The object of this work was to develop an equation to predict the pressure drop in coni-cal beds of spherical particles. Work reported earlier is limited to a single cone angle in liquid-solid systems, whereas in the present study cone angles of 10°, 30°, 45 ° and 60° were used to predict the pressure drop for fixed beds. Air was used as the fluid medium and the bed consisted of spherical glass parti-cles of various sizes. The constants C1 and C2 were determined and were used to calculate pressure drop values. Experimental and theo-retical values of pressure drop were compared and the mean and the standard deviation were calculated
Packed bed reactors are among the most common reactor types in chemical industries. The reactions in...
Abstract: "The pressure drop associated with the flow of air through a cylindrical bed of spherical ...
The effect of bed diameter to particle diameter ratio on pressure drop is studied and the hydrodynam...
Flow through packed beds of spheres is a complex phenomenon and it has been extensively studied. Alt...
Extensive new measurements on pressure drop for the flow of purely viscous non-Newtonian fluids thro...
A large number of correlations can be found in the literature for the calculation of pressure drop c...
This study uses novel methods, combining discrete element method (DEM) simulations for packing and c...
Fluid flow data are presnted for beds of uniformly sized spheres consolidated with resin over a poro...
Models have been developed for the prediction of wall pressure drop in solid-liquid fluidised beds (...
New data on the two phase pressure drop for the concurrent upflow of air-liquid (Newtonian and non-N...
Models have been developed for the prediction of wall pressure drop in solid-liquid fluidised beds (...
The pressure drop associated with the flow of air through a cylindrical bed of spherical pebbles has...
The pressure drop across the distributor signifies the total pressure drop and ensures desired fluid...
The aim of this work was the experimental investigation of the particle friction factor for air f...
This is a theoretical and experimental study on porosity and pressure losses in a packed bed of sphe...
Packed bed reactors are among the most common reactor types in chemical industries. The reactions in...
Abstract: "The pressure drop associated with the flow of air through a cylindrical bed of spherical ...
The effect of bed diameter to particle diameter ratio on pressure drop is studied and the hydrodynam...
Flow through packed beds of spheres is a complex phenomenon and it has been extensively studied. Alt...
Extensive new measurements on pressure drop for the flow of purely viscous non-Newtonian fluids thro...
A large number of correlations can be found in the literature for the calculation of pressure drop c...
This study uses novel methods, combining discrete element method (DEM) simulations for packing and c...
Fluid flow data are presnted for beds of uniformly sized spheres consolidated with resin over a poro...
Models have been developed for the prediction of wall pressure drop in solid-liquid fluidised beds (...
New data on the two phase pressure drop for the concurrent upflow of air-liquid (Newtonian and non-N...
Models have been developed for the prediction of wall pressure drop in solid-liquid fluidised beds (...
The pressure drop associated with the flow of air through a cylindrical bed of spherical pebbles has...
The pressure drop across the distributor signifies the total pressure drop and ensures desired fluid...
The aim of this work was the experimental investigation of the particle friction factor for air f...
This is a theoretical and experimental study on porosity and pressure losses in a packed bed of sphe...
Packed bed reactors are among the most common reactor types in chemical industries. The reactions in...
Abstract: "The pressure drop associated with the flow of air through a cylindrical bed of spherical ...
The effect of bed diameter to particle diameter ratio on pressure drop is studied and the hydrodynam...