Abstract
The chemical equilibrium (CE) for the quaternary reacting system ethanol–acetic acid–ethyl acetate–water was studied at 303.15, 313.15 and 323.15 K and atmospheric pressure. The CE compositions were determined by gas chromatography and nuclear magnetic resonance analytical methods. The thermodynamic constants of CE at 303.15, 313.15 and 323.15 K were calculated based on the obtained experimental data with the use of the NRTL model.
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Otera, J., Nishikido, J.: Esterification: Methods, Reactions, and Applications. Wiley, Weinheim (2010)
Tavan, Y., Hosseini, S.H.: Design and simulation of a reactive distillation process to produce high-purity ethyl acetate. J. Taiwan Inst. Chem. Eng. 44, 577–585 (2013)
Lai, I.-K., Liu, Y.-C., Yu, C.-C., Lee, M.-J., Huang, H.-P.: Production of high-purity ethyl acetate using reactive distillation: Experimental and start-up procedure. Chem. Eng. Process. Process Intensif. 47, 1831–1843 (2008)
Fernandez, M.F., Barroso, B., Meyer, X.M., Meyer, M., Le Lann, M.-V., Le Roux, G., Brehelin, M.: Dynamics of reactive distillation for the production of ethyl acetate. Comput. Aided Chem. Eng. 30, 787–791 (2012)
Brandt, S., Horstmann, S., Steinigeweg, S., Gmehling, J.: Phase equilibria and excess properties for binary systems in reactive distillation processes. Part II. Ethyl acetate synthesis. Fluid Phase Equilib. 376, 48–54 (2014)
Klöker, M., Kenig, E., Górak, A., Markusse, A., Kwant, G., Moritz, P.: Investigation of different column configurations for the ethyl acetate synthesis via reactive distillation. Chem. Eng. Process. Process Intensif. 43, 791–801 (2004)
Toikka, A.M., Samarov, A.A., Toikka, M.A.: Phase and chemical equilibria in multicomponent fluid systems with a chemical reaction. Russ. Chem. Rev. 84, 378–392 (2015)
Gmehling, J., Kleiber, M.: Vapor–Liquid Equilibrium and Physical Properties for Distillation. In: Gorak, A., Sorensen, E. (eds.) Distillation: Fundamentals and Principles, pp. 45–95. Elsevier, London (2014)
Kiss, A.A.: Advanced Distillation Technologies: Design, Wiley, Chichester (2013)
Frenkel, M., Chirico, R.D., Diky, V., Kazakov, A.F., Muzny, C.D., Magee, J.W., Abdulagatov, I., Kroenlein, K., Kang, J.W.: NIST ThermoData Engine, NIST Standard Reference Database 103b-Pure Compounds Binary Mixtures and Chemical Reactions Version 5.0; Standard Reference Data Program. National Institute of Standards and Technology, Gaithersburg (2010)
Samarov, A., Naumkin, P., Toikka, A.: Chemical equilibrium for the reactive system acetic acid+n-butanol+n-butyl acetate+water at 308.15 K. Fluid Phase Equilib. 403, 10–13 (2015)
Grob, S., Hasse, H.: Thermodynamics of phase and chemical equilibrium in a strongly nonideal esterification system. J. Chem. Eng. Data 50, 92–101 (2005)
Cantelo, R.C., Billinge, R.D.: The ethyl acetate equilibrium. J. Am. Chem. Soc. 50, 3212–3215 (1928)
Tidwell, H.C., Reid, E.E.: Vapor phase esterification in presence of silica gel. J. Am. Chem. Soc. 53, 4353–4358 (1931)
Frolich, P.K., Carpenter, G.B., Knox, W.J.: Vapor phase esterification of acetic acid by ethyl alcohol. J. Am. Chem. Soc. 52, 1565–1570 (1930)
Essex, H., Clark, J.D., Arbor, A., Clark, J.D.: The free energy of formation of ethyl acetate. Equilibrium in the gaseous state. J. Am. Chem. Soc. 54, 1290–1306 (1932)
Hawes, R.W., Kabel, R.L.: Thermodynamic equilibrium in the vapor phase esterification of acetic acid with ethanol. AIChE J. 14, 606–611 (1968)
Venkateswarlu, C., Satyanarayana, M., Rao, M.: Vapor-phase catalytic esterification of ethyl alcohol with acetic acid. Applied kinetic studies. Ind. Eng. Chem. 50, 973–978 (1958)
Kang, Y.W., Lee, Y.Y., Lee, W.K.: Vapor-liquid equilibria with chemical reaction equilibrium. Systems containing acetic acid, ethyl alcohol, water, and ethyl acetate. J. Chem. Eng. Japan 25, 649–655 (1992)
Pérez Cisneros, E.S., Gani, R., Michelsen, M.L.: Reactive separation systems—I. Computation of physical and chemical equilibrium. Chem. Eng. Sci. 52, 527–543 (1997)
Campanella, E.A., Mandagaran, B.A.: Phase equilibria for quaternary mixtures in esterification reaction systems. Lat. Am. Appl. Res. 33, 313–321 (2003)
Kenig, E.Y., Bäder, H., Górak, A., Beßling, B., Adrian, T., Schoenmakers, H.: Investigation of ethyl acetate reactive distillation process. Chem. Eng. Sci. 56, 6185–6193 (2001)
Smith, J.M., Van Ness, H.C.: Introduction to Chemical Engineering Thermodynamics, 3rd edn. McGraw-Hill, New York (1975)
Dean, J.A.: Lange’s Handbook of Chemistry, 12th edn. McGraw-Hill, New York (1979)
Okasinski, M.J., Doherty, M.F.: Thermodynamic behavior of reactive azeotropes. AIChE J. 43, 2227–2238 (1997)
Calvar, N., Domínguez, A., Tojo, J.: Vapor—liquid equilibria for the quaternary reactive system ethyl acetate+ethanol+water+acetic acid and some of the constituent binary systems at 101.3 kPa. Fluid Phase Equilib. 235, 215–222 (2005)
Toikka, A.M., Toikka, M.A., Pisarenko, Y.A., Serafimov, L.A.: Vapor–liquid equilibria in systems with esterification reaction. Theor. Found. Chem. Eng. 43, 129–142 (2009)
Maiwald, M., Fischer, H.H., Ott, M., Peschla, R., Kuhnert, C., Kreiter, C.G., Maurer, G., Hasse, H.: Quantitative NMR spectroscopy of complex liquid mixtures: Methods and results for chemical equilibria in formaldehyde–water–methanol at temperatures up to 383 K. Ind. Eng. Chem. Res. 42, 259–266 (2003)
Gottlieb, H.E., Kotlyar, V., Nudelman, A.: NMR chemical shifts of common laboratory solvents as trace impurities. J. Org. Chem. 62, 7512–7515 (1997)
Bernatova, S., Aim, K., Wichterle, I.: Vapor–liquid and chemical equilibria in the ethanol + ethanoic acid system at 348.15 K. J. Chem. Eng. Data 52, 20–23 (2007)
Renon, H., Prausnitz, J.M.: Local compositions in thermodynamic excess functions for liquid mixtures. AIChE J. 14, 135–144 (1968)
Acknowledgements
Maya Trofimova is grateful to Russian Foundation for Basic Research for the support of this study (RFBR project 16-33-00129). Maria Toikka is grateful for the scholarship of President of Russian Federation (SP-2140.2016.1). The authors acknowledge Resource Center of Saint Petersburg State University “Magnetic Resonance Research Center”. Authors are grateful to NIST ThermoData Engine group for the data on the properties of considered system.
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Golikova, A., Samarov, A., Trofimova, M. et al. Chemical Equilibrium for the Reacting System Acetic Acid–Ethanol–Ethyl Acetate–Water at 303.15 K, 313.15 K and 323.15 K. J Solution Chem 46, 374–387 (2017). https://doi.org/10.1007/s10953-017-0583-1
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DOI: https://doi.org/10.1007/s10953-017-0583-1