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dc.contributor.authorCosta, Glória Meyberg Nunes-
dc.contributor.authorGuerrieri, Y.-
dc.contributor.authorKislansky, S.-
dc.contributor.authorPessoa, F. L. P.-
dc.contributor.authorMelo, Silvio Alexandre Beisl Vieira de-
dc.contributor.authorEmbiruçu, Marcelo-
dc.creatorCosta, Glória Meyberg Nunes-
dc.creatorGuerrieri, Y.-
dc.creatorKislansky, S.-
dc.creatorPessoa, F. L. P.-
dc.creatorMelo, Silvio Alexandre Beisl Vieira de-
dc.creatorEmbiruçu, Marcelo-
dc.date.accessioned2012-01-23T15:38:55Z-
dc.date.issued2009-
dc.identifier.urihttp://www.repositorio.ufba.br/ri/handle/ri/5215-
dc.descriptionTexto completo: Acesso restrito. p. 8613–8628.pt_BR
dc.description.abstractThe Soave−Redlich−Kwong (SRK) and the Sanchez and Lacombe (SL) equations of state are applied to the flash simulation of polyethylene industrial separators, specifically low-density polyethylene (eight resins) and linear low-density polyethylene (25 resins). Three mixing rules are used in the SRK equation: van der Waals (VDW) one-fluid, Wong−Sandler, and LCVM (linear combination of the Vidal and Michelsen mixing rules). The latter two mixing rules incorporate the Bogdanic and Vidal activity coefficient model. All these models involve two adjustable parameters. The results indicate that SL is the best model to simulate the flash separation of polyethylene under industrial conditions.pt_BR
dc.language.isoenpt_BR
dc.sourcehttp://pubs.acs.org/doi/abs/10.1021/ie801652qpt_BR
dc.titleSimulation of flash separation in polyethylene industrial processing: comparison of SRK and SL equations of statept_BR
dc.title.alternativeIndustrial & Engineering Chemistry Researcpt_BR
dc.typeArtigo de Periódicoen
dc.typeArtigo de Periódicopt_BR
dc.identifier.numberv. 48, n. 18.pt_BR
dc.embargo.liftdate10000-01-01-
Aparece en las colecciones: Artigo Publicado em Periódico (PEI)

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