Predicting the Phase Equilibria, Critical Phenomena, and Mixing Enthalpies of Binary Aqueous Systems Containing Alkanes, Cycloalkanes, Aromatics, Alkenes, and Gases (N2, CO2, H2S, H2) with the PPR78 Equation of State

2013 ◽  
Vol 52 (46) ◽  
pp. 16457-16490 ◽  
Author(s):  
Jun-Wei Qian ◽  
Romain Privat ◽  
Jean-Noël Jaubert
1998 ◽  
Vol 37 (10) ◽  
pp. 4175-4182 ◽  
Author(s):  
Iakovos V. Yakoumis ◽  
Georgios M. Kontogeorgis ◽  
Epaminondas C. Voutsas ◽  
Eric M. Hendriks ◽  
Dimitrios P. Tassios

2021 ◽  
Author(s):  
Oluwakemi Victoria Eniolorunda ◽  
Antonin Chapoy ◽  
Rod Burgass

Abstract In this study, new experimental data using a reliable approach are reported for solid-fluid phase equilibrium of ternary mixtures of Methane-Carbon-dioxide- n-Hexadecane for 30-73 mol% CO2 and pressures up to 24 MPa. The effect of varying CO2 composition on the overall phase transition of the systems were investigated. Three thermodynamic models were used to predict the liquid phase fugacity, this includes the Peng Robison equation of state (PR-EoS), Soave Redlich-Kwong equation of state (SRK-EoS) and the Cubic plus Association (CPA) equation of state with the classical mixing rule and a group contribution approach for calculating binary interaction parameters in all cases. To describe the wax (solid) phase, three activity coefficient models based on the solid solution theory were investigated: the predictive universal quasichemical activity coefficients (UNIQUAC), Universal quasi-chemical Functional Group activity coefficients (UNIFAC) and the predictive Wilson approach. The solid-fluid equilibria experimental data gathered in this experimental work including those from saturated and under-saturated conditions were used to check the reliability of the various phase equilibria thermodynamic models.


1996 ◽  
Vol 29 (3) ◽  
pp. 439-448 ◽  
Author(s):  
Ki-Pung Yoo ◽  
Jisoo Kim ◽  
Hwayong Kim ◽  
Seong-Sik You ◽  
Chul Soo Lee

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