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Prediction of physical properties of hydrocarbons, petroleum, and coal liquid fractions

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dc.contributor.author Retzekas, E en
dc.contributor.author Voutsas, E en
dc.contributor.author Magoulas, K en
dc.contributor.author Tassios, D en
dc.date.accessioned 2014-03-01T01:18:14Z
dc.date.available 2014-03-01T01:18:14Z
dc.date.issued 2002 en
dc.identifier.issn 0888-5885 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/14881
dc.subject Physical Properties en
dc.subject.classification Engineering, Chemical en
dc.subject.other Boiling point en
dc.subject.other Coal liquefaction en
dc.subject.other Crude petroleum en
dc.subject.other Data reduction en
dc.subject.other Density of liquids en
dc.subject.other Error analysis en
dc.subject.other Molecular structure en
dc.subject.other Molecular weight en
dc.subject.other Pressure effects en
dc.subject.other Thermal effects en
dc.subject.other Hydrocarbons en
dc.subject.other coal en
dc.subject.other hydrocarbon en
dc.subject.other petroleum en
dc.subject.other coal en
dc.subject.other gasoline en
dc.subject.other hydrocarbon en
dc.subject.other physical property en
dc.subject.other prediction en
dc.subject.other analytic method en
dc.subject.other article en
dc.subject.other correlation analysis en
dc.subject.other density en
dc.subject.other molecular weight en
dc.subject.other physical parameters en
dc.subject.other prediction en
dc.subject.other pressure en
dc.subject.other reliability en
dc.subject.other structure analysis en
dc.title Prediction of physical properties of hydrocarbons, petroleum, and coal liquid fractions en
heal.type journalArticle en
heal.identifier.primary 10.1021/ie010642a en
heal.identifier.secondary http://dx.doi.org/10.1021/ie010642a en
heal.language English en
heal.publicationDate 2002 en
heal.abstract A simple method that uses the molecular structure and density as input parameters for the prediction of the normal boiling point (Tb), critical temperature (Tc), and critical pressure (Pc) of pure hydrocarbons is presented. For Tb the average absolute error is 1.0% as compared to 3.3% for the Joback method and 2.9% for that of Stein and Brown. Its main advantage over the first method lies with large molecular weight compounds and that over the second with highly branched compounds. For the prediction of Tc, the average absolute error is 1% similar to that of the Joback, Riazi, and Riazi-Daubert methods which, however, require knowledge of Tb. Finally, for Pc, the proposed method gives an average absolute error of 2.7% as compared to 3.9% for the Joback method and 4.2% and 4.8% for the Tb-requiring methods of Riazi and Riazi-Daubert, respectively. The proposed method gives also better results for these three properties when compared to the recently proposed and more difficult to use group interaction contribution method of Marejon and Fontevila. Using data for pure hydrocarbons, correlations have been developed for the prediction of molecular weight (MW), Tc, and Pc of petroleum and coal liquid fractions. MW prediction gives an average absolute error of 4.1% as compared to 4.6% for the Riazi-Daubert method, and both methods provide better results for coal liquids than the Starling and ""single-parameter"" expressions. Tc and Pc predictions with errors of 1.2% and 5.5% are similar to those of the Riazi-Daubert method, but no conclusion can be reached about the reliability of these methods because of the small number of available data. en
heal.publisher AMER CHEMICAL SOC en
heal.journalName Industrial and Engineering Chemistry Research en
dc.identifier.doi 10.1021/ie010642a en
dc.identifier.isi ISI:000174475800036 en
dc.identifier.volume 41 en
dc.identifier.issue 6 en
dc.identifier.spage 1695 en
dc.identifier.epage 1702 en


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