Dispersion of immiscible liquids in a static mixer without inserted elements: A CFD-PBM study on droplet size reduction and distribution

A CFD-PBM (Computational Fluid Dynamics-Population Balance Model) coupled model has been employed to investigate the turbulent dispersion of immiscible liquids through a static swirl mixer without inserted elements, aiming to mitigate the disadvantages of existing static mixers, e.g., high energy consumption and maintenance costs. The model was firstly validated in a Kenics static mixer with experimental data of a benzene-water system with a benzene volume fraction of 0.5 % and empirical correlations, and was then used to evaluate the performance of the proposed static swirl mixer in pressure losses, Sauter mean diameter, droplet size distribution, effect of number of swirl sections, and PD (pitch to diameter) ratios. The static swirl mixer demonstrated a clear effect in the dispersion of immiscible benzene into water producing fine droplets, with its dispersive mixing efficiency being more pronounced in flows with higher Weber numbers. Its droplet size reduction effect is relatively less effective than the Kenics mixer for the same Weber numbers, attributed to the absence of inserted elements, but at the expense of a much lower pressure loss than the Kenics mixer. In producing the same droplet sizes, the static swirl mixers cause a lower pressure loss than the Kenics mixer to a certain extent depending on different the Weber numbers and PD ratios, demonstrating an energy-saving potential. A decreasing PD ratio produces smaller droplet sizes but at higher pressure losses. A PD ratio between 1.5 and 3 may be optimal. Ten swirl sections would appear to be sufficient to produce the equilibrium droplet size distribution despite the different PD ratios. • A novel static swirl mixer was applied to immiscible liquids dispersion. • The size reduction and droplet size distribution were evaluated by CFD-PBM method. • Correlations characterizing swirl mixer's dispersion performance were studied. • The energy-saving potential of the static swirl mixer was revealed.

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Publication Details

Journal
Powder Technology
Published
2024-12-12
DOI
https://doi.org/10.1016/j.powtec.2024.120547
Citations
5
Primary Topic
Fluid Dynamics and Mixing
Type
article
Field-Weighted Citation Impact
0.92
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Dispersion of immiscible liquids in a static mixer without inserted elements: A CFD-PBM study on droplet size reduction and distribution

J. L. Gao, Guozhen Li, Zheng Wang, N.J. Miles et al.
5 citations
Powder Technology
Fluid Dynamics and Mixing
0.92
article

Dispersion of immiscible liquids in a static mixer without inserted elements: A CFD-PBM study on droplet size reduction and distribution

J. L. Gao, Guozhen Li, Zheng Wang, N.J. Miles, Philip Hall, Yubang Shen
article en
5 citations

Abstract

A CFD-PBM (Computational Fluid Dynamics-Population Balance Model) coupled model has been employed to investigate the turbulent dispersion of immiscible liquids through a static swirl mixer without inserted elements, aiming to mitigate the disadvantages of existing static mixers, e.g., high energy consumption and maintenance costs. The model was firstly validated in a Kenics static mixer with experimental data of a benzene-water system with a benzene volume fraction of 0.5 % and empirical correlations, and was then used to evaluate the performance of the proposed static swirl mixer in pressure losses, Sauter mean diameter, droplet size distribution, effect of number of swirl sections, and PD (pitch to diameter) ratios. The static swirl mixer demonstrated a clear effect in the dispersion of immiscible benzene into water producing fine droplets, with its dispersive mixing efficiency being more pronounced in flows with higher Weber numbers. Its droplet size reduction effect is relatively less effective than the Kenics mixer for the same Weber numbers, attributed to the absence of inserted elements, but at the expense of a much lower pressure loss than the Kenics mixer. In producing the same droplet sizes, the static swirl mixers cause a lower pressure loss than the Kenics mixer to a certain extent depending on different the Weber numbers and PD ratios, demonstrating an energy-saving potential. A decreasing PD ratio produces smaller droplet sizes but at higher pressure losses. A PD ratio between 1.5 and 3 may be optimal. Ten swirl sections would appear to be sufficient to produce the equilibrium droplet size distribution despite the different PD ratios. • A novel static swirl mixer was applied to immiscible liquids dispersion. • The size reduction and droplet size distribution were evaluated by CFD-PBM method. • Correlations characterizing swirl mixer's dispersion performance were studied. • The energy-saving potential of the static swirl mixer was revealed.

Powder TechnologyVol. 452
University of Nottingham Ningbo China (CN)
Openalex Percentile: Top 27%
Fluid Dynamics and Mixing
0.92
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