Although CFD-DEM simulation of Geldart B and D particles has been experimentally validated extensively, its experimental validation for simulating the hydrodynamics of Geldart A particles has been seldom reported, due to the fact that even the particle number in a laboratory fluidized bed is too much to be tracked individually. In this study, one-to-one comparison between experimental and CFD-DEM study of a miniaturized gas-solid fluidized bed (micro-fluidized bed) containing FCC particles was performed. It was shown that the bed expansion characteristics in bubbling fluidization regime, the mean voidage of emulsion phase as well as the bed collapse process can be predicted accurately by CFD-DEM method. The results not only provide experime...
This paper investigates the spatial resolution of computational fluid dynamics–discrete element meth...
In this work, a new drag model for TFM simulation in gas solid bubbling fluidized beds was proposed,...
© 2018 The Society of Powder Technology Japan The selection of a drag model is of critical importanc...
Polydisperse particles are ubiquitous, yet their unique roles are inadequately understood. In this s...
The Geldart Group A particles are of great importance in various chemical processes owning to advant...
The fluidization behavior of Geldart B particles in micro fluidized beds is investigated numerically...
The fluidization behavior of Geldart A particles in a gas-solid micro-fluidized bed was investigated...
We report on 3D computer simulations based on the soft-sphere discrete particle model (DPM) of Gelda...
The minimum bubbling velocity, which demarcates the homogeneous and heterogeneous fluidization regim...
The objective of the study is to identify the transitions in bed behavior as the gas velocity is inc...
A discrete element model (DEM) combined with computational fluid dynamics (CFD) was developed to mod...
The objective of this study was using computational fluid dynamics simulation with OpenFOAM to study...
Purpose: The purpose of this study is to assess the performance of ANSYS Fluent® and OpenFOAM®, at t...
This paper investigates the spatial resolution of computational fluid dynamics–discrete element meth...
In this work, a new drag model for TFM simulation in gas solid bubbling fluidized beds was proposed,...
© 2018 The Society of Powder Technology Japan The selection of a drag model is of critical importanc...
Polydisperse particles are ubiquitous, yet their unique roles are inadequately understood. In this s...
The Geldart Group A particles are of great importance in various chemical processes owning to advant...
The fluidization behavior of Geldart B particles in micro fluidized beds is investigated numerically...
The fluidization behavior of Geldart A particles in a gas-solid micro-fluidized bed was investigated...
We report on 3D computer simulations based on the soft-sphere discrete particle model (DPM) of Gelda...
The minimum bubbling velocity, which demarcates the homogeneous and heterogeneous fluidization regim...
The objective of the study is to identify the transitions in bed behavior as the gas velocity is inc...
A discrete element model (DEM) combined with computational fluid dynamics (CFD) was developed to mod...
The objective of this study was using computational fluid dynamics simulation with OpenFOAM to study...
Purpose: The purpose of this study is to assess the performance of ANSYS Fluent® and OpenFOAM®, at t...
This paper investigates the spatial resolution of computational fluid dynamics–discrete element meth...
In this work, a new drag model for TFM simulation in gas solid bubbling fluidized beds was proposed,...
© 2018 The Society of Powder Technology Japan The selection of a drag model is of critical importanc...