A one-dimensional modelling of constant pressure deliquoring based on
not more than three material specific parameters was achieved by the f
ollowing basic assumptions: two regions of void ratio are defined. Fro
m the initial value down to a threshold value e(i), the solid-solid in
teraction is neglected; only when the water content falls short of e(i
), an elastic network with increasing elasticity modulus is formed. Fi
ltration and consolidation are not regarded as subsequent stages, but
are assumed to occur at varying extents during the whole process. The
profile of porosity is approximated by a rectangular function while th
e profiles of liquid pressure and the elasticity modulus inside the co
mpressed zone are approximated by hyperbolic functions. The compressed
zone is characterized by an average solid stress sigma(c) and an aver
age filtration resistance R(c) both related to the volume of the expre
ssed or filtrated liquid V (maximal amount V(E)). The proportionality
between sigma(c) and V and that between dR(c) and dV/(V(E) - V) are in
herent empirical conditions. For the initial stage of solid-liquid sep
aration, a strong non-linear profile of the filtration resistance resu
lts and this is discussed usually to be due to a ''skin effect''. The
model was successfully applied to the kinetics of the press-dewatering
of different materials: suspension of protein, sawdust, semi-solid cl
ay and sugar-beet tissue. Additional parameters describing the seconda
ry consolidation were not required. Filtration was shown to be a bound
ary case of the model.