External mass transfer from/to a single sphere in a nonlinear uniaxial extensional creeping flow
Fluid Dynamics and Transport Phenomena|Updated:2026-01-06
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External mass transfer from/to a single sphere in a nonlinear uniaxial extensional creeping flow
External mass transfer from/to a single sphere in a nonlinear uniaxial extensional creeping flow
中国化学工程学报(英文版)2022年41卷第1期 页码:230-245
Affiliations:
1. Qilu University of Technology (Shandong Academy of Sciences), Shandong Computer Science Center(National Supercomputer Center in Jinan),Jinan,China,250101
2. CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences,Beijing,China,100190
3. School of Chemical Engineering, University of Chinese Academy of Sciences,Beijing,China,100049
4. Department of Chemical Engineering, Shenkar College of Engineering and Design, Ramat-Gan, 5252626,Israel
5. Dynamic Machinery Institute of Inner Mongolia,Inner Mongolia,Hohhot,China,010010
Author bio:
Funds:
DOI:
中图分类号:
纸质出版:2022
Accepted:
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Anjun Liu, Jie Chen, Moshe Favelukis, 等. External mass transfer from/to a single sphere in a nonlinear uniaxial extensional creeping flow[J]. 中国化学工程学报(英文版), 2022,41(1):230-245.
Anjun Liu, Jie Chen, Moshe Favelukis, Meng Guo, Meihong Yang, Chao Yang, Tao Zhang, Min Wang, Hao-yue Quan. External mass transfer from/to a single sphere in a nonlinear uniaxial extensional creeping flow[J]. Chinese Journal of Chemical Engineering, 2022, 41(1): 230-245.
Anjun Liu, Jie Chen, Moshe Favelukis, 等. External mass transfer from/to a single sphere in a nonlinear uniaxial extensional creeping flow[J]. 中国化学工程学报(英文版), 2022,41(1):230-245.DOI:
Anjun Liu, Jie Chen, Moshe Favelukis, Meng Guo, Meihong Yang, Chao Yang, Tao Zhang, Min Wang, Hao-yue Quan. External mass transfer from/to a single sphere in a nonlinear uniaxial extensional creeping flow[J]. Chinese Journal of Chemical Engineering, 2022, 41(1): 230-245.DOI:
External mass transfer from/to a single sphere in a nonlinear uniaxial extensional creeping flow
This work systematically simulates the external mass transfer from/to a spherical drop and solid particle suspended in a nonlinear uniaxial extensional creeping flow. The mass transfer problem is governed by three dimensionless parameters: the viscosity ratio (
λ
)
the Peclet number (
Pe
)
and the nonlinear intensity of the flow (
E
). The existing mass transfer theory
valid for very large Peclet numbers only
is expanded
by numerical simulations
to include a much larger range of Peclet numbers (1 ≤
Pe
≤ 10
5
). The simulation results show that the dimensionless mass transfer rate
expressed as the Sherwood number (
Sh
)
agrees well with the theoretical results at the convection-dominated regime (
Pe
10
3
). Only when
E
5/4
the simulated
Sh
for a solid sphere in the nonlinear uniaxial extensional flow is larger than theoretical results because the theory neglects the effect of the vortex formed outside the particle on the rate of mass transfer. Empirical correlations are proposed to predict the influence of the dimensionless governing parameters (
λ
Pe
E
) on the Sherwood number (
Sh
). The
maximum deviations of all empirical correlations are less than 15% when compared to the numerical simulated results.
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