<?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>2026-10-18T23:54:18Z</responseDate><request verb="GetRecord" identifier="oai:ebyu-rdlopen.rawdatalibrary.net:ebyu/12897" metadataPrefix="oai_dc">https://ebyu-rdlopen.rawdatalibrary.net/oai/request</request><GetRecord><record><header><identifier>oai:ebyu-rdlopen.rawdatalibrary.net:ebyu/12897</identifier><datestamp>2026-10-18T20:36:43Z</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>Thermal–hydraulic performance of the circular-slice-shaped-winglet for tube bank heat exchanger</dc:title><dc:creator>Tepe, Ahmet Ümit</dc:creator><dc:creator>Yilmaz, Harun</dc:creator><dc:subject>CFD</dc:subject><dc:subject>Forced convection</dc:subject><dc:subject>Tube bank heat exchanger</dc:subject><dc:subject>Winglet</dc:subject><dc:subject>Heat exchangers</dc:subject><dc:subject>Navier Stokes equations</dc:subject><dc:subject>Tubes (components)</dc:subject><dc:subject>Turbulence models</dc:subject><dc:subject>Bare tube heat exchanger</dc:subject><dc:subject>Condition</dc:subject><dc:subject>Heat transfer performance</dc:subject><dc:subject>Laminar and turbulent flow</dc:subject><dc:subject>Optimal design</dc:subject><dc:subject>Performance evaluation criteria</dc:subject><dc:subject>Thermal-hydraulic performance</dc:subject><dc:subject>Tube banks</dc:subject><dc:subject>Computational fluid dynamics</dc:subject><dc:description>In this study, heat transfer performance of circular-slice-shaped-winglet (CSSW) for tube bank heat exchanger (TBHE) was numerically investigated. Circular-slice angle (α = 5°, 10° and 20°), layer gap (h/d = 0.08, 0.14, and 0.20) and winglet diameter (D/d = 1.60, 1.76 and 1.92) were analyzed as geometric parameters to obtain optimal design. Comprehensive numerical simulations were conducted under both laminar and turbulent flow (1100 ≤ Re ≤ 8500) conditions. Navier Stokes Equations were solved by using RNG k-ε turbulence model (with enhanced wall treatment). Colburn-j factor (j), friction factor (f), modified London area goodness factor (j/f1/3) and performance evaluation criterion (PEC) were investigated quantitatively. Flow characteristics were also analyzed to elucidate the underlying physics of the effects of CSSW on thermal-hydraulic performance for TBHE. Results were compared with the data related to bare tube heat exchanger, and showed that the highest modified London area goodness factor is 26.34% with α = 10°, h/d = 0.20 and D/d = 1.92 CSSW winglet design. Additionally, numerical calculations revealed that PEC increased to 1.356 with these CSSW design parameters, which corresponds to reduction of the required total heat transfer area by 36.60% compared to the bare tube heat exchanger for the same heat duty at a fixed pumping power. © 2022 Elsevier Masson SAS</dc:description><dc:publisher>Elsevier Masson s.r.l.</dc:publisher><dc:date>2022</dc:date><dc:type>Article</dc:type><dc:identifier>https://rdlopen.rawdatalibrary.net/r/ebyu/12897</dc:identifier><dc:identifier>https://doi.org/10.1016/j.ijthermalsci.2022.107711</dc:identifier><dc:identifier>1290-0729</dc:identifier><dc:language>en</dc:language><dc:relation>International Journal of Thermal Sciences</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/12897</dc:identifier></oai_dc:dc></metadata></record></GetRecord></OAI-PMH>