Experiments on drying of moist particles by ambient air were carried out to measure the mass transfer coefficient in a bubbling fluidized bed. Fine glass beads of mean diameter 125?µm were used as the bed material. Throughout the drying process, the dynamic material distribution was recorded by electrical capacitance tomography (ECT) and the exit air condition was recorded by a temperature/humidity probe. The ECT data were used to obtain qualitative and quantitative information on the bubble characteristics. The exit air moisture content was used to determine the water content in the bed. The measured overall mass transfer coefficient was in the range of 0.0145–0.021?m/s. A simple model based on the available correlations for bubble-cloud a...
Fluidized bed dryers (FBDs) are used in the pharmaceutical industry to remove excess moisture from g...
[EN] The two-phase theory has been frequently used to model fluidised bed drying. At high air veloci...
Knowledge of gas dispersion and mass exchange between the bubble and the emulsion phases is essentia...
Experiments on drying of moist particles by ambient air were carried out to measure the mass transfe...
Bubbling fluidized bed technology is one of the most effective mean for interaction between solid an...
Air at ambient conditions was used to dry moist particles at various fluidisation velocities. Throug...
Air at ambient conditions was used to dry moist particles at various fluidisation velocities. Throug...
Investigations into drying kinetics of biomass in fluidized bed dryers are essential for the control...
The paper addresses results for the case of convective drying of particulate solids in a packed and ...
The bubbling fluidized bed flow regime is characterized by high heat and mass transfer rate and lead...
A mathematical model for the drying of particulate solids in a continuous vibrated fluidised bed dry...
A coupled heat and mass transfer model is developed for batch fluidized-bed drying of moist porous p...
This paper presents a comparison of heat and mass transfer coefficient around a horizontal cylinder ...
Humidity and temperature measurements, together with pressure fluctuation signals, were employed to ...
Naphthalene spheres (particle diameter 2 < dn < 20 mm) were vaporized in beds fluidized by air at a ...
Fluidized bed dryers (FBDs) are used in the pharmaceutical industry to remove excess moisture from g...
[EN] The two-phase theory has been frequently used to model fluidised bed drying. At high air veloci...
Knowledge of gas dispersion and mass exchange between the bubble and the emulsion phases is essentia...
Experiments on drying of moist particles by ambient air were carried out to measure the mass transfe...
Bubbling fluidized bed technology is one of the most effective mean for interaction between solid an...
Air at ambient conditions was used to dry moist particles at various fluidisation velocities. Throug...
Air at ambient conditions was used to dry moist particles at various fluidisation velocities. Throug...
Investigations into drying kinetics of biomass in fluidized bed dryers are essential for the control...
The paper addresses results for the case of convective drying of particulate solids in a packed and ...
The bubbling fluidized bed flow regime is characterized by high heat and mass transfer rate and lead...
A mathematical model for the drying of particulate solids in a continuous vibrated fluidised bed dry...
A coupled heat and mass transfer model is developed for batch fluidized-bed drying of moist porous p...
This paper presents a comparison of heat and mass transfer coefficient around a horizontal cylinder ...
Humidity and temperature measurements, together with pressure fluctuation signals, were employed to ...
Naphthalene spheres (particle diameter 2 < dn < 20 mm) were vaporized in beds fluidized by air at a ...
Fluidized bed dryers (FBDs) are used in the pharmaceutical industry to remove excess moisture from g...
[EN] The two-phase theory has been frequently used to model fluidised bed drying. At high air veloci...
Knowledge of gas dispersion and mass exchange between the bubble and the emulsion phases is essentia...