Please use this identifier to cite or link to this item: https://hdl.handle.net/11147/3543
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dc.contributor.advisorMobedi, Moghtadaen
dc.contributor.authorUçar, Eren-
dc.date.accessioned2014-07-22T13:51:46Z-
dc.date.available2014-07-22T13:51:46Z-
dc.date.issued2012en
dc.identifier.urihttp://hdl.handle.net/11147/3543-
dc.descriptionThesis (Master)--Izmir Institute of Technology, Mechanical Engineering, Izmir, 2012en
dc.descriptionIncludes bibliographical references (leaves: 140-142)en
dc.descriptionText in English; Abstract: Turkish and Englishen
dc.descriptionxv, 146 leavesen
dc.descriptionFull text release delayed at author's request until 2016.01.10en
dc.description.abstractA theoretical study is performed on heat and fluid flow in a parallel plate channel completely and partially filled with porous medium. An asymmetric heat flux is imposed onto the boundary conditions of the channel fully filled with porous media. However, a symmetrical heat flux is applied to the channel partially filled with porous medium. Dimensional analysis is performed on three parallel plates having different permeability and effective thermal conductivity values. The dimensionless analysis is performed for parallel plates with different values of Da and thermal conductivity ratio. Darcy-Brinkman model is used to investigate the velocity distribution in porous media. The dimensional and dimensionless energy equation and appropriate boundary conditions are written for the analyzed channels. The dimensional equations of motion and heat are solved by numerical methods, while the dimensionless form of those equations are analytically solved to obtain analytical expressions for the velocity and temperature fields in the channel. The dimensional temperature and velocity profiles, obtained by numerical methods, are compared with the analytical expressions of dimensionless temperature and velocity profiles and good agreement between the results were observed. For both fully filled asymmetric heated channel and partially filled symmetrical heated channel, it is observed that the traditional temperature difference (difference between surface and mean temperatures) is not proper to be used in the individual heat transfer coefficient since heat transfer coefficient approaches to infinity and changes sign without changing of heat transfer direction. Hence, a proper temperature difference is required to be defined.en
dc.language.isoenen_US
dc.publisherIzmir Institute of Technologyen
dc.rightsinfo:eu-repo/semantics/embargoedAccessen_US
dc.subject.lcshPorous materials--Thermal propertiesen
dc.subject.lcshPermeabilityen
dc.subject.lcshHeat equationen
dc.titleHeat and fluid flow analysis in a channel partially filled with permeable isotropic porous layeren_US
dc.typeMaster Thesisen_US
dc.institutionauthorUçar, Eren-
dc.departmentThesis (Master)--İzmir Institute of Technology, Mechanical Engineeringen_US
dc.relation.publicationcategoryTezen_US
item.grantfulltextopen-
item.openairecristypehttp://purl.org/coar/resource_type/c_18cf-
item.cerifentitytypePublications-
item.openairetypeMaster Thesis-
item.languageiso639-1en-
item.fulltextWith Fulltext-
Appears in Collections:Master Degree / Yüksek Lisans Tezleri
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