Regulatory Mechanisms of Particle Dynamics and Deposition Distribution in Bend Pipes with Curvature Ratio

Curvature ratio (δ) governs secondary flows in gas–solid two-phase flow through bends, thereby affecting particle dynamics and leading to non-uniform wall deposition and increased erosion risk. In this study, a coupled Reynolds stress model (RSM) and Discrete phase model (DPM) framework was employed. A wall contact model incorporating adhesion, rebound, and removal mechanisms was implemented via a User-Defined Function (UDF). The spatial distribution and deposition characteristics of particles with different inertia (Stokes number range: 0.020 ≤ St ≤ 30.176) were systematically investigated in the range of δ = 2.0~3.5. The results reveal a distinct inertial dependence in particle spatial distribution: particles with St < 1 exhibit a “high-dispersion, weak-aggregation” pattern, whereas those with St > 1 form an “outer-wall agglomeration, inner-wall cavity” characteristic. As δ increases, the secondary flow intensity decreases while the effective centrifugal path lengthens. Governed by the combined effects of the effective collision coefficient (Rc) and effective adhesion rate (ηa), particle deposition is inhibited for St < 1 but enhanced for St > 1. This study advances the understanding of deposition under geometric constraints and provides a basis for optimizing pipeline design.

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Publication Details

Journal
Processes
Published
2026-04-15
DOI
https://doi.org/10.3390/pr14081261
Primary Topic
Particle Dynamics in Fluid Flows
Type
article
Field-Weighted Citation Impact
0.00

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article

Regulatory Mechanisms of Particle Dynamics and Deposition Distribution in Bend Pipes with Curvature Ratio

Yuqin Xiao, Tianyu Gong, Xuan Tang, Zhenhai Liu et al.
Processes
Particle Dynamics in Fluid Flows
article

Regulatory Mechanisms of Particle Dynamics and Deposition Distribution in Bend Pipes with Curvature Ratio

Yuqin Xiao, Tianyu Gong, Xuan Tang, Zhenhai Liu, Youhang Zhou, Ding Li
article en

Abstract

Curvature ratio (δ) governs secondary flows in gas–solid two-phase flow through bends, thereby affecting particle dynamics and leading to non-uniform wall deposition and increased erosion risk. In this study, a coupled Reynolds stress model (RSM) and Discrete phase model (DPM) framework was employed. A wall contact model incorporating adhesion, rebound, and removal mechanisms was implemented via a User-Defined Function (UDF). The spatial distribution and deposition characteristics of particles with different inertia (Stokes number range: 0.020 ≤ St ≤ 30.176) were systematically investigated in the range of δ = 2.0~3.5. The results reveal a distinct inertial dependence in particle spatial distribution: particles with St < 1 exhibit a “high-dispersion, weak-aggregation” pattern, whereas those with St > 1 form an “outer-wall agglomeration, inner-wall cavity” characteristic. As δ increases, the secondary flow intensity decreases while the effective centrifugal path lengthens. Governed by the combined effects of the effective collision coefficient (Rc) and effective adhesion rate (ηa), particle deposition is inhibited for St < 1 but enhanced for St > 1. This study advances the understanding of deposition under geometric constraints and provides a basis for optimizing pipeline design.

ProcessesVol. 14(8)
Xiangtan University (CN)
National Natural Science Foundation of China, Hunan Provincial Innovation Foundation for Postgraduate
Openalex Percentile: Top 13%
Particle Dynamics in Fluid Flows
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