Hydrodynamics of polydisperse gas-solid flows: Kinetic theory and multifluid simulation

被引:1
作者
Zhao, Bidan [1 ,2 ]
Shi, Kun [1 ,3 ]
He, Mingming [1 ,2 ]
Wang, Junwu [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, POB 353, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Sch Chem Engn, Beijing 100049, Peoples R China
[3] Shenyang Univ Chem Technol, Sch Chem Engn, Shenyang 110142, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
Kinetic theory; Polydispersity; Multiphase flow; Multifluid model; Constitutive relation; Granular flow; PARTICLE-SIZE DISTRIBUTION; BUBBLING FLUIDIZED-BEDS; EMMS DRAG MODEL; GRANULAR MIXTURES; BINARY-MIXTURE; SEGREGATION; DISPERSE; PERFORMANCE; DERIVATION; EQUATIONS;
D O I
10.1016/j.ces.2024.119740
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Polydisperse gas -solid flows, which is notoriously difficult to model due to the complex gas -particle and particleparticle interactions, are widely encountered in industry. In this article, a refined kinetic theory for polydisperse flow is developed, which features single -parameter Chapman-Enskog expansion (the Knudsen number) and exact calculation of the integrations related to pair distribution function of particle velocity without any mathematical approximations. The Navier-Stokes order constitutive relations for multifluid modeling of polydisperse gas -solid flow are then obtained analytically, including the solid stress tensor, the solid -solid drag force, the granular heat flux and the energy dissipation rate. Finally, the model is preliminarily validated by comparing to the discrete element simulation data of one-dimensional granular shear flow and by showing that the hydrodynamic characteristics of gas -solid flows in a bubbling fluidized bed containing bidisperse particles can be successfully predicted.
引用
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页数:22
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