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• W2014916248 abstract "A model of liquid-to-particle mass transfer in packed beds with single phase non-Newtonian creeping flow is derived using a coherent approach which associates the Lévêque solution with a capillary-type representation of the porous structure. The model is compared to experimental data obtained with spherical and anisotropic parallelepipedal particles, respectively, as well as to literature results. The model allows to predict mass transfer in fixed beds of spheres and anisotropic parallelepipedal particles with a mean relative error of 11%. It is also shown that a better prediction of mass transfer is obtained for parallelepipedal particles if the surface area really offered to fluid flow is considered. Dimensionless numbers based on the pore dimension are shown to be more suitable than those based on a particle diameter." @default.
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• W2014916248 date "2002-10-01" @default.
• W2014916248 modified "2023-09-23" @default.
• W2014916248 title "Modelling of power law liquid–solid mass transfer in packed beds at Darcy regime" @default.
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• W2014916248 doi "https://doi.org/10.1016/s1385-8947(02)00007-4" @default.
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