Silicon carbide ceramic filters consisting of highly porous support and fil
tration layer were fabricated by cold isostatic pressing. The porosities of
the supports were varied near the percolation threshold, 28.7, 33.7 and 35
.8%. The silicon carbide layer with a finer pore size was coated on the sup
ports to collect dust particles. The pressure drop (JP) was measured at var
ious face velocities, dust loadings, and operation times. The separation ef
ficiency was calculated by measuring the dust concentrations at the inlet a
nd outlet of the filter vessel, and the cleaning efficiency was calculated
by comparing the pressure drops before and after back-pulse cleaning. The r
esults indicate that higher porosity of the filter support is favorable for
preventing an increase of pressure drop and for improving cleaning efficie
ncy. As the porosity in the silicon carbide filter support increased from 2
8.7% to 35.8%, the pressure drop decreased by as much as 30%. Most of dust
particles were collected by the finer pores in the coating layer with effic
iencies > 99.9%. Additionally, better cleaning efficiency was obtained at h
igher porosity. The values of flexural strengths of the filter supports wer
e over 20 MPa even though a lower value was found at high porosity.