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Numerical modeling and experimental validation of air-side forced convection on a Wire-on-tube condenser for a domestic refrigerator

dc.contributor.authorSahnali, Funda Erdem
dc.contributor.authorAtayilmaz, S. Ozgur
dc.contributor.authorGemici, Zafer
dc.date.accessioned2026-06-27T15:06:08Z
dc.date.issued2025
dc.description.abstractIn this study, the effects of various parameters on the air-side performance of a condenser used in a domestic refrigerator were investigated numerically and experimentally. A new condenser design with streamlined eye and kammtail tube shapes was studied to delay flow separation. The kammtail form was utilized in a wire-and-tube heat exchanger for the first time in this work instead of traditional round or elliptical geometry. Different design parameters were studied for the outer tube height (3, 3.5, 4, 4.5, and 5 mm), aspect ratio of the tube (1.5, 2, and 2.5), tube pitch (20 and 15 mm), tube arrangement (inline and staggered), and tube shapes (eye, kammtail, and ellipse forms) to improve the air-side performance. The model was validated using experimental data based on a performance test setup and wind tunnel measurements conducted at different air velocities. The impact of tube shape and tube dimensions on the convection coefficient and pressure drop were found to be dominant due to delayed flow separation and reduction in the recirculation area. The results showed that, for a similar heat-transfer rate, the total tube surface area was reduced by 7%, the convection coefficient was increased by 9.4%, and the static pressure drop was decreased by 27% with the new Kamm tail-form design of 3 x 6 mm compared to the respective values of the original condenser. In addition, for a similar air-side performance, decreasing the tube pitch from 20 to 15 mm resulted in subsequent decreases of up to 30% in the heat exchanger volume. When the tube arrangement was changed from inline to staggered, the convective coefficient increased by 23% and the pressure decreased by 14%. The numerical results were in good agreement with the experimental results, showing errors of less than 10% for air pressure drop and less than 9% for heat-transfer capacity.en
dc.description.sponsorshipARCELIK Central RD
dc.description.sponsorshipARCELIK Central RD
dc.description.urihttps://doi.org/10.1080/10407782.2024.2345858
dc.identifier.doi10.1080/10407782.2024.2345858
dc.identifier.eissn1521-0634
dc.identifier.endpage6807
dc.identifier.issn1040-7782
dc.identifier.issue19
dc.identifier.startpage6785
dc.identifier.urihttps://hdl.handle.net/20.500.14981/67937
dc.identifier.volume86
dc.identifier.wos001216914100001
dc.language.isoeng
dc.publisherTAYLOR & FRANCIS INC
dc.relation.ispartofNUMERICAL HEAT TRANSFER PART A-APPLICATIONS
dc.subjectComputational fluid dynamics
dc.subjectexperimental validation
dc.subjectGLM-ANOVA analysis
dc.subjectresponse optimization
dc.subjecttube shapes
dc.subjectwire-on-tube condenser
dc.subjectHEAT-TRANSFER CHARACTERISTICS
dc.subjectWAVY FIN
dc.subjectEXCHANGER
dc.subjectFLOW
dc.subjectPERFORMANCE
dc.subjectNUMBER
dc.subjectBUNDLES
dc.subjectThermodynamics
dc.subjectMechanics
dc.titleNumerical modeling and experimental validation of air-side forced convection on a Wire-on-tube condenser for a domestic refrigerator
dc.typeArticle
dspace.entity.typePublication
local.import.sourceWOS

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