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I J Sobey

Publications and source records attributed to I J Sobey.

2 recordsLinked to original sources

Enhanced filtration using flat membranes and standing vortex waves.

The performance of membrane filters is limited by concentration polarisation and membrane fouling. High shear rates reduce these effects but can damage delicate cells and proteins in biological fluids. Secondary flows to promote fluid mixing, and hence enhance filtration, can be highly effective, but usually carry the penalty of complexity. Oscillatory flow over furrowed or dimpled membrane surfaces (vortex mixing) has been shown to be very efficient in the microfiltration and oxygenation of blood, but carries the added complexity of oscillatory flow and the need to thermoform the membranes. To allow the use of asymmetric or rigid membranes, a new form of vortex mixing has been studied, in which the membranes are flat and form parallel channels. Feed flow is oscillatory and passes back-and-forth across ladder-like flow deflectors to generate standing vortex waves. Flow visualisation studies and numerical calculations of standing vortex waves (SVW) were undertaken to help optimise flow parameters and flow deflector geometry. Flat plate membrane ultrafilters were built and evaluated for different geometries of flow deflector, using solutions of bovine serum albumin (BSA) as the test fluid. Very high filtration rates were measured with BSA concentrations ranging from 1 to 24%. A SVW ultrafilter was compared with a Millipore Pellicon ultrafilter using BSA as the test fluid. Filtration flux was similar at low concentrations of BSA, but was greater by a factor of 4.5 in the SVW device at high concentrations of BSA.

Chemical Engineering↗

Gel layer limited haemofiltration rates can be increased by vortex mixing.

Haemofiltration has been used since 1976 as an alternative to haemodialysis in the treatment of chronic renal failure (1). Ultrafiltration flow rates (UFR) from blood are slow and it has been observed that when blood or plasma is ultrafiltered using highly permeable membranes, the UFR reaches a maximum which is independent of trans-membrane pressure (delta Pm) (2). We have confirmed this result during steady flow through an ultrafilter employing polyacrylonitrile membrane (Rhône Poulenc AN 69) but have also shown that this maximum can be exceeded by a factor of eight in the same device when vortex mixing is induced by pulsing the blood flow over furrowed channels.

Blood↗