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dc.contributor.author
Teruel, Federico Eduardo  
dc.contributor.author
Díaz, Leonardo  
dc.date.available
2015-10-19T13:32:21Z  
dc.date.issued
2013-02-07  
dc.identifier.citation
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; 1; 7-2-2013; 406-412  
dc.identifier.issn
0017-9310  
dc.identifier.uri
http://hdl.handle.net/11336/2545  
dc.description.abstract
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.  
dc.format
application/pdf  
dc.language.iso
eng  
dc.publisher
Pergamon-Elsevier Science Ltd  
dc.rights
info:eu-repo/semantics/openAccess  
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/  
dc.subject
DOUBLE AVERAGE  
dc.subject
INTERFACIAL HEAT TRANSFER COEFFICIENT  
dc.subject
POROUS MEDIA  
dc.subject
REV  
dc.subject.classification
Ingeniería Mecánica  
dc.subject.classification
Ingeniería Mecánica  
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INGENIERÍAS Y TECNOLOGÍAS  
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Física de los Fluidos y Plasma  
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Ciencias Físicas  
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CIENCIAS NATURALES Y EXACTAS  
dc.title
Calculation of the interfacial heat transfer coefficient in porous media employing numerical simulations  
dc.type
info:eu-repo/semantics/article  
dc.type
info:ar-repo/semantics/artículo  
dc.type
info:eu-repo/semantics/publishedVersion  
dc.date.updated
2016-03-30 10:35:44.97925-03  
dc.journal.volume
60  
dc.journal.number
1  
dc.journal.pagination
406-412  
dc.journal.pais
Países Bajos  
dc.journal.ciudad
Amsterdam  
dc.description.fil
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  
dc.description.fil
Fil: Díaz, Leonardo. Comisión Nacional de Energía Atómica; Argentina  
dc.journal.title
International Journal Of Heat And Mass Transfer  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1016/j.ijheatmasstransfer.2012.12.022  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/http://www.sciencedirect.com/science/article/pii/S0017931012009775