Author/Authors :
Parisa Sheikhbagloo Thermodynamics Research Laboratory, School of Chemical Engineering, Iran University of Science and Technology, Narmak, Tehran, Iran , Mohammad Reza Dehghani Thermodynamics Research Laboratory, School of Chemical Engineering, Iran University of Science and Technology, Narmak, Tehran, Iran , Bahman Behzadi Thermodynamics Research Laboratory, School of Chemical Engineering, Iran University of Science and Technology, Narmak, Tehran, Iran
كليدواژه :
Equation of state , Ionic liquid , Liquid-liquid equilibria , PC-SAFT
چكيده لاتين :
In this work an equation of state (EoS) based on Perturbed Chain SAFT has been used to correlate
the phase behaviour of ionic liquid+hydrocarbon systems. Pure component parameters for ionic
liquids have been adjusted using available experimental data in the literature, then liquid-liquid
equilibrium experimental data were correlated just utilizing one binary interaction parameter. The
results showed that the presented model can be useful for phase equilibrium calculations in a wide
range of temperature and pressure.
