Thermophysical behavior of n-alkane + alkylbenzoate mixed solvents. Measurements and properties modeling

Industrial and Engineering Chemistry Research

Volumn 44, Issue 19, 2005, Pages 7575-7583

  Aparicio, Santiago ^a   Alcalde, Rafael ^a   Garcia, Begoña ^a   Leal, José M ^a  

^a UNIVERSITY OF BURGOS   (Spain)

Author keywords

[No Author keywords available]

Indexed keywords

ESTERS; SOLVENTS; THERMODYNAMIC PROPERTIES; VISCOSITY MEASUREMENT;

ALKYLBENZOATE MIXED SOLVENTS; INTERMOLECULAR FORCES; VISCOMETRIC PROPERTIES;

PARAFFINS;

CHEMICAL ENGINEERING; SOLVENT; THERMODYNAMICS;

EID: 25844446794     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie0502281     Document Type: Article

References (48)

1. Cox, K. R. Physical property needs in industry. Fluid Phase Equilib. 1993, 82, 15.
2. Dohrn, R.; Pfohl, O. Thermophysical properties-Industrial directions. Fluid Phase Equilib. 2002, 194-197, 15.
3. Grolier, J. P. E.; Ballet, D.; Viallard, A. M. Thermodynamics of ester-containing mixtures. Excess enthalpies and excess volumes for alkyl acetates and alkylbenzoates + alkanes, + benzene, + toluene, and + ethylbenzene. J. Chem. Thermodyn. 1974, 6, 895.
4. Dusart, O.; Piekarski, C.; Viallard, A. Excess volumes of binary mixtures n-heptane + esters and n-heptane + ketones in homologous series. J. Chim. Phys. 1976, 73, 837.
5. Blanco, A. M.; Ortega, J.; García, B.; Leal, J. M. Studies on densities and viscosities of binary mixtures of alkylbenzoates in n-heptane. Thermochim. Acta 1993, 222, 127.
6. García, B.; Miranda, M. J.; Leal J. M.; Ortega, J.; Matos J. S. Densities and viscosities of mixing for the binary system of methyl benzoate with n-nonane at different temperatures. Thermochim. Acta 1991, 186, 285.
7. García, B.; Alcalde, R.; Aparicio, S.; Leal, J. M. Thermo-physical behavior of methylbenzoate + n-alkanes mixed solvents. Application of cubic equations of state and viscosity models. Ind. Eng. Chem. Res. 2002, 41, 4399.
8. García, B.; Alcalde, R.; Aparicio, S.; Leal, J. M. Volumetric properties, viscosities and refractive indices of binary mixed solvents containing methylbenzoate. Phys. Chem. Chem. Phys. 2002, 4, 5833.
9. Garcia, B.; Alcalde, R.; Aparicio, S.; Leal, J. M. Preferential solvation in ternary solutions containing methylbenzoate. A Kirkwood-Buff fluctuation theory study. J. Phys. Chem. B 2003, 107, 13478.
10. 11) alkan-1-ol + mixed solvents. J. Phys. Chem. B 2004, 108, 15841.
11. Soave, G. Equilibrium constants from a modified Redlich Kwong equation of state. Chem. Eng. Sci. 1972, 27, 1197.
12. Peng, Y.; Robinson, D. B. A new two-constant equation of state. Ind. Eng. Chem. Fundam. 1976, 15, 59.
13. Anderko, A. In Equations of State for Fluids and Fluid Mixtures; Sengers, J. V., Kayser, R. F., Peters, C. J., White, H. J., Eds.; Elsevier: Amsterdam, 2000; Chapter 4.
14. Valderrama, J. O. The state of cubic equations of state. Ind. Eng. Chem. Res. 2003, 42, 1603.
15. Twu, C. H.; Sim, W. D.; Tassone, V. Getting a handle on advanced cubic equations of state. Chem. Eng. Prog. 1998, 11, 58.
16. Wong, D. S. H.; Sandler, S. I. A theoretically correct mixing rule for cubic equations of state. AIChE J. 1992, 38, 671.
17. Van, H. T.; Patterson, D. Volume of mixing and the p* effect: Hexane isomers with normal and branched hexadecane. J. Solution Chem. 1982, 11, 793.
18. Piñeiro, A.; Amigo, A.; Bravo, R.; Brocos, P. Re-examination and symmetrization of the ERAS model. Review of its formulation and application. Fluid Phase Equilib. 2000, 173, 211.
19. Linek, J.; Kovacs, E. Excess molar volumes in system alkane + 1-chloroalkane. Chem. Pap. 1999, 53, 424.
20. Gascon, I.; Martin, S.; Giner, B.; Haro, M.; Lafuente, C. Experimental values and ERAS model calculations for excess molar volumes and enthalpies of the ternary system 2-butanol + 1,3-dioxolane + cyclohexane. Can. J. Chem. 2003, 81, 357.
21. Riddick, J. A.; Bunger, W. B.; Sakano, T. K. Organic Solvents; Wiley: New York, 1986.
22. Aminabhavi, T. M.; Raikar, S. K. Thermodynamic interactions in binary mixtures of 2-methoxyethanol with alkyl and aryl esters at 298.15 K, 303.15 K and 308.15 K. Collect. Czech. Chem. Commun. 1993, 58, 1761.
23. Semeniuk, B.; Wilczura-Wachnick, H. Vapor-liquid equilibria in the binary and ternary mixtures of methylbenzoate, methyl p-toluate and dimethyl terephthalate. Fluid Phase Equilib. 1998, 152, 337.
24. Aminabhavi, T. M.; Phayde, H. T. S.; Khinnavar, S.; Bindu, G.; Hansen, K. C. Densities, refractive indices, speeds of sound, and shear viscosities of diethylene glycol dimethyl ether with ethyl acetate, methyl benzoate, ethyl benzoate, and diethyl succinate in the temperature range from 298.15 to 318.15 K. J. Chem. Eng. Data 1994, 39, 251.
25. Lee, S. H.; Lee. H.; Pak, H.; Rasaiah, J. C. Molecular dynamics simulations of liquid alkanes. I. Thermodynamics and structures of normal alkanes: n-Butane to n-heptadecane. Bull. Korean Chem. Soc. 1996, 17, 735.
26. Fort, R.; Moore, W. R. Viscosities of binary liquid mixtures. Trans. Faraday Soc. 1966, 62, 112.
27. Sandler, S. I.; Orbey, H. In Equations of State for Fluids and Fluid Mixtures; Sengers, J. V., Kayser, R. F., Peters, C. J., White, H. J., Eds.; Elsevier: Amsterdam, 2000; Chapter 9.
28. Solorzano, M.; Barragán, F.; Bazúa, E. R. Comparative study of mixing rules for cubic equations of state in the prediction of multicomponent vapour-liquid equilibria. Fluid Phase Equilib. 1996, 122, 99.
29. Panagiotopoulos, A. Z.; Reid, R. C. New mixing rules for cubic equations of state for accurate vapor-liquid equilibria calculations. ACS Symp. Ser. 1986, 300, 571.
30. Adachi, Y.; Sugie, H. A new mixing rule-Modified mixing rule. Fluid Phase Equilib. 1986, 28, 103.
31. Sandoval, R.; Wilczek-Vera, G.; Vera, J. H. Prediction of ternary vapor-liquid equilibria with PRSV equation of state. Fluid Phase Equilib. 1989, 52, 119.
32. Schwartzentruber, J.; Renon, H. Development of a new equation of state for phase equilibria calculations. Fluid Phase Equilib. 1989, 52, 127.
33. Strykek, R.; Vera, J. H. PRSW: An improved Peng-Robinson equation of state for pure compounds and mixtures. Can. J. Chem. Eng. 1986, 64, 323.
34. Michelsen, M. L.; Kistenmacher, H. On composition dependent interaction coefficients. Fluid Phase Equilib. 1990, 58, 229.
35. Mathias, P.; Klotz, H. C.; Prausnitz, J. M. Equation of state mixing rules for multicomponent mixtures: The problem of invariance. Fluid Phase Equilib. 1991, 67, 31.
36. Wilson, G. M. Vapor-liquid equilibrium. XI. A new expresion for the excess free energy of mixing. J. Am. Chem. Soc. 1964, 86, 127.
37. Renon, H.; Praunitz, J. M. Local compositiqn in thermodynamic excess functions for liquid mixtures. AIChE J. 1965, 14, 135.
38. Abrams, D. S.; Praunitz, J. M. Statistical thermodynamics of liquid mixtures: A new expresion for the excess Gibbs energy of partly or completely miscible systems. AIChE J. 1976, 21, 116.
39. Reid, R. C.; Prausnitz, J. M. The Properties of Gases and Liquids; McGraw-Hill: Singapore, 1987.
40. Torres, R. B.; Francesconi, A. Z. Modeling of excess molar volume of binary mixtures of acetonitrile with amines using the Prigogine-Flory-Patterson theory. J. Mol. Liq. 2003, 103, 99.
41. Lee, B. I.; Kesler, M. G. A Generalized thermodynamic correlation based on three-parameter corresponding states. AIChE J. 1975, 21, 510.
42. Cerdeiriña, C. A.; Tovar, C. A.; Gonzalez, D.; Carballo, E.; Romaní, L. Isobaric thermal expansivity and thermophysical characterization of liquids and liquid mixtures. Phys. Chem. Chem. Phys. 2001, 3, 5230.
43. Peleteiro, J.; González, D.; Cerdeiriña, C. A.; Romaní, L. Isobaric heat capacities, densities, isentropic compressibilities and second-order excess derivatives for 1-propanol + n-decane. J. Chem. Thermodyn. 2002, 34, 485.
44. Tovar, C. A.; Cerdeiriña, C. A.; Gonzalez, D.; Carballo, E.; Romaní, L. Second-order excess derivatives for liquid mixtures of non-electrolytes. Fluid Phase Equilib. 2000, 169, 209.
45. Lee, L. L.; Lee, Y. The application of the equations of state incorporated with mixing rules for viscosity estimations of binary mixtures. Fluid Phase Equilib. 2001, 181, 47.
46. Rangaiah, G. P. Evaluation of genetic algorithms and simulated annealing for phase equilibrium and stability problems. Fluid Phase Equilib. 2001, 83, 187.
47. Heintz, A. A new theoretical approach for predicting excess properties of alkanol/alkane mixtures. Ber. Bunsen-Ges. Phys. Chem. 1985, 89, 172.
48. Prausnitz, J. M.; Lichtenthaler, R. N.; Azevedo, E. G. Molecular Thermodynamics of Fluid Phase Equilibria; Prentice-Hall: New York, 1999.