Effect of flow geometry parameters on transient heat transfer for turbulent flow in a circular tube with baffle inserts

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The effect of the flow geometry parameters on transient forced convection heat transfer for turbulent flow in a circular tube with baffle inserts has been investigated. The characteristic parameters of the tubes are pitch to tube inlet diameter ratio H/D = 1, 2 and 3, baffle orientation angle β = 45°, 90° and 180°. Air, Prandtl number of which is 0.71, was used as working fluid, while stainless steel was considered as pipe and baffle material. During the experiments, different geometrical parameters such as the baffle spacing H and the baffle orientation angle β were varied. Totally, nine types of baffle inserted tube were used. The general empirical equations of time averaged Nusselt number and time averaged pressure drop were derived as a function of Reynolds number corresponding to the baffle geometry parameters of pitch to diameter ratio H/D, baffle orientation angle β, ratio of smooth to baffled cross-section area So/Sa and ratio of tube length to baffle spacing L/H were derived for transient flow conditions. The proposed empirical correlations were considered to be applicable within the range of Reynolds number 3000 {less-than or slanted equal to} Re {less-than or slanted equal to} 20,000 for the case of constant heat flux. © 2006 Elsevier Ltd. All rights reserved.

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dc.contributor.authorTandiroglu, Ahmet
dc.date.accessioned2026-10-18T20:30:58.808166488Z
dc.date.available2026-10-18T20:30:58.808166488Z
dc.date.issued2006
dc.description.abstractThe effect of the flow geometry parameters on transient forced convection heat transfer for turbulent flow in a circular tube with baffle inserts has been investigated. The characteristic parameters of the tubes are pitch to tube inlet diameter ratio H/D = 1, 2 and 3, baffle orientation angle β = 45°, 90° and 180°. Air, Prandtl number of which is 0.71, was used as working fluid, while stainless steel was considered as pipe and baffle material. During the experiments, different geometrical parameters such as the baffle spacing H and the baffle orientation angle β were varied. Totally, nine types of baffle inserted tube were used. The general empirical equations of time averaged Nusselt number and time averaged pressure drop were derived as a function of Reynolds number corresponding to the baffle geometry parameters of pitch to diameter ratio H/D, baffle orientation angle β, ratio of smooth to baffled cross-section area So/Sa and ratio of tube length to baffle spacing L/H were derived for transient flow conditions. The proposed empirical correlations were considered to be applicable within the range of Reynolds number 3000 {less-than or slanted equal to} Re {less-than or slanted equal to} 20,000 for the case of constant heat flux. © 2006 Elsevier Ltd. All rights reserved.
dc.identifier.doi10.1016/j.ijheatmasstransfer.2006.01.018
dc.identifier.endpage1567
dc.identifier.issn0017-9310
dc.identifier.issue9-10
dc.identifier.scopus2-s2.0-33645895270
dc.identifier.startpage1559
dc.identifier.urihttps://rdlopen.rawdatalibrary.net/r/ebyu/16173
dc.identifier.volume49
dc.language.isoen
dc.relation.ispartofInternational Journal of Heat and Mass Transfer
dc.rightsinfo:eu-repo/semantics/openAccess
dc.subjectCircular tube with baffle inserts
dc.subjectEffects of flow geometry parameters
dc.subjectHeat transfer augmentation
dc.subjectTransient forced convection
dc.subjectFlow patterns
dc.subjectForced convection
dc.subjectNusselt number
dc.subjectPipe flow
dc.subjectPrandtl number
dc.subjectReynolds number
dc.subjectStainless steel
dc.subjectTurbulent flow
dc.subjectBaffle inserts
dc.subjectCircular tubes
dc.subjectFlow geometry
dc.subjectTransient heat transfer
dc.titleEffect of flow geometry parameters on transient heat transfer for turbulent flow in a circular tube with baffle inserts
dc.typeArticle
dspace.entity.typePublication
rdl.citation.scopus69
rdl.source.indexSCOPUS