Isothermal vapor-liquid equilibria of 1,3-dioxolane or 1,4-dioxane + Hexane or + cyclohexane or + ethanol mixtures at T = 308.15 K

Journal of Chemical and Engineering Data

Volumn 44, Issue 2, 1999, Pages 193-196

  Calvo, Encina ^a,b   Artal, Manuela ^a   Embid, José Muñoz ^a   Velasco, Inmaculada ^a   Otín, Santos ^a  

^a UNIVERSITY OF ZARAGOZA   (Spain)

^b UNIVERSITY OF SANTIAGO DE COMPOSTELA   (Spain)

Author keywords

[No Author keywords available]

Indexed keywords

BINARY MIXTURES; COMPOSITION; ETHANOL; GIBBS FREE ENERGY; LIQUIDS; MOLECULAR WEIGHT; NUMERICAL METHODS; PHASE EQUILIBRIA; PRESSURE; TEMPERATURE; VAPORS; VOLUME FRACTION;

MOLAR VIRIAL COEFFICIENTS; MOLE FRACTION; REDLICH-KISTER EQUATION;

ETHERS;

EID: 0032662956     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je980132w     Document Type: Article

References (20)

1. E for 1,4-Dioxane-Ethanol-Water at 50 °C. J. Chem. Eng. Data 1979, 24, 133-136.
2. Berro, C.; Rogalski, M.; Peneloux, A. A new ebulliometric technique for vapour-liquid equilibria in the binary systems ethanol-n-heptane and ethanol-n-nonane. Fluid Phase Equilib. 1982, 8, 55-73.
3. Calvo, E. Thermodynamic properties of binary cyclic diethers + alkane, or + alkanol mixtures. Ph.D. Thesis, 1997, Santiago de Compostela, Spain.
4. Deshpande, D. D.; Oswal, S. L. Thermodynamics of mixtures containing p-dioxane or tetrahydrofuran 1. Excess Gibbs free energies and excess volumes. J. Chem. Thermodyn. 1975, 7, 155-159.
5. Fredenslund, A.; Gmehling, J.; Rasmussen, P. Vapor-liquid equilibria using UNIFAC; Elsevier: Amsterdam, 1977.
6. González, C.; Van Ness, H. C. Excess Thermodynamic Functions for Ternary Systems. 8. Total-Pressure Data and GE for Ethanol/ Chloroform/1,4-Dioxane at 50 °C. J. Chem. Eng. Data 1983, 28, 407-409.
7. Hopkins, R. N.; Yerger, E. S.; Lynch, C. C. Some properties of the Dioxane-Ethanol System. J. Am. Chem. Soc. 1939, 61, 2460-2461.
8. Kato, M.; Konishi, H.; Sato, T.; Hirata, M. Measurement of vapor-liquid equilibriums by the dew-bubble point method and the bubble-condensation point method. J. Chem. Eng. Jpn. 1971, 4, 6-10.
9. Muñoz Embid, J.; Artal, M.; Fernández, J.; Velasco, I.; Otín, S. Excess Enthalpies of α,ω-Dibromoalkane + n-Hexane Mixtures at 298.15 K and Isothermal Vapor-Liquid Equilibrium of 1,3-Dibromopropane + n-Nonane at 348.15 K. J. Chem. Eng. Data 1991, 36, 428-430.
10. Nath, J. Thermodynamic Behaviour of Binary Systems of 1,4-Dioxane with 1,2-Dichloroethane, Dichloromethane, Trichloroethene, Tetrachloroethene and Cyclohexane. J. Chem. Soc., Faraday Trans. 1991, 87, 1345-1350.
11. Reid, R. C.; Prausnitz, J. M.; Poling, B. E. The Properties of Gases and Liquids; McGraw-Hill: New York, 1986.
12. Riddick, J. A.; Bunger, W. B.; Sakano, T. K. Organic Solvents; John Wiley & Sons: New York, 1986.
13. Suryanarayana, Y. S.; Van Winkle, M. Solvent effect on relative volatility. Hexane-1-hexene system. J. Chem. Eng. Data 1966, 11, 7-12.
14. Taasios, D.; Van Winkle, M. Prediction of binary vapor-liquid equilibria. Members of homologous series and a common solvent. J. Chem. Eng. Data 1967, 12, 555-561.
15. TRC Thermodynamic Tables. Non-Hydrocarbons; Thermodynamics Research Center, The Texas A&M University System: College Station, TX, 1994.
16. Tsonopoulos, C. An Empirical Correlation of Second Virial Coefficients. AIChE J. 1974, 20, 263-272.
17. Tsonopoulos, C. Second Virial Coefficients of Polar Chloroalkanes. AIChE J. 1975, 21, 827-829.
18. Van Ness, H. C.; Byer, S. M.; Gibbs, R. E. Vapor-liquid equilibrium. I. Appraisal of data reduction methods. AIChE J. 1973, 19, 238-244.
19. Vierk, A. L. The two-component systems: Water-acetonitrile, water-dioxane, ethanol-acetonitrile, and cyclohexane-dioxane. Z. Anorg. Chem. 1950, 267, 283-296.
20. Wu, H. S.; Sandler, S. I. Vapor-Liquid Equilibrium of 1,3-Dioxolane Systems. J. Chem. Eng. Data 1989, 34, 209-213.