Numerical computation of fluid–solid mixture flow using the SPH–VCPM–DEM method

2021 ◽  
Vol 106 ◽  
pp. 103369
Author(s):  
K.C. Ng ◽  
A. Alexiadis ◽  
Hailong Chen ◽  
T.W.H. Sheu
2017 ◽  
Vol 97 ◽  
pp. 197-213 ◽  
Author(s):  
Kailun Guo ◽  
Ronghua Chen ◽  
Yonglin Li ◽  
Suizheng Qiu ◽  
G.H. Su

Author(s):  
Shuai Zhang ◽  
Koji Morita ◽  
Noriyuki Shirakawa ◽  
Yuichi Yamamoto

The COMPASS code is designed based on the moving particle semi-implicit (MPS) method to simulate various complex mesoscale phenomena relevant to core disruptive accidents (CDAs) of sodium-cooled fast reactors (SFRs). The MPS method, which is a fully Lagrangian method, can be extended for fluid-solid mixture flow simulations in a straightforward approach. In this study, a computational framework for fluid-solid mixture flow simulations was developed for the COMPASS code. In the present framework, the passively moving solid (PMS) model, which is originally proposed to describe the motion of a rigid body in a fluid, used to simulate hydrodynamic interactions between fluid and solids. In addition, mechanical interactions between solids were modeled by the distinct element method (DEM). Since the typical time step size in DEM calculation, which uses an explicit time integration scheme, is much smaller than that in MPS calculation, a multi-time-step algorithm was introduced to couple these two calculations. In order to verify the proposed computational framework for fluid-solid mixture flow simulations, a series of experiments of water-dam break with multiple solid rods was simulated using the COMPASS code. It was found that simulations considering only fluid-solid interactions using the PMS model can not reasonably represent typical behaviors of solid rods observed in the experiments. However, results of simulations taking account of solid-solid interactions using DEM as well as fluid-solid ones were in good agreement with experimental observations. It was demonstrated that the present computational framework enhances the capability of the COMPASS code for mesoscale simulations of fluid-solid mixture flow phenomena relevant to CDAs of SFRs. To improve the computational efficiency for fluid-solid mixture flow simulations, it will be necessary to optimize the time step size used in DEM calculations by adjusting DEM parameters based on additional experiments and numerical tests.


2017 ◽  
Author(s):  
Kailun Guo ◽  
Ronghua Chen ◽  
Yonglin Li ◽  
Suizheng Qiu ◽  
G. H. Su

2010 ◽  
Vol 4 (1) ◽  
pp. 126-137 ◽  
Author(s):  
Shuai ZHANG ◽  
Koji MORITA ◽  
Noriyuki SHIRAKAWA ◽  
Yuichi YAMAMOTO

Author(s):  
Fernando Z. Sierra ◽  
David Jua´rez ◽  
Juan C. Garci´a ◽  
Janusz Kubiak ◽  
Rube´n Nicola´s

In this paper a numerical computation of the flow dynamics in a compact cyclonic separator (CCS) for multiphase mixtures is presented. The study is directed to power plants consumption requirements where fuel gas must be free of solid particulate. A finite volume approach has been employed with body-fitted coordinates in a 3-D solution of the CCS dynamics. The cylindrical geometry under study includes aspect ratios in the range 2.5<R<3.8 (where R = height/diameter). The CCS has three exits as follows: one on the top for gas; one on the bottom for low particle concentration liquid; and the last one tangentially located on the lower part of the CCS for high particle concentration liquid. The turbulence was resolved using a RNG model, while the interactions between each component of the flow were addressed using a mixture slip model. The three-phase liquid-gas-solid mixture considered was gasoil-propane-mineral coal particles with the composition in volume fraction of liquid to gas of 0.9 to 0.1 in addition to 109 kg/m3 of 40 microns coal particles as the disperse phase. The results indicate that reversible flow of liquid through the upper gas-outlet may be a function of the outlet pressure conditions. Also, velocity conditions of the income mixture flow at the inlet defined the residence time of the flow during the operation of the CCS, which affects the separation too. In this work density profiles are shown to indicate the regions of up flow for gas and liquid drag. The presence of a third phase in the form of solid particles affects the flow patterns in a CCS.


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