Numerical modelling of mass transfer in slits with semi‐permeable membrane walls

A mathematical model to predict the concentration polarisation in nanofiltration/reverse osmosis is described. It incorporates physical modelling for mass transfer, laminar hydrodynamics and the membrane rejection coefficient. The SIMPLE algorithm solves the discretised equations derived from the governing differential equations. The convection and diffusive terms of those equations are discretised by the upwind, the hybrid and the exponential schemes for comparison purposes. The hybrid scheme appears as the most suitable one for the type of flows studied herein. The model is first applied to predict the concentration polarisation in a slit, for which mathematical solutions for velocities and concentrations exist. Different grids are used within the hybrid scheme to evaluate the model sensitivity to the grid refinement. The 55×25 grid results agree excellently for engineering purposes with the known solutions. The model, incorporating a variation law for the membrane intrinsic rejection coefficient, was also applied to the predictions of a laboratory slit where experiments are performed and reported, yielding excellent results when compared with the experiments.

[1]  P. L. T. Brian,et al.  Concentration Polar zation in Reverse Osmosis Desalination with Variable Flux and Incomplete Salt Rejection , 1965 .

[2]  Ken Darcovich,et al.  Turbulent transport in membrane modules by CFD simulation in two dimensions , 1995 .

[3]  B. P. Leonard,et al.  A stable and accurate convective modelling procedure based on quadratic upstream interpolation , 1990 .

[4]  R. J. Goldstein,et al.  Laminar Separation, Reattachment, and Transition of the Flow Over a Downstream-Facing Step , 1970 .

[5]  A. S. Berman Laminar Flow in Channels with Porous Walls , 1953 .

[6]  Robert L. Laurence,et al.  Influence of slip velocity at a membrane surface on ultrafiltration performance—I. Channel flow system , 1979 .

[7]  O. Hassager,et al.  Simulation of transport phenomena in ultrafiltration , 1993 .

[8]  Internal separated flows at large Reynolds number , 1980 .

[9]  Thomas K. Sherwood,et al.  Desalination by Reverse Osmosis , 1967 .

[10]  B. Armaly,et al.  Experimental and theoretical investigation of backward-facing step flow , 1983, Journal of Fluid Mechanics.

[11]  R. A. Seban Heat Transfer to the Turbulent Separated Flow of Air Downstream of a Step in the Surface of a Plate , 1964 .

[12]  S. Patankar Numerical Heat Transfer and Fluid Flow , 2018, Lecture Notes in Mechanical Engineering.

[13]  S. J. Kline,et al.  Experimental Investigation of Subsonic Turbulent Flow Over Single and Double Backward Facing Steps , 1962 .

[14]  D. Spalding A novel finite difference formulation for differential expressions involving both first and second derivatives , 1972 .

[15]  Michael A. Leschziner,et al.  Practical evaluation of three finite difference schemes for the computation of steady-state recirculating flows , 1980 .

[16]  Pierre J. Carreau,et al.  Modeling of ultrafiltration : predictions of concentration polarization effects , 1994 .

[17]  Christian Bouchard,et al.  Computer simulation of membrane separartion processes , 1989 .

[18]  R. I. Kermode,et al.  Prediction of concentration polarization and flux behavior in reverse osmosis by numerical analysis , 1990 .

[19]  Christian Trägårdh,et al.  Computer simulations of mass transfer in the concentration boundary layer over ultrafiltration membranes , 1993 .

[20]  Thomas K. Sherwood,et al.  Salt Concentration at Phase Boundaries in Desalination by Reverse Osmosis , 1965 .