NUMERICAL SIMULATION OF A SEMI-INDUSTRIAL SCALE CFB RISER USING COARSE-GRAINED DDPM-EMMS MODELLING

被引:22
作者
Adnan, Muhammad [1 ,2 ]
Zhang, Nan [1 ,2 ]
Sun, Fangfang [1 ,3 ]
Wang, Wei [1 ,2 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
[3] China Univ Min & Technol, Sch Resources & Safety Engn, Beijing 100083, Peoples R China
关键词
circulating fluidized bed; CFD; dense discrete phase model; coarse-grained simulation; CIRCULATING FLUIDIZED-BED; GAS-SOLID FLOWS; DISCRETE PARTICLE METHOD; EULERIAN SIMULATION; SUBGRID MODEL; GRANULAR FLOW; 2-PHASE FLOW; DRAG MODEL; TRANSPORT; COMBUSTION;
D O I
10.1002/cjce.23071
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, a coarse-grained Dense Discrete Phase Model (DDPM) coupled with the Energy-Minimization Multi-Scale (EMMS) drag, was used to simulate the hydrodynamics of a 3D semi-industrial scale Circulating Fluidized Bed (CFB) with Geldart A particles. The effect of particle numbers in a parcel, an important parameter in a coarse-grained approach, was investigated. It was found that when parcel diameter falls into the size range of clusters, simulation results are insensitive to particle number in a parcel and generally agree with the experimental data. Further, a comparison between DDPM and Eulerian Two-Fluid Modelling (TFM) approaches was investigated, both coupled with EMMS and conventional homogenous drag. The simulation results suggested that the effect of meso-scale structures on drag force needs to be considered in both modelling approaches.
引用
收藏
页码:1403 / 1416
页数:14
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