Vapor-liquid equilibria at 101.32 KPA mixtures of butyl Esters and propan-2-ol

Journal of Chemical Engineering of Japan

Volumn 29, Issue 2, 1996, Pages 294-299

  Gonzalez, Eduardo ^a   Ortega, ^a  

^a UNIVERSITY OF LAS PALMAS DE GRAN CANARIA   (Spain)

Author keywords

Butyl esters; Experimental; Propan 2 ol; VLE

Indexed keywords

EID: 0345632719     PISSN: 00219592     EISSN: None     Source Type: Journal    
DOI: 10.1252/jcej.29.294     Document Type: Article

References (17)

1. Fredenslund, Aa., J. Gmehling and P. Rasmussen; Vapor-Liquid Equilibria Using UNIFAC. A Group-Contribution Method, Elsevier, Amsterdam (1977)
2. Fredenslund, Aa., R. L. Jones and J. M. Prausnitz: "Group Contribution Estimation of Activity Coefficients in Nonideal Liquid Mixtures," AIChE J., 21, 1086-1099 (1975)
3. Gmehling, J., J. Li and M. Schiller; "A Modified UNIFAC Model. 2. Present Parameter Matrix and Results for Different Thermodynamic Properties," Ind. Eng. Chem. Res., 32, 178-193 (1993)
4. Gmehling, J., J. Menke, J. Krafczyk and K. Fischer; Azeotropic Data, part I, p. 615, VCH, Weinheim, New York, Basel, Cambridge, Tokyo (1994)
5. Gmehling, J., U. Onken and U. Weidlich; Vapor-Liquid Equilibrium Data Co;;ection, vol. I, part 2d, p. 75, Dechema, Frankfurt (1982)
6. González, E. and J. Ortega; "Densities and Isobaric Vapor-Liquid Equilibria of Butyl Esters (Methanoate to Butanoate) with Etanoi at 101.32 kPa," J. Chem. Eng. Data, in press (1995)
7. Hansen, H. K., P. Rasmussen, Aa. Fredenslund, M. Schiller and J. Gmehling; "Vapor-Liquid Equilibria by UNIFAC Group contribution. 5. Revision and Extension," Ind. Eng. Chem. Res., 30, 2355-2358 (1991)
8. Larsen, B. L., P. Rasmussen and Aa. Fredenslund; " A Modified UNIFAC Group-Contribition Model for Prediction of Phase Equilibria and Heats of Mixing," Ind. Eng. Chem. Res., 26, 2274-2286 (1987)
9. Macedo, E. A., U. Weidlich, J. Gmehling and P. Rasmussen; "Vapor-Liquid Equilibria by UNIFAC Group Contribution. Revision and Extension. 3.," Ind. Eng. Chem. Process Des. Dev., 22, 676-678 (1983)
10. Ortega, J., J. S. Matos, M. I. Paz-Andrade and E. Jiménez; "Excess Molar Volumes of (Ethyl Formate or Ethyl Acetate + an Isomer of Hexanol) at 298.15 K," J. Chem. Thermodynamics, 17, 1127-1132 (1985)
11. Ortega, J. and P. Susial; "Vapor-Liquid Equilibria of Mixtures of Methyl Butanoate+2-Propanol at 74.66, 101.32, and 127.99 kPa," Ber. Bunsenges. Phys. Chem., 10, 1214-1219 (1991a)
12. Ortega, J. and P. Susial; "Isobaric Vapor-Liquid Equilibria for Binary Systems Composed of Methyl Butanoate with Ethanol and with Propan-1-ol at 114.66 and 127.99 kPa," Can. J. Chem. Eng., 69, 394-397 (1991b)
13. Riddick, J. A., W. B. Nunger and T. K. Sakano; Organic Solvents. Techniques of Chemistry, 4th ed., vol. II, Wiley-Interscience, New York (1986)
14. Spencer, C. F. and R. P. J. Danner; "Improved Equation for Predicting of Saturated Liquid Density," J. Chem. Eng. Data, 17, 236-241 (1972)
15. Tochigi, K., D. Tiegs, J. Gmehling and K. Kojima; "Determination of New ASOG Parameters," J. Chem. Eng. Japan., 23, 453-462 (1990)
16. TRC; Thermodynamics Tables Non-Hydrocabons, Texas A & M University College Station, TX (1993)
17. Tsonopoulos, C.; "An Empirical Correlation of Second Virial Coefficients," AIChE J., 20, 263-272 (1974)