Take the surfaces ,
,
, and
to be
one unit length in the
-direction. (To figure out the correct
direction of the normal vector
at a given surface point,
note that the control volume in this case is the right half of the
region in between two cylinders of radii
and
and of unit
length in the
-direction. The vector
is a unit normal
vector sticking out of this control volume.)
The faucet exit velocity is assumed to be of the form of Poisseuille
flow:
Take the faucet exit as the entrance of your control volume. Take
as exit to your control volume a slighly lower plane at which the
radius of the jet has stabilized to and the flow velocity has
become uniform (independent of r). For a uniform flow velocity
there are no viscous stresses. Gravity and pressure forces can be
ignored compared to the high viscous forces in this very viscous
fluid.