Analysis of the Nonrandom Two-Liquid Model for Prediction of Liquid–liquid Equilibria

The structure of solutions of the nonrandom two-liquid (NRTL) model for prediction of liquid–liquid equilibria is investigated in ternary and quaternary systems. We graphically analyze the isoactivity equations of a ternary system and examine the structure of their solutions. Three types of solutions are revealed. In addition, we find that the convexity check of the Gibbs free energy does not always exclude erroneous predictions for either ternary or quaternary systems. Finally, we propose a procedure to identify the correct predictions as well as to investigate the structure of solutions of isoactivity equations, which works effectively for tested ternary and quaternary systems and theoretically is applicable to systems with multiple components. Both the graphical analysis method and the proposed procedure are transferable to analyzing liquid–liquid equilibria based on other thermodynamic models.

[1]  W. Seider,et al.  Computation of phase and chemical equilibrium: Part I. Local and constrained minima in Gibbs free energy , 1979 .

[2]  J. Prausnitz,et al.  Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systems , 1975 .

[3]  J. Prausnitz,et al.  LOCAL COMPOSITIONS IN THERMODYNAMIC EXCESS FUNCTIONS FOR LIQUID MIXTURES , 1968 .

[4]  Herbert I. Britt,et al.  Local composition model for excess Gibbs energy of electrolyte systems. Part I: Single solvent, single completely dissociated electrolyte systems , 1982 .

[5]  L. Mei,et al.  A modified NRTL equation for the calculation of phase equilibrium of polymer solutions , 1996 .

[6]  Chau‐Chyun Chen Molecular Thermodynamics for Pharmaceutical Process Modeling and Simulation , 2010 .

[7]  F. García-Sánchez,et al.  (Liquid–liquid) equilibria for ternary and quaternary systems of representative compounds of gasoline+methanol at 293.15K: Experimental data and correlation , 2013 .

[8]  G. M. Wilson,et al.  Vapor-Liquid Equilibrium. XI. A New Expression for the Excess Free Energy of Mixing , 1964 .

[9]  Aage Fredenslund,et al.  Liquid—liquid equilibrium data: Their retrieval, correlation and prediction Part II: Correlation , 1979 .

[10]  Jianguo Mi,et al.  Liquid–liquid equilibria of multi-component systems including n-hexane, n-octane, benzene, toluene, xylene and sulfolane at 298.15 K and atmospheric pressure , 2000 .

[11]  Chau-Chyun Chen,et al.  A segment-based local composition model for the gibbs energy of polymer solutions , 1993 .

[12]  Chau‐Chyun Chen,et al.  Segment-Based Eyring−NRTL Viscosity Model for Mixtures Containing Polymers , 2004 .

[13]  Lawrence B. Evans,et al.  A local composition model for the excess Gibbs energy of aqueous electrolyte systems , 1986 .

[14]  Chau‐Chyun Chen,et al.  Symmetric Electrolyte Nonrandom Two-Liquid Activity Coefficient Model , 2009 .

[15]  M. Michelsen The isothermal flash problem. Part I. Stability , 1982 .

[16]  Lawrence B. Evans,et al.  Thermodynamic representation of phase equilibria of mixed‐solvent electrolyte systems , 1986 .

[17]  E. Macedo,et al.  Liquid-liquid equilibria for ternary systems of water-phenol and solvents: data and representation with models , 1986 .