DEM-CFD simulation of a dense fluidized bed: Wall boundary and particle size effects

被引:34
作者
Gupta, Prashant [1 ]
Sun, J. [1 ]
Ooi, J. Y. [1 ]
机构
[1] Univ Edinburgh, Sch Engn, Edinburgh EH9 3JL, Midlothian, Scotland
关键词
DEM-CFD; Fluidization; PARDEM; Particle-wall interaction; DISCRETE ELEMENT MODEL; MAGNETIC-RESONANCE MEASUREMENTS; PRESSURE FLUCTUATION; GRANULAR TEMPERATURE; FLOWS;
D O I
10.1016/j.powtec.2015.11.050
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
We simulate a small-scale dense gas solid fluidized bed using an approach coupling the averaged Navier-Stokes equation with a discrete description of particle dynamics. The simulation results are compared to the voidage, solid velocity and granular temperature measured using magnetic resonance (MR), and other experimental measurements for the same fluidized bed. It is found that the simulation is able to predict the minimum fluidization velocity and pressure drop with reasonable agreement and qualitatively capture the solid circulation pattern to a similar degree achieved by previous such simulations. The discrepancies for the solid velocities near the walls and in the central region at upper and lower bed heights were investigated by examining various models of the physical system and the sensitivity of the simulation results to these models. We demonstrate that the particle wall interaction dominates the particle dynamics in a boundary layer of about 5 particle diameters to the wall and that modeling the wall using fixed particle of comparable size to the fluidized particles provides enhanced resistance reducing solid wall-slip velocity and granular temperature at the boundary layer. Modeling of particle size is shown to be important for capturing the variation of bed dynamics along the bed height direction. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:37 / 47
页数:11
相关论文
共 34 条
[1]
A FLUID MECHANICAL DESCRIPTION OF FLUIDIZED BEDS [J].
ANDERSON, TB ;
JACKSON, R .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (04) :527-&
[2]
Characterization of gas fluidized beds of group C, A and B particles based on pressure fluctuations [J].
Bai, DR ;
Grace, JR ;
Zhu, JX .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (02) :319-324
[3]
Drag force of intermediate Reynolds number flow past mono- and bidisperse arrays of spheres [J].
Beetstra, R. ;
van der Hoef, M. A. ;
Kuipers, J. A. M. .
AICHE JOURNAL, 2007, 53 (02) :489-501
[4]
The origin of pressure oscillations in slugging fluidized beds: Comparison of experimental results from magnetic resonance imaging with a discrete element model [J].
Boyce, C. M. ;
Davidson, J. F. ;
Holland, D. J. ;
Scott, S. A. ;
Dennis, J. S. .
CHEMICAL ENGINEERING SCIENCE, 2014, 116 :611-622
[5]
Adapting Data Processing To Compare Model and Experiment Accurately: A Discrete Element Model and Magnetic Resonance Measurements of a 3D Cylindrical Fluidized Bed [J].
Boyce, Christopher M. ;
Holland, Daniel J. ;
Scott, Stuart A. ;
Dennis, John S. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (50) :18085-18094
[6]
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
[7]
Ergun Sabri., 1952, Chem. Eng. Prog, P48
[8]
Shear strength and force transmission in granular media with rolling resistance [J].
Estrada, Nicolas ;
Taboada, Alfredo ;
Radjai, Farhang .
PHYSICAL REVIEW E, 2008, 78 (02)
[9]
Time series analysis of pressure fluctuation in gas-solid fluidized beds [J].
Felipe, CAS ;
Rocha, SCS .
BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, 2004, 21 (03) :497-507
[10]
Microdynamic modelling and analysis of the mixing and segregation of binary mixtures of particles in gas fluidization [J].
Feng, Y. Q. ;
Yu, A. B. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) :256-268