Numerical prediction of flow hydrodynamics of wet molecular sieve particles in a liquid-fluidized bed

被引:6
作者
Liu, Guodong [1 ,2 ]
Wang, Peng [1 ]
Lu, Huilin [2 ]
Yu, Fan [2 ]
Zhang, Yanan [2 ]
Wang, Shuai [2 ]
Sun, Liyan [2 ]
机构
[1] Harbin Inst Technol, Sch Municipal & Environm Engn, Harbin 150001, Peoples R China
[2] Harbin Inst Technol, Sch Energy Sci & Engn, 92 West Dazhi St, Harbin 150001, Peoples R China
来源
PARTICUOLOGY | 2016年 / 25卷
基金
中国国家自然科学基金;
关键词
Liquid-solid fluidized bed; Wet particle collision; Kinetic theory of granular flow; Restitution coefficient; CFD; SUSPENSIONS; DYNAMICS; VELOCITY; SEDIMENTATION; SIMULATIONS; PRESSURE; MOTION; RISER;
D O I
10.1016/j.partic.2015.01.010
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The Eulerian-Eulerian framework was used in the numerical simulation of liquid hydrodynamics and particle motion in liquid-fluidized beds. The kinetic theory of granular flow, which accounts for the viscous drag influence on the interstitial liquid phase, was used in combination with two-fluid models to simulate unsteady liquid-solid two-phase flows. We focus on local unsteady features predicted by the numerical models. The solid fraction power spectrum was analyzed. A typical flow pattern, such as core annular flow and particle back-mixing near the wall region of liquid-solid fluidized beds is obtained from this calculation. Effects of the restitution coefficient of particle-particle collisions on the distribution of granular pressure and temperature are discussed. Good agreement was achieved between the simulated results and experimental findings. (C) 2015 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:42 / 50
页数:9
相关论文
共 35 条
[1]  
[Anonymous], THERMOFLUID MODEL 2
[2]  
[Anonymous], 1993, PARTICULATE 2 PHASE
[3]  
Cheng Y, 2005, CAN J CHEM ENG, V83, P177
[4]   Hydrodynamics and scale-up of liquid-solid circulating fluidized beds: Similitude method vs. CFD [J].
Cheng, Yi ;
Zhu, Jesse .
CHEMICAL ENGINEERING SCIENCE, 2008, 63 (12) :3201-3211
[5]   EFFECT OF PARTICLE-SHAPE ON HINDERED SETTLING IN CREEPING FLOW [J].
CHONG, YS ;
RATKOWSKY, DA ;
EPSTEIN, N .
POWDER TECHNOLOGY, 1979, 23 (01) :55-66
[6]   CFD modelling of a liquid-solid fluidized bed [J].
Cornelissen, Jack T. ;
Taghipour, Fariborz ;
Escudie, Renaud ;
Ellis, Naoko ;
Grace, John R. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (22) :6334-6348
[7]   HINDERED SETTLING OF SEMIDILUTE MONODISPERSE AND POLYDISPERSE SUSPENSIONS [J].
DAVIS, RH ;
BIRDSELL, KH .
AICHE JOURNAL, 1988, 34 (01) :123-129
[8]   The sedimentation velocity of dilute suspensions of nearly monosized spheres [J].
Di Felice, R .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1999, 25 (04) :559-574
[9]  
Doroodchi E, 2005, POWDER TECHNOL, V156, P1, DOI 10.1016/j.powtec.2005.05.057
[10]   VELOCITY-VOIDAGE RELATIONSHIPS FOR FLUIDIZATION AND SEDIMENTATION IN SOLID-LIQUID SYSTEMS [J].
GARSIDE, J ;
ALDIBOUNI, MR .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (02) :206-214