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Collect. Czech. Chem. Commun. 1994, 59, 1729-1737
https://doi.org/10.1135/cccc19941729

Modified Apparatus for Measuring V-L Equilibria by Static Method

Július Surový, Elena Graczová and Soňa Bafrncová

Department of Chemical and Biochemical Engineering, Slovak Technical University, 812 37 Bratislava, Slovak Republic

Crossref Cited-by Linking

  • Dragoescu Dana, Teodorescu Mariana, Gheorghe Daniela: Isothermal vapor–liquid equilibria and excess Gibbs free energies in some binary nitroalkane+chloroalkane mixtures at temperatures from 298.15K to 318.15K. Fluid Phase Equilibria 2013, 338, 16. <https://doi.org/10.1016/j.fluid.2012.10.015>
  • Polakovič Milan: Fifty years of the Department of Chemical and Biochemical Engineering at the Slovak University of Technology in Bratislava — brief history of research. Chemical Papers 2013, 67. <https://doi.org/10.2478/s11696-013-0464-z>
  • Dragoescu Dana, Barhala Alexandru, Teodorescu Mariana, Chiscan Daniela: Isothermal vapour-liquid equilibria in cyclohexanone + dichloroalkane binary mixtures at temperatures from 298.15 to 318.15K. J. Serb. Chem. Soc. 2011, 76, 305. <https://doi.org/10.2298/JSC090127020D>
  • Dragoescu Dana, Barhala Alexandru, Teodorescu Mariana: (Vapour+liquid) equilibria and excess Gibbs free energies of (cyclohexanone+1-chlorobutane and+1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15)K. The Journal of Chemical Thermodynamics 2009, 41, 1025. <https://doi.org/10.1016/j.jct.2009.04.006>
  • Dragoescu Dana, Barhala Alexandru, Teodorescu Mariana: Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane+cyclohexanone, chloroform+cyclopentanone and chloroform+cyclohexanone mixtures at temperatures from 298.15 to 318.15K. Fluid Phase Equilibria 2008, 267, 70. <https://doi.org/10.1016/j.fluid.2008.02.018>
  • Steltenpohl Pavol, Graczová Elena: Vapor−Liquid Equilibria of Selected Components in Propylene Oxide Production. J. Chem. Eng. Data 2008, 53, 1579. <https://doi.org/10.1021/je800122x>
  • Graczová Elena, Steltenpohl Pavol: Phase Equilibria of Binary Systems Comprising Formic Acid, N,N-Dimethylformamide, 1-Chloro-2-ethylhexane, and 2-Ethyl-1-hexanol. J. Chem. Eng. Data 2008, 53, 1785. <https://doi.org/10.1021/je800123c>
  • Dragoescu Dana, Teodorescu Mariana, Barhala Alexandru: Isothermal (vapour+liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone+chloroalkane) mixtures at temperatures from 298.15K to 318.15K. The Journal of Chemical Thermodynamics 2007, 39, 1452. <https://doi.org/10.1016/j.jct.2007.03.008>
  • Barhala Alexandru, Dragoescu Dana, Teodorescu Mariana, Wichterle Ivan: Isothermal (vapour+liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15)K. The Journal of Chemical Thermodynamics 2006, 38, 617. <https://doi.org/10.1016/j.jct.2005.07.016>
  • Šoóš M, Graczová E, Markoš J, Molnár A, Steltenpohl P: Design and simulation of a distillation column for separation of dichloropropane from a multicomponent mixture. Chemical Engineering and Processing: Process Intensification 2003, 42, 273. <https://doi.org/10.1016/S0255-2701(02)00021-1>
  • Dragoescu Dana, Barhala Alexandru, Vilcu Rodica: Isothermal vapour–liquid equilibrium data for the binary propan-2-one+chloroalkanes mixtures at temperatures from 298.15 K to 313.15 K. Fluid Phase Equilibria 1999, 157, 41. <https://doi.org/10.1016/S0378-3812(99)00012-6>
  • Dragoescu Dana, Barhala Alexandru, Vilcu Rodica: Vapour pressures and excess Gibbs energy of propane-2-one+chloroalkanes binary mixtures. Fluid Phase Equilibria 1998, 146, 247. <https://doi.org/10.1016/S0378-3812(98)00213-1>