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