PERMEATE FLOW IN HEXAGONAL 19-CHANNEL INORGANIC MEMBRANE UNDER FILTRATION AND BACKFLUSH OPERATING MODES

Numerical simulations and experimental study of incompressible Newtoni an permeate flow in porous support of hexagonal 19-channel inorganic m embrane are presented both for filtration and backflush operating mode s. Under several simplifying assumptions the problem could be treated as two-dimensional potential flow. The mathematical model was solved u sing finite element method. The results of numerical simulations show that the contributions of particular channels to the total permeate fl ux are not equal and depend on the ratio of skin layer to porous suppo rt permeability as well as on the distance of a channel from the membr ane outer surface. For membranes with high permeability of skin layer there is an area of nearly constant pressure around inner channels and their contribution to total flux is negligible. This effect will prob ably be more pronounced in backflush operating mode while in filtratio n mode possible dynamic membrane adds a resistance to that of skin lay er which leads to more uniform permeate flux distribution. Qualitative trends of the numerical simulations were verified by experiments with ceramic 19-channel membranes of Membralox(R) type in backflush operat ing mode. (C) 1998 Elsevier Science B.V. All rights reserved.