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dc.contributor.authorDorao, Carlos Alberto
dc.contributor.authorDrewes, S
dc.contributor.authorFernandino, Maria
dc.date.accessioned2019-03-29T11:18:15Z
dc.date.available2019-03-29T11:18:15Z
dc.date.created2018-02-07T11:48:05Z
dc.date.issued2018
dc.identifier.citationApplied Physics Letters. 2018, 112 (6), 064101-1-064101-4.nb_NO
dc.identifier.issn0003-6951
dc.identifier.urihttp://hdl.handle.net/11250/2592445
dc.description.abstractDuring the past few decades, heat transfer during convective flow boiling inside pipes has been widely studied with the goal of unveiling the physics of the process. Different heat transfer mechanisms have been suggested based on different assumptions. This fact has resulted in a large number of models including different dimensionless numbers and in some cases up to a dozen of adjusted parameters. Here, we show that the convective flow boiling heat transfer coefficient is equivalent to the one for single-phase flow when the influence of the vapour velocity is taken into account.nb_NO
dc.language.isoengnb_NO
dc.publisherAIP Publishingnb_NO
dc.titleCan the heat transfer coefficients for single-phase flow and for convective flow boiling be equivalent?nb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.pagenumber064101-1-064101-4nb_NO
dc.source.volume112nb_NO
dc.source.journalApplied Physics Lettersnb_NO
dc.source.issue6nb_NO
dc.identifier.doi10.1063/1.5018659
dc.identifier.cristin1562729
dc.relation.projectNorges forskningsråd: 231529nb_NO
dc.description.localcode© 2018 Author(s).nb_NO
cristin.unitcode194,64,25,0
cristin.unitnameInstitutt for energi- og prosessteknikk
cristin.ispublishedtrue
cristin.fulltextpreprint
cristin.qualitycode2


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