The paper addresses the transition to the bubbling regime of solid beds belonging to Geldart’s group A, from ambient temperature to 500°C. The analysis of the influence exerted by operating temperature on the variables that characterize both the homogeneous expansion of the bed and the onset of a steady bubbling regime is conducted on the fluidization map of the fluidized bed, namely the voidage velocity diagram into which results of the fluidization and bed collapse experiments are merged. The results obtained show that at elevated temperatures the ability of the fluidized bed to preserve the homogeneous fluidization regime is extended to unusually high voidage levels. Even past the appearance of a steady bubble flow, the dense phase void...
This work explores the effect of interparticle friction on the stability of a structured bubble flow...
Enhanced mass and heat transfer, resulting in a more homogeneous heat and mass distribution, makes t...
The fluidization behavior of cracking catalyst was studied at pressures of 1-15 bar with different f...
The paper analyses the dependence on process temperature of parameters that characterize the dense p...
In order to understand the factors responsible for changes in the fluidization behaviour of industri...
Some important characteristics of the bubbling regime, relevant to a cut of FCC catalyst with an ave...
AbstractTwo-dimensional DEM–CFD simulations have been performed in order to examine the effect of su...
Gas-fluidized powders of fine particles display a fluidlike regime in which the bed does not have a ...
The hydrodynamics of gas-solid fluidized beds at high temperature is a critical factor in their desi...
In this work, a new approach for increasing and controlling inter-particle forces (IPFs) was applied...
Recent experiments have shown an influence of temperature on the minimum fluidization conditions in ...
Gas-fluidization of Geldart A particles was simulated for a domain of lab-scale dimensions. Hydrodyn...
Many commercial fluidized bed processes (e.g. catalytic and gas-solid reactions, drying) operate in ...
AbstractUsing DEM simulations, the paper examines the different types of behaviour as the gas veloci...
This work explores the effect of interparticle friction on the stability of a structured bubble flow...
Enhanced mass and heat transfer, resulting in a more homogeneous heat and mass distribution, makes t...
The fluidization behavior of cracking catalyst was studied at pressures of 1-15 bar with different f...
The paper analyses the dependence on process temperature of parameters that characterize the dense p...
In order to understand the factors responsible for changes in the fluidization behaviour of industri...
Some important characteristics of the bubbling regime, relevant to a cut of FCC catalyst with an ave...
AbstractTwo-dimensional DEM–CFD simulations have been performed in order to examine the effect of su...
Gas-fluidized powders of fine particles display a fluidlike regime in which the bed does not have a ...
The hydrodynamics of gas-solid fluidized beds at high temperature is a critical factor in their desi...
In this work, a new approach for increasing and controlling inter-particle forces (IPFs) was applied...
Recent experiments have shown an influence of temperature on the minimum fluidization conditions in ...
Gas-fluidization of Geldart A particles was simulated for a domain of lab-scale dimensions. Hydrodyn...
Many commercial fluidized bed processes (e.g. catalytic and gas-solid reactions, drying) operate in ...
AbstractUsing DEM simulations, the paper examines the different types of behaviour as the gas veloci...
This work explores the effect of interparticle friction on the stability of a structured bubble flow...
Enhanced mass and heat transfer, resulting in a more homogeneous heat and mass distribution, makes t...
The fluidization behavior of cracking catalyst was studied at pressures of 1-15 bar with different f...