Gas-solid fluidized beds have drawn the attention of engineers and researchers as an
effective technology for a large variety of applications, and numerical simulations can play …

Gas maldistribution is an operational challenge peculiar to all industrial fluidized bed
applications, resulting in poor reactor performance. In the present work, the multi-phase …

The liquid-solid two-phase fluidized bed has the advantages of high liquid-solid contact
efficiency, good mass and heat transfer performance, uniform particle distribution, etc., and …

Abstract A Computational Particle Fluid Dynamics (CPFD) model, which has the ability of
revealing the coupled flow-reaction behaviors on the scales ranging from an individual …

Insufficient consideration of the coupled effect of multi-scale and turbulent mass transfer
impedes thorough understanding of the dynamic adsorption process in the fixed bed. To …

For simultaneously predicting the hydrodynamics and protein adsorption process in a liquid-
solids fluidized bed (LSFB), a computational fluid dynamics (CFD) model is established by …

In this paper, a recently developed two-equation turbulent (TET) model based on the
methodology of computational mass transfer (CMT)[1] is adopted to simulate the capture …

In this study, the fluid flow and mixing process in an im**ing stream-rotating packed bed
(IS-RPB) is simulated by using a new three-dimensional computational fluid dynamics …

Turbulence caused by high superficial gas velocity has significant impact on the CO 2
capture process by adsorption. However, the poor consideration of turbulent diffusion in …

Rigorous prediction of species concentration distribution has been challenging in the
simulation of bubble column reactors. In the present manuscript, a theoretical model of …