The mixing process in a mechanically agitated vessel is a widespread phenomenon which
plays an important role among industrial processes. In that process, one of the crucial …

Gas dispersion in non-Newtonian fluids is encountered in a broad range of chemical,
biochemical, and food industries. Mechanically agitated vessels are commonly employed in …

In this work, simulations have been performed for three phase stirred dispersions using
computational fluid dynamics model (CFD). The effects of tank diameter, impeller diameter …

Coaxial mixers are efficient in mixing of highly viscous fluids. The main objective of this study
was to assess the power consumption for the gas dispersion in carboxymethyl cellulose …

Gas dispersion in non‐Newtonian fluids is a challenging task due to the formation of large
cavities behind the impeller blades, which leads to the generation of very large bubbles. In …

The performance of an agitated bioreactor is hampered by an intense shear environment
and low mass-transfer coefficient (k L a). The gas hold-up, k L a, and shear environment …

One of the significant challenges in the efficient operation of bioreactors is uniform gas
dispersion in very viscous non-Newtonian fluids because of the complex rheology exhibited …

In this work, the hydrodynamics and mass transfer in a gas–liquid dual turbine stirred tank
reactor are investigated using multiphase computational fluid dynamics coupled with …

The performance of a coaxial bioreactor in the intensification of gas dispersion in shear-
thinning fluids in terms of the power consumption of the central and anchor impellers, torque …

Our research findings challenge the paradigm that a high rotational speed of impellers can
intensify the gas dispersion. Interestingly, we observed the deterioration in the gas holdup at …