Please use this identifier to cite or link to this item: https://doi.org/10.1080/10407780701852852
DC FieldValue
dc.titleForced convection over a backward-facing step with a porous floor segment
dc.contributor.authorChen, X.B.
dc.contributor.authorYu, P.
dc.contributor.authorWinoto, S.H.
dc.contributor.authorLow, H.T.
dc.date.accessioned2014-06-17T06:22:16Z
dc.date.available2014-06-17T06:22:16Z
dc.date.issued2008-01
dc.identifier.citationChen, X.B., Yu, P., Winoto, S.H., Low, H.T. (2008-01). Forced convection over a backward-facing step with a porous floor segment. Numerical Heat Transfer; Part A: Applications 53 (11) : 1211-1230. ScholarBank@NUS Repository. https://doi.org/10.1080/10407780701852852
dc.identifier.issn10407782
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/60357
dc.description.abstractForced convection after a backward-facing step, with a porous floor segment, is investigated numerically using the SIMPEC method. The Brinkman-Forcheimmer extended model is used to govern the flow in the porous-medium region. At the interface, the flow boundary condition imposed is a shear stress jump, which includes the inertial effect, together with a continuity of normal stress. The thermal interfacial condition is continuities of temperature and heat flux. Results are presented for Reynolds number up to 800 and Darcy number up to 10-1. Also varied are the length and depth of the porous segment. Compared with the case with no porous floor, the local heat transfer is augmented after the porous floor. Within the porous floor, the heat transfer is reduced, but this may be offset by using a porous medium of higher conductivity than the fluid. To obtain good heat enhancement after the porous segment, it should approximately match the length of the recirculation region. The porous segment should have large permeability (Darcy number around 10-1), but it is not necessary that it be of great depth. The interfacial stress jump coefficients and 1 are varied from-5 to+5, and some effects are observed on the local Nusselt numbers, velocity profile, and temperature distribution.
dc.description.urihttp://libproxy1.nus.edu.sg/login?url=http://dx.doi.org/10.1080/10407780701852852
dc.sourceScopus
dc.typeArticle
dc.contributor.departmentMECHANICAL ENGINEERING
dc.description.doi10.1080/10407780701852852
dc.description.sourcetitleNumerical Heat Transfer; Part A: Applications
dc.description.volume53
dc.description.issue11
dc.description.page1211-1230
dc.description.codenNHAAE
dc.identifier.isiut000252893500005
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