Numerical study of a lab-scale double slot-rectangular spouted bed with the parallel CFD-DEM coupling approach

被引:45
作者
Yang, Shiliang [1 ]
Luo, Kun [1 ]
Zhang, Ke [1 ]
Qiu, Kunzan [1 ]
Fan, Jianren [1 ]
机构
[1] Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Peoples R China
基金
中国国家自然科学基金;
关键词
Double slot-rectangular spouted bed; Discrete element method; Parallel computation; Hydrodynamics; Multiphase flow; DISCRETE PARTICLE SIMULATION; FLOW PATTERNS; HYDRODYNAMIC CHARACTERISTICS; FLUIDIZED-BED; DRAFT TUBE; DYNAMICS; TRANSITIONS; COMBUSTION; PYROLYSIS; POWDERS;
D O I
10.1016/j.powtec.2014.11.035
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The hydrodynamics of a three-dimensional double slot-rectangular spouted bed with two uniform chambers and two parallel slots are numerically studied by means of the parallel CFD-DEM coupling approach. In the coupling framework, the gas flow is described using the Navier-Stokes equations while the particles are tracked with the discrete element method. The start-up procedure and the typical flow structure of the system are explored in a microscopic view. Then, the distribution properties of the bed hydrodynamics are investigated. Moreover, the influence of turbulence model on gas-solid motion is discussed. Finally, the specialty of double slot-rectangular spouted bed is explored as compared with one chamber system. The results show that four distinct stages can be identified in the startup procedure. In the steady operation, the particles of each individual chamber of the bed interact with each other in the fountain region and the intensity initially increases and then decreases along the bed height. Excellently symmetrical properties can be obtained for the gas velocity, the voidage and the solid flux with a peak appearing in the central part of each individual chamber. Moreover, unequal size of the slot in the width and depth influences the distribution properties of these important parameters. The gas turbulent effect on the gas-solid motion is weak in the annulus region but explicit in the spout and fountain region. Five typical flow patterns can be observed in the double slot-rectangular spouted bed. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:85 / 99
页数:15
相关论文
共 43 条
[1]   Defluidization modelling of pyrolysis of plastics in a conical spouted bed reactor [J].
Aguado, R ;
Prieto, R ;
San José, MJ ;
Alvarez, S ;
Olazar, M ;
Bilbao, J .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2005, 44 (02) :231-235
[2]   Emissions from multiple-spouted and spout-fluid fluidized beds using rice husks as fuel [J].
Albina, D. O. .
RENEWABLE ENERGY, 2006, 31 (13) :2152-2163
[3]   Combustion of rice husk in a multiple-spouted fluidized bed [J].
Albina, DO .
ENERGY SOURCES, 2003, 25 (09) :893-904
[4]   Hot melt granulation of coarse pharmaceutical powders in a spouted bed [J].
Borini, G. B. ;
Andrade, T. C. ;
Freitas, Luis A. P. .
POWDER TECHNOLOGY, 2009, 189 (03) :520-527
[5]   Hydrodynamic study of fine metallic powders in an original spouted bed contactor in view of chemical vapor deposition treatments [J].
Caussat, Brigitte ;
Juarez, Fernando L. ;
Vahlas, Constantin .
POWDER TECHNOLOGY, 2006, 165 (02) :65-72
[6]  
Chen Z., 2008, STABILITY SCALE UP S
[7]   DISCRETE NUMERICAL-MODEL FOR GRANULAR ASSEMBLIES [J].
CUNDALL, PA ;
STRACK, ODL .
GEOTECHNIQUE, 1979, 29 (01) :47-65
[8]   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
[9]   Numerical Analysis of Solids Mixing in Pressurized Fluidized Beds [J].
Deen, Niels C. ;
Willem, Godlieb ;
Sander, Gorter ;
Kuipers, J. A. M. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (11) :5246-5253
[10]   Scale-up relationships of spouted beds by solid stress analyses [J].
Du, Wei ;
Xu, Jian ;
Ji, Ye ;
Wei, Weisheng ;
Bao, Xiaojun .
POWDER TECHNOLOGY, 2009, 192 (03) :273-278