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Distributed parameter control of a batch fluidised bed dryer

โœ Scribed by Javier A. Villegas; Stephen R. Duncan; Haigang G. Wang; Wuquiang Q. Yang; Rambali S. Raghavan

Book ID
118435263
Publisher
Elsevier Science
Year
2009
Tongue
English
Weight
689 KB
Volume
17
Category
Article
ISSN
0967-0661

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๐Ÿ“œ SIMILAR VOLUMES

Distribution of gas flow in a fluidised
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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

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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

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Based on the observed pattern of coalescence of bubble pairs in vertical alignment in a two-dimensional bed, a theory is developed which describes how bubble size and frequency changes with height in a gas fluidised bed. It is confirmed by comparison with the reported data from 10 separate investiga