Hostname: page-component-78c5997874-ndw9j Total loading time: 0 Render date: 2024-11-05T13:40:59.092Z Has data issue: false hasContentIssue false

Note on Murray's paper on bubbles in fluidized beds

Published online by Cambridge University Press:  28 March 2006

P. N. Rowe
Affiliation:
Chemical Engineering Division, A.E.R.E. Harwell Present address: Department of Chemical Engineering, University College London.
B. A. Partridge
Affiliation:
Chemical Engineering Division, A.E.R.E. Harwell

Abstract

Murray's equation (53) for the velocity of rise of a three-dimensional (spherical) bubble of diameter dB can be written $U_B = K[gd_B|6c]^{\frac{1}{2}}$ where the unassigned coefficient c enters Murray's analysis in the linearization of the convective momentum term in the momentum equation for the solids (17). (Equations (53) and (17) are as numbered in Murray 1965b.) This compares with the expression $U_B = K[\frac{1}{2}gd_B]^{\frac{1}{2}}$ used by Rowe & Partridge (1965), who determined the velocity coefficient, K, for several fluidized systems by measuring bubble diameter and velocity from X-ray ciné photographs. Values of c calculated from the measured values of K are listed in table 1, from which it is seen that the coefficients are not truly constant. The observed values of Murray's c are also appreciably less than c = 1 or c = ⅗, the two values tentatively suggested by mathematical reasoning, and Murray's figure 13, based on earlier velocity measurements over a limited range of particle sizes, is not a critical test of the value of the constancy of c.

Type
Research Article
Copyright
© 1965 Cambridge University Press

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

Murray, J. D. 1965a J. Fluid Mech. 21, 465.
Murray, J. D. 1965b J. Fluid Mech. 22, 57.
Rowe, P. N. & Partridge, B. A. 1965 Trans. Inst. Chem. Engrs. 43, 157.