International audienceGas holdup of water/nitrogen, water-phenol/nitrogen and water-phenol/air systems was successfully measured by a method based on the use of a differential pressure sensor installed on a bubble column reactor, in a wide domain of temperature (from 100 to 300 degrees C) and pressure (from 10 to 30 MPa). These experimental conditions are little or no explored in literature. Results show a predominant influence of the superficial gas velocity, the evaporation of the liquid phase, the ratio of the gas volume flowrate on the liquid volume flowrate and the phenol concentration. Pressure and chemical reaction have little effect on gas holdup. The temperature has an effect in the case of phenol solutions. The different correlati...
A comprehensive experimental study of gas holdup in bubble columns of varying diameters, fitted with...
The aim of this study was to develop a practically usable model to describe the influence of increas...
Interfacial areas and gas hold-ups have been determined at pressures up to 8.0 MPa in a mechanically...
International audienceGas holdup of water/nitrogen, water-phenol/nitrogen and water-phenol/air syste...
International audienceSurface tension of water/nitrogen and water-phenol/nitrogen systems was succes...
International audienceThe design of bubble column for industrial applications is well known under ne...
The effect of temperature on the gas hold-up and flow regimes for air-water and air-electrolyte solu...
Interfacial areas and gas hold-ups have been determined at pressures up to 1.85 MPa in a bubble colu...
Experiments were carried out in bubble columns for a number of liquids at pressures between 0.1 and ...
International audienceBubble column reactors are multiphase contactors based on the dispersion of a ...
The liquid axial-dispersion coefficient and gas hold-up are measured in a batch-type bubble column o...
The aim of this study was to develop a practically usable model to describe the influence of increas...
The liquid axial-dispersion coefficient and gas hold-up are measured in a batch-type bubble column o...
A comprehensive experimental study of gas holdup in bubble columns of varying diameters, fitted with...
The aim of this study was to develop a practically usable model to describe the influence of increas...
Interfacial areas and gas hold-ups have been determined at pressures up to 8.0 MPa in a mechanically...
International audienceGas holdup of water/nitrogen, water-phenol/nitrogen and water-phenol/air syste...
International audienceSurface tension of water/nitrogen and water-phenol/nitrogen systems was succes...
International audienceThe design of bubble column for industrial applications is well known under ne...
The effect of temperature on the gas hold-up and flow regimes for air-water and air-electrolyte solu...
Interfacial areas and gas hold-ups have been determined at pressures up to 1.85 MPa in a bubble colu...
Experiments were carried out in bubble columns for a number of liquids at pressures between 0.1 and ...
International audienceBubble column reactors are multiphase contactors based on the dispersion of a ...
The liquid axial-dispersion coefficient and gas hold-up are measured in a batch-type bubble column o...
The aim of this study was to develop a practically usable model to describe the influence of increas...
The liquid axial-dispersion coefficient and gas hold-up are measured in a batch-type bubble column o...
A comprehensive experimental study of gas holdup in bubble columns of varying diameters, fitted with...
The aim of this study was to develop a practically usable model to describe the influence of increas...
Interfacial areas and gas hold-ups have been determined at pressures up to 8.0 MPa in a mechanically...