CFD–DEM simulation of fine particles in a spouted bed apparatus with a Wurster tube

Particuology ◽  
2019 ◽  
Vol 42 ◽  
pp. 114-125 ◽  
Author(s):  
Paul Breuninger ◽  
Dominik Weis ◽  
Isabell Behrendt ◽  
Philipp Grohn ◽  
Fabian Krull ◽  
...  
2017 ◽  
Vol 81 ◽  
pp. 275-287 ◽  
Author(s):  
Bayazid Mahmoodi ◽  
Seyyed Hossein Hosseini ◽  
Martin Olazar ◽  
Haritz Altzibar

Energies ◽  
2021 ◽  
Vol 14 (8) ◽  
pp. 2276
Author(s):  
Zhao Chen ◽  
Lin Jiang ◽  
Mofan Qiu ◽  
Meng Chen ◽  
Rongzheng Liu ◽  
...  

Particle adhesion is of great importance to coating processes due to its effect on fluidization. Currently, Computational Fluid Dynamics-Discrete Element Method (CFD-DEM) has become a powerful tool for the study of multiphase flows. Various contact force models have also been proposed. However, particle dynamics in high temperature will be changed with particle surface properties changing. In view of this, an adhesion model is developed based on approaching-loading-unloading-detaching idea and particle surface change under high temperature in this paper. Analyses of the adhesion model are given through two particle collision process and validated by experiment. Effects of inlet gas velocity and adhesion intensity on spouted bed dynamics are investigated. It is concluded that fluidization cycle will be accelerated by adhesion, and intensity of fluidization will be marginally enhanced by slight adhesion. Within a certain range, increasing inlet gas velocity will lead to strong intensity of particle motion. A parameter sensitivity comparison of linear spring-damping model and Hertz-Mindlin Model is given, which shows in case of small overlaps, forces calculated by both models have little distinction, diametrically opposed to that of large overlaps.


Particuology ◽  
2019 ◽  
Vol 43 ◽  
pp. 171-180 ◽  
Author(s):  
B. Mahmoodi ◽  
S.H. Hosseini ◽  
G. Ahmadi

2016 ◽  
Vol 290 ◽  
pp. 63-73 ◽  
Author(s):  
Ziliang Wang ◽  
Maysam Saidi ◽  
C. Jim Lim ◽  
John R. Grace ◽  
Hassan Basirat Tabrizi ◽  
...  

2011 ◽  
Vol 48-49 ◽  
pp. 362-365
Author(s):  
Wei Bing Zhu ◽  
Run Ru Zhu ◽  
Li Chao Xing ◽  
Xiao Bin Zhang

In this work, the mixing characteristic of ternary diameter particle system in a rectangular spouted bed was carried out three-dimensional discrete element method (DEM). In particular, the standard k- two-equation model and the Beer & Johnson equation were adopted to investigate the influence of turbulence and rolling friction, and Ashton mixing index was adopted to evaluate the dynamic mixing process of the ternary diameter particle systems. The particle velocity profiles, the gas-solid flow patterns, the particles distribution and the effect of gas velocity on mixing are discussed.


2013 ◽  
Vol 2013 ◽  
pp. 1-7 ◽  
Author(s):  
Pranati Sahoo ◽  
Abanti Sahoo

The fluidization characteristics of fine particles have been studied in both the fluidized bed and spouted bed. The effect of different system parameters (viz. static bed height, particle size, particle density and superficial velocity of the fluidizing medium, rotational speed of stirrer, and spout diameter) on the fluidization characteristics such as bed expansion/fluctuation ratios, bed pressure drop, minimum fluidizing/spouting velocity, and fluidization index of fine particles (around 60 micron particle size) have been analyzed. A stirrer/rod promoter has been used in the bed to improve the bed fluidity for fluidization process and spout diameter has been varied for spouted bed. Mathematical expressions for these bed dynamics have been developed on the basis of dimensionless analysis. Finally calculated values of these bed dynamics are compared with the experimentally observed values thereby indicating the successful applications of these developed correlations over a wide range of parameters.


2013 ◽  
Vol 92 (6) ◽  
pp. 1130-1138 ◽  
Author(s):  
Shiliang Yang ◽  
Kun Luo ◽  
Mingming Fang ◽  
Jianren Fan
Keyword(s):  

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