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.
The unknown velocities used in the computation should be taken to be
the polar components and
. But momentum
conservation for
-momentum is asked. (Conservation of
-momentum or
-momentum would be complete nonsense.) So
you will need to write the
-component of velocity in terms of the
polar unknowns. Note that