Vapor-liquid equilibrium data for the binary methyl esters (butyrate, pentanoate, and hexanoate) (1) + acetonitrile (2) systems at 93.32 kPa

Journal of Chemical and Engineering Data

Volumn 51, Issue 5, 2006, Pages 1536-1540

  Camacho, Alberto G ^a   Mariano, Alejandra ^a   Mussari, Lelia ^a   Postigo, Miguel A ^a,b  

^a UNIVERSIDAD NACIONAL DEL COMAHUE   (Argentina)

^b Facultad de Ciencias Naturales e Instituto M Lillo   (Argentina)

Author keywords

[No Author keywords available]

Indexed keywords

BINARY METHYL ESTERS; LIQUID PHASES; METHYL BUTYRATES;

CONDENSATION; MATHEMATICAL MODELS; THERMODYNAMIC PROPERTIES; VAPORS;

ESTERS;

EID: 33749847512     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je060001s     Document Type: Article

References (24)

1. Camacho, A.; Postigo, M. Vapor liquid equilibria for the systems methyl ester (methanoate, ethanoate and propanoate) (1) + acetonitrile (2) at 93.32 kPa. Inf. Tecnol 1999, 10 (5), 111-121.
2. Redlich O.; Kister A. T. Thermodynamics of non electrolyte solutions. Algebraic representation of thermodynamic properties and the classification of solutions. Ind. Eng. Chem. 1948, 40, 345-348.
3. Margules, M. S. Akad. B. Wien. Math-Naturwiss. KI. II 1895, 104, 1234-1239.
4. van Laar, J. J. The vapor pressure of binary mixtures. Z. Phys. Chem. 1910, 72, 723-751.
5. Wilson, G. M. Vapor-liquid equilibrium. IX: A new expression for the excess free energy of mixing. J. Am. Chem. Soc. 1964, 86, 127-135.
6. Renon, H.; Prausnitz, J. M. Local compositions in thermodynamic excess functions for liquid mixtures. AIChE J. 1968, 14, 135-142.
7. Kojima, K.; Tochigi, K. Prediction of Vapor-Liquid Equilibria by the ASOG Method; Kodansha Ltd.: Tokyo, 1979.
8. Tochigi, K.; Tiegs, D.; Gmehling, J.; Kojima, K. Determination of new ASOG parameters. J. Chem. Eng. Jpn. 1990 23, 453-429.
9. Fredenslund, Aa.; Jones, R. L.; Prausnitz, J. M. Group contribution estimation of activity coefficients in nonideal liquid mixtures. AIChE J. 1975, 21, 1086-1092.
10. Larsen, B. L.; Rasmussen, P.; Fredenslund, Aa. A modified UNIFAC group contribution model for prediction of phase equilibria and heats of mixing. Ind. Eng. Chem. Res. 1987, 26, 2274-2280.
11. E, and γy. Ind. Eng. Chem. Res. 1987, 26, 1372-1382.
12. Gmehling J.; Li, J.; Schiller, M. A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties. Ind. Eng. Chem. Res. 1993, 32, 178-193.
13. Leonetti, J.; Camacho, A.; Postigo, M. Isobaric vapor-liquid equilibrium of benzene with dichloromethane at 86.65 and 99.99 kPa. Latin Am. Appl. Res. 1999, 29 (2), 77-87.
14. TRC Thermodynamic Tables Hydrocarbons; Thermodynamics Research Center, The Texas A&M University: College Station, TX, 1993.
15. Ortega, J.; Matos, J. S.; Pena, J. A. Enthalpies of mixing at 298.15 K of methylalkanoate (from acetate to pentanoate) with n-alkanes (n-tridecane and pentadecane). Thermochim. Acta 1990, 168, 121-126.
16. Tsonopoulos, C. An empirical correlation of second virial coefficients. AIChE J. 1974, 20, 263-272.
17. Spencer, C. F.; Danner, R. P. J. Improved equation for predicting saturated liquid density. J. Chem. Eng. Data 1972, 17, 236-241.
18. Rupert, G. Physpropsfor Windows, Version 1.6.1; 9x/NT/ME/2000/ XP; G&P Engineering Software: 1999-2004.
19. Ortega, J.; Susial, P.; De Alfonso, C. J. Chem. Eng. Data 1990, 35, 216-219.
20. Camacho, A. Doctoral Thesis. Universidad Nacional de Tucuman, Tucuman, Argentina, 2006.
21. Reid, R. C.; Prausnitz, J. M.; Poling, B. E. The Properties of Gases and Liquids, 4th ed.; McGraw-Hill: New York, 1987.
22. Fredenslund, Aa.; Gmehling, J.; Rasmussen, P. Vapour-Liquid Equilibria Using UNIFAC. A Group-Contribution Method; Elsevier: Amsterdam. 1977.
23. Wisniak, J. A new test for the thermodynamic consistency of vaporliquid equilibrium. Ind. Eng. Chem. Res. 1993, 32, 1531-1533.
24. Apelblat, A.; Wisniak, J. A simple method for evaluating the Wilson constants. Ind. Eng. Chem. Res. 1989, 28, 324-328.