Add to ORKGAn additional parameter, the particle-particle coefficient of restitution was added to the scaling relationship of spouted beds proposed by He et al. (4) by granular kinetic theory analysis of the particle movements in both spout and annulus regions. The experimental verification was conducted in two spouted beds with 80 and 120 mm ID. It has been found that good similarity could not be obtained when the coefficients of restitution were not matched
Spout fluidized beds find widespread application in the process industry in granulation processes, i...
The particle-scale characteristics of the solid phase in the three distinct regions of the dual-colu...
Spout fluidized beds find widespread application in the process industry in granulation processes, i...
The scaling relationships proposed by Glicksman (1984) for fluidized bed scale-up have been modifie...
A thorough understanding of the complex flow structure of gas-solid spouted bed is crucial for desig...
Important global hydrodynamic relationships for shallow spouted beds of high-density particles were ...
Spouted bed as one of the typical fluidization reactors, has been widely used in many industrial are...
Fluidization behavior of spouted bed for a gas-solid system has been studied by carrying out a numbe...
We implemented for the first time our radioactive particle tracking as an advanced noninvasive techn...
A new mechanistic methodology of scale-up for gas-solid spouted beds has been proposed and validated...
Spout fluidized beds find widespread application in the process industry in granulation processes, i...
The work focuses on implementing for the first time advanced non-invasive measurement techniques to ...
In this work, the scale-up methodology of He et al. (1997) that is based on maintaining similar or c...
In this article we study the effect of the inter-particle interaction on the bed dynamics, by consid...
The characteristics of coarse / fine particles have been studied using a cylindrical spouted bed. Th...
Spout fluidized beds find widespread application in the process industry in granulation processes, i...
The particle-scale characteristics of the solid phase in the three distinct regions of the dual-colu...
Spout fluidized beds find widespread application in the process industry in granulation processes, i...
The scaling relationships proposed by Glicksman (1984) for fluidized bed scale-up have been modifie...
A thorough understanding of the complex flow structure of gas-solid spouted bed is crucial for desig...
Important global hydrodynamic relationships for shallow spouted beds of high-density particles were ...
Spouted bed as one of the typical fluidization reactors, has been widely used in many industrial are...
Fluidization behavior of spouted bed for a gas-solid system has been studied by carrying out a numbe...
We implemented for the first time our radioactive particle tracking as an advanced noninvasive techn...
A new mechanistic methodology of scale-up for gas-solid spouted beds has been proposed and validated...
Spout fluidized beds find widespread application in the process industry in granulation processes, i...
The work focuses on implementing for the first time advanced non-invasive measurement techniques to ...
In this work, the scale-up methodology of He et al. (1997) that is based on maintaining similar or c...
In this article we study the effect of the inter-particle interaction on the bed dynamics, by consid...
The characteristics of coarse / fine particles have been studied using a cylindrical spouted bed. Th...
Spout fluidized beds find widespread application in the process industry in granulation processes, i...
The particle-scale characteristics of the solid phase in the three distinct regions of the dual-colu...
Spout fluidized beds find widespread application in the process industry in granulation processes, i...