Large-scale CFD-DEM simulations of fluidized granular systems

被引:205
作者
Jajcevic, Dalibor [1 ]
Siegmann, Eva [1 ]
Radeke, Charles [1 ]
Khinast, Johannes G. [1 ,2 ]
机构
[1] Res Ctr Pharmaceut Engn GmbH, Graz, Austria
[2] Graz Univ Technol, Inst Proc & Particle Engn, Graz, Austria
关键词
Computational fluid dynamics; Discrete element modeling; CFD-DEM; Multiphase flow; Fluidization; Granular flow; DISCRETE PARTICLE SIMULATION; MODEL FORMULATIONS; FLOW; RISER; MIXER; VALIDATION; DYNAMICS; SOLIDS; BEDS;
D O I
10.1016/j.ces.2013.05.014
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The combination of Computational Fluid Dynamics (CFD) and Discrete Element Model (DEM) is a powerful tool for studying fluidized particulate systems and granular flows. In DEM, the individual interaction forces between particles are treated on a particle particle pair basis, and therefore, this method is computational expensive. In addition, the CFD-calculation of the fluid flow increases the computational effort. Thus, current CFD-DEM simulations are limited to systems with particle numbers not exceeding 10(5). In order to simulate realistic systems, the recently available Compute Unified Device Architecture (CUDA) technology can be applied, which can perform massively-parallel DEM-simulations with several million particles on a single desk-side Graphics Processing Unit (GPU). The objective of this work is to present a new hybrid approach to solve CFD-DEM problems in gas solid fluidized beds systems applying an efficient coupling method suitable for large-scale simulations. We are using the CUDA technology for the particle simulation and introducing a coupling methodology with a commercial CFD-code. The coupling method between a CFD-code, running on the CPU and our CUDA-based DEM-code running on the GPU, is introduced and discussed. The numerical results are compared to the CFD-DEM and the experimental results of Van Buijtenen et al. (2011). A good agreement was achieved. Finally, fluidized system simulations with up to 25 million particles are presented, which is an unprecented number. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:298 / 310
页数:13
相关论文
共 41 条
[21]   Characterization of granular flow of wet solids in a bladed mixer [J].
Lekhal, Azzeddine ;
Conway, Stephen L. ;
Glasser, Benjamin J. ;
Khinast, Johannes G. .
AICHE JOURNAL, 2006, 52 (08) :2757-2766
[22]   MP-PIC simulation of CFB riser with EMMS-based drag model [J].
Li, Fei ;
Song, Feifei ;
Benyahia, Sofiane ;
Wang, Wei ;
Li, Jinghai .
CHEMICAL ENGINEERING SCIENCE, 2012, 82 :104-113
[23]  
Link J, 2004, CAN J CHEM ENG, V82, P30
[24]   Hydrodynamics of binary fluidization in a riser: CFD simulation using two granular temperatures [J].
Lu, HL ;
Gidaspow, D .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (16) :3777-3792
[25]   Particle simulation of vibrated gas-fluidized beds of cohesive fine powders [J].
Moon, Sung Joon ;
Kevrekidis, I. G. ;
Sundaresan, S. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (21) :6966-6977
[26]   CFD-DEM study and direct measurement of the granular flow in a rotor granulator [J].
Neuwirth, Johannes ;
Antonyuk, Sergiy ;
Heinrich, Stefan ;
Jacob, Michael .
CHEMICAL ENGINEERING SCIENCE, 2013, 86 :151-163
[27]   Numerical analysis of the dynamics of two- and three-dimensional fluidized bed reactors using an Euler-Lagrange approach [J].
Pepiot, Perrine ;
Desjardins, Olivier .
POWDER TECHNOLOGY, 2012, 220 :104-121
[28]   Large-scale powder mixer simulations using massively parallel GPU architectures [J].
Radeke, Charles A. ;
Glasser, Benjamin J. ;
Khinast, Johannes G. .
CHEMICAL ENGINEERING SCIENCE, 2010, 65 (24) :6435-6442
[29]   Experiments and simulations of cohesionless particles with varying roughness in a bladed mixer [J].
Remy, Brenda ;
Canty, Thomas M. ;
Khinast, Johannes G. ;
Glasser, Benjamin J. .
CHEMICAL ENGINEERING SCIENCE, 2010, 65 (16) :4557-4571
[30]   The Effect of Mixer Properties and Fill Level on Granular Flow in a Bladed Mixer [J].
Remy, Brenda ;
Glasser, Benjamin J. ;
Khinast, Johannes G. .
AICHE JOURNAL, 2010, 56 (02) :336-353