Please use this identifier to cite or link to this item: https://repositorio.ufba.br/handle/ri/15214
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dc.contributor.authorRocha, Inaura Carolina C. da-
dc.contributor.authorFialho, Rosana Lopes-
dc.contributor.authorMarques, Jose Jailton-
dc.contributor.authorPessoa, Fernando Luiz Pellegrini-
dc.creatorRocha, Inaura Carolina C. da-
dc.creatorFialho, Rosana Lopes-
dc.creatorMarques, Jose Jailton-
dc.creatorPessoa, Fernando Luiz Pellegrini-
dc.date.accessioned2014-07-16T16:05:21Z-
dc.date.available2014-07-16T16:05:21Z-
dc.date.issued2011-
dc.identifier.issn0009-2460-
dc.identifier.urihttp://repositorio.ufba.br/ri/handle/ri/15214-
dc.descriptionp. 559-564pt_BR
dc.description.abstractTo carry out a feasible exploitation of the pre-salt Brazilian reserves, it is crucial to understand the phase behavior of these highly non ideal systems well and to obtain accurate models for the simulation of such severe operational conditions. In this work, the performance of two thermodynamics models based on Peng-Robinson cubic equation of state (PREOS) are compared to achieve the best representation for the ternary hexadecane, water and carbon dioxide system. The interaction parameters obtained from each model were compared and then the pressure composition diagram for the multicomponent system was created. Further research is going on to determine the experimental phase envelope data points of this system.pt_BR
dc.language.isoenpt_BR
dc.rightsAcesso Abertopt_BR
dc.sourcehttp://dx.doi.org/ 10.3303/CET1124094pt_BR
dc.subjectDioxide carbonpt_BR
dc.subjectPressurept_BR
dc.subjectTemperaturept_BR
dc.titleHigh-pressure and high-temperature pressure composition diagram of hexadecane, water and Carbon dioxide systemspt_BR
dc.title.alternativeChemical Engineering Transactionspt_BR
dc.typeArtigo de Periódicoen
dc.typeArtigo de Periódicopt_BR
dc.identifier.numberv. 24pt_BR
dc.publisher.countryBrasilpt_BR
Appears in Collections:Artigo Publicado em Periódico (PEI)

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