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The principle of centrifugal separation

The principle of centrifugation of a particle within a rotating flow has already been treated in section 16.6 of Chapter 16 using the BBOT equations. Here, we formulate differently the behavior of a particle in a rotational flow, using a physical approach that sets out the main forces governing the dynamics. [Pg.377]

We consider an axisymmetric fluid flow rotating about an axis Oz. The rotation dominates, that is, Ur ue and ue. This hypothesis is, to a very large extent, [Pg.377]

There is in the fluid a radial pressure gradient which balances the centrifugal force applied on a fluid particle. [Pg.378]

Let us now consider a spherical particle of diameter d and density ps, placed in the fluid flow. We denote by, uep, and u p the radial, azimuthal, and axial components of the particle s velocity in the cylindrical coordinate system of axis Oz. The main results from Chapter 16 are the following  [Pg.378]

Since the particle is small, the friction resistance to the relative radial displacement of the particle with respect to the fluid is expressed by Stokes law (Chapter 15, section 15.1)  [Pg.378]


In the following, we successively apply the principle of centrifugal separation to the configuration of discontinuous decanter and then to that of a continuous decanter. [Pg.381]


See other pages where The principle of centrifugal separation is mentioned: [Pg.377]   


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