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- W2058794164 abstract "Most mass transfer models for describing polarization and fouling in porous membrane ducts require some knowledge of the fluid mechanics. Mass transfer correlations for porous membrane systems are usually borrowed from studies of flow in non-porous ducts. In this paper we show that friction coefficients are higher for flow in a duct with wall suction than without. We also show that the onset of turbulence is delayed from 2100 to about 4000 Reynolds number for flow in porous tubes with suction when compared to flow in non-porous tubes. In the laminar regime at a given axial Reynolds number increased suction results in a maximum value for the friction coefficient. Using a trajectory analysis, we have compared the performance of several commercial modules for capturing suspended particles from dilute solution. Under the assumptions of the theoretical models, and all things being equal (besides fractional recovery per unit length), tubular systems will capture more particles from dilute suspensions than slits with two porous walls." @default.
- W2058794164 created "2016-06-24" @default.
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- W2058794164 date "1985-01-01" @default.
- W2058794164 modified "2023-09-26" @default.
- W2058794164 title "Fluid mechanics and cross-flow filtration: some thoughts" @default.
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- W2058794164 doi "https://doi.org/10.1016/0011-9164(85)85052-9" @default.
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