As the use of hydrocyclones for liquid-liquid separation becomes incre
asingly common, the need for a satisfactory method to assess their eff
iciency increases. Currently available efficiency theories were develo
ped for liquid-solid separations based on the velocity distributions i
nside a hydrocyclone. These theories, however; appear less suitable fo
r emulsions where the dispersed phase is slightly lighter than the con
tinuous phase, such as oil/water emulsions. An efficiency computation
based on the analysis of the trajectories of the droplets is presented
. Trajectories are characterized through a differential equation combi
ning models for the three bulk velocity distributions (axial, radial,
and tangential) and the settling velocity defined by Stokes' law. From
the critical trajectory and given operating conditions, a characteris
tic droplet diameter d(100) can be deduced that corresponds to the sma
llest droplet with a 100% efficiency. Other efficiencies are obtained
by changing the initial condition for the trajectory equation. The eff
iciency results of different hydrocyclone configurations are compared
with experimental results, and residual emulsion distributions are est
imated.