CFD-PBM Coupled with Dynamic Interfacial Tension Model for Simulating Liquid–Liquid Two-Phase Flow and Interphase Mass Transfer in a Pulsed Column

Computational fluid dynamics (CFD) simulation has proven to be a powerful tool in studying the two-phase flow. The dynamic change of interfacial tension under mass transfer conditions has a significant influence on the accuracy of the simulation, yet it has never been considered in previous study because of the lack of experimental data on dynamic interfacial tension (DIFT). In this study, the DIFT model from previous work (Wang et al., AIChE J. 2024; e18411) is incorporated into the CFD-population balance model simulation to simulate two-phase flow in a pulsed column under conditions of mass transfer. Simulation results, including the cumulative droplet size distribution (Q3) and solute concentration in two phases, are in good agreement with experimental results, demonstrating the necessity of the DIFT model. As height decreases, it is found that the reduction in mass transfer flux and solute concentration, leading to an increase in DIFT, is the reason for the decrease in droplet breakup frequency.

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Publication Details

Journal
Industrial & Engineering Chemistry Research
Published
2025-02-26
DOI
https://doi.org/10.1021/acs.iecr.4c04317
Citations
2
Primary Topic
Fluid Dynamics and Mixing
Type
article
Field-Weighted Citation Impact
1.35
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article

CFD-PBM Coupled with Dynamic Interfacial Tension Model for Simulating Liquid–Liquid Two-Phase Flow and Interphase Mass Transfer in a Pulsed Column

Bo Wang, Wenjie Lan, Xiong Bill Yu, Han Zhou et al.
2 citations
Industrial & Engineering Chemistry Research
Fluid Dynamics and Mixing
1.35
article

CFD-PBM Coupled with Dynamic Interfacial Tension Model for Simulating Liquid–Liquid Two-Phase Flow and Interphase Mass Transfer in a Pulsed Column

Bo Wang, Wenjie Lan, Xiong Bill Yu, Han Zhou, Shan Jing, Shaowei Li, Qiang Zheng
article en
2 citations

Abstract

Computational fluid dynamics (CFD) simulation has proven to be a powerful tool in studying the two-phase flow. The dynamic change of interfacial tension under mass transfer conditions has a significant influence on the accuracy of the simulation, yet it has never been considered in previous study because of the lack of experimental data on dynamic interfacial tension (DIFT). In this study, the DIFT model from previous work (Wang et al., AIChE J. 2024; e18411) is incorporated into the CFD-population balance model simulation to simulate two-phase flow in a pulsed column under conditions of mass transfer. Simulation results, including the cumulative droplet size distribution (Q3) and solute concentration in two phases, are in good agreement with experimental results, demonstrating the necessity of the DIFT model. As height decreases, it is found that the reduction in mass transfer flux and solute concentration, leading to an increase in DIFT, is the reason for the decrease in droplet breakup frequency.

Industrial & Engineering Chemistry ResearchVol. 64(10)
China University of Petroleum, Beijing (CN), State Key Laboratory of Chemical Engineering (CN), State Key Laboratory of Heavy Oil (CN), Tsinghua University (CN)
Affordable and clean energy
Openalex Percentile: Top 22%
Fluid Dynamics and Mixing
1.35
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