The results of an experimental study indicating a significant effect of column diameter on the
pressure drop and capacity of corrugated sheet structured packing are presented. The …

The volume-averaged equations for velocity and concentration fields have been used to
simulate the hydrodynamics and mass-transfer processes in randomly packed distillation …

A review of research articles dealing with estimation of the rate of gas flow maldistribution in
packed‐bed columns is presented. The proposed relations for determination of the …

Large-scale liquid and gas flow patterns were measured in a 0.5-m diameter column
dumped with 25-and 50-mm plastic Pall rings and 38-mm ceramic Intalox saddles. Liquid …

Abstract Design and optimization of separation units, eg, distillation and absorption columns
with flow distribution packings, require detailed knowledge about the internal flow conditions …

Comprehensive liquid distribution experiments were conducted with common-size
conventional and high-capacity, corrugated-sheet structured packings in a 1.4 m internal …

A macroscopic model, based on the volume-averaged equations of momentum and
continuity, is presented to predict hydrodynamic characteristics of gas and liquid …

In this work, gas maldistribution in random packings of cylinders and Raschig rings is
studied with particle-resolved direct numerical simulation (PRDNS) employing a finite …

The distribution of gas flow over the cross section of packed columns depends on the
manner of gas flow feeding, on packing type, packing arrangement, and internal devices in …

Solvent-based post combustion CO2 capture is a promising technology for industrial
application. Gas-liquid interfaces and interactions in the packed bed are considered one of …