T. Moritz et al., Influence of the surface charge on the permeate flux in the dead-end filtration with ceramic membranes, SEP PURIF T, 25(1-3), 2001, pp. 501-508
The filtering properties of membranes in the ultra and nano filtration rang
e cannot only be derived from a pure sieving effect. With decreasing membra
ne pore size the surface charge of the membranes and the charge density bec
ome more and more important with regard to its retention and selectivity. T
ypical parameters like permeate flux and retention of salt ions, particles
or molecules are governed by a so-called effective pore diameter depending
on the surface charge and the thickness of the electrochemical double layer
on the pore walls. Fouling mechanisms, i.e. cake forming and pore blocking
, which cause a permeate flux decline in the filtration process are also st
rongly influenced by the surface charge of the membrane. In the case of liq
uid saturated oxide ceramic membranes a surface charge results from dissoci
ated surface groups and adsorbed charge determining ions. Ceramic ultra fil
tration membranes made of TiO2, ZrO2, alpha- and gamma -Al2O3 were investig
ated by streaming potential measurements. For these measurements an Electro
kinetic Analyser EKA from Anton Paar, Austria, was used. The membranes were
characterized by a tangential flow method. This means, an electrolyte solu
tion is forced through a narrow slit formed by the surfaces of two similar
membranes which are positioned facing one another. In this way the dependen
ce of the surface charge on the pH was shown. Using the Helmholtz-Smoluchow
ski equation the surface charge density can be expressed by the C-potential
. The permeate fluxes of polyethylenimine solutions and dextrane solutions
through the membranes in a dead-end filtration process at different pH-valu
es were investigated by means of a filtration testing device. The pH values
chosen for these experiments result either in a high positive, a high nega
tive or in a net zero charge of the appropriate membrane material. The abso
lute permeate flux and its drop with increasing filtering time strongly dep
end on the charge conditions of the membrane surface and the charge of the
particles, molecules or ions in the feed solution. Improved filtering condi
tions can be achieved if the membrane and the content of the feed solution
show a similar charge, since the electrostatic repulsion decelerates the fo
rmation of a flux reducing fouling layer on the membrane surface. (C) 2001
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