into which we have to insert dz|da.
Virtually no error is introduced
by making the upper limit infinite. From the definition of o
z2 = —4(fl — r)2 o 2 + 4x(fl — r)o
The first term on the right is smaller than the second, at least for
small z. Then dz — ( )da / , and the pressure drop expression
becomes (with § 2 = n)
3’2
-4 2(A — r)3 ’0 /(y 2 ) d) = 3*A*o
) 5/2
2(X-
where
4 2
2J' = 0. 531
3
The pressure drop multiplied by the tube cross-section
must, according to an overall force balance, be equal to the net force
acting cm the sphere by gravity and buoyancy
where p, and p are the densities of the sphere and fluid respectively.
Combining the last three results gives the equation for the viscosity
5/2
(pt —p)gsinjS
'
9
2D.2 Drainage of liquids
n. The unsteady mass balance is
(pdW)=(p »,)wa)| — p(»,)wa)|,+
Divide by pWAz and take the limit as Az —+ 0, to get Eq. 2D.2-1.
h. Then use Eq. 2.2-22 to get Eq. 2D.2-1:
b6 pg 863 pg62 #6
8f 3y 8z p 8z
which is a first-order partial differential equation.
c. First let A = pgf , so that the equation in (b) becomes:
Inspection of the equation suggests that A = , which can be seen
to satisfy the differential equation exactly. Therefore Eq. 2D.2-3
follows at once. This equation has a reasonable form, since for long
times the boundary layer is thin, whereas for short times the
boundary layer is thlCk.