Ternary Liquid – Liquid and Binary Liquid – Liquid, Solid – Liquid, and Vapour – Liquid equilibria of systems containing ε-Caprolactam, Water, n-Hexadecane, and o-Xylene

dc.contributorAalto-yliopistofi
dc.contributorAalto Universityen
dc.contributor.authorRiaz, Zubair
dc.contributor.authorUusi-Kyyny, Petri
dc.contributor.authorDahal, Roshi
dc.contributor.authorPokki, Juha-Pekka
dc.contributor.authorAlopaeus, Ville
dc.contributor.departmentDepartment of Chemical and Metallurgical Engineeringen
dc.contributor.groupauthorChemical engineeringen
dc.contributor.organizationChemical engineering
dc.date.accessioned2025-08-04T07:06:21Z
dc.date.available2025-08-04T07:06:21Z
dc.date.issued2025-11
dc.descriptionPublisher Copyright: © 2025 The Author(s)
dc.description.abstractThis study reports equilibrium experimental data of binary and ternary systems containing ε-caprolactam. Solid – liquid equilibria (SLE), and isobaric bubble points were measured for the binary system ε-caprolactam + o-xylene. SLE and liquid – liquid equilibria (LLE) were measured for the binary system ε-caprolactam + n-hexadecane. Ternary LLE were measured for the systems ε-caprolactam + water + n-hexadecane or o-xylene at temperatures 298 – 323 K and atmospheric pressure. The isobaric bubble point and the ternary systems’ phase boundaries were predicted prior to the experiments with the universal quasi-chemical functional group activity coefficients – Dortmund modified (UNIFAC–Dortmund) model to ascertain the experimental conditions. Binary interaction parameters for the nonrandom, two-liquid (NRTL) model were regressed based on the measured systems of this work and additional data from the literature sources. Good agreement was found between the experimental data and the NTRL model. The results from this study provide insights into the phase behaviour of mixtures containing ε-caprolactam, facilitating process design in relevant industrial processes.en
dc.description.versionPeer revieweden
dc.format.extent12
dc.format.mimetypeapplication/pdf
dc.identifier.citationRiaz, Z, Uusi-Kyyny, P, Dahal, R, Pokki, J-P & Alopaeus, V 2025, 'Ternary Liquid – Liquid and Binary Liquid – Liquid, Solid – Liquid, and Vapour – Liquid equilibria of systems containing ε-Caprolactam, Water, n-Hexadecane, and o-Xylene', Fluid Phase Equilibria, vol. 598, 114503. https://doi.org/10.1016/j.fluid.2025.114503en
dc.identifier.doi10.1016/j.fluid.2025.114503
dc.identifier.issn0378-3812
dc.identifier.issn1879-0224
dc.identifier.otherPURE UUID: ce279e84-23cc-46e0-a3fd-eede773a1eff
dc.identifier.otherPURE ITEMURL: https://research.aalto.fi/en/publications/ce279e84-23cc-46e0-a3fd-eede773a1eff
dc.identifier.otherPURE FILEURL: https://research.aalto.fi/files/186607194/Ternary_Liquid_Liquid_and_Binary_Liquid_Liquid_Solid_Liquid_and_Vapour_Liquid_equilibria_of_systems_containing_-Caprolactam_Water_n-Hexadecane_and_o-Xylene.pdf
dc.identifier.urihttps://aaltodoc.aalto.fi/handle/123456789/137515
dc.identifier.urnURN:NBN:fi:aalto-202508045754
dc.language.isoenen
dc.publisherElsevier
dc.relation.fundinginfoThe authors acknowledge the financial support received from Business Finland for the UrbanMill project (207/31/2021). Zubair Riaz acknowledges Fortum and Neste Foundation for the grant received for postgraduate studies.
dc.relation.ispartofseriesFluid Phase Equilibriaen
dc.relation.ispartofseriesVolume 598en
dc.rightsopenAccessen
dc.rightsCC BY
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/
dc.subject.keywordNylon-6
dc.subject.keywordPlastic recycling
dc.subject.keywordSeparation
dc.subject.keywordSolubility
dc.subject.keywordSolvent extraction
dc.subject.keywordThermodynamic modelling
dc.titleTernary Liquid – Liquid and Binary Liquid – Liquid, Solid – Liquid, and Vapour – Liquid equilibria of systems containing ε-Caprolactam, Water, n-Hexadecane, and o-Xyleneen
dc.typeA1 Alkuperäisartikkeli tieteellisessä aikakauslehdessäfi
dc.type.versionpublishedVersion

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