๐”– Bobbio Scriptorium
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Thermal dispersion and wall heat transfer in packed beds

โœ Scribed by D.J. Gunn; M. Khalid


Publisher
Elsevier Science
Year
1975
Tongue
English
Weight
548 KB
Volume
30
Category
Article
ISSN
0009-2509

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โœฆ Synopsis


Abstxact-A new analysis showing the effect of axial and radial thermal dispersion and wall thermal resistance upon heat transfer to fixed beds of solids is presented. By application of this theory and non-linear regression, coefficients of axial and radial dispersion and wall heat transfer coefficients are calculated from experimental measurements of radial temperature protiles in fixed beds heated at the wail.

The experiments have been performed for beds packed with glass and with metallic particles within the particle Reynolds number range from 1 to 400.

The calculated coefficients are compared with experimental values reported by other workers. Some dzerences are attributed to the neglect of axial dispersion in the work of others, but other differences are significant in that, for example, thermal characteristics of fixed beds of metallic particles diier from those of non-metallic particles.


๐Ÿ“œ SIMILAR VOLUMES


Heat transfer and axial dispersion in pa
โœ D.J. Gunn; J.F.C. De Souza ๐Ÿ“‚ Article ๐Ÿ“… 1974 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 657 KB

The thermal frequency response of beds packed with glass and metallic particles has been measured in the range of Reynolds numbers from 0.05 to 330. Values of the coefficients of axial dispersion of heat, intraparticle thermal conductivity and fluid-particle heat transfer coefficients have been foun

Nature of wall heat transfer coefficient
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A mechanism of heat transfer from a tube wall to fluid flowing in a packed bed is proposed whereby : (1) a mass of fluid is thrown against the wall ; (2) the fluid at the wall assumes the wall temperature and transfer occurs inward ; (3) this mass of fluid moves away from the wall and is replaced by

Heat transfer in packed beds
โœ A.P. de Wasch; G.F. Froment ๐Ÿ“‚ Article ๐Ÿ“… 1972 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 743 KB

The heat transfer between a fluid flowing through a packed bed and the wall is interpreted according to a one-dimensional model characterized by an overall heat transfer coefficient, h, and by two-dimensional models with one parameter, the effective thermal conductivity, k, or two parameters, the ef