Models have been developed for the prediction of wall pressure drop in solid-liquid fluidised beds (SLFB). Both laminar and turbulent regimes have been considered. These models explain the pressure drop characteristics of the limiting cases of SLFB: the fixed bed and the single-phase pipe flow. Pressure drop was measured in a 78 mm i.d. solid-liquid fluidised bed. Particle size was varied in the range of 0.55 - 3.1 mm. The bed voidage was varied in the range of 0.4 to 0.9. Good agreement has been shown between model predictions and experimental observations of pressure drop
Hydrodynamics of gas-liquid-solid semi-fluidized bed relating to packed bed formation and bed pressu...
Campbell and Wang (1991) showed that the particle pressures in gas-fluidized beds were largely gener...
This project studies the particle pressure, which may be thought of as the force exerted by the part...
Models have been developed for the prediction of wall pressure drop in solid-liquid fluidised beds (...
This study is concerned with pressure drop and bed expansion behaviour of a solid liquid fluidized b...
The pressure drop at the wall and the radial profiles of pressure drop along the bed height were mea...
The control of the solids circulation rate in circulating fluidized beds (CFB) can be obtained by me...
The aim of this study is computational fluid dynamic (CFD) simulation of the single-phase pressure d...
This paper deals with the experimentation conducted to obtain pressure drop in a squared gas-solid f...
An attempt has been made to reconcile and to critically analyze the voluminous literature available ...
CFD simulation of bed expansion of mono size solid-liquid fluidized beds has been performed in creep...
Fluidized beds are widely used in chemical, petrochemical and process industries. They are preferred...
The pressure drop across the distributor signifies the total pressure drop and ensures desired fluid...
With a Euler-two-phase (E2P) approach, through computational fluid dynamics (CFD) techniques, a math...
The unusual trend of pressure loss relative to that estimated on the basis of a homogeneous bed - i....
Hydrodynamics of gas-liquid-solid semi-fluidized bed relating to packed bed formation and bed pressu...
Campbell and Wang (1991) showed that the particle pressures in gas-fluidized beds were largely gener...
This project studies the particle pressure, which may be thought of as the force exerted by the part...
Models have been developed for the prediction of wall pressure drop in solid-liquid fluidised beds (...
This study is concerned with pressure drop and bed expansion behaviour of a solid liquid fluidized b...
The pressure drop at the wall and the radial profiles of pressure drop along the bed height were mea...
The control of the solids circulation rate in circulating fluidized beds (CFB) can be obtained by me...
The aim of this study is computational fluid dynamic (CFD) simulation of the single-phase pressure d...
This paper deals with the experimentation conducted to obtain pressure drop in a squared gas-solid f...
An attempt has been made to reconcile and to critically analyze the voluminous literature available ...
CFD simulation of bed expansion of mono size solid-liquid fluidized beds has been performed in creep...
Fluidized beds are widely used in chemical, petrochemical and process industries. They are preferred...
The pressure drop across the distributor signifies the total pressure drop and ensures desired fluid...
With a Euler-two-phase (E2P) approach, through computational fluid dynamics (CFD) techniques, a math...
The unusual trend of pressure loss relative to that estimated on the basis of a homogeneous bed - i....
Hydrodynamics of gas-liquid-solid semi-fluidized bed relating to packed bed formation and bed pressu...
Campbell and Wang (1991) showed that the particle pressures in gas-fluidized beds were largely gener...
This project studies the particle pressure, which may be thought of as the force exerted by the part...