In the present investigation, bed porosity and solid holdup in viscous three-phase inverse fluidized bed (TPIFB) are determined for aqueous solutions of carboxy methyl cellulose (CMC) system using polyethylene and polypropylene as a particles with low-density and diameter (5 mm) in a (9.2 cm) inner diameter with height (200 cm) of vertical perspex column. The effectiveness of gas velocity Ug , liquid velocity UL, liquid viscosity μL, and particle density ρs on bed porosity BP and solid holdups εg were determined. The bed porosity increases with "increasing gas velocity", "liquid velocity", and "liquid viscosity". Solid holdup decreases with increasing gas, liquid velocities and liquid viscosity. Solid holdup with "low density particles" sho...
ABSTRACT: The present investigation entails a procedure by which the surface tension and viscosity o...
Settling velocities of particles in viscous non-Newtonian pseudoplastic solutions were measured. Sph...
It is proposed that scaling of three-phase fluidized bed hydrodynamics can be carried out based on ...
327-331Fluidization of a three-phase system can be achieved either with co-current up flow of gas a...
This study quantitatively measures the solid flow properties using an optical fiber probe (OFP) in a...
The minimum fluidization velocity (Umf) and maximum pressure drop (ΔPmax) of a gas-solid fluidized b...
Three-phase fluidizing beds have emerged in recent years as one of the most promising devices for th...
For an accurate prediction of the porosity of a liquid-solid homogenous fluidized bed, various empir...
Hydrodynamics of conical fluidized bed differ from that of columnar beds by the fact that a velocity...
In light of the little understanding of the hydrodynamics of multicomponent particle beds involving ...
The hydrodynamics of inverse liquid-solid circulating fluidized bed (ILSCFB) is experimentally studi...
Polymers are often produced in pressurized fluidized beds. Large surface area and good mixing proper...
Poly Propylene Particles of size 6.1mm and density 0.93kg/liter were fluidized by a downward flow of...
The present work proposes a novel radially cross-flow multistage solid-liquid circulating fluidized ...
Tapered beds are extensively used in various industrial chemical processes. These beds are remedy fo...
ABSTRACT: The present investigation entails a procedure by which the surface tension and viscosity o...
Settling velocities of particles in viscous non-Newtonian pseudoplastic solutions were measured. Sph...
It is proposed that scaling of three-phase fluidized bed hydrodynamics can be carried out based on ...
327-331Fluidization of a three-phase system can be achieved either with co-current up flow of gas a...
This study quantitatively measures the solid flow properties using an optical fiber probe (OFP) in a...
The minimum fluidization velocity (Umf) and maximum pressure drop (ΔPmax) of a gas-solid fluidized b...
Three-phase fluidizing beds have emerged in recent years as one of the most promising devices for th...
For an accurate prediction of the porosity of a liquid-solid homogenous fluidized bed, various empir...
Hydrodynamics of conical fluidized bed differ from that of columnar beds by the fact that a velocity...
In light of the little understanding of the hydrodynamics of multicomponent particle beds involving ...
The hydrodynamics of inverse liquid-solid circulating fluidized bed (ILSCFB) is experimentally studi...
Polymers are often produced in pressurized fluidized beds. Large surface area and good mixing proper...
Poly Propylene Particles of size 6.1mm and density 0.93kg/liter were fluidized by a downward flow of...
The present work proposes a novel radially cross-flow multistage solid-liquid circulating fluidized ...
Tapered beds are extensively used in various industrial chemical processes. These beds are remedy fo...
ABSTRACT: The present investigation entails a procedure by which the surface tension and viscosity o...
Settling velocities of particles in viscous non-Newtonian pseudoplastic solutions were measured. Sph...
It is proposed that scaling of three-phase fluidized bed hydrodynamics can be carried out based on ...