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- W3211281409 endingPage "117924" @default.
- W3211281409 startingPage "117924" @default.
- W3211281409 abstract "• The bubble pressure and vapor phase concentration have been precisely modeled. • The precise model is provided for hydrocarbon-alcohol mixtures. • Patel-Teja equation of state with Wong-Sandler mixing rules were employed. • Small error for alcohol-hydrocarbon mixtures at low and moderate pressures is seen. This study aims to precisely model vapor phase concentration and bubble pressure in correlating alcohol-hydrocarbon mixtures to accurate assessment with effects from literature by employed Patel-Teja equation of state and together with Wong-Sandler mixing rules. Even though other intricate equations have been used for some selected systems, it is the first time that a systematic approach for measuring hydrocarbon-alcohol mixtures in the range of low to moderate pressures has been practiced by this research. Results show that models employed in this work, average-absolute deviations are fewer than the previous EoSs for alcohol-hydrocarbons binary mixtures. The complex models calculate bubble pressure and vapor phase concentration respectively with 2.25% and 3.25% of average-absolute deviations, whiles our models show a better result for them (respectively, 0.00 % and 0.47% averagely)." @default.
- W3211281409 created "2021-11-08" @default.
- W3211281409 creator A5001036927 @default.
- W3211281409 creator A5014310300 @default.
- W3211281409 creator A5042586114 @default.
- W3211281409 creator A5060698834 @default.
- W3211281409 creator A5082486777 @default.
- W3211281409 creator A5089545525 @default.
- W3211281409 date "2022-01-01" @default.
- W3211281409 modified "2023-10-11" @default.
- W3211281409 title "Thermodynamic modeling of several alcohol-hydrocarbon binary mixtures at low to moderate conditions" @default.
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