PHASE VAPOR–LIQUID EQUILIBRIUM FOR THE SOLUTIONS OF DIMETHYLZINC AND DIMETHYL SELENIDE

1
Lviv Polytechnic National University
2
Lviv Polytechnic National University
3
Lviv Polytechnic National University
4
Lviv Polytechnic National University
5
Lviv Polytechnic National University

The thermodynamic parameters were calculated. for the vapor-liquid equilibrium of “dimethylzinc-dimethyl selenide” system using the tensometric data obtained for high-purity dimethylzinc, dimethylselene and their equimolecular solution. For this purpose, the Wilson’s model, whose parameters were calculated by the activity coefficients of components in the azeotrope, were used. The calculation was made using the mathematical package MathCad 14. The parameters of the Wilson’s model allowed to calculate the activity coefficients, the vapor compositions, the partial pressures, the component separation coefficient, the excess functions for the solution, and to draw isothermal diagrams for vapor-liquid equilibrium. The table lists the calculated activity coefficients and the excess functions for the solution (HE, GE, kJ/mole).

The values of the activity coefficients (γi <1), the excess enthalpy of the solution (HE <0), and the shapes of isothermal P-X equilibrium diagrams indicate on the existence of an azeotrope in this system and the negative deviation of this solution from the ideal. The values of Gibbs excess energy for this solution (GE) in the whole range of concentrations and temperatures is negative, that indicates on the formation of homogeneous solutions. As the temperature rises, then excess enthalpy increases, that indicates a positive value of the heat capacity change in during the formation of the dimethylzinc-dimethyl selenіde solution. The deviation of this system from the Raoult’s law is explained, in our opinion, by the enthalpy factor. In the investigated solution, the energy of interaction between different molecules is greater than that between identical molecules. This indicates on significant difference between the parameters (l12 – l11) and (l12 – l22) in the Wilson’s equation.

 

1. Gerasimchuk, S. I., Pavlovskii, Y. P., & Van-Chin-Syan, Y. Y. (2012). Thermodynamics of the eva¬poration of dimethylzinc, dimethylselenium, and their equimo-lecular solutions. Russian Journal of Physical Chemistry A,86(10), 1500-1506. doi:10.1134/ s003602441210010x
https://doi.org/10.1134/S003602441210010X 2. Gerasimchuk, S. I., Pavlovskii, Y. P., Sobechko, I. B., & Van-Chin-Syan, Y. Y. (2014). Thermodynamics of the vaporization of alkyl compounds of zinc, selenium, cadmium, tellurium, and their equimolecular solu-tions. Russian Journal of Physical Chemistry A, 88(3), 365-371. doi:10.1134/s0036024414030054
https://doi.org/10.1134/S0036024414030054 3. Aleksandrov, Ju. I. (1975). Tochnaja kriometrija organicheskih veshhestv. Leningrad: Himija. 4. Kulagina, T. G. (1988). Termodinamicheskie svojstva jekvimolekuljarnyh kompleksov dimetilcink-dimetilselen, trimetilgallij-trimetilmysh'jak v oblasti 0-330, XII Vsesojuzn. konf. po kalorimetrii i himicheskoj termodinamike. Tez. dokl. Gor'kij. 5. Kulagina, T. G., & Lebedev B. V. (1990). Termodinamika kompleksov metil'nyh i jetil'nyh proizvo¬dnyh selena, cinka i tellura v oblasti 0-330 K, VI Vsesojuzn. konf. po termodinamike organicheskih soedi-nenij. Tez. dokl. Minsk, Respúblika Belarús' 6. Poling, B. E., Prausnitz, J. M., & OConnell, J. P. (2001). The properties of gases and liquids. New York: McGraw-Hill. 7. Scatchard, G., & Hamer, W. J. (1935). The Application of Equations for the Chemical Potentials to Partially Miscible Solutions. Journal of the American Chemical Society, 57(10), 1805-1809. doi:10.1021 /ja01313a016
https://doi.org/10.1021/ja01313a016 8. Wilson, G. M. (1964). Vapor-Liquid Equilibrium. XI. A New Expression for the Excess Free Energy of Mixing. Journal of the American Chemical Society, 86(2), 127-130. doi:10.1021/ ja01056a002
https://doi.org/10.1021/ja01056a002 9. Suncov, Ju. K., & Vlasov, M V. (2010). Fazovye ravnovesija zhidkost'-par i termodinamicheskie svojstva rastvorov n-propanol-dimetilketon, n-propanol-metiljeti-lketon. Vestn. Voronezhskogo gos. univer., (2), 41-47. 10. Guo, B., Bai, J., Li, Y., Xia, S., & Ma, P. (2012). Isobaric vapor-liquid equilibrium for four binary systems of 3-methylthiophene. Fluid Phase Equilibria, 320, 26-31. doi:10.1016/ j.fluid.2012.02.005
https://doi.org/10.1016/j.fluid.2012.02.005 11. Londoño, A., Jongmans, M. T., Schuur, B., & Haan, A. B. (2012). Isobaric low pressure vapor-liquid equilibrium data for the binary system monochloroacetic acid dichloroacetic acid. Fluid Phase Equilibria, 313, 97-101. doi:10.1016/j.fluid.2011.09.020
https://doi.org/10.1016/j.fluid.2011.09.020 12. Dell'Era, C., Pokki, J., Uusi-Kyyny, P., Pakkanen, M., & Alopaeus, V. (2010). Vapour-liquid equilibrium for the systems diethyl sulphide 1-butene, cis-2-butene, 2-me-thyl¬propane, 2-methylpropene, n-butane, trans-2-butene. Fluid Phase Equilibria, 291(2), 180-187. doi:10.1016/ j.fluid.2010.01.006
https://doi.org/10.1016/j.fluid.2010.01.006 13. Lladosa, E., Martínez, N. F., Montón, J. B., & Torre, J. D. (2011). Measurements and correlation of vapour-liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures. Fluid Phase Equilibria,307(1), 24-29. doi:10.1016/j.fluid.2011.05.004
https://doi.org/10.1016/j.fluid.2011.05.004 14. Gupta, B. S., & Lee, M. (2012). Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclo¬hexane, toluene, m-xylene, or p-xylene at 101.3kPa. Fluid Phase Equilibria, 313, 190-195. doi:10.1016/ j.fluid.2011.10.009
https://doi.org/10.1016/j.fluid.2011.10.009 15. Mejía, A., Segura, H., Cartes, M., & Pérez-Correa, J. R. (2012). Experimental determination and theoretical modeling of the vapor-liquid equilibrium and surface tensions of hexane tetrahydro-2H-pyran. Fluid Phase Equilibria, 316, 55-65. doi:10.1016/j.fluid.2011.12.007
https://doi.org/10.1016/j.fluid.2011.12.007 16. Yadav, S. S., Mali, N. A., Joshi, S. S., & Chavan, P. V. (2017). Isobaric Vapor-Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa. Journal of Chemical & Engineering Data,62(8), 2436-2442. doi:10.1021/acs.jced.7b00372
https://doi.org/10.1021/acs.jced.7b00372 17. Serheiev, V. (2013). Khimichna termodynamika spoluk akrylovoho riadu. (Dys. dokt. khim. nauk). Natsio-nalnyi Universytet Ukrainy "Lvivska Politekhnika", Lviv. 18. Porshnev, S. V., & Belenkova, I. V. (2005). Chislennye metody na baze Mathcad. Sankt-Peterburg: BHV-Peterburg. 19. Naryshkin, D. G. (2016). Himicheskaja termo-dinamika s Mathcad. Moskva: RIOR: INFRA-M. 20. Sergeev, V. V., Gerasimchuk, S. I., & Pavlovskiy, Yu. P. (2019) Termodinamicheskie funktsii sme-sheniya metilmetakrilata s organicheskimi rastvoritelyami. Zhur¬nal fizicheskoy khimii, 93 (2), A, 188-194. doi:10.1134/ S0044453719020274 21. Serheyev, V., & Thanh, T. V. (2018). Thermodynamic Properties of Butyl Methacrylate Solutions in Organic Solvents. Chemistry & Chemical Technology, 12(1), 7-12. doi:10.23939/chcht12.01.007
https://doi.org/10.23939/chcht12.01.007 22. Sergeev, V. V., & Kos, Y. V. (2017). Thermody-namic functions of the mixing of methacrylic acid in organic solvents. Russian Journal of Physical Chemistry A, 91(11), 2131-2136. doi:10.1134/s003602441711022x
https://doi.org/10.1134/S003602441711022X 23. Serheyev, V., Kos, Y., & Van-Chin-Syan, Y. (2015). Thermodynamic Properties of Solutions of Ethacrylic Acid in Acetonitrile and Acetic Acid. Chemistry & Chemical Technology, 9(2), 131-135. doi:10.23939/ chcht09.02.131
https://doi.org/10.23939/chcht09.02.131 24. Belousov, V. P. (1970). Teploty smeshenija zhidkostej. Leningrad: Himija.