A gas convection model of heat transfer in large particle fluidized beds
β Scribed by Ronald L. Adams; James R. Welty
- Publisher
- American Institute of Chemical Engineers
- Year
- 1979
- Tongue
- English
- Weight
- 999 KB
- Volume
- 25
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
β¦ Synopsis
Abstract
A steady gas convection model of heat transfer to a horizontal cylinder immersed in a large particle gas fluidized bed has been developed. The model is based upon the hypothesis that the large particles will be isothermal and includes the effect of radiation as well as interstitial turbulence.
Results of calculations based on the model, for a twoβdimensional bubbling bed, indicate that a single bubble, having a diameter equal to the cylinder diameter, has a relatively small influence on the total heat transfer.
π SIMILAR VOLUMES
## Abstract Fluidized beds are particularly favored as chemical reactors because of their ability to exchange heat through immersed heatβexchange surfaces. However, little is known about how the heatβexchange process works on a singleβparticle level. The most commonly applied theory of fluidized be