Add to ORKGPressure fluctuations were measured in three gas-solids bubbling fluidized beds (10cm, 20cm, and 30cm diameter, 1.0m high) using polyethylene particles of different sizes and particle size distributions. Both bed scale and particle size distribution significantly affect the gas-solids flow behavior. Bubble diameters measured from X-ray fluoroscopy in the 10cm diameter column were compared to various correlations in the literature
Low density polyethylene and polypropylene are produced at large scale via the Unipol process. In th...
Low density polyethylene and polypropylene are produced at large scale via the Unipol process. In th...
Low density polyethylene and polypropylene are produced at large scale via the Unipol process. In th...
Pressure fluctuations were measured in three gas-solids bubbling fluidized beds (10cm, 20cm, and 30c...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The hydrodynamics have been studied in a cold, freely bubbling, pressurized fluidized bed. The bed h...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The hydrodynamics have been studied in a cold, freely bubbling, pressurized fluidized bed. The bed h...
Numerical simulations using the Two Fluid Model are performed for gas-solid bubbling fluidized beds....
© 2017 Elsevier B.V. Gas-flow distribution plays a critical role in the performance of fluidized bed...
Measurements of the visible bubble flow rate and the through-flow velocity of gas inside bubbles hav...
Measurements of the visible bubble flow rate and the through-flow velocity of gas inside bubbles hav...
Low density polyethylene and polypropylene are produced at large scale via the Unipol process. In th...
Low density polyethylene and polypropylene are produced at large scale via the Unipol process. In th...
Low density polyethylene and polypropylene are produced at large scale via the Unipol process. In th...
Pressure fluctuations were measured in three gas-solids bubbling fluidized beds (10cm, 20cm, and 30c...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The hydrodynamics have been studied in a cold, freely bubbling, pressurized fluidized bed. The bed h...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The time-averaged solids velocity profiles in a freely bubbling, three dimensional, gas–solid fluidi...
The hydrodynamics have been studied in a cold, freely bubbling, pressurized fluidized bed. The bed h...
Numerical simulations using the Two Fluid Model are performed for gas-solid bubbling fluidized beds....
© 2017 Elsevier B.V. Gas-flow distribution plays a critical role in the performance of fluidized bed...
Measurements of the visible bubble flow rate and the through-flow velocity of gas inside bubbles hav...
Measurements of the visible bubble flow rate and the through-flow velocity of gas inside bubbles hav...
Low density polyethylene and polypropylene are produced at large scale via the Unipol process. In th...
Low density polyethylene and polypropylene are produced at large scale via the Unipol process. In th...
Low density polyethylene and polypropylene are produced at large scale via the Unipol process. In th...