Charge effects on inorganic membrane performance in a cross-flow microfiltration process

Abstract Cross-flow microfiltration experiments were performed with 0.5 μm silica particles using an inorganic membrane of 0.2 μm pore size. We analysed how several physico-chemical factors, such as solution pH, salt concentration, and valency of the salt influenced permeate flux and fouling tendencies. The electrostatic properties of silica particles (feed suspension) and α-alumina particles (active layer of the membrane) were characterised by performing zeta potential measurements. It was found that the permeate flux is dependent on the surface charge of the suspended particles and possibly dependent on the surface charge of the membrane. High permeate fluxes are obtained at high pH and low salt concentration. Under these circumstances the repulsion between the silica particles is strong. In contrast, low filtration fluxes are measured at high salt concentration, low pH, and with a CaCl2 electrolyte, i.e. when the surface charges are weak and in the presence of specific cations. The net energy of interaction between the charged surfaces involved in the microfiltration process was calculated using the DLVO theory. This gave qualitative arguments for the explanation of the observed changes in the permeate flux.

[1]  H. C. Hamaker The London—van der Waals attraction between spherical particles , 1937 .

[2]  W. Bowen,et al.  Dynamic ultrafiltration model for charged colloidal dispersions : a Wigner-Seitz cell approach , 1995 .

[3]  Richard A. Williams,et al.  PARTICLE DEPOSITION AT A CHARGED SOLID/LIQUID INTERFACE , 1990 .

[4]  R. Horn,et al.  Double-Layer and Hydration Forces Measured between Silica Sheets Subjected to Various Surface Treatments , 1993 .

[5]  B. Derjaguin,et al.  Inclusion of structural forces in the theory of stability of colloids and films , 1985 .

[6]  Anthony G. Fane,et al.  Surface charge and permeability in the ultrafiltration of non-flocculating colloids , 1984 .

[7]  A. Trägårdh,et al.  Properties of the cake layer formed during crossflow microfiltration , 1998 .

[8]  E. Verwey,et al.  Theory of the stability of lyophobic colloids. , 1955, The Journal of physical and colloid chemistry.

[9]  M. Wiesner,et al.  pH and ionic strength effects on the performance of ceramic membranes in water filtration , 1994 .

[10]  J. Israelachvili Intermolecular and surface forces , 1985 .

[11]  T. Healy,et al.  Effect of particle size on colloid stability , 1970 .

[12]  R. J. Hunter Zeta potential in colloid science : principles and applications , 1981 .

[13]  J. Israelachvili,et al.  Forces Between Surfaces in Liquids , 1982, Science.

[14]  Feng-Chia Hsu,et al.  Steady-state permeate flux of cross-flow microfiltration , 1995 .

[15]  Anthony G. Fane,et al.  Charge effects in the cross-flow filtration of colloids and particulates , 1989 .