𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Residence times in fluidized beds with secondary gas injection

✍ Scribed by D. Christensen; J. Nijenhuis; J.R. van Ommen; M.-O. Coppens


Publisher
Elsevier Science
Year
2008
Tongue
English
Weight
518 KB
Volume
180
Category
Article
ISSN
0032-5910

No coin nor oath required. For personal study only.

✦ Synopsis


Experiments were carried out to determine the effects of secondary gas injection on the gas residence time and macromixing characteristics in a bubbling fluidized bed. Primary gas is introduced via a bottom distributor plate, while secondary gas is introduced via a fractal injector submerged in the bed. Results indicate that the average residence time decreases only slightly. Calculated overall reactor PΓ©clet numbers indicate that the gas experiences less back-mixing with secondary gas injection. The bubble size was observed to decrease by up to 70%, indicating improved gassolid contact. Taking this improved contact and plug flow behavior into account, the conversion in a fluidized bed with secondary gas injection is expected to increase significantly, particularly for mass-transfer limited reactions.


πŸ“œ SIMILAR VOLUMES


Particle Residence Times in Fluidized Be
✍ M. BΓΆrner; M. Peglow; E. Tsotsas πŸ“‚ Article πŸ“… 2011 πŸ› John Wiley and Sons 🌐 English βš– 450 KB πŸ‘ 1 views

## Abstract Various types of fluidized bed equipments used in granulation were experimentally investigated in order to gain a more detailed insight in particle recirculation behavior and particle residence times in the two considered compartments, namely the spray compartment and the drying compart

Fluidized-solids reactors with continuou
✍ Sakae Yagi; Daizo Kunii πŸ“‚ Article πŸ“… 1961 πŸ› Elsevier Science 🌐 English βš– 638 KB

The distribution of residence times of solid particles is examined in fluidized beds at steady state with continuous feed and discharge of solids, both for beds consisting of a single particle size and for beds consisting of a wide spectrum of particle sizes. The mean age (residence time in bed) of

Moisture Distribution in Fluidized Beds
✍ L. Fries; M. Dosta; S. Antonyuk; S. Heinrich; S. Palzer πŸ“‚ Article πŸ“… 2011 πŸ› John Wiley and Sons 🌐 English βš– 474 KB

Coupled discrete element method-computational fluid dynamics (DEM-CFD) simulations have been performed to study the fluid and particle dynamics in a fluidized-bed granulator on the scale of individual particles. Simulation of the gas and particle dynamics is combined with heat and mass transfer mech