The effect of shell side hydrodynamics on the performance of axial flow hollow fibre modules

• Published in: Journal of membrane science Vol. 80; no. 1; pp. 1 - 11
• Main Authors: Costello, M.J., Fane, A.G., Hogan, P.A., Schofield, R.W.
• Format: Journal Article Conference Proceeding
• Language: English
• Published: Amsterdam Elsevier B.V 02.06.1993; Elsevier
• Subjects: Chemistry; Colloidal state and disperse state; contactor; Exact sciences and technology; fluid flow; General and physical chemistry; hollow fibre; mass transfer; Membranes; shell side; hollow fibre; shell side; fluid flow; mass transfer; contactor; Water; Propylene polymer; Hollow fiber; Membrane; Experimental study; Dissolved oxygen; Mass transfer
• ISSN: 0376-7388; 1873-3123
• DOI: 10.1016/0376-7388(93)85127-I

Fluid flow and mass transfer experiments have been performed on axial flow hollow fibre modules of varying packing density (32 to 76%). Shell-side pressure drop was found to be proportional to (flowrate) n , where n varied from about 1.1 at high packing density to 1.5 at low packing density, for shellside Reynolds numbers < 350. Assuming an Ergun-type pressure drop relationship it was found that for packing densities < about 50% the inertial (turbulent) losses exceeded the viscous (laminar) losses. Inspection of cross-sections taken from the middle of modules revealed non-uniform fibre packing with regions of high and low packing density. The cross-sections also change along the length of the module. It is inferred that, in addition to axial flow along fibres, there is also a degree of stream splitting which provides transverse flow across fibres as fluid continuously seeks preferential paths through regions of lower packing density. The presence of transverse flow would explain the higher than expected velocity exponent. Mass transfer experiments involving the removal of oxygen from water flowing through the shell to a sweep gas in the fibre lumens produced higher than expected shell-side mass transfer coefficients. The results are correlated within ± 15% by Sh = (0.53 − 0.58φ) Re 0.53 Sc 0.33. The exponent on Re is consistent with entry region conditions, caused by repeated stream splitting and transverse flow. Compared with mass transfer predicted for axial flow through a uniformly packed shell the experimental results are up to 2× higher, with the most significant enhancement at the lower packing densities. The implication of this work is that module design requires a more sophisticated approach than the traditional assumption of laminar flow through parallel axial ducts.