EXCESS ENTHALPY AND VAPOR-LIQUID EQUILIBRIA WITH THE MHV2 AND SOAVE MIXING RULES

References

• Abdel-Ghani , R. M. , and Heidemann , R. A. ( 1996 ). Comparison of delta G excess mixing rules for multi-phase equilibria in some ternary systems , Fluid Phase Equilib. , 116 , 495 – 502 .
   Google Scholar
• Abrams , D. S. , and Prausnitz , J. M. ( 1975 ). Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systems , AIChE J. , 21 , 116 – 128 .
   Web of Science ®Google Scholar
• Anderson , T. F. , and Prausnitz , J. M. ( 1978 ). Application of the UNIQUAC equation to calculation of multicomponent phase equilibria. 1. Vapor-liquid equilibria , Ind. Eng. Chem. Process Des. Dev. , 17 , 552 – 561 .
   Web of Science ®Google Scholar
• Bard , Y. ( 1974 ). Nonlinear Parameter Estimation , Academic Press , New York .
   Google Scholar
• Belousov , V. P. , and Sokolova , E. P. ( 1966 ). Heats of mixing for liquids. IV. Heat of mixing for the binary systems acetone-water, methylethylketone-water, and cyclohexanone-water , Vestn. Leningr. Univ. Fiz. Khim. ser. 3 , 21 , 90 – 93 .
   Google Scholar
• Boublík , T. , Fried , V. , and Hála , E. ( 1984 ). The Vapour Pressures of Pure Substances , Elsevier , Amsterdam .
   Google Scholar
• Brown , I. , and Smith , F. ( 1957 ). Liquid-vapour equilibria: VIII. The system acetone + benzene and acetone + carbon tetrachloride , Austr. J. Chem. , 10 , 423 – 428 .
   Google Scholar
• Brown , I. , Fock , W. , and Smith , F. ( 1969 ). The thermodynamic properties of solutions of normal and branched alcohols in benzene and n-hexane , J. Chem. Thermodyn. , 1 , 273 – 291 .
   Google Scholar
• Burman , Å. U. , and Ström , K. H. U. ( 2007 ). Calculation of vapor liquid equilibrium and excess enthalpy with the UNIQUAC equation , Chem. Eng. Commun. , 194 , 1029 – 1052 .
   Web of Science ®Google Scholar
• Cézac , P. , Castaing-Lavignottes , J. , Reneaume , J. M. , and Maunoury , A. ( 2009 ). Description of ice slurry composition and enthalpy calculation from gE models: Application to water-ethanol systems , Chem. Eng. Commun. , 196 , 715 – 728 .
   Web of Science ®Google Scholar
• Christensen , C. , Gmehling , J. , Christensen , C. , Rasmussen , P. , Weidlich , U. , and Holderbaum , T. ( 1984–1991 ). Heats of Mixing Data Collection , DECHEMA Chemistry Data Series , Frankfurt .
   Google Scholar
• Christensen , J. J. , and Rowley , R. L. ( 1988 ). Handbook of Heats of Mixing: Supplementary Volume , Wiley-Interscience , New York .
   Google Scholar
• Collins , S. G. , Christensen , J. J. , Izatt , R. M. , and Hanks , R. W. ( 1980 ). The excess enthalpies of 10 (n-pentane + an n-alkohol) mixtures at 298.15 K , J. Chem. Thermodyn. , 12 , 609 – 612 .
   Google Scholar
• Dahl , S. , and Macedo , E. ( 1992 ). The MHV2 Model: A UNIFAC-based equation of state model for vapor-liquid and liquid-liquid equilibria of mixtures with strong electrolytes , Ind. Eng. Chem. Res. , 31 , 1195 – 1201 .
   Web of Science ®Google Scholar
• Dahl , S. , and Michelsen , M. L. ( 1990 ). High-pressure vapour-liquid equilibrium with a UNIFAC-based equation of state , AIChE J. , 36 , 1829 – 1836 .
   Web of Science ®Google Scholar
• Dahl , S. , Fredenslund , A. A. , and Rasmussen , P. ( 1991 ). The MHV2 model: A UNIFAC-based equation of state model for prediction of gas solubility and vapor-liquid equilibria at low and high pressures , Ind. Eng. Chem. Res. , 30 , 1936 – 1945 .
   Web of Science ®Google Scholar
• Daubert , T. E. , and Danner , R. P. ( 1986 ). DIPPR Data Compilation , AIChE , New York .
   Google Scholar
• Fischer , K. , and Gmehling , J. ( 1996 ). Further development, status and results of the PSRK method for the prediction of vapor-liquid equilibria and gas solubilities , Fluid Phase Equilib. , 121 , 185 – 206 .
   Google Scholar
• Fuchs , R. , Krenzer , L. , and Gaube , J. ( 1984 ). Excess properties of binary mixtures composed of a polar component and an alkane , Ber. Bunsenges. Phys. Chem. , 88 , 642 – 649 .
   Google Scholar
• Gmehling , J. , Onken , U. , Arlt , W. , Grenzheuser , P. , Kolbe , B. , Rarey , J. , and Weidlich , U. ( 1977–1996 ). Vapor-Liquid Equilibrium Data Collection , DECHEMA Chemistry Data Series , Frankfurt .
   Google Scholar
• Heidemann , R. A. ( 1996 ). Excess free energy mixing rules for cubic equations of state , Fluid Phase Equilib. , 116 , 454 – 464 .
   Google Scholar
• Holderbaum , T. , and Gmehling , J. ( 1991 ). PSRK: A group contribution equation of state based on UNIFAC , Fluid Phase Equilib. , 70 , 251 – 265 .
   Web of Science ®Google Scholar
• Huang , H. , and Sandler , S. I. (1993). Prediction of vapor-liquid equilibria at high pressures using activity coefficient parameters obtained from low-pressure data: A comparison of two equations of state mixing rules, Ind. Eng. Chem. Res. , 32, 1498–1503.
   Google Scholar
• Huron , M. J. , and Vidal , J. ( 1979 ). New mixing rules in simple equations of state for representing vapor-liquid equilibria of strongly nonideal mixtures , Fluid Phase Equilib. , 3 , 255 – 271 .
   Web of Science ®Google Scholar
• Kalospiros , N. S. , Tzouvaras , N. , Coutsikos , P. , and Tassios , D. P. ( 1995 ). Analysis of zero-reference-pressure EoS/GE models , AIChE J. , 41 , 928 – 937 .
   Google Scholar
• Knudsen , K. , Stenby , E. H. , and Fredenslund , A A. ( 1993 ). A comprehensive comparison of mixing rules for calculation of phase equilibria in complex systems , Fluid Phase Equilib. , 82 , 361 – 368 .
   Google Scholar
• Kudryavtseva , L. S. , and Susarev , M. P. ( 1963 ). Vapour-liquid equilibrium in the systems chloroform-hexane and acetone-chloroform , Zh. Prikl. Khim. , 36 , 1231 – 1237 .
   Google Scholar
• Kundu , M. , and Bandyopadhyay , S. S. ( 2007 ). Thermodynamics of alkanolamine + water system , Chem. Eng. Commun. , 194 , 1138 – 1159 .
   Web of Science ®Google Scholar
• Larkin , J. A. ( 1975 ). Thermodynamic properties of aqueous non-electrolyte mixtures. I. Excess enthalpy for water + ethanol at 298.15 to 383.15 K , J. Chem. Thermodyn. , 7 , 137 – 148 .
   Web of Science ®Google Scholar
• Lieberwirth , I. , and Schubert , H. ( 1979 ). Das isoterme Dampf-Flüssigkeits-Phasengleichgewichtsverhalten des Systems Aceton/Wasser bei 35°C , Z. Phys. Chem. (Leipzig) , 260 , 669 – 672 .
   Google Scholar
• Mathias , P. M. , and Copeman , T. W. ( 1983 ). Extension of the Peng-Robinson equation of state to complex mixtures: Evaluation of the various forms of local composition concept , Fluid Phase Equilib. , 13 , 91 – 108 .
   Web of Science ®Google Scholar
• Mertl , I. ( 1972 ). Phase equilibria in the ternary system ethyl acetate – ethanol – water , Collect. Czech. Chem. Commun. , 37 , 366 – 374 .
   Google Scholar
• Michelsen , M. L. ( 1996 ). Matching equation of state mixing rules to activity coefficient model expressions , Fluid Phase Equilib. , 121 ( 1–2 ), 15 – 26 .
   Google Scholar
• Michelsen , M. L. , and Heidemann , R. A. ( 1996 ). Some properties of equation of state mixing rules derived from excess Gibbs energy expressions , Ind. Eng. Chem. Res. , 35 , 278 – 287 .
   Web of Science ®Google Scholar
• Orbey , H. , and Sandler , S. I. ( 1995 ). On the combination of equation of state and excess free energy models , Fluid Phase Equilib. , 111 , 53 – 70 .
   Google Scholar
• Pando , C. , Renuncio , J. A. R. , Hanks , R. W. , and Christensen , J. J. ( 1983 ). The prediction of vapor-liquid equilibrium from heat of mixing data of binary hydrocarbon-ether and hydrocarbon-aldehyde mixtures , Thermochim. Acta , 62 , 113 – 124 .
   Google Scholar
• Ratcliff , G. A. , and Chao , K. C. ( 1969 ). Prediction of thermodynamic properties of polar mixtures by a group solution model , Can. J. Chem. Eng. , 47 , 148 – 153 .
   Web of Science ®Google Scholar
• Row , K. H. , Park , J. K. , and Gasem , K. A. M. ( 2008 ). The modified PGR equation of state: Asymmetric mixture VLE representation and predictions , Chem. Eng. Commun. , 195 , 492 – 510 .
   Web of Science ®Google Scholar
• Sandler , S. I. , Orbey , H. , and Lee , B.-I. ( 1994 ). Equations of state , in Models for Thermodynamic and Phase Equilibria Calculations , ed. S. I. Sandler , Marcel Dekker , New York .
   Google Scholar
• Smirnova , N. A. , and Kurtynina , L. M. ( 1969 ). Thermodynamic functions of mixing for a number of binary alcohol-hydrocarbon solutions , Zh. Fiz. Khim. , 43 , 1883 – 1885 .
   Google Scholar
• Soave , G. ( 1972 ). Equilibrium constants from a modified Redlich-Kwong equation of state , Chem. Eng. Sci. , 27 , 1197 – 1203 .
   Web of Science ®Google Scholar
• Soave , G. ( 1992 ). A new expression of q(α) for the modified Huron-Vidal method , Fluid Phase Equilib. , 72 , 325 – 327 .
   Google Scholar
• van Ness , H. C. , and Abbott , M. M. ( 1982 ). Classical Thermodynamics of Non-electrolyte Solutions , Pergamon , Oxford .
   Google Scholar
• Vesely , F. , Uchtil , P. , Zabransky , M. , and Pick , J. ( 1979 ). Heats of mixing of cyclohexane with 1-propanol and 2-propanol , Collect. Czech. Chem. Commun. , 44 , 2869 – 2881 .
   Google Scholar
• Wong , D. S. H. , and Sandler , S. I. ( 1992 ). Theoretically correct mixing rules for cubic equations of state , AIChE J. , 38 , 671 – 680 .
   Web of Science ®Google Scholar
• Yoon , J.-H. , Chun , M.-K. , Hong , W.-H. , and Lee , H. ( 1993 ). High-pressure phase equilibria for carbon dioxide-methanol-water system: Experimental data and critical evaluation of mixing rules , Ind. Eng. Chem. Res. , 32 , 2881 – 2887 .
   Web of Science ®Google Scholar