<?xml version="1.0" encoding="UTF-8"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-10-19T00:23:46Z</responseDate><request verb="GetRecord" identifier="oai:ebyu-rdlopen.rawdatalibrary.net:ebyu/14342" metadataPrefix="oai_dc">https://ebyu-rdlopen.rawdatalibrary.net/oai/request</request><GetRecord><record><header><identifier>oai:ebyu-rdlopen.rawdatalibrary.net:ebyu/14342</identifier><datestamp>2026-10-18T20:39:01Z</datestamp><setSpec>openaire</setSpec><setSpec>driver</setSpec><setSpec>com_ebyu_10000</setSpec><setSpec>col_ebyu_10001</setSpec></header><metadata><oai_dc:dc xmlns:oai_dc="http://www.openarchives.org/OAI/2.0/oai_dc/" xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd"><dc:title>Investigation of boiling heat transfer characteristics of R134a flowing in smooth and microfin tubes</dc:title><dc:creator>Celen, Ali</dc:creator><dc:creator>Çebi, Alican</dc:creator><dc:creator>Dalkılıç, Ahmet Selim</dc:creator><dc:subject>Boiling heat transfer coefficient</dc:subject><dc:subject>Heat transfer enhancement</dc:subject><dc:subject>Microfin tube</dc:subject><dc:subject>Pressure drop</dc:subject><dc:subject>Heat flux</dc:subject><dc:subject>Heat transfer coefficients</dc:subject><dc:subject>Tubes (components)</dc:subject><dc:subject>Boiling heat transfer</dc:subject><dc:subject>Boiling heat-transfer coefficients</dc:subject><dc:subject>Frictional pressure drops</dc:subject><dc:subject>Heat transfer and pressure drop</dc:subject><dc:subject>Saturation temperature</dc:subject><dc:subject>Total pressure drop</dc:subject><dc:subject>Drops</dc:subject><dc:description>In this study, boiling heat transfer and pressure drop experiments are performed in order to investigate heat transfer enhancement of microfin tube comparing with smooth one. During constant heat flux (10 kW m−2) experiments, effect of mass flux (190–381 kg m−2 s−1), saturation temperature (15–22 °C) and vapor quality (0.21–0.77) on heat transfer coefficient and pressure drop are investigated. In addition, boiling heat transfer coefficient and frictional pressure drop correlations given in the literature are compared with measured ones. Moreover, the experiments revealed that experimental boiling heat transfer coefficient and total pressure drop of R134a flowing microfin tube are 1.9 and 3.0 times higher than smooth one having the same fin root diameter, respectively. Furthermore, 94 number of heat transfer and pressure drop raw experimental data belonging to the microfin tube are given for researchers to validate their theoretical models. © 2018 Elsevier Ltd</dc:description><dc:publisher>Elsevier Ltd</dc:publisher><dc:date>2018</dc:date><dc:type>Article</dc:type><dc:identifier>https://rdlopen.rawdatalibrary.net/r/ebyu/14342</dc:identifier><dc:identifier>https://doi.org/10.1016/j.icheatmasstransfer.2018.03.006</dc:identifier><dc:identifier>0735-1933</dc:identifier><dc:language>en</dc:language><dc:relation>International Communications in Heat and Mass Transfer</dc:relation><dc:rights>info:eu-repo/semantics/openAccess</dc:rights><dc:type>info:eu-repo/semantics/article</dc:type><dc:identifier>https://ebyu-rdlopen.rawdatalibrary.net/tr/items/ebyu/14342</dc:identifier></oai_dc:dc></metadata></record></GetRecord></OAI-PMH>