Isobaric vapor-liquid equilibrium of benzene with dichloromethane at 86.65, 93.32 and 99.99 kPa

Latin American Applied Research

Volumn 29, Issue 2, 1999, Pages 77-81

  Leonetti, Juan C ^a   Camacho, Alberto G ^a   Postigo, Miguel A ^a  

^a UNIVERSIDAD NACIONAL DEL COMAHUE   (Argentina)

Author keywords

ASOG; Excess properties; UNIFAC; Vapor liquid equilibrium

Indexed keywords

EID: 0040706981     PISSN: 03270793     EISSN: None     Source Type: Journal    
DOI: None     Document Type: Article

References (19)

1. Apelblat, A; J. A. Wisniak "Simple Method for Evaluating the Wilson Constants", Ind. Eng. Chem. Res. 28, 324-328, (1989).
2. Aznarez, S. B; L. Mussari, M. A. Postigo, "Temperature dependence of molar excess volumes for dimethylsulfoxide + thiophene system and thermal expansion coefficients between 293.15 and 313.15 K", J. Chem. Eng. Data., 38 (2), 270, (1993).
3. De Alfonso, C., R. Ezama, P. Losada, M.A. Calama, B. Llanas, M. Pintado, A.F. Saenz de la Torre, "Equilibrio Isobárico Líquido-Vapor. III. Desarrollo y ensayo de un aparato de equilibrio de pequeña capacidad", Anales de Quúmica. 79, 243-253, (1983).
4. Fredenslund, Aa., R.L. Jones, J.M. Prausnitz, "Group Contribution Estimation of Activity Coefficients in Non-ideal Liquid Mixtures", AIChE J. 21, 1086-1099, (1975).
5. Fredenslund, Aa., J. Gmehling, P. Rasmussen, "Vapor-Liquid Equilibria Using UNIFAC. A Group-Contribution Method", Elsevier: Amsterdam, (1977).
6. Kojima, K., K. Tochigi, "Prediction of Vapor-Liquid Equilibria by the ASOG Method", Kodansha Ldt. Tokyo, (1979).
7. Larsen, B. L., P. Rasmussen, Aa. Fredenslund, "A Modified UNIFAC group-contribution Model for Prediction of Phase Equilibria and Heat of Mixing" Ind. Eng. Chem. Res, 26 (11) 2274-2286, (1987).
8. Postigo, M. A., P.H. García, J. Ortega, G. Tardajos, "Excess molar volume of binary mixtures containing a methyl ester (Ethanoate to tetradecanoate) with odd n-alkanes at 298.15 K", Chem. Eng. Data, 40(1), 283-289, (1995).
9. Prausnitz, J. M., T.F. Anderson, E.A Greus, C. Eckert, R. Hsieh, J. O'Connell, Computer Calculations for Multicomponent Vapor-Liquid and Liquid-Liquid Equilibria, Prentice-Hall, Englevvood Cliffs, NJ, (1980).
10. Renon, H., J.M. Prausnitz, "Local Compositions in Thermodynamic Excess Functions for Liquid Mixtures", AIChE J, 14, 135, (1968)
11. Riddick, J. A., W.B. Hunger, T.K. Sakano, Organic Solvents, 4th de.; Wiley-Interscience: New York, (1986).
12. Spencer, C. F., R.P.J. Danner, "Improved Equation for Predicting Saturated Liquid Density", J. Chem. Eng. Data 17, 236-241, (1972).
13. Srivastava, R., B.D. Smith, "Total pressure Vapor-Liquid Equilibrium Data for Binary Systems of Dichloromethane with Benzene", J. Chem. Eng. Data 30, 313-318, (1985).
14. Tochigi, K., D. Tiegs, J. Gmehling, K. Kojima, "Determination of new ASOG parameters", J. Chem. Eng. Jpn. 23, 453-463.(1990).
15. TRC-Thermodynamics Tables. Thermodynamics Research Center, The Texas A&M University System: College Station, TX, (1993).
16. Tsonopoulos, C, "An Empirical Correlation of Second Virial Coefficients", AIChE J. 20, 263-272(1974).
17. E, and γ", nd. Eng. Chem. Res. 26, 1372-1381, (1987).
18. Wilson, G. M, "Vapor-Liquid Equilibrium. IX: A New Expression for the Excess Free Energy of Mixing", J. Am. Chem. Soc. 86, 127-130(1964).
19. Wisniak, J. A "New Test for the Thermodynamic Consistency of Vapor-Liquid Equilibrium", Ind. Eng. Chem. Res. 32, 1531-1533, (1993).