1997
DOI: 10.1016/s0376-7388(96)00125-1
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Flux enhancement during Dean vortex microfiltration. 8. Further diagnostics1

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Cited by 62 publications
(42 citation statements)
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“…609 -627, April -June, 2015 particulates away from the membrane wall and dramatically enhance permeation rates compared to operation without vortices, although at the expense of a larger axial pressure drop. Flux improvements of up to 43% have been reported by Mallubhotla and Belfort (1997) in CFMF of particulate suspensions, while Gehlert et al (1998) found enhancements of 30−120% for ultrafiltration and microfiltration of relatively low concentrated baker's yeast suspensions and 30-90% for microfiltration of relatively concentrated beer yeast. The flux enhancement was found to increase with feed flow rate and transmembrane pressure drop, and decrease with increasing feed concentration of suspended matter (Mallubhotla and Belfort, 1997).…”
Section: Introductionmentioning
confidence: 94%
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“…609 -627, April -June, 2015 particulates away from the membrane wall and dramatically enhance permeation rates compared to operation without vortices, although at the expense of a larger axial pressure drop. Flux improvements of up to 43% have been reported by Mallubhotla and Belfort (1997) in CFMF of particulate suspensions, while Gehlert et al (1998) found enhancements of 30−120% for ultrafiltration and microfiltration of relatively low concentrated baker's yeast suspensions and 30-90% for microfiltration of relatively concentrated beer yeast. The flux enhancement was found to increase with feed flow rate and transmembrane pressure drop, and decrease with increasing feed concentration of suspended matter (Mallubhotla and Belfort, 1997).…”
Section: Introductionmentioning
confidence: 94%
“…In a series of publications, Belfort and co-workers conducted comprehensive theoretical and experimental investigations on the nature of the flow field in curved channels and the effects of the resulting centrifugal instabilities, known as Dean vortices, on the performance of nanofiltration, ultrafiltration and microfiltration membrane modules (Chung et al, 1996;Mallubhotla and Belfort, 1997;Chung et al, 1998;Gehlert et al, 1998;Mallubhotla et al, 1998;Luque et al, 1999;Mallubhotla et al, 1999;Mallubhotla et al, 2001). The central conclusion that can be drawn from this body of work is that such vortices induce back migration of accumulated solute molecules or Brazilian Journal of Chemical Engineering Vol.…”
Section: Introductionmentioning
confidence: 99%
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“…Compared to the film and boundarylayer models of membrane filtration, the surfacerenewal model has the potential to more faithfully describe the transfer of dissolved/suspended solids due to random hydrodynamic impulses generated at the membrane surface, e.g., due to membrane roughness or by the use of spacers or turbulence promoters. Such instabilities, when introduced deliberately into the main flow (e.g., by means of Dean vortices), induce back migration of accumulated solute molecules or particulates away from the membrane surface and significantly enhance permeation rates (Mallubhotla and Belfort, 1997;Gehlert et al, 1998;Mallubhotla et al, 1998). Almeida et al (2010) experimentally studied the effect of wall roughness and three different spacer configurations on the microflow hydrodynamics of deionized water flowing in slits for a Reynolds number range of 58−500.…”
Section: Introductionmentioning
confidence: 99%