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On the two-phase theory of fluidisation

✍ Scribed by M.J. Lockett; J.F. Davidson; D. Harrison


Publisher
Elsevier Science
Year
1967
Tongue
English
Weight
499 KB
Volume
22
Category
Article
ISSN
0009-2509

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✦ Synopsis


Theory is given to predict the value of k in the equation for a bubbling fluidised bed U=kUo+ QB/A; here U is the superficial fluidising velocity, U= U0 at incipient fluidisation, Qn is the observed bubble flow, and A the cross-sectional area of the bed. In the simple two-phase theory, k = 1 ; but the theory herein, assuming constant voidage fraction between the bubbles, shows that for a regular array of bubbles, k = 1 +e~ for a two-dimensional system, provided tb =volume of all bubbles/ bed volume, is small. It is inferred that for a three-dimensional system, k= 1 +2e~.

Thus the simple two-phase theory, though not strictly correct, is not much in error; the error is likely to be largest when U is not much greater than U0, and particularly just above the distributor of a fluidised bed.


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