Add to ORKGExperiments were performed in a cylindrical bubble column 0.19 m in diameter and 4 m in height. Metal perforated plate with a constant free plate area 0.2 % and holes with diameters 0.5 mm was used for gas distribution. Air was used as gas phase, water and non-coalescent 0.5 M solution of sodium sulphate (Na2SO4) as liquid phases. The kLa values obtained using air in coalescent and non-coalescent batch are discussed. For the homogeneous regime an empirical correlation between kLaL and gas holdup ?G was found
The effect of gas sparger type, clear liquid height, liquid viscosity and addition of electrolyte on...
The hydrodynamics of bubble columns with concentrated slurries of paraffin oil (density, ΡL = 7...
The aim of this study was to develop a practically usable model to describe the influence of increas...
The dependences of the volumetric liquid-side mass transfer coefficient, kLa and the gas holdup on g...
Volumetric mass transfer coefficient, kLaL and gas holdup, εG were measured in distilled water and i...
The main objective of this research is to determine the effect of solids on gas holdup and flow patt...
A comprehensive experimental study of gas holdup in bubble columns of varying diameters, fitted with...
Bubble columns are used in the chemical industry to perform gas liquid reactions, like oxidation, h...
This work concerns the performance of bubble columns equipped with porous sparger and investigates t...
A two-gas-fraction model previously tested with gas-phase residence time distribution tests was used...
Many correlations are available in the literature for computing the gas hold-up in bubble columns, m...
Gas-liquid volumetric mass transfer coefficient kLa for CH4, CO2, and Ar were experimentally measu...
The influence of pressure on the gas hold-up in a bubble column is determined for a sodium sulphite ...
Radial variation of the gas hold-up was investigated in 0.385 m ID bubble column using gamma ray tom...
International audienceGas holdup of water/nitrogen, water-phenol/nitrogen and water-phenol/air syste...
The effect of gas sparger type, clear liquid height, liquid viscosity and addition of electrolyte on...
The hydrodynamics of bubble columns with concentrated slurries of paraffin oil (density, ΡL = 7...
The aim of this study was to develop a practically usable model to describe the influence of increas...
The dependences of the volumetric liquid-side mass transfer coefficient, kLa and the gas holdup on g...
Volumetric mass transfer coefficient, kLaL and gas holdup, εG were measured in distilled water and i...
The main objective of this research is to determine the effect of solids on gas holdup and flow patt...
A comprehensive experimental study of gas holdup in bubble columns of varying diameters, fitted with...
Bubble columns are used in the chemical industry to perform gas liquid reactions, like oxidation, h...
This work concerns the performance of bubble columns equipped with porous sparger and investigates t...
A two-gas-fraction model previously tested with gas-phase residence time distribution tests was used...
Many correlations are available in the literature for computing the gas hold-up in bubble columns, m...
Gas-liquid volumetric mass transfer coefficient kLa for CH4, CO2, and Ar were experimentally measu...
The influence of pressure on the gas hold-up in a bubble column is determined for a sodium sulphite ...
Radial variation of the gas hold-up was investigated in 0.385 m ID bubble column using gamma ray tom...
International audienceGas holdup of water/nitrogen, water-phenol/nitrogen and water-phenol/air syste...
The effect of gas sparger type, clear liquid height, liquid viscosity and addition of electrolyte on...
The hydrodynamics of bubble columns with concentrated slurries of paraffin oil (density, ΡL = 7...
The aim of this study was to develop a practically usable model to describe the influence of increas...