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dc.contributor.authorSolheim, Asbjørn
dc.contributor.authorSkybakmoen, Egil
dc.date.accessioned2020-12-11T07:47:17Z
dc.date.available2020-12-11T07:47:17Z
dc.date.created2020-06-21T14:42:08Z
dc.date.issued2020
dc.identifier.citationLight Metals 2020en_US
dc.identifier.isbn978-3-030-36407-6
dc.identifier.urihttps://hdl.handle.net/11250/2717056
dc.description.abstractDissolution of alumina in industrial aluminium cells is a complicated process, not least because it involves formation of agglomerates, and it involves mass- and heat transfer phenomena taking place simultaneously. In the present study, the diffusion coefficient of alumina in cryolitic melts was measured using a rotating alumina disc. It was found that the temperature dependence of the diffusion coefficient is relatively large. The enthalpies for heating of alumina, conversion, and dissolution are summarised. The addition of 1 wt% alumina causes adiabatic cooling of typically 10–12 °C in a normal industrial bath. The dissolution can be regarded as being purely mass transfer controlled, since the heat required for dissolution only brings about 1 °C temperature drop from the bath bulk to the alumina surface. The bath at the alumina surface is saturated in alumina and has a lower liquidus temperature than the bulk. Alumina dissolution can, therefore, take place in a supercooled bath.en_US
dc.language.isoengen_US
dc.publisherSpringeren_US
dc.relation.ispartofLight Metals 2020
dc.relation.ispartofseriesThe Minerals, Metals & Materials Series;2367-1181
dc.subjectHeat transferen_US
dc.subjectMass transferen_US
dc.subjectEnthalpyen_US
dc.subjectDiffusion coefficienten_US
dc.subjectAluminaen_US
dc.titleMass- and Heat Transfer during Dissolution of Aluminaen_US
dc.typeChapteren_US
dc.typePeer revieweden_US
dc.description.versionacceptedVersionen_US
dc.rights.holder© The Minerals, Metals & Materials Society 2020. This is the accepted, peer-reviewed version. The published article is available at SpringerLink https://link.springer.com/chapter/10.1007%2F978-3-030-36408-3_90en_US
dc.source.pagenumber664-671en_US
dc.identifier.doi10.1007/978-3-030-36408-3_90
dc.identifier.cristin1816487
dc.relation.projectNorges forskningsråd: 237738en_US
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode1


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