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 …

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 …

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 …

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 …

Traditional methods based on local equilibrium assumption are unsuitable to describe the
non-linear and non-equilibrium mass transfer in turbulent fluidized beds (TFBs), especially …

A two-dimensional numerical model has been developed to simulate combustion of sesame
and broad bean stalks in the freeboard zone of a pilot-scale Bubbling Fluidized Bed …

Particle-fluid system is one of the most popular systems in chemical processes. Owing to
complex interface structure and high-velocity turbulence, the momentum and mass transfer …

An integrated model, namely the two-equation turbulent model, is introduced to simulate
mass transfer in a liquid–solid circulating fluidized bed (LSCFB) riser. Protein desorption is …