๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

On atomising a liquid into a gas fluidised bed

โœ Scribed by P.G. Smith; A.W. Nienow


Publisher
Elsevier Science
Year
1982
Tongue
English
Weight
375 KB
Volume
37
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.


๐Ÿ“œ SIMILAR VOLUMES


A circulating liquid fluidised bed
โœ L.G. Gibilaro; R. Di Felice; P.U. Foscolo ๐Ÿ“‚ Article ๐Ÿ“… 1988 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 286 KB
A model for a segregating gas fluidised
โœ L.G. Gibilaro; P.N. Rowe ๐Ÿ“‚ Article ๐Ÿ“… 1974 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 736 KB

A differential equation model is derived to describe particle segregation in a binary mixture of solids fluidised by gas. The model, which is formulated to conform with qualitative descriptions of the mechanism of segregation, yields solutions displaying the unusual features of the steady-state soli

Spontaneous oscillation of a gas-fluidis
โœ M.H.I. Baird; A.J. Klein ๐Ÿ“‚ Article ๐Ÿ“… 1973 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 834 KB

Well dellned spontaneous oscillations can occur in a gas-fluidised bed with a low resistance support and a large gas space beneath the support. Measurements of the instantaneous pressure drop as a function of time have been carried out in a 10 cm dia. bed with gas space volumes between 11 and 191. A

Distribution of gas flow in a fluidised
โœ K. Godard; J.F. Richardson ๐Ÿ“‚ Article ๐Ÿ“… 1968 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 85 KB

NOTATION diffusion coefficient of Fe(CN&" in the solution; m2/sec diameter of the sphere; m mass-transfer coefficient; m/set translational velocity; m/set angular velocity: rad./sec kinematic viscosity of the fluid; m\*/sec Reynolds number for translation, Vd/v Reynolds number for rotation, od\*/v R

Distribution of gas flow in a fluidised
โœ M.J. Lockett; J.F. Davidson; D. Harrison ๐Ÿ“‚ Article ๐Ÿ“… 1968 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 106 KB

WE HAVE the following comments to make in reply to the communication by Mr. Godard and Professor Richardson: I. Equation (I) in our paper [ I] refers to a bubbling fluidised bed with constant voidage fraction between bubbles. Most liquid-solid systems are non-bubbling and of course fall outside the