Please use this identifier to cite or link to this item: http://hdl.handle.net/10773/20619
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dc.contributor.authorVaz, Raquel V.pt
dc.contributor.authorMagalhaes, Ana L.pt
dc.contributor.authorSilva, Carlos M.pt
dc.date.accessioned2017-12-07T19:53:34Z-
dc.date.issued2013pt
dc.identifier.issn0378-3812pt
dc.identifier.urihttp://hdl.handle.net/10773/20619-
dc.description.abstractThe tracer diffusion coefficients are fundamental quantities in simulation and design. Due to the increasing interest upon biorefinery and sustainability in general, green solvents and processes, like carbon dioxide and supercritical fluid extraction, are attracting relevance in both chemistry and chemical engineering research and development. In this work, tracer diffusion coefficients at infinite dilution are focused aiming to propose reliable models for their pure estimation. Four predictive hydrodynamic models were proposed on the basis of modifications introduced in the original expressions of Wilke-Chang, Scheibel, Lusis-Ratcliff, and Tyn-Calus. The modified equations provide reliable results with average absolute errors between 7.86% and 8.56%, and inferior dispersion around the averages. On the contrary, the original correlations taken from the literature achieve errors between 11.89% and 27.25%, along with higher scattering of results. Furthermore, the new expressions offer average errors between 0.47% and 0.53%, while the original ones provide systematic overestimations between 2.95% and 27.23%. In the whole, the new expressions proposed in this work are equally able to predict accurately tracer diffusion coefficients of any solutes in supercritical carbon dioxide. (C) 2013 Elsevier B.V. All rights reserved.pt
dc.language.isoengpt
dc.publisherELSEVIER SCIENCE BVpt
dc.relationinfo:eu-repo/grantAgreement/FCT/SFRH/SFRH%2FBD%2F69257%2F2010/PTpt
dc.relationinfo:eu-repo/grantAgreement/FCT/SFRH/SFRH%2FBD%2F46776%2F2008/PTpt
dc.relationinfo:eu-repo/grantAgreement/FCT/COMPETE/132936/PTpt
dc.rightsrestrictedAccesspor
dc.subjectBINARY DIFFUSION-COEFFICIENTSpt
dc.subjectFLUID CHROMATOGRAPHY SFCpt
dc.subjectIMPULSE-RESPONSE METHODpt
dc.subjectTAYLOR DISPERSION TECHNIQUEpt
dc.subjectPARTIAL MOLAR VOLUMESpt
dc.subjectLENNARD-JONES FLUIDpt
dc.subjectACID METHYL-ESTERSpt
dc.subjectHARD-SPHERE THEORYpt
dc.subjectINFINITE-DILUTIONpt
dc.subjectTRACER DIFFUSIONpt
dc.titleImproved hydrodynamic equations for the accurate prediction of diffusivities in supercritical carbon dioxidept
dc.typearticlept
dc.peerreviewedyespt
ua.distributioninternationalpt
degois.publication.firstPage401pt
degois.publication.lastPage415pt
degois.publication.titleFLUID PHASE EQUILIBRIApt
degois.publication.volume360pt
dc.date.embargo10000-01-01-
dc.relation.publisherversion10.1016/j.fluid.2013.09.052pt
dc.identifier.doi10.1016/j.fluid.2013.09.052pt
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