The faucet exit velocity may be 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 can be ignored compared to
the high viscous forces in this very viscous fluid. (However, over
a longer distance gravity will lead to a further thinning of the
jet.) And you can assume that the pressure at the exit is already
atmospheric, as it definitely is in the lower plane below.
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 in Cartesian coordinates, the polar unit
vectors are given by