2020
DOI: 10.1017/jfm.2019.1083
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Unsteady solute dispersion by electrokinetic flow in a polyelectrolyte layer-grafted rectangular microchannel with wall absorption

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Cited by 24 publications
(18 citation statements)
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“…However, attention should be given to the fact that, because of the lower permitivity value of polyelectrolyte brushes relative to that of water, the PEL permittivity is generally lower than the solution permittivity. A range of 52.8–78 was reported for the relative permittivity of the PEL. , Although the lower limit differs significantly from water permittivity, the upper limit is quite close to it. This is in accordance with the cases for which the grafting density is low, similar to the conditions considered in the present study.…”
Section: Molecular Theory For a Coated Nanopore In Contact With Reser...mentioning
confidence: 85%
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“…However, attention should be given to the fact that, because of the lower permitivity value of polyelectrolyte brushes relative to that of water, the PEL permittivity is generally lower than the solution permittivity. A range of 52.8–78 was reported for the relative permittivity of the PEL. , Although the lower limit differs significantly from water permittivity, the upper limit is quite close to it. This is in accordance with the cases for which the grafting density is low, similar to the conditions considered in the present study.…”
Section: Molecular Theory For a Coated Nanopore In Contact With Reser...mentioning
confidence: 85%
“…The body force density vector F is the superposition of the force densities exerted on the ions by the electric field E , given as ρ e E , and the drag force density created by the PE brush. The widely accepted approach for accounting the drag force is to consider a volumetric resistive force proportional to the velocity, which is equivalent to modeling the PEL as a porous medium utilizing the Brinkman equation . Following the earlier models for polymer brushes, such a resistive force is given as ξ PEL U z , where ξ PEL is the drag coefficient of the PEL and equals ξ PEL = μ­[ϕ p ( r )/ l e ] 2 , where ϕ p ( r ) is the monomer volume fraction and l e is the effective monomer size. It is important to mention that ϕ p ( r ), which is obtained in the previous section by utilizing the molecular theory, varies locally inside the system and is not a fixed value across the brush layer.…”
Section: Molecular Theory For a Coated Nanopore In Contact With Reser...mentioning
confidence: 99%
See 2 more Smart Citations
“…Hydrodynamics and dispersion phenomena of EOF were addressed in the context of non-Newtonian fluids [ 24 , 25 , 26 ]. For instance, recently, the unsteady solute dispersion by electrokinetic flow was studied [ 27 ] by considering wall absorption. Besides, some studies were conducted on the hydrodynamics of the OEOF for non-Newtonian fluids [ 28 , 29 , 30 ], and, recently, the mass transfer of an electroneutral solute in a concentric-annulus microchannel driven by an OEOF for a fluid whose behavior follows the Maxwell model was reported by Peralta et al [ 31 ].…”
Section: Introductionmentioning
confidence: 99%