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 …

A three-dimensional reactive gas-particle CFD model was built to study the hydrodynamics,
heat transfer and cracking reaction behaviors within an industrial Fluid Catalytic Cracking …

The cohesive model and traction-separation curves have brought a considerable possibility
for researchers and fracture engineers to assess and simulate failure in composite …

It has been widely recognized that the exit geometry of circulating fluidized bed (CFB) risers
may have significant effects on the hydrodynamics of gas–solid flow. However, a …

Operating sorbent-enhanced steam reforming (SE-SR) of methane in fluidised bed reactors
presents a promising pathway for industrial low-carbon hydrogen production. However …

Bioreactors are commonly used in industry, owing to their low energy requirement. These
reactors are often operated at reduced flow rates in order to maintain a high retention time …

A three dimensional gas-solid reactive flow model based on the Eulerian-Eulerian approach
was used to simulate the hydrodynamic, heat transfer and catalytic cracking reaction within …

Most studies neglect the presence of thermal cracking reactions in industrial FCC process.
Nevertheless, the present work proposes a new model which modified the 10-lumps kinetic …

A detailed steady state FCC riser process model is simulated for the first time with different
compressibility (Z) factor correlations using gPROMS software. A 4-lump kinetic model is …

ANSYS Fluent is used to examine the mixing of catalyst zeolite particles with petroleum
feedstock and water vapor in a fluid catalytic cracking (FCC) riser. A two‐fluid model is …