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• Misikov Georgii, Trofimova Maya, Prikhodko Igor: Vapor-Liquid Equilibrium in the Acetic Acid-Ethanol-Ethyl Acetate-Water Quaternary System: Critical Literature Review and Thermodynamic Consistency of the Experimental Data. Chemistry 2023, 5, 2542. <https://doi.org/10.3390/chemistry5040165>
• Iwai Yoshio, Matsubara Koji: Simultaneous correlation of liquid-liquid equilibria for ternary systems and phase equilibria for constituent binary systems by modified new activity coefficient model. Fluid Phase Equilibria 2022, 556, 113411. <https://doi.org/10.1016/j.fluid.2022.113411>
• Wu Xumin, Wu Jimin, Wang Suxu, Gao Jun, Xu Dongmei, Zhang Lianzheng, Wang Yinglong: Liquid–Liquid Equilibrium for Ternary Systems (Ethyl Acetate/Isopropyl Acetate + 2,2-Difluoroethanol + Water) at 298.15 and 308.15 K. J. Chem. Eng. Data 2021, 66, 1399. <https://doi.org/10.1021/acs.jced.0c01011>
• Trofimova Maya, Sadaev Alexey, Samarov Artemiy, Golikova Alexandra, Tsvetov Nikita, Toikka Maria, Toikka Alexander: Liquid-liquid equilibrium of acetic acid – ethanol – ethyl acetate – water quaternary system: Data review and new results at 323.15 K and 333.15 K. Fluid Phase Equilibria 2020, 503, 112321. <https://doi.org/10.1016/j.fluid.2019.112321>
• Jaubert Jean-Noël, Le Guennec Yohann, Piña-Martinez Andrés, Ramirez-Velez Nicolas, Lasala Silvia, Schmid Bastian, Nikolaidis Ilias K., Economou Ioannis G., Privat Romain: Benchmark Database Containing Binary-System-High-Quality-Certified Data for Cross-Comparing Thermodynamic Models and Assessing Their Accuracy. Ind. Eng. Chem. Res. 2020, 59, 14981. <https://doi.org/10.1021/acs.iecr.0c01734>
• Sosa Adriel, Fernández Luís, Ortega Juan, Jiménez Laureano: The Parametrization Problem in the Modeling of the Thermodynamic Behavior of Solutions. An Approach Based on Information Theory Fundamentals. Ind. Eng. Chem. Res. 2019, 58, 12876. <https://doi.org/10.1021/acs.iecr.9b01493>
• Khalifa Mejbri, Housam Binous, Ahmed Bellagi: Modeling of the phase behavior of CO 2 in water, methanol, ethanol and acetone by different equations of state. Fluid Phase Equilibria 2018, 469, 9. <https://doi.org/10.1016/j.fluid.2018.04.006>
• NguyenHuynh Dong: Accurate modeling of multiphase behavior of aqueous systems. I. Alkanes, alkenes, cycloalkanes, alcohols, aromatics. Fluid Phase Equilibria 2018, 473, 201. <https://doi.org/10.1016/j.fluid.2018.06.019>
• Ravetti Duran Renan, Escudero Falsetti Priscilla, Muhr Laurence, Privat Romain, Barth Danielle: Phase Equilibrium Study of the Ternary System CO2 + H2O + Ethanol At Elevated Pressure: Thermodynamic Model Selection. Application to Supercritical Extraction of Polar Compounds. The Journal of Supercritical Fluids 2018, 138, 17. <https://doi.org/10.1016/j.supflu.2018.03.016>
• Fernández Luís J., Ortega Juan, Wisniak Jaime: A rigorous method to evaluate the consistency of experimental data in phase equilibria. Application to VLE and VLLE. AIChE Journal 2017, 63, 5125. <https://doi.org/10.1002/aic.15876>
• Mathias Paul M., Kister Henry Z.: Effect of Phase-Equilibrium Uncertainties on Ethyl Acetate Purification. J. Chem. Eng. Data 2017, 62, 2872. <https://doi.org/10.1021/acs.jced.7b00172>
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• Ganbavale G., Zuend A., Marcolli C., Peter T.: Improved AIOMFAC model parameterisation of the temperature dependence of activity coefficients for aqueous organic mixtures. Atmos. Chem. Phys. 2015, 15, 447. <https://doi.org/10.5194/acp-15-447-2015>
• Goutaudier Christelle, Bonnet Fabrice, Tenu Richard, Baudouin Olivier, Counioux Jean-Jacques: Calculation of critical point coordinates of ternary miscibility gap from experimental tie-lines. Chemical Engineering Research and Design 2014, 92, 3008. <https://doi.org/10.1016/j.cherd.2014.06.026>
• Brandt Sarah, Horstmann Sven, Steinigeweg Sven, Gmehling Jürgen: Phase equilibria and excess properties for binary systems in reactive distillation processes. Part II. Ethyl acetate synthesis. Fluid Phase Equilibria 2014, 376, 48. <https://doi.org/10.1016/j.fluid.2014.05.031>
• Mäder A., Zimon A., Fleischmann A., Munack A., Ruck W., Krahl J.: Influences of entrainers to engine oil to improve the drag-out of biodiesel – Experiments and simulations. Fuel 2014, 117, 488. <https://doi.org/10.1016/j.fuel.2013.09.039>
• Ganbavale G., Zuend A., Marcolli C., Peter T.: Improved AIOMFAC model parameterisation of the temperature dependence of activity coefficients for aqueous organic mixtures. Atmos. Chem. Phys. Discuss. 2014, 14, 16907. <https://doi.org/10.5194/acpd-14-16907-2014>
• Cristino A.F., Rosa S., Morgado P., Galindo A., Filipe E.J.M., Palavra A.M.F., Nieto de Castro C.A.: High-temperature vapour–liquid equilibrium for the water–alcohol systems and modeling with SAFT-VR: 1. Water–ethanol. Fluid Phase Equilibria 2013, 341, 48. <https://doi.org/10.1016/j.fluid.2012.12.014>
• Ferrando Nicolas, Lachet Véronique, Boutin Anne: Transferable Force Field for Carboxylate Esters: Application to Fatty Acid Methylic Ester Phase Equilibria Prediction. J. Phys. Chem. B 2012, 116, 3239. <https://doi.org/10.1021/jp212060u>
• Chen C, Liu Y, Maruvada S, Myers M, Khismatullin D: Effect of ethanol injection on cavitation and heating of tissues exposed to high-intensity focused ultrasound. Phys. Med. Biol. 2012, 57, 937. <https://doi.org/10.1088/0031-9155/57/4/937>
• de Villiers A.J., Schwarz C.E., Burger A.J.: Extension of the CPA equation of state with dipolar theories to improve vapour–liquid-equilibria predictions. Fluid Phase Equilibria 2011, 312, 66. <https://doi.org/10.1016/j.fluid.2011.09.007>
• Burman Åsa U., Ström Krister H. U.: EXCESS ENTHALPY AND VAPOR-LIQUID EQUILIBRIA WITH THE MHV2 AND SOAVE MIXING RULES. Chemical Engineering Communications 2011, 198, 1435. <https://doi.org/10.1080/00986440903287874>
• Pavlíček Jan, Bogdanić Grozdana, Wichterle Ivan: Circulation micro-ebulliometer for determination of pressure above mixtures containing solvent and non-volatile component. Fluid Phase Equilibria 2010, 297, 142. <https://doi.org/10.1016/j.fluid.2010.05.022>
• Browarzik D.: Extension of the chemical associating lattice model (CALM) to cross association. Journal of Molecular Liquids 2010, 156, 171. <https://doi.org/10.1016/j.molliq.2010.07.006>
• Pellegrini Laura A., Gamba Simone, Moioli Stefania: Using an Adaptive Parameter Method for Process Simulation of Nonideal Systems. Ind. Eng. Chem. Res. 2010, 49, 4923. <https://doi.org/10.1021/ie901773q>
• Góral Marian, Shaw David G., Mączyński Andrzej, Wiśniewska-Gocłowska Barbara, Jezierski Aleksander: IUPAC-NIST Solubility Data Series. 88. Esters with Water—Revised and Updated. Part 1. C2 to C4 Esters. Journal of Physical and Chemical Reference Data 2009, 38, 1093. <https://doi.org/10.1063/1.3243853>
• Enders Sabine, Kahl Heike: Interfacial properties of water+alcohol mixtures. Fluid Phase Equilibria 2008, 263, 160. <https://doi.org/10.1016/j.fluid.2007.10.006>
• Freitag Jörg, Kato Satoru: Evaluation of cluster formation using the infinite dilution partial molar excess entropies and enthalpies of 1-alkanols in supercritical carbon dioxide. The Journal of Supercritical Fluids 2008, 43, 398. <https://doi.org/10.1016/j.supflu.2007.07.007>
• Shulgin Ivan L., Ruckenstein Eli: An Improved Local Composition Expression and Its Implication for Phase Equilibrium Models. Ind. Eng. Chem. Res. 2008, 47, 7877. <https://doi.org/10.1021/ie800897j>
• Durling Nicola E., Catchpole Owen J., Tallon Stephen J., Grey John B.: Measurement and modelling of the ternary phase equilibria for high pressure carbon dioxide–ethanol–water mixtures. Fluid Phase Equilibria 2007, 252, 103. <https://doi.org/10.1016/j.fluid.2006.12.014>
• Bazaev A.R., Abdulagatov I.M., Bazaev E.A., Abdurashidova A.: (p,v,T,x) Measurements of {(1−x)H2O+xC2H5OH} mixtures in the near-critical and supercritical regions. The Journal of Chemical Thermodynamics 2007, 39, 385. <https://doi.org/10.1016/j.jct.2006.08.002>
• Wyczesany Andrzej: Modeling of Simultaneous Chemical and Phase Equilibria in Esterification of Acetic Acid with Ethanol in High-Pressure Carbon Dioxide. Ind. Eng. Chem. Res. 2007, 46, 5437. <https://doi.org/10.1021/ie070260q>
• Perakis Christophoros, Voutsas Epaminondas, Magoulas Kostis, Tassios Dimitrios: Thermodynamic modeling of the vapor–liquid equilibrium of the water/ethanol/CO2 system. Fluid Phase Equilibria 2006, 243, 142. <https://doi.org/10.1016/j.fluid.2006.02.018>
• Vu Dung T., Lira Carl T., Asthana Navinchandra S., Kolah Aspi K., Miller Dennis J.: Vapor−Liquid Equilibria in the Systems Ethyl Lactate + Ethanol and Ethyl Lactate + Water. J. Chem. Eng. Data 2006, 51, 1220. <https://doi.org/10.1021/je050537y>
• Resa José M., Goenaga José M., Iglesias Miguel, Gonzalez-Olmos Rafael, Pozuelo Daniel: Liquid−Liquid Equilibrium Diagrams of Ethanol + Water + (Ethyl Acetate or 1-Pentanol) at Several Temperatures. J. Chem. Eng. Data 2006, 51, 1300. <https://doi.org/10.1021/je060054+>
• Kurihara Kiyofumi, Egawa Yusuke, Ochi Kenji, Kojima Kazuo: Evaluation of thermodynamic consistency of isobaric and isothermal binary vapor–liquid equilibrium data using the PAI test. Fluid Phase Equilibria 2004, 219, 75. <https://doi.org/10.1016/j.fluid.2004.01.018>
• Tischmeyer M, Arlt W: Determination of binary vapor–liquid equilibria (VLE) of three fast reacting esterification systems. Chemical Engineering and Processing: Process Intensification 2004, 43, 357. <https://doi.org/10.1016/S0255-2701(03)00115-6>
• Hong Gui-Bing, Lee Ming-Jer, Lin Ho-mu: Vapor−Liquid and Vapor−Liquid−Liquid Equilibria for Mixtures Containing Water, Ethanol, and Ethyl Benzoate. Ind. Eng. Chem. Res. 2003, 42, 4234. <https://doi.org/10.1021/ie030209w>
• Gmehling Jürgen, Steinigeweg Sven, Pöpken Tim: Comments on “Optimization of a Wastewater System Containing the Ternary Homogeneous Azeotropic System Ethyl Acetate−Ethanol−Water”. Ind. Eng. Chem. Res. 2001, 40, 492. <https://doi.org/10.1021/ie000652w>
• Clausen Iven, Arlt Wolfgang: A priori-Berechnung von Phasengleichgewichten für die thermische Verfahrenstechnik mit COSMO-RS. Chem.-Ing.-Tech. 2000, 72, 727. <https://doi.org/10.1002/1522-2640(200007)72:7<727::AID-CITE727>3.0.CO;2-S>
• Hernández-Garduza Otilio, Garcı́a-Sánchez Fernando, Neau Evelyne, Rogalski Marek: Equation of state associated with activity coefficient models to predict low and high pressure vapor–liquid equilibria. Chemical Engineering Journal 2000, 79, 87. <https://doi.org/10.1016/S1385-8947(00)00138-8>
• Figurski G., Malanowski S.K.: Vapor–liquid equilibrium studies of the ethanol+ethyl acetate system. Fluid Phase Equilibria 1998, 148, 161. <https://doi.org/10.1016/S0378-3812(97)00341-5>
• Adrian T., Wendland M., Hasse H., Maurer G.: High-pressure multiphase behaviour of ternary systems carbon dioxide–water–polar solvent: review and modeling with the Peng–Robinson equation of state. The Journal of Supercritical Fluids 1998, 12, 185. <https://doi.org/10.1016/S0896-8446(98)00087-4>
• Herraiz J., Shen Shubao, Coronas A.: Vapor−Liquid Equilibria for Methanol + Poly(ethylene glycol) 250 Dimethyl Ether. J. Chem. Eng. Data 1998, 43, 191. <https://doi.org/10.1021/je970206o>
• Hoch Michael: Thermodynamics of binary and larger organic-organic and organic-water systems. Calphad 1997, 21, 359. <https://doi.org/10.1016/S0364-5916(97)00037-0>
• Nagata Isamu, Tamura Kazuhiro: Phase equilibrium calculations using a modified form of the complete local concentration model. Fluid Phase Equilibria 1997, 135, 209. <https://doi.org/10.1016/S0378-3812(97)00082-4>
• Abdel-Ghani Rida M., Heidemann Robert A.: Comparison of ΔG excess mixing rules for multi-phase equilibria in some ternary systems. Fluid Phase Equilibria 1996, 116, 495. <https://doi.org/10.1016/0378-3812(95)02923-0>
• Kurihara K, Kojima K: An implicit type EOS-GE(VP) model employing vapor pressure standard state I. Prediction of high-pressure vapor-liquid equilibria based on low temperature data. Fluid Phase Equilibria 1995, 113, 27. <https://doi.org/10.1016/0378-3812(95)02802-0>
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• Mathias Paul M., Klotz Herbert C., Prausnitz John M.: Equation-of-State mixing rules for multicomponent mixtures: the problem of invariance. Fluid Phase Equilibria 1991, 67, 31. <https://doi.org/10.1016/0378-3812(91)90045-9>
• Nagata Isamu: Simultaneous correlation of ternary vapour-liquid and liquid-liquid equilibria. Thermochimica Acta 1990, 164, 119. <https://doi.org/10.1016/0040-6031(90)80428-2>
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