Vapor-liquid equilibrium of binary and ternary mixtures containing isopropyl ether, 2-butanol, and benzene at T = 313.15 K

Journal of Chemical and Engineering Data

Volumn 51, Issue 1, 2006, Pages 148-152

  Villamañán, Rosa M ^a   Martín, M Carmen ^a   Chamorro, César R ^a   Segovia, José J ^a  

^a UNIVERSITY OF VALLADOLID   (Spain)

Author keywords

[No Author keywords available]

Indexed keywords

ALCOHOLS; BENZENE; BINARY MIXTURES; ETHERS; ISOTHERMS; MATHEMATICAL MODELS;

MARGULES EQUATION; PRESSURE CELLS; TERNARY MIXTURES; VAPOR-LIQUID EQUILIBRIUM;

TERNARY SYSTEMS;

EID: 31444439212     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je0502896     Document Type: Article

References (28)

1. Villamañán, R. M.; Martín, M. C.; Chamorro, C. R.; Villamañán, M. A.; Segovia, J. J. Phase equilibrium properties of binary and ternary systems containing di-isopropyl ether + 1-butanol + benzene at 313.15 K. J. Chem. Thermodyn. (in press).
2. Villamañán, R. M.; Chamorro, C. R.; Martín, M. C.; Segovia, J. J. Phase equilibria properties of binary and ternary systems containing di-isopropyl ether + iso-butanol + benzene at 313.15K. Fluid Phase Equilib. (submitted for publication).
3. Van Ness, H. C.; Abbott, M. M. A procedure for rapid degassing of liquids. Ind. Eng. Chem. Fundam. 1978, 17, 66-67.
4. Gibbs, R. E.; Van Ness, H. C. Vapor-liquid equilibria from total-pressure measurements. A new apparatus. Ind. Eng. Chem. Fundam. 1972, 11, 410-413.
5. E for acetone-acetonitrile-methyl acetate at 50°C. J. Chem. Eng. Data 1978, 23, 242-245.
6. Lozano, L. M.; Montero, E. A.; Martín, M. C.; Villamañ án, M. A. Vapor-liquid equilibria of binary mixtures containing methyl tert-butyl ether (MTBE) and/or substitution hydrocarbons at 298.15 K and 313.15 K. Fluid Phase Equilib. 1995, 110, 219-230.
7. Segovia, J. J.; Martin, M. C.; Chamorro, C. R.; Villamãán, M. A. Excess thermodynamics functions for ternary systems containing fuel oxygenates and substitution hydrocarbons. 1. Total-pressure data and & for methyl tert-butyl ether-benzene-cyclohexane. Fluid Phase Equilib. 1997, 133, 163-172.
8. Barker, J. A. Determination of activity coefficients from total pressure measurements. Aust. J. Chem. 1953, 6, 207-210.
9. E. AIChE J. 1975, 21, 62-71.
10. Abbott, M. M.; Floess, J. K.; Walsh, G. E., Jr.; Van Ness, H. C. Vapor-liquid equilibrium: Part IV. Reduction of P-x data for ternary systems. AIChE J. 1975, 21, 72-76.
11. Hayden, J. G.; O'Connell, J. P. A generalized method for predicting second virial coefficients. Ind. Eng. Chem. Process Des. Dev. 1975, 14, 209-216.
12. Dymond, J. H.; Smith, E. B. The Virial Coefficients of Pure Gases and Mixtures- A Critical Compilation; Clarendon Press: Oxford, 1980.
13. Margules, M. Akad. Wiss. Wien, Math. Naturwiss. 1895, 104, 1243.
14. Wohl, K. Thermodynamic evaluation of binary and ternary liquid systems. Chem. Eng. Prog. 1953, 49, 218-219.
15. Wilson, G. M. Vapor-liquid equilibrium. XI: A new expression for the excess free energy of mixing. J. Am. Chem. Soc. 1964, 86, 127-130.
16. Renon, H.; Prausnitz, J. M. Local compositions in thermodynamic excess functions for liquid mixtures. AIChE J. 1968, 14, 135-144.
17. Abrams, D. S.; Prausnitz, J. M. Statistical thermodynamics of liquid mixtures: a new expression for the excess Gibbs energy of partly or completely miscible systems. AIChE J. 1975, 21, 116-128.
18. Chamorro, C. R.; Segovia, J. J.; Martín, M. C.; Villamanan, M. A. Thermodynamics of octane enhancing additives in gasolines: vaporliquid equilibrium of the system di-isopropyl ether (DIPE) + cyclohexane + benzene at 313.15 K. Entropie 2000, 224/225, 67-73.
19. Ambrose, D.; Ellender, J. H.; Sprake, C. H. S.; Townsend, R. Thermodynamic properties of organic oxygen compounds XLIII. Vapour pressures of some ethers. J. Chem. Thermodyn. 1976, 8, 165-178.
20. Riddick, J. A.; Bunger, W. B.; Sakano, T. K. Organic Solvents, Physical Properties and Methods of Purification, Techniques of Chemistry, Vol. II; Wiley-Interscience: New York, 1986.
21. Garriga, R.; Martínez, S.; Pérez, P.; Gracia, M. Vapor pressures at several temperatures, and excess functions at T = 298.15 K of (butanone + 2-butanol). J. Chem. Thermodyn. 1999, 31, 117-127.
22. Garriga, R.; Martínez, S.; Pérez, P.; Gracia, M. Thermodynamic excess properties of binary mixtures of 1 -chlorobutane with 2-butanol or 2-methyl-1-propanol. Fluid Phase Equilib. 2001, 181, 203-214.
23. 10. J. Chem. Thermodyn. 1987, 19, 505-519.
24. Garriga, R.; Pérez, P.; Gracia, M. Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures. Fluid Phase Equilib. 2005, 227, 79-86.
25. Oracz, P. Liquid-vapor equilibrium 1-butanol + benzene. Int. Data Ser. Sel. Data Mixtures 1996, 24, 280.
26. Ambrose, D. Reference values of vapour pressure, the vapour pressures of benzene and hexafluorobenzene. J. Chem. Thermodyn. 1981, 13, 1161-1167.
27. TRC. Thermodynamic Tables of Hydrocarbons and Non Hydrocarbons: Densities; Thermodynamics Research Center, The Texas A&M University System: College Station, TX, 1973.
28. Gmehling, J.; Rasmussen, P.; Fredenslund, F. Vapor liquid equilibria by UNIFAC group contribution revision and extension. 2. Ind. Eng. Chem. Process Des. Dev. 1982, 21, 118-127.