## IN THEIR paper "Consecutive film and surface renewal mechanisms for heat and mass transfer from a wall", Wasan and Ahluwalia [l] formulate a model to describe the consequences of fluid replacement taking place to within some limiting distance of the transfer surface. Thus, they combine the effe
A single particle model for surface-to-bed heat transfer in fluidized beds
β Scribed by Francesco Di Natale; Amedeo Lancia; Roberto Nigro
- Publisher
- Elsevier Science
- Year
- 2008
- Tongue
- English
- Weight
- 789 KB
- Volume
- 187
- Category
- Article
- ISSN
- 0032-5910
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β¦ Synopsis
This paper presents a semi empirical single particle model for the description of heat transfer coefficient between a submerged surface and a fluidized bed. The model is applied to several experimental data and gives a satisfactory description of the effect of pressure, temperature and bed material properties on the heat transfer coefficient either in bubbling or slugging fluidized beds. The model considers the averaged surface void fraction as the only regression parameter for the description of experimental data. Surface void fraction results to be a function of Archimedes number and minimum fluidization bed voidage and its value is consistent with the numerical and experimental data reported in literature.
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## 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
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 mve
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