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Capsules Rheology in Carreau–Yasuda Fluids

In this paper, a Multi Relaxation Time Lattice Boltzmann scheme is used to describe the evolution of a non-Newtonian fluid. Such method is coupled with an Immersed-Boundary technique for the transport of arbitrarily shaped objects navigating the flow. The no-slip boundary conditions on immersed bodi...

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Autores principales: Coclite, Alessandro, Coclite, Giuseppe Maria, De Tommasi, Domenico
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2020
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7692258/
https://www.ncbi.nlm.nih.gov/pubmed/33153075
http://dx.doi.org/10.3390/nano10112190
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author Coclite, Alessandro
Coclite, Giuseppe Maria
De Tommasi, Domenico
author_facet Coclite, Alessandro
Coclite, Giuseppe Maria
De Tommasi, Domenico
author_sort Coclite, Alessandro
collection PubMed
description In this paper, a Multi Relaxation Time Lattice Boltzmann scheme is used to describe the evolution of a non-Newtonian fluid. Such method is coupled with an Immersed-Boundary technique for the transport of arbitrarily shaped objects navigating the flow. The no-slip boundary conditions on immersed bodies are imposed through a convenient forcing term accounting for the hydrodynamic force generated by the presence of immersed geometries added to momentum equation. Moreover, such forcing term accounts also for the force induced by the shear-dependent viscosity model characterizing the non-Newtonian behavior of the considered fluid. Firstly, the present model is validated against well-known benchmarks, namely the parabolic velocity profile obtained for the flow within two infinite laminae for five values of the viscosity model exponent, n = 0.25, 0.50, 0.75, 1.0, and 1.5. Then, the flow within a squared lid-driven cavity for Re = 1000 and 5000 (being Re the Reynolds number) is computed as a function of n for a shear-thinning (n < 1) fluid. Indeed, the local decrements in the viscosity field achieved in high-shear zones implies the increment in the local Reynolds number, thus moving the position of near-walls minima towards lateral walls. Moreover, the revolution under shear of neutrally buoyant plain elliptical capsules with different Aspect Ratio (AR = 2 and 3) is analyzed for shear-thinning (n < 1), Newtonian (n = 1), and shear-thickening (n > 1) surrounding fluids. Interestingly, the power law by Huang et al. describing the revolution period of such capsules as a function of the Reynolds number and the existence of a critical value, Re [Formula: see text] , after which the tumbling is inhibited in confirmed also for non-Newtonian fluids. Analogously, the equilibrium lateral position [Formula: see text] of such neutrally buoyant capsules when transported in a plane-Couette flow is studied detailing the variation of [Formula: see text] as a function of the Reynolds number as well as of the exponent n.
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spelling pubmed-76922582020-11-28 Capsules Rheology in Carreau–Yasuda Fluids Coclite, Alessandro Coclite, Giuseppe Maria De Tommasi, Domenico Nanomaterials (Basel) Article In this paper, a Multi Relaxation Time Lattice Boltzmann scheme is used to describe the evolution of a non-Newtonian fluid. Such method is coupled with an Immersed-Boundary technique for the transport of arbitrarily shaped objects navigating the flow. The no-slip boundary conditions on immersed bodies are imposed through a convenient forcing term accounting for the hydrodynamic force generated by the presence of immersed geometries added to momentum equation. Moreover, such forcing term accounts also for the force induced by the shear-dependent viscosity model characterizing the non-Newtonian behavior of the considered fluid. Firstly, the present model is validated against well-known benchmarks, namely the parabolic velocity profile obtained for the flow within two infinite laminae for five values of the viscosity model exponent, n = 0.25, 0.50, 0.75, 1.0, and 1.5. Then, the flow within a squared lid-driven cavity for Re = 1000 and 5000 (being Re the Reynolds number) is computed as a function of n for a shear-thinning (n < 1) fluid. Indeed, the local decrements in the viscosity field achieved in high-shear zones implies the increment in the local Reynolds number, thus moving the position of near-walls minima towards lateral walls. Moreover, the revolution under shear of neutrally buoyant plain elliptical capsules with different Aspect Ratio (AR = 2 and 3) is analyzed for shear-thinning (n < 1), Newtonian (n = 1), and shear-thickening (n > 1) surrounding fluids. Interestingly, the power law by Huang et al. describing the revolution period of such capsules as a function of the Reynolds number and the existence of a critical value, Re [Formula: see text] , after which the tumbling is inhibited in confirmed also for non-Newtonian fluids. Analogously, the equilibrium lateral position [Formula: see text] of such neutrally buoyant capsules when transported in a plane-Couette flow is studied detailing the variation of [Formula: see text] as a function of the Reynolds number as well as of the exponent n. MDPI 2020-11-03 /pmc/articles/PMC7692258/ /pubmed/33153075 http://dx.doi.org/10.3390/nano10112190 Text en © 2020 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Coclite, Alessandro
Coclite, Giuseppe Maria
De Tommasi, Domenico
Capsules Rheology in Carreau–Yasuda Fluids
title Capsules Rheology in Carreau–Yasuda Fluids
title_full Capsules Rheology in Carreau–Yasuda Fluids
title_fullStr Capsules Rheology in Carreau–Yasuda Fluids
title_full_unstemmed Capsules Rheology in Carreau–Yasuda Fluids
title_short Capsules Rheology in Carreau–Yasuda Fluids
title_sort capsules rheology in carreau–yasuda fluids
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7692258/
https://www.ncbi.nlm.nih.gov/pubmed/33153075
http://dx.doi.org/10.3390/nano10112190
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