Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations

Autores
Teruel, Federico Eduardo; Díaz, Leonardo
Año de publicación
2013
Idioma
inglés
Tipo de recurso
artículo
Estado
versión publicada
Descripción
Numerical experiments in multiple representative elementary volumes (REVs) were conducted to validate calculations of macroscopic parameters for porous media models carried out employing a unit periodic cell (single REV). The simulation of a microscopic flow that develops through a porous medium formed by staggered square cylinders is presented to that purpose. A laminar steady flow regime is considered together with Péclet numbers in the 1–103 range and porosities between 55 and 95%. In particular, the interfacial heat transfer coefficient (hsf) is analyzed by comparing results found in literature with those reported here. First, the outlet boundary condition that is generally employed in single REV simulations for the case of constant wall temperature was tested by comparing the values it imposes in the flow with those obtained far away from the outlet (unperturbed). It was found that this outlet boundary condition is adequate and moreover, that the flow rapidly develops to satisfy it (one or two REVs in simulated cases). Additionally, two definitions found in the literature to calculate the hsf were compared, and it was shown that both calculations differ in approximately 20% for the 55% porosity case and still present ignificant differences (>5%) for greater porosities. The hsf coefficient was also calculated as a function of the REV’s positions in the porous structure to show that it is position dependent or, in other words, it shows pore scale fluctuations. Therefore, it is concluded that single REV simulations are, in general, not sufficient to compute the parameter. A double average that filters pore scale fluctuations was employed and differences between this quantity and those obtained in a single REV were quantified. The results show these differences are small (<2%) for Pe > 100 but differences can be up to 15% for Pe = 10 or larger, for lower Pe numbers. Finally, a method that allows capturing the pore scale fluctuation of the parameter by employing single REV values was proposed. This method can be employed to calculate the double average of the hsf coefficient for other boundary conditions, or to calculate other macroscopic parameters, such as the thermal dispersion coefficients.
Fil: Teruel, Federico Eduardo. Comisión Nacional de Energía Atómica; Argentina; Comisión Nacional de Energía Atómica. Gerencia del Area de Energía Nuclear. Instituto Balseiro; Argentina; Universidad Nacional de Cuyo; Argentina;
Fil: Díaz, Leonardo. Comisión Nacional de Energía Atómica; Argentina;
Materia
Porous Media
Interfacial Heat Transfer Coefficient
Double Average
Nivel de accesibilidad
acceso abierto
Condiciones de uso
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
Repositorio
CONICET Digital (CONICET)
Institución
Consejo Nacional de Investigaciones Científicas y Técnicas
OAI Identificador
oai:ri.conicet.gov.ar:11336/2545

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spelling Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulationsTeruel, Federico EduardoDíaz, LeonardoPorous MediaInterfacial Heat Transfer CoefficientDouble Averagehttps://purl.org/becyt/ford/2.3https://purl.org/becyt/ford/2https://purl.org/becyt/ford/2.3https://purl.org/becyt/ford/2https://purl.org/becyt/ford/1.3https://purl.org/becyt/ford/1Numerical experiments in multiple representative elementary volumes (REVs) were conducted to validate calculations of macroscopic parameters for porous media models carried out employing a unit periodic cell (single REV). The simulation of a microscopic flow that develops through a porous medium formed by staggered square cylinders is presented to that purpose. A laminar steady flow regime is considered together with Péclet numbers in the 1–103 range and porosities between 55 and 95%. In particular, the interfacial heat transfer coefficient (hsf) is analyzed by comparing results found in literature with those reported here. First, the outlet boundary condition that is generally employed in single REV simulations for the case of constant wall temperature was tested by comparing the values it imposes in the flow with those obtained far away from the outlet (unperturbed). It was found that this outlet boundary condition is adequate and moreover, that the flow rapidly develops to satisfy it (one or two REVs in simulated cases). Additionally, two definitions found in the literature to calculate the hsf were compared, and it was shown that both calculations differ in approximately 20% for the 55% porosity case and still present ignificant differences (>5%) for greater porosities. The hsf coefficient was also calculated as a function of the REV’s positions in the porous structure to show that it is position dependent or, in other words, it shows pore scale fluctuations. Therefore, it is concluded that single REV simulations are, in general, not sufficient to compute the parameter. A double average that filters pore scale fluctuations was employed and differences between this quantity and those obtained in a single REV were quantified. The results show these differences are small (<2%) for Pe > 100 but differences can be up to 15% for Pe = 10 or larger, for lower Pe numbers. Finally, a method that allows capturing the pore scale fluctuation of the parameter by employing single REV values was proposed. This method can be employed to calculate the double average of the hsf coefficient for other boundary conditions, or to calculate other macroscopic parameters, such as the thermal dispersion coefficients.Fil: Teruel, Federico Eduardo. Comisión Nacional de Energía Atómica; Argentina; Comisión Nacional de Energía Atómica. Gerencia del Area de Energía Nuclear. Instituto Balseiro; Argentina; Universidad Nacional de Cuyo; Argentina;Fil: Díaz, Leonardo. Comisión Nacional de Energía Atómica; Argentina;Pergamon-elsevier Science Ltd2013-02-07info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/2545Teruel, Federico Eduardo; Díaz, Leonardo; Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations; Pergamon-elsevier Science Ltd; International Journal Of Heat And Mass Transfer; 60; 7-2-2013; 406-4120017-9310enginfo:eu-repo/semantics/altIdentifier/doi/10.1016/j.ijheatmasstransfer.2012.12.022info:eu-repo/semantics/altIdentifier/url/http://www.sciencedirect.com/science/article/pii/S0017931012009775info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-10T13:09:03Zoai:ri.conicet.gov.ar:11336/2545instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-09-10 13:09:03.668CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse
dc.title.none.fl_str_mv Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations
title Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations
spellingShingle Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations
Teruel, Federico Eduardo
Porous Media
Interfacial Heat Transfer Coefficient
Double Average
title_short Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations
title_full Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations
title_fullStr Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations
title_full_unstemmed Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations
title_sort Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations
dc.creator.none.fl_str_mv Teruel, Federico Eduardo
Díaz, Leonardo
author Teruel, Federico Eduardo
author_facet Teruel, Federico Eduardo
Díaz, Leonardo
author_role author
author2 Díaz, Leonardo
author2_role author
dc.subject.none.fl_str_mv Porous Media
Interfacial Heat Transfer Coefficient
Double Average
topic Porous Media
Interfacial Heat Transfer Coefficient
Double Average
purl_subject.fl_str_mv https://purl.org/becyt/ford/2.3
https://purl.org/becyt/ford/2
https://purl.org/becyt/ford/2.3
https://purl.org/becyt/ford/2
https://purl.org/becyt/ford/1.3
https://purl.org/becyt/ford/1
dc.description.none.fl_txt_mv Numerical experiments in multiple representative elementary volumes (REVs) were conducted to validate calculations of macroscopic parameters for porous media models carried out employing a unit periodic cell (single REV). The simulation of a microscopic flow that develops through a porous medium formed by staggered square cylinders is presented to that purpose. A laminar steady flow regime is considered together with Péclet numbers in the 1–103 range and porosities between 55 and 95%. In particular, the interfacial heat transfer coefficient (hsf) is analyzed by comparing results found in literature with those reported here. First, the outlet boundary condition that is generally employed in single REV simulations for the case of constant wall temperature was tested by comparing the values it imposes in the flow with those obtained far away from the outlet (unperturbed). It was found that this outlet boundary condition is adequate and moreover, that the flow rapidly develops to satisfy it (one or two REVs in simulated cases). Additionally, two definitions found in the literature to calculate the hsf were compared, and it was shown that both calculations differ in approximately 20% for the 55% porosity case and still present ignificant differences (>5%) for greater porosities. The hsf coefficient was also calculated as a function of the REV’s positions in the porous structure to show that it is position dependent or, in other words, it shows pore scale fluctuations. Therefore, it is concluded that single REV simulations are, in general, not sufficient to compute the parameter. A double average that filters pore scale fluctuations was employed and differences between this quantity and those obtained in a single REV were quantified. The results show these differences are small (<2%) for Pe > 100 but differences can be up to 15% for Pe = 10 or larger, for lower Pe numbers. Finally, a method that allows capturing the pore scale fluctuation of the parameter by employing single REV values was proposed. This method can be employed to calculate the double average of the hsf coefficient for other boundary conditions, or to calculate other macroscopic parameters, such as the thermal dispersion coefficients.
Fil: Teruel, Federico Eduardo. Comisión Nacional de Energía Atómica; Argentina; Comisión Nacional de Energía Atómica. Gerencia del Area de Energía Nuclear. Instituto Balseiro; Argentina; Universidad Nacional de Cuyo; Argentina;
Fil: Díaz, Leonardo. Comisión Nacional de Energía Atómica; Argentina;
description Numerical experiments in multiple representative elementary volumes (REVs) were conducted to validate calculations of macroscopic parameters for porous media models carried out employing a unit periodic cell (single REV). The simulation of a microscopic flow that develops through a porous medium formed by staggered square cylinders is presented to that purpose. A laminar steady flow regime is considered together with Péclet numbers in the 1–103 range and porosities between 55 and 95%. In particular, the interfacial heat transfer coefficient (hsf) is analyzed by comparing results found in literature with those reported here. First, the outlet boundary condition that is generally employed in single REV simulations for the case of constant wall temperature was tested by comparing the values it imposes in the flow with those obtained far away from the outlet (unperturbed). It was found that this outlet boundary condition is adequate and moreover, that the flow rapidly develops to satisfy it (one or two REVs in simulated cases). Additionally, two definitions found in the literature to calculate the hsf were compared, and it was shown that both calculations differ in approximately 20% for the 55% porosity case and still present ignificant differences (>5%) for greater porosities. The hsf coefficient was also calculated as a function of the REV’s positions in the porous structure to show that it is position dependent or, in other words, it shows pore scale fluctuations. Therefore, it is concluded that single REV simulations are, in general, not sufficient to compute the parameter. A double average that filters pore scale fluctuations was employed and differences between this quantity and those obtained in a single REV were quantified. The results show these differences are small (<2%) for Pe > 100 but differences can be up to 15% for Pe = 10 or larger, for lower Pe numbers. Finally, a method that allows capturing the pore scale fluctuation of the parameter by employing single REV values was proposed. This method can be employed to calculate the double average of the hsf coefficient for other boundary conditions, or to calculate other macroscopic parameters, such as the thermal dispersion coefficients.
publishDate 2013
dc.date.none.fl_str_mv 2013-02-07
dc.type.none.fl_str_mv info:eu-repo/semantics/article
info:eu-repo/semantics/publishedVersion
http://purl.org/coar/resource_type/c_6501
info:ar-repo/semantics/articulo
format article
status_str publishedVersion
dc.identifier.none.fl_str_mv http://hdl.handle.net/11336/2545
Teruel, Federico Eduardo; Díaz, Leonardo; Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations; Pergamon-elsevier Science Ltd; International Journal Of Heat And Mass Transfer; 60; 7-2-2013; 406-412
0017-9310
url http://hdl.handle.net/11336/2545
identifier_str_mv Teruel, Federico Eduardo; Díaz, Leonardo; Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations; Pergamon-elsevier Science Ltd; International Journal Of Heat And Mass Transfer; 60; 7-2-2013; 406-412
0017-9310
dc.language.none.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv info:eu-repo/semantics/altIdentifier/doi/10.1016/j.ijheatmasstransfer.2012.12.022
info:eu-repo/semantics/altIdentifier/url/http://www.sciencedirect.com/science/article/pii/S0017931012009775
dc.rights.none.fl_str_mv info:eu-repo/semantics/openAccess
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
eu_rights_str_mv openAccess
rights_invalid_str_mv https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.format.none.fl_str_mv application/pdf
application/pdf
dc.publisher.none.fl_str_mv Pergamon-elsevier Science Ltd
publisher.none.fl_str_mv Pergamon-elsevier Science Ltd
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instname:Consejo Nacional de Investigaciones Científicas y Técnicas
reponame_str CONICET Digital (CONICET)
collection CONICET Digital (CONICET)
instname_str Consejo Nacional de Investigaciones Científicas y Técnicas
repository.name.fl_str_mv CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas
repository.mail.fl_str_mv dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar
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