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Spherical Drop Revisited

Previously the drag on a spherical droplet falling through an infinite fluid was obtained at Equation 7.25. On balancing this force with gravity, the terminal velocity U = U is obtained as [Pg.407]

There are two different ways of accounting for y or Vjy. The first consists of postulating a physical mechanism, which in this case is the effect of the presence of minute quantities of surface active impurities. The second is to define an effective surface viscosity, a matter considered further in Section 8. [Pg.407]

With the first of these models, y is the change in y due to adsorption of the impurities. The transport of these materials in bulk is governed at steady state by the conservation equation [Pg.407]

Finally, one has the equation of conservation of the adsorbed species, which at steady state simplifies from Equation 6.2 to [Pg.408]

In this special case it is considered that the adsorption-desorption is the rate limiting step, consequently c a) = the bulk concentration. It is further assumed that F deviates only a little from the equilibrium given by [Pg.408]


See other pages where Spherical Drop Revisited is mentioned: [Pg.407]    [Pg.407]   


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