Permeability and compressibility data are required for an adequate pro
cess model for compressible-cake filtration and mechanical expression.
Experimental and modeling results of the permeability of palm-oil fil
ter cakes (a highly compressible viscoelastic material) are combined w
ith compressibility data, leading to a model for the expression step.
Permeability measurements show that permeability depends strongly on t
he quantity of fine particles in the cake. Removal of fine particles f
rom the slurry before expression significantly increases the solid-pha
se content during expression due to higher permeability. Modeling resu
lts of the expression step show that for palm-oil filter cakes there i
s a pressure above which the attainable mass fraction of solids become
s independent of pressure. Decrease in specific cake resistance has tw
o effects: a higher mass fraction of solids at the same pressure and a
higher pressure at which the mass fraction of solids is not affected
further.