Novel Close-Clearance Impeller Structure for Solid–Liquid Mixing at Low Reynolds Numbers Based on the Paravisc Impeller

This paper presents an enhancement for Paravisc impellers, commonly used for low-Reynolds-number solid–liquid mixing. The design of the new impellers is based on chaos theory and presents an asymmetrically curved structure. Two new impellers, PVS and PVW, are designed, and their multiphase mixing processes are simulated using CFD–DEM models. The new impellers were found to be more advantageous for particle dispersion and suspension at low Reynolds numbers (Re= 92). The PVW was observed to suspend 70.2% more particles than PV under the simulated conditions, and the energy spent on suspending particles was reduced by 36.9%. The change in distance of particle pairs in the flow field is quantified, resulting in an increase of 76.8% in the particle mixing efficiency of PVW. This indicates a more homogeneous dispersion of solid-phase particles in the flow field.

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Publication Details

Journal
Industrial & Engineering Chemistry Research
Published
2024-08-21
DOI
https://doi.org/10.1021/acs.iecr.4c02001
Citations
4
Primary Topic
Granular flow and fluidized beds
Type
article
Field-Weighted Citation Impact
1.50

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article

Novel Close-Clearance Impeller Structure for Solid–Liquid Mixing at Low Reynolds Numbers Based on the Paravisc Impeller

Jingtao Wang, Yang Jiao, Fan Bu
4 citations
Industrial & Engineering Chemistry Research
Granular flow and fluidized beds
1.50
article

Novel Close-Clearance Impeller Structure for Solid–Liquid Mixing at Low Reynolds Numbers Based on the Paravisc Impeller

Jingtao Wang, Yang Jiao, Fan Bu
article en
4 citations

Abstract

This paper presents an enhancement for Paravisc impellers, commonly used for low-Reynolds-number solid–liquid mixing. The design of the new impellers is based on chaos theory and presents an asymmetrically curved structure. Two new impellers, PVS and PVW, are designed, and their multiphase mixing processes are simulated using CFD–DEM models. The new impellers were found to be more advantageous for particle dispersion and suspension at low Reynolds numbers (Re= 92). The PVW was observed to suspend 70.2% more particles than PV under the simulated conditions, and the energy spent on suspending particles was reduced by 36.9%. The change in distance of particle pairs in the flow field is quantified, resulting in an increase of 76.8% in the particle mixing efficiency of PVW. This indicates a more homogeneous dispersion of solid-phase particles in the flow field.

Industrial & Engineering Chemistry ResearchVol. 63(35)
Tianjin University (CN)
National Natural Science Foundation of China, National Key Research and Development Program of China
Openalex Percentile: Top 21%
Granular flow and fluidized beds
1.50
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