Isobaric vapor-liquid equilibria for methyl esters + butan-2-ol at different pressures

Fluid Phase Equilibria

Volumn 118, Issue 2, 1996, Pages 249-270

  Ortega, Juan ^a   Hernandez, Pablo ^a  

^a NONE

Author keywords

Butan 2 ol; Esters; Experiments; VLE Data

Indexed keywords

ALCOHOLS; EQUATIONS OF STATE OF LIQUIDS; ESTERS; MEASUREMENTS; MIXTURES; OPTIMIZATION; REGRESSION ANALYSIS; THERMODYNAMIC PROPERTIES; VAPORS;

AZEOTROPE; ISOBARIC VAPOR LIQUID EQUILIBRIA; MAXIMUM LIKELIHOOD PRINCIPLE; METHYL ESTER BUTANOL; WORKING PRESSURE;

PHASE EQUILIBRIA;

EID: 0030121502     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/0378-3812(95)02821-8     Document Type: Article

References (28)

1. Ambrose, D., Ellender, J.H., Gundry, H.A., Lee, D.A. and Townsend, R., 1981. Thermodynamic properties of organic oxygen compounds. LI. The vapour pressures of some esters and fatty acids. J. Chem. Thermodyn., 13: 795-802.
2. Ambrose, D. and Sprake, C.H.S., 1970. Thermodynamic properties of organic oxygen compounds. XXV. Vapor pressures and normal boiling temperatures of aliphatic alcohols. J. Chem. Thermodyn., 2: 631-645.
3. Boublik, T., Fried, V. and Hála, H., 1973. The Vapour Pressures of Pure Substances. Elsevier, Amsterdam.
4. Fredenslund, Aa., Jones, R.L. and Prausnitz, J.M., 1975. Group contribution estimation of activity coefficients in nonideal liquid mixtures. AIChE J., 21: 1086-1099.
5. Fredenslund, Aa, Gmehling, J. and Rasmussen, P, 1977. Vapor-Liquid Equilibria Using UNIFAC. A Group Contribution Method. Elsevier, Amsterdam.
6. Gmehling, J., Li, J. and Schiller, M., 1993. A modified UNIFAC model. 2. Present parameter matrix and results for different thermodynamic properties. Ind. Chem. Eng. Res., 32: 178-193.
7. Gmehling, J., Rasmussen, P. and Fredenslund, Aa., 1982. Vapor-liquid equilibria by UNIFAC group contribution. Revision and extension. 2 Ind. Eng. Chem. Process Des. Dev., 21: 118-127.
8. Horsley, L.H., 1973. Azeotropic Data - III. Advances in Chemistry Series 116, A.C.S. Washington DC.
9. Kojima, K. and Tochigi, K., 1979. Prediction of Vapor-Liquid Equilibria by the ASOG Method. Kodansha Ltd., Tokyo.
10. Larsen, B.L., Rasmussen, P. and Fredenslund, Aa., 1987. A modified UNIFAC group contribution model for prediction of phase equilibria and heats of mixing. Ind. Eng. Chem. Res., 26: 2274-2286.
11. Macedo, E.A., Weidlich, U., Gmehling, J. and Rasmussen, P., 1983. Vapor-liquid equilibria by UNIFAC group contribution Revision and extension 3. Ind. Eng. Chem. Process Des. Dev., 22: 676-678.
12. Ortega, J., Peña, J.A. and de Alfonso, C., 1986. Isobaric vapor-liquid equilibria of ethyl acetate + ethanol mixtures at 760 ± 0.5 mmHg. J. Chem. Eng. Data, 31: 339-342.
13. Ortega, J., Ocón, J., Peña, J.A., de Alfonso, C., PazAndrade, M.I. and Fernández, J., 1987. Vapor-liquid equilibrium of the binary mixtures CnH2n+ 1(OH) (n = 2, 3, 4) + propyl ethanoate and ethyl ethanoate. Can. J. Chem. Eng., 65: 982-990.
14. Ortega, J. and Susial, P., 1990a. Measurements and prediction of VLE of methyl propanoate/ethanol/propan-1-ol at 114.66 and 127.66 kPa. J. Chem. Eng. Jpn., 23: 349-353.
15. Ortega, J. and Susial, P., 1990b. VLE at 114.66 and 127.99 kPa for the systems methyl acetate + ethanol and methyl acetate + propan-1-ol. Measurements and prediction. J. Chem. Eng. Jpn., 23: 621-626.
16. Ortega, J. and Susial, P., 1993. Vapor-liquid equilibria behavior of methyl esters and propa-2-ol at 74.66, 101.32, and 127.99 kPa. J. Chem. Eng. Jpn., 26: 259-265.
17. Ortega, J., Susial, P. and de Alfonso, C., 1990a. Vapor-liquid equilibrium measurements at 101.32 kPa for binary mixtures of methyl acetate + ethanol or propan-1-ol. J. Chem. Eng. Data, 35: 350-352.
18. Ortega, J., Susial, P. and de Alfonso, C., 1990b. Isobaric vapor-liquid equilibrium of methyl butanoate with ethanol and 1-propanol binary systems. J. Chem. Eng. Data, 35: 216-219.
19. Ortega, J. and Susial, P., 1991. Vapor-liquid equilibria of mixtures of methyl butanoate + propan-2-ol at 74.66, 101.32, and 127.99 kPa. Ber. Bunsenges Phys. Chem., 95: 1214-1219.
20. Prausnitz, J.M., Anderson, T.F., Greens, E.A., Eckert, C.A., Hsieh, R. and O'Connell, J.P., 1980. Computer calculations for multicomponent V-L and L-L equilibria. Prentice-Hall, Inc., Englewood Cliffs, NJ.
21. Reid, R.C., Prausnitz, J.M. and Sherwood, T.K., 1977. The Properties of Gases and Liquids, 3rd edn., MacGraw-Hill, New York.
22. Riddick, J.A., Bunger, W.B. and Sakano, T.K., 1986. Organic Solvents. Techniques of Chemistry, Vol. II, 4th edn., Wiley-Interscience, New York.
23. Spencer, C.F. and Danner, R.P.J., 1972. Improved equation for predicting of saturated liquid density. J. Chem. Eng. Data, 17: 236-241.
24. Susial, P., Ortega, J., de Alfonso, C. and Alonso, C., 1989. Vapor-liquid equilibrium measurements for methyl propanoate-ethanol and methyl propanoate-propan-1-ol at 101.32 kPa. J. Chem. Eng. Data, 34: 247-250.
25. Susial, P. and Ortega, J., 1995. Vapor-liquid equilibria of methyl ethanoate with n-butyl and iso-butyl alcohol at 74.66 and 127.99 kPa. J. Chem. Eng. Jpn., 28: 66-70.
26. TRC, 1991. Thermodynamic Tables of Non-hydrocarbons, Texas A and M University, College Station, TX.
27. Tsonopoulos, C., 1974. An empirical correlation of second virial coefficients. AIChE J., 20: 263-272.
28. E. Ind. Eng. Chem. Res., 26: 1372-1381.