The influence of internal geometry and angular velocity on the performance
of a rotating-disk filtration device is described. This module consists of
a disk rotating at speeds up to 2,000 rpm inside a cylindrical housing equi
pped with a fixed flat membrane. The test fluid was a calcium carbonate sus
pension (4.7-mu m mean particle diameter), and the membranes were in nylon
(0.2-mu m mean pore diameter) and PVDF (0.1 and 0.18 mu m). The shear stres
s on the stationary membrane in the laminar boundary-layer regime was estim
ated from a similarity solution, and in the turbulent regime from the frict
ion coefficient for a flat plate. Several inlet and outlet configurations w
ere tested. The permeate flux was independent of the axial gap (disk to mem
brane), but increased when the radial gap (from disk to housing) was raised
from 2 to 5 mm. The inviscid fluid core in the axial gap was observed to r
otate at 42% of angular velocity with a smooth disk. This factor rose to 64
% when the disk was equipped with small vanes. Fouling was limited to the c
entral part of the membrane at 1,500 rpm and disappeared completely for a d
isk equipped with vanes. Permeate fluxes were consistently much higher than
in classic cross-flow filtration.