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Terminal particle velocity Single spheres

Temperature rise, centrifugal pump, 207-209 Terminal particle velocity, 228, 230 Particles, different densities, 238 Single spheres, 274 Solids in air, 237 Solids in water, 237 Test pressure, piping, 18 Thickeners and settleix/decanters, Decanter, 242... [Pg.630]

In concentrated suspensions, the settling velocity of a sphere is less than the terminal falling velocity of a single particle. For coarse (non-colloidal) particles in mildly shear-thinning liquids (1 > n > 0.8) [Chhabra et al., 1992], the expression proposed by Richardson and Zaki [1954] for Newtonian fluids applies at values of Re(= up to about 2 ... [Pg.222]

The equations for minimum fluidization velocity are similar to those for the terminal velocity of a single particle, and it is instructive to examine the ratio of these velocities. For small spheres, the equation for Stokes law divided by Eq. (9.2) gives... [Pg.366]

The single particle terminal velocity of the spheres in water may be taken as 1.1 mm/s. Calculate ... [Pg.81]

It is worthwhile to note that at both small and large Archimedes numbers, the minimum fluidization velocity, t/jjif, is directly proportional to the corresponding terminal velocity, Ut, of a single spherical particle of diameter in an infinite medium. For small spheres where the Stokes law applies, Ut/U ( approaches 74. For large spheres in the Newton s law regime, Ui/U ni approaches 8.6. [Pg.73]


See other pages where Terminal particle velocity Single spheres is mentioned: [Pg.109]    [Pg.326]    [Pg.252]    [Pg.601]    [Pg.82]    [Pg.58]   
See also in sourсe #XX -- [ Pg.274 ]




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