2017
DOI: 10.1103/physreve.95.063310
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Flow and mass transfer around a core-shell reservoir

Abstract: I have developed an alternative numerical approach to study mass transfer from a stationary core-shell reservoir under channel flow conditions. I use the lattice Boltzmann method to compute both the solvent fluid flow and the diffusion and advection of the solute. I have investigated the impact of the flow by reporting mass transfer quantities such as the instantaneous solute concentration and the local Sherwood number at the surface of the reservoir. The flow is found to enhance the release of the encapsulate… Show more

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Cited by 17 publications
(12 citation statements)
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“…with D i is the diffusion coefficient in the i-th layer Ω i (any possible convection, as in Ref. [20] or reaction terms in Ω s are excluded). We set a perfect sink condition far away (see Sect.…”
Section: A General Model For Drug Release From a Multilayer Capsulementioning
confidence: 99%
“…with D i is the diffusion coefficient in the i-th layer Ω i (any possible convection, as in Ref. [20] or reaction terms in Ω s are excluded). We set a perfect sink condition far away (see Sect.…”
Section: A General Model For Drug Release From a Multilayer Capsulementioning
confidence: 99%
“…For the hydrodynamic part, the computation domain consists of only two subdomains: the fluid and the obstacle, i.e., the reservoir (the core and the shell all together). However, for the mass transfer part, the domain is decomposed into three adjacent subdomains that correspond to the core Ω c , the shell Ω s and the fluid Ω f , where the solute has different diffusion coefficients [14,17]: D c in the core, D s in the shell, and D f in the fluid. Both…”
Section: Problem Setup and Computational Methodsmentioning
confidence: 99%
“…The average Sherwood number, which is computed as the integration of the local Sherwood number Eq. ( 12) over the surface of the reservoir [14],…”
Section: B Key Physical Quantitiesmentioning
confidence: 99%
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“…Here, the obtained value of D m is close to 6:75 Â 10 À10 m 2 =s, which is expectedly small. The flow around the capsule induced by stirring is expected to enhance the release rate due to convection, 25,33,34 but not to significantly increase the intrinsic permeability of the capsule membrane.…”
Section: Application To Experimental Data Of Glucose Releasementioning
confidence: 99%