Experimental (solid + liquid) and (liquid + liquid) equilibria and excess molar volume of alkanol + acetonitrile, propanenitrile, and butanenitrile mixtures

Journal of Chemical and Engineering Data

Volumn 50, Issue 6, 2005, Pages 2035-2044

  Domańska, Urszula ^a   Marciniak, Małgorzata ^a  

^a WARSAW UNIVERSITY OF TECHNOLOGY   (Poland)

Author keywords

[No Author keywords available]

Indexed keywords

AROMATIC COMPOUNDS; ATMOSPHERIC PRESSURE; CONCENTRATION (PROCESS); ENTHALPY; PHASE DIAGRAMS; PHASE EQUILIBRIA; SOLUBILITY;

CRITICAL POINTS; MOLAR ENTHALPY; MOLAR VOLUMES;

BINARY MIXTURES;

EID: 28544433136     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je050262m     Document Type: Article

References (61)

1. Domańska, U.; Głoskowska, M. Experimental solid + liquid equilibria and excess molar volumes of alkanol + hexylamine mixtures. Analysis in terms of the ERAS, DISQUAC and modified UNIFAC models. Fluid Phase Equilib. 2004, 276, 135-145.
2. Domańska, U.; Głoskowska, M. Experimental solid + liquid equilibria and excess molar volumes of alkanol + octylamine mixtures. Analysis in terms of the ERAS, DISQUAC, and modified UNIFAC models. J. Chem. Eng. Data 2004, 49, 101-108.
3. Domańska, U.; Marciniak, M. Volumetric and solid + liquid equilibria data for linear 1-alkanol + decylamine mixtures. Analysis in terms of ERAS, DISQUAC, and modified UNIFAC. Ind. Eng. Chem. Res. 2004, 43, 7647-7656.
4. Domańska, U.; Marciniak, M. Experimental solid-liquid equilibria for systems containing (alkan-1-ol + 1,3-diaminopropane). Heat capacities of alkan-1-ols and amines. Thermodynamic functions of dissociation and enthalpies of melting of the congruently melting compounds for the systems (alkan-1-ol + amine). Fluid Phase Equilib. 2005, 235, 30-41.
5. Torres, R. B.; Francesconi, A. Z.; Volpe, P. L. O. Thermodynamics of binary liquid mixtures: application of the Prigogine-Flory-Patterson theory to excess molar volumes of acetonitrile + 1-alkanol systems. J. Mol. Liq. 2004, 110, 81-85.
6. Torres, R. B.; Pina, C. G.; Francesconi, A. Z. Application of the Prigogine-Flory-Patterson theory to excess molar volume of binary mixtures of acetonitrile with 1-alkanols. J. Mol. Liq. 2003, 107, 127-139.
7. Grguric, I. R.; Tasic, A. Z.; Djordjevic, B. D.; Kijevcanin, M. L.; Serbanovic, S. P. Excess molar volume of the acetonitrile plus alcohol systems at 298.15 K. Part I: Density measurements for acetonitrile plus methanol, plus ethanol systems. J. Serb. Chem. Soc. 2002, 67, 581-586.
8. Grguric, I. R.; Kijevcanin, M. L.; Djordjevic, B. D.; Tasic, A. Z.; Serbanovic, S. P. Excess molar volume of acetonitrile plus alcohol systems at 298.15 K. Part II: Correlation by cubic equation of state. J. Serb. Chem. Soc. 2003, 68, 47-56.
9. Torres, R. B.; Francesconi, A. Z.; Volpe, P. L. O. Experimental study and modeling using the ERAS-model of the excess molar volume of acetonitrile-alkanol mixtures at different temperatures and atmospheric pressure. Fluid Phase Equilib. 2003, 210, 287-306.
10. Martins, A.; Laurent, R.; Aznarez, S. B. Interactional parameters fitting in thermodynamics models. Ecletica Quim. 2000, 25, 41-50.
11. Saha, N.; Das, B.; Hazra, D. K. Viscosities and excess molar volumes for acetonitrile + methanol at 298.15, 308.15, and 318.15 K. J. Chem. Eng. Data 1995, 40, 1264-1266.
12. 5) binary mixtures with acetonitrile. J. Chem. Eng. Data 1986, 31, 152-154.
13. Pina, C. G.; Francesconi, A. Z. New applications of the ERAS-model: excess volumes of binary liquid mixtures of 1-alkanols with acetonitrile. Fluid Phase Equilib. 1998, 143, 143-152.
14. Cibulka, I.; Nguyen, D.; Holub, R. Excess molar volumes of (an alkanol + acetonitrile) at 298.15 and 308.15 K. J. Chem. Thermodyn. 1984, 16, 159-164.
15. Nikam, P. S.; Shirsat, L. N.; Hasan, M. M. Density and viscosity studies of binary mixtures of acetonitrile with methanol, ethanol, propan-1-ol, propan-2-ol, butan-1-ol, 2-methylpropan-1-ol, and 2-methylpropan-2-ol at (298.15, 303, 15, 308.15, and 313.15) K. J. Chem. Eng. Data 1998, 43, 732-737.
16. Nagata, I.; Tamura, K. Thermodynamics of solutions containing acetonitrile and 1-butanol. Thermochem. Acta 1988, 124, 53-64.
17. Nagata, I.; Tamura, K. Excess molar enthalpies of (propan-1-ol or propan-2-ol + acetonitrile), (propan-1-ol or propan-2-ol + chlorobenzene), and (propan-1-ol or propan-2-ol + acetonitrile + chlorobenzene) at 298.15 K. J. Chem. Thermodyn. 1988, 20, 87-93.
18. Garriga, R.; Putze, I.; Perez, P.; Gracia, M. Vapour pressures at several temperatures T and excess functions at T = 298.15 K of (butanenitrile + ethanol or butan-1-ol). J. Chem. Thermodyn. 1995, 27, 481-491.
19. Garriga, R.; Sanchez, F.; Perez, P.; Gracia, M. Vapour pressures at several temperatures T and excess functions at T = 298.15 K of (butanenitrile + propan-1-ol or propan-2-ol). J. Chem. Thermodyn. 1995, 27, 887-895.
20. Garriga, R.; Perez, P.; Gracia, M. Vapour pressures at several temperatures T and excess functions at T = 298.15 K of (butanenitrile + hexan-1-ol or octan-1-ol). J. Chem. Thermodyn. 1995, 27, 1057-1066.
21. Martinez, S.; Garriga, R.; Perez, P.; Gracia, M. Densities and viscosities of binary mixtures of butanenitrile with butanol isomers at several temperatures. J. Chem. Eng. Data 2000, 45, 1182-1188.
22. Garriga, R.; Sanchez, F.; Perez, P.; Gracia, M. Excess Gibbs free energies at eight temperatures and excess enthalpies and volumes at T = 298.15 K for butanenitrile + 2-butanol. J. Chem. Eng. Data 1997, 42, 78-83.
23. Garriga, R.; Sanchez, F.; Perez, P.; Gracia, M. Excess Gibbs free energies at several temperatures and excess enthalpies and volumes at 298.15 K of butanenitrile with 2-methyl-1-propanol or 2-methyl-2-propanol. Fluid Phase Equilib. 1997, 130, 195-206.
24. Garriga, R.; Ilarraza, J.; Perez, P.; Gracia, M. Excess functions at T = 298.15 K of (butanenitrile + methanol, + pentan-1-ol, + heptan-1-ol, + nonan-1-ol, or + decan-1-ol). J. Chem. Thermodyn. 1996, 28, 233-243.
25. Letcher, T. M.; Naicker, P. K. Excess molar enthalpies and excess molar volumes of (an alkanol + nitrile compound) at T = 298.15 K and p = 0.1 MPa. J. Chem. Thermodyn. 2001, 33, 1035-1047.
26. Funke, H,; Wetzel M.; Heintz, A. New applications of the ERAS model. Thermodynamics of amine + alkane and alcohol + amine mixtures. Pure Appl. Chem. 1989, 67, 1429-1439.
27. Gonzalez, J. A.; Gracia de la Fuenta, I.; Cobos, J. C. Thermodynamics of mixtures with strongly negative deviations from Raoult's law. Part 3. Application of the DISQUAC model to mixtures of Methylamine with alkanols. Comparison with Dortmund UNIFAC and ERAS results. Can. J. Chem. 2000, 78, 1272-1284.
28. Heintz, A. A new theoretical approach for predicting excess properties of alkanol/alkane mixtures. Ber. Bunsen-Ges. Phys. Chem. 1985, 89, 172-181.
29. Kretschmer, C. B.; Wiebe, R. Thermodynamics of alcohol-hydrocarbon mixtures. J. Chem. Phys. 1954, 22, 1697-1701.
30. Kehiaian, H. V.; Treszczanowicz, A. J. Thermodynamics of chemically reacting mixtures. Excess free enthalpy of athermal associated mixtures of the Mecke-Kempter type. Bull. Acad. Pol. Sci., Ser. Sci. Chim. 1968, 16, 445-449.
31. Flory, P. J. Statistical thermodynamics of liquid mixtures. J. Am. Chem. Soc 1965, 87, 1833-1835.
32. Treszczanowicz, A.; Benson, G. C. Excess volumes of alkanol + alkane binary systems in terms of an association model with a Flory contribution term. Fluid. Phase Equilib. 1985, 23, 117-135.
33. Treszczanowicz, A.; Benson, G. C. Excess volumes of cycloalkanol + cycloalkane binary systems in terms of an associated solution theory with a Flory equation of state contribution. Thermochim. Acta 1991, 179, 39-47.
34. 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.
35. Liu, A.; Pusicha, K.; Demiriz, A. M.; Kohler, F. A model for alkanol + alkane mixtures: extension and experimental verification. J. Solution Chem. 1991, 20, 39-56.
36. Handbook of Chemistry and Physics, 84th ed.; CRC: Boca Raton, FL, 2003-2004.
37. Paljk, Š.; Klofutar, C.; Domanska, U. Heats of solution of 1-nonanol, 1-decanol and 1-undecanol in cyclohexane at 298.15 K and 308.15 K. Thermochim. Acta 1990, 164, 211-225.
38. 18. J. Am. Chem. Soc. 1933, 55, 1574-1584.
39. Heintz, A.; Naicker, P. K.; Verevkin, S. P.; Pfestorf, R. Thermodynamics of alkanol + amine mixtures. Experimental results and ERAS model calculations of the heat of mixing. Ber. Bunsen-Ges. Phys. Chem. 1998, 102, 953-959.
40. McKenna, F. E.; Tartar, H. V.; Lingafelter, E. C. Studies of hemiacetal formation in alcohol-aldehyde systems. II. Refraction studies. J. Am. Chem. Soc. 1953, 75 (3), 604-607.
41. Domanska, U. Thermodynamics of mixtures containing a very strongly polar compound. Part II. Solid-liquid equilibria for sulfolane + nitrile systems and characterization of the sulfolane-nitrile and sulfolane-1-alkyne in terms of DISQUAC. Can. J. Chem. 2002, 80, 476-482.
42. Riddick, J. A.; Bunger, W. B.; Sakano, T. K. Organic Solvents: Physical Properties and Methods of Purification, 4th ed.; Techniques of Chemistry Vol. II; Wiley: New York, 1986.
43. Domanska, U. Vapour-liquid-solid equilibrium of eicosanoic acid in one- and two-component solvents. Fluid Phase Equilib. 1986, 26, 201-220.
44. Sazonov, V. P.; Shaw, D. G. IUPAC-NIST solubility data series. 78. Acetonitrile binary systems. J. Phys. Chem. Ref. Data 2002, 31 (4), 989-1131.
45. Renon, H.; Prausnitz, J. M. Local compositions in thermodynamic excess functions for liquid mixtures. AIChE J. 1968, 14, 135-144.
46. Walas, S. M. Phase Equilibria in Chemical Engineering; Buttersworth: New York, 1985.
47. Nagata, I.; Nakamiya, Y.; Katoh, K.; Koyabu, J. Ternary liquid-liquid equilibria and their representation by modified NRTL equations. Thermochim. Acta 1981, 45, 153-165.
48. Wilson, G. M. Vapor-liquid equilibrium. XI. A new expression for the excess free energy of mixing. J. Am. Chem. Soc. 1964, 86, 127-130.
49. Nagata, I. On the thermodynamics of alcohol solutions. Phase equilibria of binary and ternary mixtures containing any number of alcohols. Fluid Phase Equilib. 1985, 19, 153-174.
50. E and applications of a multiple cross-association theory based on the ERAS model. Fluid Phase Equilib. 1997, 133, 247-264.
51. Abe, A.; Flory, P. J. The thermodynamic properties of mixtures of small, nonpolar molecules. J. Am. Chem. Soc. 1965, 87, 1838-1842.
52. Heintz, A.; Papaioannou, D. Excess enthalpies of alcohol + amine mixtures. Experimental results and theoretical description using ERAS-model. Thermochim. Act 1998, 310, 69-76.
53. Treszczanowicz, A. J.; Benson, G. C. Prediction of excess volumes of 1-alkanol + branched aliphatic hydrocarbon binary systems in terms of an association model with a Flory contribution term. Fluid Phase Equilib. 1988, 41, 31-42.
54. Nagata, I. Thermodynamics of alcohol solutions. Phase equilibria and excess molar enthalpies of mixtures containing two alcohols. Thermochim. Acta 1986, 107, 199-217.
55. Nagata, I.; Inaguma, K. The UNIQUAC associated-solution model, excess enthalpies of mixtures of hydrocarbons with alcohol. Thermochim. Acta 1986, 97, 51-60.
56. Davolio, F.; Schaefer, C. R.; Ruiz Holgado, M. F.; Katz, M. Excess molar volumes and viscosities of the ternary system n-butylamine + 1,4-dioxane + acetonitrile at 25°C. J. Solution Chem. 1990, 19, 1085-1094.
57. TRC thermodynamics tables. Texas Engineering Experimental Station, Thermodynamics Research Centre, Texas A&M University System: 1988.
58. Fredenslund, A.; Jones, R. L.; Prausnitz, J. M. Group contribution estimation of activity coefficients in nonideal liquid mixtures. AIChE J. 1975, 21, 1086-1099.
59. Gonzalez, J. A.; Gracia de la Fuenta, I.; Cobos, J. C. Thermodynamics of mixtures with strongly negative deviations from Raoult's law. Part 4. Application of the DISQUAC model to mixtures of 1-alkanols with primary or secondary linear amines. Comparison with Dortmund UNIFAC and ERAS results. Fluid Phase Equilib. 2000, 168, 31-58.
60. Martins, A.; Laurent, R.; Aznarez, S. B. Interactional parameters fitting in thermodynamic models. Ecletica Quim. 2000, 25, 41-50; ISSN 0100-4670.
61. Kehiaian, H. V. Group contribution methods for liquid mixtures: a critical review. Fluid Phase Equilib. 1983, 13, 243-252.