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Pore partitioning hydrodynamic modeling

To evaluate the solute diffusion coefficient in the stationary phase, and the solute partition coefficient, fCq, a model for the pore is required. A simple model where the pore is considered as an infinitely long cylinder and the solute is a rigid sphere adequately describes the elution process [58]. Using this model, Dg, the solute diffusivity within the porous particles, can be estimated from the hydrodynamic theory of hindered diffusion [59] ... [Pg.15]

Transport through nanofiltration membranes is controlled primarily by electrostatic and steric interactions. The extended Nemst-Plank equation commonly is used with Donnan and steric partitioning to predict transport rates based on effective membrane charge density, pore radius, and thickness to porosity ratio [131-132]. Inclusion of solute-pore hydrodynamic interactions and a pore size distribution improves the predictive and correlative capabilities of the models [133]. [Pg.320]


See other pages where Pore partitioning hydrodynamic modeling is mentioned: [Pg.219]    [Pg.349]    [Pg.191]    [Pg.298]    [Pg.743]   
See also in sourсe #XX -- [ Pg.8 , Pg.9 , Pg.10 , Pg.11 , Pg.12 , Pg.13 , Pg.14 , Pg.15 , Pg.16 , Pg.17 , Pg.18 , Pg.19 , Pg.20 , Pg.21 ]




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