2002
DOI: 10.2516/ogst:2002024
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A New Group-Contribution Method for the Estimation of Physical Properties of Hydrocarbons

Abstract: Résumé -Nouvelle méthode de contribution de groupes pour l'estimation des propriétés physiques des hydrocarbure -Dans le présent article, nous proposons une nouvelle méthode de contribution de groupes pour l'estimation de la température d'ébullition, du point de congélation et de la densité liquide à 20°C des hydrocarbures purs. La méthode a été établie avec une assez bonne précision et, comparée à d'autres méthodes de contributions de groupes, elle a enregistré de meilleurs résultats en termes de déviations s… Show more

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Cited by 9 publications
(7 citation statements)
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“…However, this is not the case in the literature where the estimation of acentric factor requires an estimation of critical properties. Hence, to carryout the comparison, we use relations (8) and (9) to compute the critical temperature and relations (10) and (11) to compute the critical pressure. More precisely, the obtained values of acentric factor from model (7) are compared against two approaches: the first ones use both Riazi-Daubert relations for computing critical temperature and pressure and the second one uses both Lee-Kesler relations.…”
Section: Acentric Factormentioning
confidence: 99%
See 1 more Smart Citation
“…However, this is not the case in the literature where the estimation of acentric factor requires an estimation of critical properties. Hence, to carryout the comparison, we use relations (8) and (9) to compute the critical temperature and relations (10) and (11) to compute the critical pressure. More precisely, the obtained values of acentric factor from model (7) are compared against two approaches: the first ones use both Riazi-Daubert relations for computing critical temperature and pressure and the second one uses both Lee-Kesler relations.…”
Section: Acentric Factormentioning
confidence: 99%
“…Simmrock et al [1] surveyed 56 methods for estimating critical temperature, 55 for critical pressure and 54 for critical volume. Even if several accurate methods are reported, the characterization of the petroleum fractions still remains an active research area [2][3][4][5][6][7][8][9][10][11]. This is mainly due to the fact that a small error in critical property estimation can lead to a much higher error in thermo-physical property prediction, which can deteriorate the system operation efficiency.…”
Section: Introductionmentioning
confidence: 99%
“…This limitation is observed when experiments are carried out at extreme conditions or when experimentation is very expensive and time consuming. For example, modeling of extraheavy oil fractions presents these circumstances especially in VLE simulation [12] because very few experimental data are available. So, the property estimation (e.g.…”
Section: Introductionmentioning
confidence: 99%
“…Essentially, they proposed a general linear regression model that relates the contribution of the functional groups to several physical and thermodynamic properties such as: critical temperature, critical pressure, critical volume, melting point, normal boiling point, standard Gibbs energy, and standard enthalpy. Skander and Chitour (2002, 2003) proposed a different group contribution design to estimate some physical properties of hydrocarbons: boiling point, freezing point, and liquid density. They grouped experimental data into the following compound families: n ‐paraffins, i ‐paraffins, olefins, alcyns, naphthenes, and aromatics.…”
Section: Introductionmentioning
confidence: 99%