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Experimental investigation of the heat transfer and pressure drop characteristics of SiO2/water nanofluids flowing through a circular tube equipped with free rotating swirl generators

dc.contributor.authorJumpholkul, Chaiwat
dc.contributor.authorAsirvatham, Lazarus Godson
dc.contributor.authorDalkilic, Ahmet Selim
dc.contributor.authorMahian, Omid
dc.contributor.authorAhn, Ho Seon
dc.contributor.authorJerng, Dong-Wook
dc.contributor.authorWongwises, Somchai
dc.date.accessioned2026-06-27T14:30:42Z
dc.date.issued2020
dc.description.abstractThe heat transfer and pressure drop characteristics of SiO2/water nanofluids flowing through a horizontal circular stainless steel tube equipped with free rotating swirl generators (FRSGs) at the entrance of a test tube are reported in this article. The experimental studies were performed with a Reynolds number ranging from 3500 to 13,000; volume concentrations of 0.5, 1, and 2 vol%; and inlet temperatures of 25, 30, and 35 degrees C, where a constant heat flux was imposed on a test tube. FRSGs made from aluminum, with three different twisted angles (30 degrees, 60 degrees, and 90 degrees) and a length of 2.3 cm, were located at the entrance of the test tube. The results indicated that FRSGs had significant effects on heat transfer and pressure drop characteristics for the flow of both water and nanofluids in the tube. The Nusselt number increased with increasing volume concentration, inlet temperature, and Reynolds number. However, the friction factor of nanofluids flowing through FRSGs was significantly greater than that of water when the Reynolds number was lower than 6000. This is because FRSGs do not rotate under the given conditions. A maximum efficiency index of 1.57-1.7 was obtained when using SiO2/water nanofluids with FRSGs at a volume concentration of 2 vol%, inlet temperature of 35 degrees C, and Reynolds number greater than 7000. On the other hand, the efficiency index value was lower than unity when the Reynolds number was lower than 7000 and with volume concentrations of 0.5 and 1 vol%. No significant differences were found among twisted angles of FRSGs on heat transfer, pressure drop, and efficiency index.en
dc.description.urihttps://doi.org/10.1007/s00231-019-02782-z
dc.identifier.doi10.1007/s00231-019-02782-z
dc.identifier.eissn1432-1181
dc.identifier.endpage1626
dc.identifier.issn0947-7411
dc.identifier.issue5
dc.identifier.startpage1613
dc.identifier.urihttps://hdl.handle.net/20.500.14981/61467
dc.identifier.volume56
dc.identifier.wos000528599400017
dc.language.isoeng
dc.publisherSPRINGER
dc.relation.ispartofHEAT AND MASS TRANSFER
dc.subjectEfficiency index
dc.subjectFree rotating swirl generators
dc.subjectSiO2
dc.subjectwater nanofluids
dc.subjectHeat transfer enhancement
dc.subjectPressure drop
dc.subjectTWISTED TAPE INSERTS
dc.subjectFRICTION FACTOR CHARACTERISTICS
dc.subjectAL2O3/WATER NANOFLUID
dc.subjectTRANSFER ENHANCEMENT
dc.subjectAL2O3 NANOFLUID
dc.subjectTURBULENT PIPE
dc.subjectTRANSFER AUGMENTATION
dc.subjectTRANSFER COEFFICIENT
dc.subjectPLAIN TUBE
dc.subjectU-TUBE
dc.subjectThermodynamics
dc.subjectMechanics
dc.titleExperimental investigation of the heat transfer and pressure drop characteristics of SiO2/water nanofluids flowing through a circular tube equipped with free rotating swirl generators
dc.typeArticle
dspace.entity.typePublication
local.import.sourceWOS

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