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Mass transfer from a slug in a fluidised bed: Wall effect

โœ Scribed by J.R.F.Guedes de Carvalho; J.F. Davidson

Publisher
Elsevier Science
Year
1978
Tongue
English
Weight
389 KB
Volume
33
Category
Article
ISSN
0009-2509

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โœฆ Synopsis

Ah&act

-The mass transfer coel&xent IS predxted for cfiffuslon from a large gas bubble (slug) nsmg m a gas-tidised bed of fine particles cU&uaed m 8 verhcal tube The theory *) 8 modiiicatma of an ex~stmg result for gas/hqmd systems, to allow for the w&effect tlus IS .s&ca.nt m a gas-fhudwd bed because the III& &as phase dhsmty Do gwes penetrahm of the ddhsant to the tube wall

๐Ÿ“œ SIMILAR VOLUMES

48 Catalytic oxidation of o-xylene in a
48 Catalytic oxidation of o-xylene in a slugging fluidised bed
โœ J.G. Yates; J.-Y. Gregoire ๐Ÿ“‚ Article ๐Ÿ“… 1980 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 440 KB

A slugging-bed reactor has been used to study the catalytic oxidation of o-xylene Predictions of conversion based on published theoretical reactor models have been compared with the experimental results and it has been found that the model of Raghuraman and Potter suitably modified to account for re