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• Zhang Minhua, Wang Yuankang, Liu Shuhan, Zhang Yan, Yu Yingzhe: A study on the vapor–liquid equilibria of vinyl acrylate-acetic acid and vinyl acetate-acetic acid with GEMC method. Separation and Purification Technology 2024, 330, 125509. <https://doi.org/10.1016/j.seppur.2023.125509>
• Trofimova M., Samarov A., Misikov G., Zaripova S.: Vapor–Liquid Equilibrium in Chemically Equilibrium Systems: The System with Reaction of Ethyl Acetate Synthesis. Russ J Gen Chem 2024, 94, S165. <https://doi.org/10.1134/S1070363224140172>
• Guo Yimin, Zou Yun, Huang Kelei, Li Qing, Tong Zhangfa: Vapor–Liquid and Chemical Equilibrium for Esterification of Acetic Acid + Isopropanol with [HSO3-bmim][HSO4] at 101.33 kPa. J Solution Chem 2023, 52, 1209. <https://doi.org/10.1007/s10953-023-01311-1>
• Shu Chang, Li Xingang, Li Hong, Gao Xin: Determining catalyst loading in reactive distillation column. Chemical Engineering Science 2023, 277, 118807. <https://doi.org/10.1016/j.ces.2023.118807>
• Polkovnichenko Andrei V., Lupachev Egor V., Kulov Nikolai N., Voshkin Andrey A.: Methylpyrrolidonium Trifluoroacetate Protic Ionic Liquid: Distillation Boundary in the Ethyl Trifluoroacetate–Trifluoroacetic Acid–N-Methyl-2-pyrrolidone System. J. Chem. Eng. Data 2023, 68, 2296. <https://doi.org/10.1021/acs.jced.3c00259>
• Wang Jing, Cheng Yuan, Kwon Young Min, Zhang Hui, Wang Xiaochen, Liu Anqiu, Zhang Lingyun, Gao Daming, Kim Chan Kyung: Theoretically and Experimentally Exploring the Isobaric Vapor–Liquid Associating Behavior for Binary and Ternary Mixtures Containing Methanol, Water, and Ethanoic Acid. J. Chem. Eng. Data 2023, 68, 2610. <https://doi.org/10.1021/acs.jced.3c00334>
• 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>
• Zhang Lidong, Zhang Hui, Kwon Young Min, Shahzad Nasir, Chen Hong, Wang Xiaochen, Liu Anqiu, Zhang Lingyun, Zhu Dechun, Xia Xiaoxiao, Gao Daming, Kim Chan Kyung: Combined Experimental and Theoretical Studies on the Prediction of the Isobaric Vapor–Liquid Association Phenomena for Binary and Ternary Mixtures of Water, Ethanoic Acid, and Propanoic Acid. Ind. Eng. Chem. Res. 2020, 59, 13290. <https://doi.org/10.1021/acs.iecr.0c01963>
• Baird Zachariah Steven, Uusi-Kyyny Petri, Witos Joanna, Rantamäki Antti H., Sixta Herbert, Wiedmer Susanne K., Alopaeus Ville: Vapor–Liquid Equilibrium of Ionic Liquid 7-Methyl-1,5,7-triazabicyclo[4.4.0]dec-5-enium Acetate and Its Mixtures with Water. J. Chem. Eng. Data 2020, 65, 2405. <https://doi.org/10.1021/acs.jced.9b01039>
• Galeotti Nadia, Burger Jakob, Hasse Hans: Vapor-liquid equilibrium in the ternary systems acetic acid + water + (xylose or glucose). Fluid Phase Equilibria 2018, 473, 323. <https://doi.org/10.1016/j.fluid.2018.06.011>
• Slavchov Radomir I., Novev Javor K., Mosbach Sebastian, Kraft Markus: Vapor Pressure and Heat of Vaporization of Molecules That Associate in the Gas Phase. Ind. Eng. Chem. Res. 2018, 57, 5722. <https://doi.org/10.1021/acs.iecr.7b04241>
• Huang Zhixian, Li Ling, Zhou Miaomiao, Jiang Haiming, Qiu Ting: Isobaric vapor–liquid equilibrium of trifluoroacetic acid+water, trifluoroacetic acid+ethyl trifluoroacetate and ethyl trifluoroacetate+ ethanol binary mixtures. Fluid Phase Equilibria 2016, 408, 88. <https://doi.org/10.1016/j.fluid.2015.08.012>
• Harvianto Gregorius Rionugroho, Kim Seo Eun, Kang Ki Joon, Bahadori Alireza, Lee Moonyong: Liquid–liquid equilibrium data and correlation for quaternary systems of acetic acid + water + methyl acetate + p-xylene at 313.2 K. Journal of Industrial and Engineering Chemistry 2016, 35, 369. <https://doi.org/10.1016/j.jiec.2016.01.016>
• Huang Dan, Yang Chen, Xue Xueliang, Wang Qinglian, Qiu Ting: Isobaric vapor–liquid equilibrium of the binary system sec-butyl acetate +para-xylene and the quaternary system methyl acetate +para-xylene +sec-butyl acetate + acetic acid at 101.3 kPa. Fluid Phase Equilibria 2015, 402, 50. <https://doi.org/10.1016/j.fluid.2015.05.032>
• Sachsenhauser Tobias, Rehfeldt Sebastian, Klamt Andreas, Eckert Frank, Klein Harald: Consideration of dimerization for property prediction with COSMO-RS-DARE. Fluid Phase Equilibria 2014, 382, 89. <https://doi.org/10.1016/j.fluid.2014.08.030>
• Pirola Carlo, Galli Federico, Manenti Flavio, Corbetta Michele, Bianchi Claudia L.: Simulation and Related Experimental Validation of Acetic Acid/Water Distillation Using p-Xylene as Entrainer. Ind. Eng. Chem. Res. 2014, 53, 18063. <https://doi.org/10.1021/ie502758v>
• HUANG Xiuhui, ZHONG Weimin, PENG Changjun, QIAN Feng: Isobaric Vapor-Liquid Equilibrium of Binary Systems: p-Xylene + (Acetic Acid, Methyl Acetate and n-Propyl Acetate) and Methyl Acetate + n-Propyl Acetate in an Acetic Acid Dehydration Process. Chinese Journal of Chemical Engineering 2013, 21, 171. <https://doi.org/10.1016/S1004-9541(13)60455-3>
• Zhu Dechun, Gao Daming, Zhang Hui, Winter Bernhard, Lücking Peter, Sun Hong, Guan Hangmin, Chen Hong, Shi Jianjun: Geometric Structures of Associating Component Optimized toward Correlation and Prediction of Isobaric Vapor–Liquid Equilibria for Binary and Ternary Mixtures of Ethanal, Ethanol, and Ethanoic Acid. J. Chem. Eng. Data 2013, 58, 7. <https://doi.org/10.1021/je300810p>
• Kobuchi Shigetoshi, Takakura Kei, Yonezawa Setsuko, Fukuchi Kenji, Arai Yasuhiko: Correlation of Vapor^|^#8211;Liquid Equilibria of Binary Systems Containing Carboxylic Acid by Using Wilson Equation with Parameters Estimated from Pure-Component Properties. J. Chem. Eng. Japan / JCEJ 2013, 46, 100. <https://doi.org/10.1252/jcej.12we191>
• Idris Elrashid A.N., Engell Sebastian: Economics-based NMPC strategies for the operation and control of a continuous catalytic distillation process. Journal of Process Control 2012, 22, 1832. <https://doi.org/10.1016/j.jprocont.2012.10.005>
• Gao Daming, Zhang Hui, Lücking Peter, Sun Hong, Si Jingyu, Zhu Dechun, Chen Hong, Shi Jianjun: Computation of Isobaric Vapor-Liquid Equilibrium Data for Binary and Ternary Mixtures of Methanol, Water, and Ethanoic Acid from T, p, x, and HmE Measurements. Journal of Thermodynamics 2012, 2012, 1. <https://doi.org/10.1155/2012/641251>
• Rahul Mayur, Kumar M.V. Pavan, Dwivedi Deeptanshu, Kaistha Nitin: An efficient algorithm for rigorous dynamic simulation of reactive distillation columns. Computers & Chemical Engineering 2009, 33, 1336. <https://doi.org/10.1016/j.compchemeng.2009.01.015>
• Forner F., Brehelin M., Rouzineau D., Meyer M., Repke J.-U.: Startup of a reactive distillation process with a decanter. Chemical Engineering and Processing: Process Intensification 2008, 47, 1976. <https://doi.org/10.1016/j.cep.2007.09.005>
• Belkadi A., Llovell F., Gerbaud V., Vega L.F.: Modeling the vapor–liquid equilibrium and association of nitrogen dioxide/dinitrogen tetroxide and its mixtures with carbon dioxide. Fluid Phase Equilibria 2008, 266, 154. <https://doi.org/10.1016/j.fluid.2008.01.026>
• Pavan Kumar M.V., Kaistha Nitin: Role of multiplicity in reactive distillation control system design. Journal of Process Control 2008, 18, 692. <https://doi.org/10.1016/j.jprocont.2007.12.001>
• Binous Housam: Residue curve map for homogeneous reactive quaternary mixtures. Comp Applic In Engineering 2007, 15, 73. <https://doi.org/10.1002/cae.20099>
• Forner F., Döker M., Gmehling J., Repke J.‐U., Wozny G.: Anfahrstrategien für die Reaktivrektifikation in Boden‐ und Packungskolonnen. Chemie Ingenieur Technik 2007, 79, 367. <https://doi.org/10.1002/cite.200600145>
• Singh Ram, Kumar M. V Pavan, Kaistha Nitin: Steady‐State Reactive Distillation Simulation Using the Naphtali‐Sandholm Method. Can J Chem Eng 2007, 85, 75. <https://doi.org/10.1002/cjce.5450850107>
• Apelblat Alexander: Erratum to “The concept of associated solutions in historical development: Part 1. The 1884–1984 period” [J. Mol. Liq. 128 (2006) 1–31]. Journal of Molecular Liquids 2007, 130, 133. <https://doi.org/10.1016/j.molliq.2006.09.001>
• Kumar M.V.P., Kaistha N.: Temperature Based Inferential Control of a Methyl Acetate Reactive Distillation Column. Chemical Engineering Research and Design 2007, 85, 1268. <https://doi.org/10.1205/cherd06053>
• Bernatová Svatoslava, Aim Karel, Wichterle Ivan: Isothermal vapour–liquid equilibrium with chemical reaction in the quaternary water+methanol+acetic acid+methyl acetate system, and in five binary subsystems. Fluid Phase Equilibria 2006, 247, 96. <https://doi.org/10.1016/j.fluid.2006.06.005>
• Apelblat Alexander: The concept of associated solutions in historical development. Part 1. The 1884–1984 period. Journal of Molecular Liquids 2006, 128, 1. <https://doi.org/10.1016/j.molliq.2006.02.005>
• Clifford Scott L., Ramjugernath Deresh, Raal J. David: Vapour–liquid equilibrium of carboxylic acid systems: Propionic acid+valeric acid and isobutyric acid+valeric acid. Fluid Phase Equilibria 2005, 237, 89. <https://doi.org/10.1016/j.fluid.2005.08.006>
• Singh B.P., Singh R., Kumar M.V.P., Kaistha N.: Steady State Analysis of Reactive Distillation Using Homotopy Continuation. Chemical Engineering Research and Design 2005, 83, 959. <https://doi.org/10.1205/cherd.04279>
• Vercher Ernesto, Orchillés A. Vicent, Vázquez M. Isabel, Martínez-Andreu Antoni: Isobaric Vapor−Liquid Equilibria for Water + Acetic Acid + Potassium Acetate. J. Chem. Eng. Data 2004, 49, 566. <https://doi.org/10.1021/je034169e>
• Vercher Ernesto, Vázquez M. Isabel, Martínez-Andreu Antoni: Isobaric Vapor−Liquid Equilibria for Water + Acetic Acid + Sodium Acetate. J. Chem. Eng. Data 2003, 48, 217. <https://doi.org/10.1021/je0255123>
• Al-Arfaj Muhammad A, Luyben William L: Comparative control study of ideal and methyl acetate reactive distillation. Chemical Engineering Science 2002, 57, 5039. <https://doi.org/10.1016/S0009-2509(02)00415-3>
• Peng Jianjun, Lextrait Sebastien, Edgar Thomas F., Eldridge R. Bruce: A Comparison of Steady-State Equilibrium and Rate-Based Models for Packed Reactive Distillation Columns. Ind. Eng. Chem. Res. 2002, 41, 2735. <https://doi.org/10.1021/ie010969b>
• Teodorescu Mariana, Aim Karel, Wichterle Ivan: Isothermal Vapor−Liquid Equilibrium in the Quaternary Water + 2-Propanol + Acetic Acid + Isopropyl Acetate System with Chemical Reaction. J. Chem. Eng. Data 2001, 46, 261. <https://doi.org/10.1021/je0001476>
• Vercher Ernesto, Vázquez M. Isabel, Martínez-Andreu Antoni: Isobaric Vapor−Liquid Equilibria for Water + Acetic Acid + Lithium Acetate. J. Chem. Eng. Data 2001, 46, 1584. <https://doi.org/10.1021/je010106p>
• Maier Robert W., Brennecke Joan F., Stadtherr Mark A.: Reliable computation of reactive azeotropes. Computers & Chemical Engineering 2000, 24, 1851. <https://doi.org/10.1016/S0098-1354(00)00564-0>
• Kreul L. U., Górak A., Barton P. I.: Dynamic rate‐based model for multicomponent batch distillation. AIChE Journal 1999, 45, 1953. <https://doi.org/10.1002/aic.690450912>
• Xu Zhanping, Afacan Artin, Chuang Karl T.: Removal of acetic acid from water by catalytic distillation. Part 2: Modeling and simulation studies. Can J Chem Eng 1999, 77, 682. <https://doi.org/10.1002/cjce.5450770409>
• Xu Z. P., Chuang K. T.: Correlation of Vapor−Liquid Equilibrium Data for Methyl Acetate−Methanol−Water−Acetic Acid Mixtures. Ind. Eng. Chem. Res. 1997, 36, 2866. <https://doi.org/10.1021/ie9701175>
• Shiah I-Min, Tseng Hsieng-Cheng: Prediction of vapor-liquid equilibria for acetic acid aqueous solutions containing salt. Fluid Phase Equilibria 1996, 124, 1. <https://doi.org/10.1016/S0378-3812(96)03076-2>
• Francesconi Romolo, Castellari Carlo, Comelli Fabio, Bandini Elisa: Enthalpy of Mixing with H-Bonds Interactions. The Role of the Reactional Contributions. Zeitschrift für Physikalische Chemie 1991, 173, 37. <https://doi.org/10.1524/zpch.1991.173.Part_1.037>
• Onken U., Rarey-Nies J., Gmehling J.: The Dortmund Data Bank: A computerized system for retrieval, correlation, and prediction of thermodynamic properties of mixtures. Int J Thermophys 1989, 10, 739. <https://doi.org/10.1007/BF00507993>
• Nagata Isamu, Yamamoto Toshihiro: Thermodynamics of associated solutions: vapour-liquid equilibrium for the acetic acid-propanoic acid and propanoic acid-water systems with association. Thermochimica Acta 1989, 143, 253. <https://doi.org/10.1016/0040-6031(89)85064-6>
• Carvoli G., Delogu P.: Phase equilibria of the quaternary system acetic acid—ethylene glycol monoethyl ether acetate—ethylene glycol monoethyl ether—water. Fluid Phase Equilibria 1986, 25, 91. <https://doi.org/10.1016/0378-3812(86)85063-4>
• Savkovic-stevanovic Jelenka: Murphree, Hausen, Vaporization, and Overall Efficiencies in Binary Distillation of Associated Systems. Separation Science and Technology 1984, 19, 283. <https://doi.org/10.1080/01496398408068583>
• Tamir Abraham, Dragoescu Claudia, Apelblat Alexander, Wisniak Jaime: Heats of vaporization and vapor-liquid equilibria in associated solutions containing formic acid, acetic acid, propionic acid and carbon tetrachloride. Fluid Phase Equilibria 1983, 10, 9. <https://doi.org/10.1016/0378-3812(83)80002-8>
• Savković-Stevanović J., Tasić A., Djordjević B.: Vapour liquid equilibrium with association in both phases. Chemical Engineering Science 1982, 37, 1491. <https://doi.org/10.1016/0009-2509(82)80006-7>
• Tamir Abraham, Wisniak Jaime: Activity coefficient calculations in multicomponent associating systems. Chemical Engineering Science 1978, 33, 651. <https://doi.org/10.1016/0009-2509(78)80041-4>
• Bender Eberhard, Block Ulrich: Bedeutung der Mischphasen‐Thermodynamik für die thermische Trenntechnik aus der Sicht der chemischen Industrie. Chemie Ingenieur Technik 1977, 49, 479. <https://doi.org/10.1002/cite.330490606>
• Vetere Alessandro, Cojutti Alessandro, Scaramucci Maria Antonietta: Vapour—liquid equilibria of the acetylene—ammonia system. Chemical Engineering Science 1975, 30, 301. <https://doi.org/10.1016/0009-2509(75)80080-7>
• Tamir Abraham, Wisniak Jaime: Vapour-liquid equilibria in associating solutions. Chemical Engineering Science 1975, 30, 335. <https://doi.org/10.1016/0009-2509(75)80083-2>
• Francesconi R., Trevissoi C.: Liquid—vapour equilibrium in binary mixtures with associations of the components—I General consistency criterion. Chemical Engineering Science 1971, 26, 1331. <https://doi.org/10.1016/0009-2509(71)80053-2>
• Francesconi R., Cojutti A.: Liquid-vapour equilibrium in binary mixtures with associations of the components—II the acetic acid—trichloroethylenen system. Chemical Engineering Science 1971, 26, 1341. <https://doi.org/10.1016/0009-2509(71)80054-4>
• Hamer G.: Stripping in sparged fermentation systems. III. The acetic acid‐water system. Biotech & Bioengineering 1968, 10, 243. <https://doi.org/10.1002/bit.260100211>
• Sebastiani E., Lacquaniti L.: Acetic acid—water system thermodynamical correlation of vapor—liquid equilibrium data. Chemical Engineering Science 1967, 22, 1155. <https://doi.org/10.1016/0009-2509(67)80182-9>
• Werner Günter: Die Phasengleichgewichte dampfförmig—flüssig der Systeme Benzol—Essigsäure und n‐Heptan—Essigsäure bei 20,0°C. J. Prakt. Chem. 1965, 29, 26. <https://doi.org/10.1002/prac.19650290104>
• Meehan G.F., Murphy N.F.: A new correlation for binary systems with an associating component. Chemical Engineering Science 1965, 20, 757. <https://doi.org/10.1016/0009-2509(65)80063-X>