An overlappable coarsening strategy for discrete element method simulations of bi-disperse granular flows

被引:0
作者
Yu, Yaxiong [1 ]
Duan, Fan [2 ]
Wang, Lingxue [2 ]
Zhou, Qiang [2 ]
机构
[1] Cent South Univ, Sch Energy Sci & Engn, Changsha 410083, Hunan, Peoples R China
[2] Xi An Jiao Tong Univ, Sch Chem Engn & Technol, Xian 710049, Peoples R China
基金
中国国家自然科学基金;
关键词
Bi-disperse granular flows; Fluidized bed; CFD-DEM; Coarse-graining; DEM; VALIDATION; DYNAMICS; MODEL;
D O I
10.1016/j.powtec.2025.120765
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The coarsening strategy provides a promising avenue for industrial applications of the discrete element method by profoundly reducing computational costs. However, its application in multi-particle-size systems often results in underestimations of the packing solid volume fraction when employing different coarsening ratios. To address this issue, we propose a novel overlappable coarse-grained model specifically designed for bi-disperse systems. In this model, particles are allowed to overlap to a certain extent without experiencing collision forces, with the degree of overlapping described by an overlapping coefficient. This coefficient is determined through fitting discrete element method simulation of bi-disperse packings. Posterior analyses reveal that the traditional coarse- grained discrete element method significantly underpredicts the packing solid volume fraction and consequently the segregation behavior. In contrast, our proposed overlappable coarsening strategy accurately predicts both the packing solid volume fraction and segregation behavior when employing the fitted overlapping coefficient.
引用
收藏
页数:12
相关论文
共 39 条
[1]   Progress in CFD Simulations of Fluidized Beds for Chemical and Energy Process Engineering [J].
Alobaid, Falah ;
Almohammed, Naser ;
Farid, Massoud Massoudi ;
May, Jan ;
Rossger, Philip ;
Richter, Andreas ;
Epple, Bernd .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2022, 91
[2]   RAPID GRANULAR FLOWS [J].
CAMPBELL, CS .
ANNUAL REVIEW OF FLUID MECHANICS, 1990, 22 :57-92
[3]   Evaluation of particle packing models by comparing with published test results [J].
Chan, K. W. ;
Kwan, A. K. H. .
PARTICUOLOGY, 2014, 16 :108-115
[4]   Investigation of Void Fraction Schemes for Use with CFD-DEM Simulations of Fluidized Beds [J].
Clarke, Daniel A. ;
Sederman, Andrew J. ;
Gladden, Lynn F. ;
Holland, Daniel J. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (08) :3002-3013
[5]   Review of discrete particle modeling of fluidized beds [J].
Deen, N. G. ;
Annaland, M. Van Sint ;
Van der Hoef, M. A. ;
Kuipers, J. A. M. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) :28-44
[6]  
Fan L.S., 1999, Principles of Gas-Solid Flows
[7]  
Gidaspow D., 1994, MULTIPHASE FLOW FLUI
[8]   Digital image analysis measurements of bed expansion and segregation dynamics in dense gas-fluidised beds [J].
Goldschmidt, MJV ;
Link, JM ;
Mellema, S ;
Kuipers, JAM .
POWDER TECHNOLOGY, 2003, 138 (2-3) :135-159
[9]  
He X., 2024, Int. J. Fluid Eng., V1
[10]   A revised coarse-graining approach for simulation of highly poly-disperse granular flows [J].
Kanjilal, Suranita ;
Schneiderbauer, Simon .
POWDER TECHNOLOGY, 2021, 385 :517-527