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dc.contributor.authorDenardin, F.
dc.contributor.authorVieira De Melo, S.
dc.contributor.authorMammucari, R.
dc.contributor.authorFoster, Neil
dc.date.accessioned2017-08-24T02:17:54Z
dc.date.available2017-08-24T02:17:54Z
dc.date.created2017-08-23T07:21:43Z
dc.date.issued2013
dc.identifier.citationDenardin, F. and Vieira De Melo, S. and Mammucari, R. and Foster, N. 2013. Phase transition and volume expansion in CO2-expanded liquid systems, pp. 529-534.
dc.identifier.urihttp://hdl.handle.net/20.500.11937/55285
dc.identifier.doi10.3303/CET1332089
dc.description.abstract

Binary mixtures of conventional solvents are very useful in the dense gas processing of pharmaceuticals. However, the lack of experimental data for ternary systems of organic solvents and dense carbon dioxide hinders the full exploitation of solvent engineering for particle formation by dense gas processing. In this work, volume expansion and mixture critical points for binary and ternary systems of organic solvents and carbon dioxide were experimentally determined at different temperatures and pressures. Results show an exponential behavior of the liquid volume expansion with pressure as the mixture come close to the mixture critical point. Copyright © 2013, AIDIC Servizi S.r.l.

dc.titlePhase transition and volume expansion in CO2-expanded liquid systems
dc.typeConference Paper
dcterms.source.volume32
dcterms.source.startPage529
dcterms.source.endPage534
dcterms.source.issn2283-9216
dcterms.source.titleChemical Engineering Transactions
dcterms.source.seriesChemical Engineering Transactions
curtin.departmentDepartment of Chemical Engineering
curtin.accessStatusFulltext not available


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