Publication:
Gibbs energy additivity approaches to QSPR in modeling of high pressure density and kinematic viscosity of FAME and biodiesel

dc.contributor.authorThinnaphop Chum-inen_US
dc.contributor.authorKaokanya Sudapraserten_US
dc.contributor.authorSuriya Phankosolen_US
dc.contributor.authorSupathra Lilitchanen_US
dc.contributor.authorKornkanok Aryusuken_US
dc.contributor.authorKanit Krisnangkuraen_US
dc.contributor.otherKing Mongkut s University of Technology Thonburien_US
dc.contributor.otherBansomdejchaopraya Rajabhat Universityen_US
dc.contributor.otherMahidol Universityen_US
dc.date.accessioned2018-12-21T07:06:14Z
dc.date.accessioned2019-03-14T08:03:13Z
dc.date.available2018-12-21T07:06:14Z
dc.date.available2019-03-14T08:03:13Z
dc.date.issued2017-02-01en_US
dc.description.abstract© 2016 Elsevier B.V. Density (ρ) and kinematic viscosity (μ) are important physical properties of biodiesel. They are directly affected by both temperature and pressure. Accordingly, models which correlate density and kinematic viscosity of fatty acid methyl ester (FAME) and biodiesel to their carbon numbers, number of double bonds of fatty acid are proposed. Gibbs free energy additivity is used as an alternative approach to quantitative structure-property relationship (QSPR) in estimating density and kinematic viscosity at high temperature and pressure of FAME and biodiesel. It is one of the best models for estimating density of FAME, mixtures of FAMEs or biodiesels and biodiesel blends at different temperatures (283.15–333.15 K) and pressures (0.2–40 MPa). For kinematic viscosity, the model is simply derived from the sum (or subtraction) of the Gibbs energies of dynamic viscous flow and volumetric expansion. Thus, this is the first model proposed for prediction of kinematic viscosity of FAME and biodiesel ay different temperatures and pressures. Because there is no experimental value in the literature, the accuracy of the model is tested against the experimental density and experimental dynamic viscosity (η) via the classical equation (μ = η/ρ).en_US
dc.identifier.citationFuel Processing Technology. Vol.156, (2017), 385-393en_US
dc.identifier.doi10.1016/j.fuproc.2016.09.025en_US
dc.identifier.issn03783820en_US
dc.identifier.other2-s2.0-84999837808en_US
dc.identifier.urihttps://repository.li.mahidol.ac.th/handle/20.500.14594/42187
dc.rightsMahidol Universityen_US
dc.rights.holderSCOPUSen_US
dc.source.urihttps://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84999837808&origin=inwarden_US
dc.subjectChemical Engineeringen_US
dc.subjectEnergyen_US
dc.titleGibbs energy additivity approaches to QSPR in modeling of high pressure density and kinematic viscosity of FAME and biodieselen_US
dc.typeArticleen_US
dspace.entity.typePublication
mu.datasource.scopushttps://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84999837808&origin=inwarden_US

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