The high-shear rotary ultrafiltration (UF) system uses membrane rotati
on to provide the turbulence required to minimize concentration polari
zation and flux decline. The high-shear UF system was effective in con
centrating oily wastes from about 5% to as high as 65%. The decoupling
of turbulence promotion from feed pressurization/recirculation by rot
ating the membrane was the primary reason for the improvement in perfo
rmance over that observed with conventional UF systems. Transitional a
nd gel layer oil concentrations (20% and 50-59%, respectively) were hi
gher than values reported in the literature. Permeate flux was depende
nt on the temperature and rotational speed. Flux increased by about 45
% when the temperature was increased from 43 to 60 degrees C. A larger
decrease in waste viscosity, over that predicted for water alone, and
increased oil droplet diffusivity were hypothesized as reasons for th
e stronger than expected flux-temperature relationship. The flux-rotat
ional speed (omega) relationship was described by J = f(omega)(0.90);
however, the gel layer exhibited stability with increasing omega. The
ceramic membrane was superior to the polymeric membrane in regards to
permeate flux and quality as well as cleaning and durability.