(431b) On Cubic Eos Interaction Parameter Estimation for Long Chain n-Alkane + Aromatic Binary Mixtures
AIChE Annual Meeting
2017
2017 Annual Meeting
Engineering Sciences and Fundamentals
In Honor of Marco Satyro II (Invited Talks)
Tuesday, October 31, 2017 - 3:40pm to 4:05pm
References:
 [1] Ahitan, S., Satyro, M. A., Shaw, J. M. Systematic misprediction of n-alkane + aromatic and naphthenic hydrocarbon phase behavior using common equations of state. J. Chem. Eng. Data 2015, 60, 3300-3318.
[2] Ahitan, S., Shaw, J. M. Quantitative comparison between predicted and experimental binary n-alkane+ benzene phase behaviors using cubic and PC-SAFT EOS. Fluid Phase Equilib. 2016, 428, 4-17.
[3] Gao, G.; Daridon, J.; Saint-Guirons, H.; Xans, P.; Montel, F. A simple correlation to evaluate binary interaction parameters of the Peng-Robinson equation of state: binary light hydrocarbon systems. Fluid Phase Equilibria 1992, 85-93.
[4] Chueh, P. L.; Prausnitz, J. M. Vapor-liquid equilibria at high pressures: Calculation of partial molar volumes in nonpolar liquid mixtures. AIChE J. 1967, 6, 1099-1107.
[5] Klamt, A.; Eckert, F. COSMO-RS: a novel and efficient method for the a priori prediction of thermophysical data of liquids. Fluid Phase Equilibria 2000, 1, 43-72.
[6] Gross, J.; Sadowski, G. Perturbed-Chain SAFT: An Equation of State Based on a Perturbation Theory for Chain Molecules. Ind. Eng. Chem. Res. 2001, 4, 1244-1260.
[7] Jaubert, J.; Vitu, S.; Mutelet, F.; Corriou, J. Extension of the PPR78 model (predictive 1978, PengâRobinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing aromatic compounds. Fluid Phase Equilib. 2005, 1â2, 193-211.
[8] Liu, Q. MSc. Thesis, University of Alberta (in progress 2017).