A CFD-DEM study of the behaviour of single-solid and binary mixtures in a pyramidal spouted bed

被引:18
作者
Marchelli, Filippo [1 ]
Moliner, Cristina [2 ]
Bosio, Barbara [2 ]
Arato, Elisabetta [2 ]
机构
[1] Free Univ Bozen Bolzano, Fac Sci & Technol, Piazza Univ 5, I-39100 Bolzano, Italy
[2] Univ Genoa, Dept Civil Chem & Environm Engn, Via Opera Pia 15, I-16145 Genoa, Italy
来源
PARTICUOLOGY | 2019年 / 42卷
关键词
Spouted beds; Computational fluid dynamics; Discrete element method; Binary mixtures; Segregation phenomena; FLUIDIZED-BED; NUMERICAL-SIMULATION; PARTICLE-SIZE; BIO-OIL; FLOW; HYDRODYNAMICS; SEGREGATION; VELOCITY; GASIFICATION; PERFORMANCE;
D O I
10.1016/j.partic.2018.03.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We simulated a lab-scale cold-flow spouted bed through computational fluid dynamics (CFD), coupled with the discrete element method (DEM) for the solid phase, using a commercial CFD program, ANSYS FLUENT 18.0. To limit the computational expense, we tested both a simplified pseudo-2D geometry and a complete 3D geometry. We found that the Haider and Levenspiel drag model is suitable for the pseudo-2D geometry; however, this model does not correctly predict fluidisation in the 3D geometry. Conversely, the Gidaspow drag model behaves accurately in the 3D geometry but overestimates the motion of particles in the pseudo-2D geometry. We studied several single-solid and binary mixtures to assess the reproducibility of segregation phenomena. The pseudo-2D model was able to predict the onset and minimum spouting flow rates of all mixtures with good accuracy. An analysis of the volume fraction contours of the binary mixtures permitted us to confirm that segregation phenomena were correctly predicted at low gas velocities. We showed that segregation decreased as the inlet gas flow rate was increased. Calculations performed in the complete 3D geometry were preliminarily assessed as more reliable but required almost four times as much computational time as those for the pseudo 2D geometry. (C) 2018 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:79 / 91
页数:13
相关论文
共 56 条
[1]   A comparative study on the influence of the gas flow rate on the hydrodynamics of a gas-solid spouted fluidized bed using Euler-Euler and Euler-Lagrange/DEM models [J].
Almohammed, Naser ;
Alobaid, Falah ;
Breuer, Michael ;
Epple, Bernd .
POWDER TECHNOLOGY, 2014, 264 :343-364
[2]  
ANSYS, 2015, ANSYS FLUENT THEOR G
[3]  
ANSYS, 2015, ANSYS FLUENT US GUID
[4]  
ANSYS, 2015, ANSYS FLUENT THEOR G
[5]  
ANSYS, 2015, ANSYS FLUENT THEOR G
[6]   A new mechanistic scale-up methodology for gas-solid spouted beds [J].
Aradhya, Shreekanta ;
Taofeeq, Haidar ;
Al-Dahhan, Muthanna .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2016, 110 :146-159
[7]   Transient reacting flow simulation of spouted fluidized bed for coal-direct chemical looping combustion with different Fe-based oxygen carriers [J].
Banerjee, Subhodeep ;
Agarwal, Ramesh .
APPLIED ENERGY, 2015, 160 :552-560
[8]  
Bao X., 2010, SPOUTED SPOUT FLUID, P57
[9]   AN OVERVIEW ON THE RECENT ADVANCES IN COMPUTATIONAL FLUID DYNAMICS SIMULATION OF SPOUTED BEDS [J].
Bao, Xiaojun ;
Du, Wei ;
Xu, Jian .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2013, 91 (11) :1822-1836
[10]   HYDRODYNAMIC AND THERMAL EXPERIMENTATION ON SQUARE-BASED SPOUTED BEDS FOR POLYMER UPGRADING AND UNIT SCALE-UP [J].
Beltramo, Carlo ;
Rovero, Giorgio ;
Cavaglia, Giuliano .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2009, 87 (03) :394-402