Basit öğe kaydını göster

dc.contributor.authorBayram H.
dc.date.accessioned2024-03-12T19:35:29Z
dc.date.available2024-03-12T19:35:29Z
dc.date.issued2022
dc.identifier.issn21525102
dc.identifier.urihttps://doi.org/10.1615/InterJFluidMechRes.2022042499
dc.identifier.urihttps://hdl.handle.net/20.500.12450/2922
dc.description.abstractThe effects of the inner pipe design of a double pipe heat exchanger (DPHE) on the thermal performance were numerically investigated by using a three-dimensional computational fluid dynamics (CFD) method under various Reynolds numbers and steady state conditions. Two different passive heat transfer enhancement methods were applied to the DPHE, and the heat exchanger was tried to be compact. The first method is the addition of a conventional longitudinal fin to the outer surface of the inner pipe. The other method is the fractal application; the fractal pattern applied in heat exchangers in the available literature is generally used in the fin geometry. But in this study, the fractal pattern was used in the geometry of the inner pipe. Heat transfer occurred over the entire wall of the inner pipe due to using the fractal pattern to the inner pipe of the heat exchanger. The heat exchanger model with the Koch Snowflake fractal pattern cross-section showed the highest heat transfer rate values. It was easily observed that the total pressure drop values increased as the number of iterations increased. As a result of fin attachment, relatively lower increases were observed in heat transfer rate values. In general, the n = 1 fractal model has both high heat transfer and relatively low pressure drop values that make this model more remarkable than the others. The heat transfer rate and pressure drop (cold side) values of this model varied between nearly 6–18 kW and 1.2–13 kPa, respectively. The numerical results were compatible with the values obtained from the literature and theoretical calculations. © 2022 by Begell House, Inc.en_US
dc.language.isoengen_US
dc.publisherBegell House Inc.en_US
dc.relation.ispartofInternational Journal of Fluid Mechanics Researchen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectCFDen_US
dc.subjectdouble pipeen_US
dc.subjectheat exchangersen_US
dc.subjectheat transfer enhancementen_US
dc.subjectKoch Snowflakeen_US
dc.subjectDropsen_US
dc.subjectFins (heat exchange)en_US
dc.subjectFractalsen_US
dc.subjectHeat transfer coefficientsen_US
dc.subjectPressure dropen_US
dc.subjectReynolds numberen_US
dc.subjectSnowen_US
dc.subjectDouble pipesen_US
dc.subjectDouble-pipe heat exchangersen_US
dc.subjectFractal patternsen_US
dc.subjectHeat Transfer enhancementen_US
dc.subjectHeat transfer rateen_US
dc.subjectHigh heat transfersen_US
dc.subjectKoch snowflakeen_US
dc.subjectLongitudinal finen_US
dc.subjectNumerical investigationsen_US
dc.subjectPipe designen_US
dc.subjectComputational fluid dynamicsen_US
dc.titleNUMERICAL INVESTIGATION OF HEAT TRANSFER IMPROVEMENT OF A DOUBLE PIPE HEAT EXCHANGER WITH KOCH SNOWFLAKE FRACTAL AND LONGITUDINAL FIN DESIGNSen_US
dc.typearticleen_US
dc.departmentAmasya Üniversitesien_US
dc.identifier.volume49en_US
dc.identifier.issue1en_US
dc.identifier.startpage57en_US
dc.identifier.endpage73en_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.identifier.scopus2-s2.0-85139501274en_US
dc.identifier.doi10.1615/InterJFluidMechRes.2022042499
dc.department-tempBayram, H., Department of Mechanical Engineering, Engineering Faculty, Amasya University, Amasya, 05100, Turkeyen_US
dc.authorscopusid57195356819


Bu öğenin dosyaları:

DosyalarBoyutBiçimGöster

Bu öğe ile ilişkili dosya yok.

Bu öğe aşağıdaki koleksiyon(lar)da görünmektedir.

Basit öğe kaydını göster