Wr. Bowen et Ao. Sharif, HYDRODYNAMIC AND COLLOIDAL INTERACTIONS EFFECTS ON THE REJECTION OF APARTICLE LARGER THAN A PORE IN MICROFILTRATION AND ULTRAFILTRATION MEMBRANES, Chemical Engineering Science, 53(5), 1998, pp. 879-890
The application of membrane separation processes, such as microfiltrat
ion and ultrafiltration, is one of the most important developments in
chemical engineering in recent years. Membrane fouling is the most imp
ortant problem which restricts application of membrane processes. Rece
ntly, it has been demonstrated that colloidal and hydrodynamic interac
tions govern membrane fouling and they can be manipulated by choice of
processing conditions, for example, pH, ionic strength and applied pr
essure. The paper presents a quantification of both colloidal (electro
static and van der Waals) and hydrodynamic effects to identify conditi
ons for the operation of such processes with much greater efficiency.
In particular, the hydrodynamic and colloidal forces on a charged sphe
rical particle slightly larger than a pore at various distances from a
charged cylindrical pore in a charged planar surface have been calcul
ated. In the absence of electrostatic interactions, filtration of such
particles can result in a catastrophic loss in flux as they can plug
pores highly effectively. The rejection of the particle at a membrane
pore is described in terms of a balance between the hydrodynamic force
which is driving the particle towards the membrane and the colloidal
forces between the charged particle and the charged membrane surface.
A Galerkin finite element scheme combined with automatic mesh refineme
nt and error estimation strategy has been used to provide numerical so
lutions of the non-linear Poisson-Boltzmann equation for electrostatic
interactions and of the Navier-Stokes equation for hydrodynamic inter
actions. The results show that under the conditions covered by the cal
culations, which correspond to those occurring in practice, the electr
ostatic interactions can play a crucial role in controlling the approa
ch of such a particle to a pore. The calculations have a number of imp
ortant consequences for membrane separation processes. Firstly, the qu
antification of the operating conditions which allow separation withou
t the particles coming into intimate contact with the membrane-potenti
ally non-fouling conditions. Secondly, a demonstration that the manufa
cture of membranes with a high surface potential would be very benefic
ial to the efficient operation of such processes. (C) 1998 Elsevier Sc
ience Ltd. All rights reserved.