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dc.contributor.authorLervåg, Karl Yngve
dc.contributor.authorSkarsvåg, Hans Langva
dc.contributor.authorAursand, Eskil
dc.contributor.authorOuassou, Jabir Ali
dc.contributor.authorHammer, Morten
dc.contributor.authorReigstad, Gunhild Allard
dc.contributor.authorErvik, Åsmund
dc.contributor.authorFyhn, Eirik Holm
dc.contributor.authorGjennestad, Magnus Aashammer
dc.contributor.authorAursand, Peder
dc.contributor.authorWilhelmsen, Øivind
dc.date.accessioned2021-05-07T14:23:57Z
dc.date.available2021-05-07T14:23:57Z
dc.date.created2020-12-15T13:06:04Z
dc.date.issued2020
dc.identifier.citationJournal of Loss Prevention in the Process Industries. 2020, .en_US
dc.identifier.issn0950-4230
dc.identifier.urihttps://hdl.handle.net/11250/2754244
dc.description.abstractTransport of liquefied natural gas (LNG) by ship occurs globally on a massive scale. The large temperature difference between LNG and water means LNG will boil violently if spilled onto water. This may cause a physical explosion known as rapid phase transition (RPT). Since RPT results from a complex interplay between physical phenomena on several scales, the risk of its occurrence is difficult to estimate. In this work, we present a combined fluid-dynamic and thermodynamic model to predict the onset of delayed RPT. On the basis of the full coupled model, we derive analytical solutions for the location and time of delayed RPT in an axisymmetric steady-state spill of LNG onto water. These equations are shown to be accurate when compared to simulation results for a range of relevant parameters. The relative discrepancy between the analytic solutions and predictions from the full coupled model is within 8% for the RPT position and within 2% for the time of RPT. This provides a simple procedure to quantify the risk of occurrence for delayed RPT for LNG on water. Due to its modular formulation, the full coupled model can straightforwardly be extended to study RPT in other systems. © 2020 The Author(s)en_US
dc.language.isoengen_US
dc.publisherElsevieren_US
dc.rightsNavngivelse 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/deed.no*
dc.titleA combined fluid-dynamic and thermodynamic model to predict the onset of rapid phase transitions in LNG spillsen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.rights.holderThe Authorsen_US
dc.source.pagenumber13en_US
dc.source.volume69en_US
dc.source.journalJournal of Loss Prevention in the Process Industriesen_US
dc.identifier.doi10.1016/j.jlp.2020.104354
dc.identifier.cristin1860030
dc.relation.projectNorges forskningsråd: 244076en_US
dc.source.articlenumber104354en_US
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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