## Abstract Fluidized beds are particularly favored as chemical reactors because of their ability to exchange heat through immersed heatโexchange surfaces. However, little is known about how the heatโexchange process works on a singleโparticle level. The most commonly applied theory of fluidized be
Particle-to-particle heat transfer in fluidized bed drying
โ Scribed by J. Vanderschuren; C. Delvosalle
- Publisher
- Elsevier Science
- Year
- 1980
- Tongue
- English
- Weight
- 808 KB
- Volume
- 35
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
โฆ Synopsis
Partlcle-to-emulsion and mterpartrcle heat transfer rates were estimated in the range 1 5 G u/u,,,f 6 3 5, 0 69 c $ G 2 15 mm by drymg wet refractory partlcles m fluldlzed beds of smular dry partlcles of the same sues Overall particle-toemulslon heat transfer coefficients decrease roughly as the mverse of the particle diameter Particle to-particle heat transfer coefficients vary with the power-2 of the particle diameter and decrease as the flmdlzatlon velocity increases
๐ SIMILAR VOLUMES
Abstraet-Fluid-particle heat transfer in lixed and fluid&d beds is re-examined. The heat transfer factor depends not only on the particle Reynolds number but also on the void fraction of the bed. The available experimental data has been correlated to yield a non-linear relationship between rJh and t
## Abstract Heat conduction during contact between a heat transfer surface and fluidizing particles, a phenomenon which is one of the effective heat transfer mechanisms in a gasโsolid fluidized bed, has been empirically investigated. The temperature profile of the fluidizing particles during the co