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Vapour–Liquid Equilibria in the Polystyrene + Toluene System at Higher Concentrations of Solvent

handle: 11104/0246638
Vapour–Liquid Equilibria in the Polystyrene + Toluene System at Higher Concentrations of Solvent
Vapour–liquid equilibria (VLE) were determined in the polystyrene + toluene system under isothermal conditions at 363.15, 373.15, and 383.15 K using an improved all-glass microebulliometer with circulation of the liquid phase for the dynamic measurement of total pressure over liquid mixtures. The experimental data were correlated using the UNIQUAC-free volume model. Additionally, the applicability of three known predictive models was tested. It was found that both the GC-Flory equation of state and the UNIFAC-vdW-FV model provide better prediction of VLE than the Entropic-FV model, which very slightly underestimates the experimental data for the system studied.
- Institute of Chemical Process Fundamentals Czech Republic
- Czech Academy of Sciences Czech Republic
- The Czech Academy of Sciences
- Institute of Chemical Process Fundamentals of CAS Finland
- Academy of Sciences Library Czech Republic
Microsoft Academic Graph classification: Inorganic chemistry Toluene chemistry.chemical_compound chemistry Ebulliometer Polystyrene Solvent
Process Chemistry and Technology, General Chemistry, Biochemistry, vapour–liquid equilibrium; polymer–solvent system; ebulliometer; experimental data; correlation, polymer-solvent system, vapor-liquid equilibrium, correlation
Process Chemistry and Technology, General Chemistry, Biochemistry, vapour–liquid equilibrium; polymer–solvent system; ebulliometer; experimental data; correlation, polymer-solvent system, vapor-liquid equilibrium, correlation
Microsoft Academic Graph classification: Inorganic chemistry Toluene chemistry.chemical_compound chemistry Ebulliometer Polystyrene Solvent
15 references, page 1 of 2
1. Pavlíček, J., Bogdanić, G., Wichterle, I., Circulation Micro-ebulliometer for Determination of Pressure above Mixtures Containing Solvent and Non-volatile Component, Fluid Phase Equilib. 297 (2010) 142. doi: http://dx.doi.org/10.1016/j.fluid.2010.05.022. [OpenAIRE]
2. Bogdanić, G., Wichterle, I., Vapor-Liquid Equilibrium in Diluted Polymer + Solvent Systems, J. Chem. Eng. Data 56 (2011) 1080. doi: http://dx.doi.org/10.1021/je101052a. [OpenAIRE]
3. Pavlíček, J., Bogdanić, G., Wichterle, I., Vapour-Liquid Equilibria in the Polymer + Solvent System Containing Lower Concentrations of Solute at Normal or Reduced Pressures, Fluid Phase Equilib. 358 (2013) 301. doi: http://dx.doi.org/10.1016/j.fluid.2013.08.036.
4. Pavlíček, J., Bogdanić, G., Wichterle, I., Vapour-Liquid Equilibria in the Poly(methyl methacrylate) + 2-Butanone System Containing Lower Concentrations of Solute at Normal or Reduced Pressures, Chem. Biochem. Eng. Q. 28 (2014) 447. doi: http:/dx.doi.org/10.15255/CABEQ.2014.19388
5. Hao, W., Elbro, H. S., Alessi, P., Polymer Solution Data Collection. 1: Vapor-Liquid Equilibrium, Chemistry Data Series XVI, Part 1, DECHEMA: Frankfurt/M., 1992.
6. Jonquières, A., Perrin, L., Arnold, S., Lochon, P., Comparison of UNIQUAC with related models for modelling vapour sorption in polar materials, J. Membrane Sci. 150 (1998) 125. doi: http://dx.doi.org/10.1016/S0376-7388(98)00221-X. [OpenAIRE]
7. Daubert, T. E., Danner, R. P., Data Compilation Tables of Properties of Pure Compounds, Design Institute for Physical Property Data, American Institute of Chemical Engineers (DIPPR/AIChE), 1985.
8. Rodgers, P. A., Pressure-volume-temperature relationships for polymeric liquids: A review of equations of state and their characteristic parameters for 56 polymers, J. Appl. Polym. Sci. 48 (1993) 1061. doi: http://dx.doi.org/10.1002/app.1993.070480613.
9. Bondi, A., Physical Properties of Macromolecular Crystals, Liquid and Glasses, Wiley, New York, 1968.
10. Danner, R. P., High, M. S., Handbook of Polymer Solution Thermodynamics, DIPPR Project, AIChE, New York, 1993.
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- Institute of Chemical Process Fundamentals Czech Republic
- Czech Academy of Sciences Czech Republic
- The Czech Academy of Sciences
- Institute of Chemical Process Fundamentals of CAS Finland
- Academy of Sciences Library Czech Republic
Vapour–liquid equilibria (VLE) were determined in the polystyrene + toluene system under isothermal conditions at 363.15, 373.15, and 383.15 K using an improved all-glass microebulliometer with circulation of the liquid phase for the dynamic measurement of total pressure over liquid mixtures. The experimental data were correlated using the UNIQUAC-free volume model. Additionally, the applicability of three known predictive models was tested. It was found that both the GC-Flory equation of state and the UNIFAC-vdW-FV model provide better prediction of VLE than the Entropic-FV model, which very slightly underestimates the experimental data for the system studied.