield stress fluids was investigated numerically using volume-of-fluid and user-defined function methods in this study. The CO2 concentration profiles inside the liquid phase near the bubble equator at different bubble diameters, yield stresses, consistency coefficients, and flow indices were observed. The results revealed that the rate of mass transfer decreased with the increase of yield stress, consistency coefficient, and flow index of the liquid phase and the decrease of bubble diameter. Moreover, two empirical correlations for the drag coefficients and Sherwood numbers were developed by introducing one correction factor X for C-D correlation and another correction factor f(c) for Sherwood numbers for correcting the influence of yield stress behavior on bubble motion and mass transfer, respectively. The predictions of the two correlations were compared with the simulated data, and a satisfactory agreement was found.
引用
收藏
页码:13878 / 13885
页数:8
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