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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Main Authors: Alessandro Coclite, Giuseppe Maria Coclite, Domenico De Tommasi
Format: Article
Language:English
Published: MDPI AG 2020-11-01
Series:Nanomaterials
Subjects:
Online Access:https://www.mdpi.com/2079-4991/10/11/2190
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spelling doaj-9aee77e2ac244797846647a8801a85b02020-11-25T04:05:30ZengMDPI AGNanomaterials2079-49912020-11-01102190219010.3390/nano10112190Capsules Rheology in Carreau–Yasuda FluidsAlessandro Coclite0Giuseppe Maria Coclite1Domenico De Tommasi2School of Engineering, Università della Basilicata, 85100 Potenza, ItalyDipartimento di Meccanica, Matematica e Management, 70126 Politecnico di Bari, ItalyDipartimento di Scienze dell’Ingegneria e dell’Architettura, 70126 Politecnico di Bari, ItalyIn 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, <i>n</i> = 0.25, 0.50, 0.75, 1.0, and 1.5. Then, the flow within a squared lid-driven cavity for <i>Re</i> = 1000 and 5000 (being <i>Re</i> the Reynolds number) is computed as a function of <i>n</i> for a shear-thinning (<i>n</i> < 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 (<i>AR</i> = 2 and 3) is analyzed for shear-thinning (<i>n</i> < 1), Newtonian (<i>n</i> = 1), and shear-thickening (<i>n</i> > 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, <i>Re</i><inline-formula><math display="inline"><semantics><msub><mrow></mrow><mi>c</mi></msub></semantics></math></inline-formula>, after which the tumbling is inhibited in confirmed also for non-Newtonian fluids. Analogously, the equilibrium lateral position <inline-formula><math display="inline"><semantics><msub><mi>y</mi><mrow><mi>e</mi><mi>q</mi></mrow></msub></semantics></math></inline-formula> of such neutrally buoyant capsules when transported in a plane-Couette flow is studied detailing the variation of <inline-formula><math display="inline"><semantics><msub><mi>y</mi><mrow><mi>e</mi><mi>q</mi></mrow></msub></semantics></math></inline-formula> as a function of the Reynolds number as well as of the exponent <i>n</i>.https://www.mdpi.com/2079-4991/10/11/2190immersed boundary method (IBM)dynamic forcing IBMmulti relaxation time (MRT)moving least squaresnon-Newtonian rheologyparticle margination
collection DOAJ
language English
format Article
sources DOAJ
author Alessandro Coclite
Giuseppe Maria Coclite
Domenico De Tommasi
spellingShingle Alessandro Coclite
Giuseppe Maria Coclite
Domenico De Tommasi
Capsules Rheology in Carreau–Yasuda Fluids
Nanomaterials
immersed boundary method (IBM)
dynamic forcing IBM
multi relaxation time (MRT)
moving least squares
non-Newtonian rheology
particle margination
author_facet Alessandro Coclite
Giuseppe Maria Coclite
Domenico De Tommasi
author_sort Alessandro Coclite
title Capsules Rheology in Carreau–Yasuda Fluids
title_short 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_sort capsules rheology in carreau–yasuda fluids
publisher MDPI AG
series Nanomaterials
issn 2079-4991
publishDate 2020-11-01
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, <i>n</i> = 0.25, 0.50, 0.75, 1.0, and 1.5. Then, the flow within a squared lid-driven cavity for <i>Re</i> = 1000 and 5000 (being <i>Re</i> the Reynolds number) is computed as a function of <i>n</i> for a shear-thinning (<i>n</i> < 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 (<i>AR</i> = 2 and 3) is analyzed for shear-thinning (<i>n</i> < 1), Newtonian (<i>n</i> = 1), and shear-thickening (<i>n</i> > 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, <i>Re</i><inline-formula><math display="inline"><semantics><msub><mrow></mrow><mi>c</mi></msub></semantics></math></inline-formula>, after which the tumbling is inhibited in confirmed also for non-Newtonian fluids. Analogously, the equilibrium lateral position <inline-formula><math display="inline"><semantics><msub><mi>y</mi><mrow><mi>e</mi><mi>q</mi></mrow></msub></semantics></math></inline-formula> of such neutrally buoyant capsules when transported in a plane-Couette flow is studied detailing the variation of <inline-formula><math display="inline"><semantics><msub><mi>y</mi><mrow><mi>e</mi><mi>q</mi></mrow></msub></semantics></math></inline-formula> as a function of the Reynolds number as well as of the exponent <i>n</i>.
topic immersed boundary method (IBM)
dynamic forcing IBM
multi relaxation time (MRT)
moving least squares
non-Newtonian rheology
particle margination
url https://www.mdpi.com/2079-4991/10/11/2190
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