Vapor-liquid equilibrium for the systems 2-methylpropane + methanol, + 2-propanol, + 2-butanol, and + 2-methyl-2-propanol at 364.5 K

Journal of Chemical and Engineering Data

Volumn 53, Issue 4, 2008, Pages 913-918

  Laavi, Helena ^a   Uusi Kyyny, Petri ^a   Pokki, Juha Pekka ^a   Pakkanen, Minna ^a   Alopaeus, Ville ^a  

^a AALTO UNIVERSITY   (Finland)

Author keywords

[No Author keywords available]

Indexed keywords

BINARY MIXTURES; MATHEMATICAL MODELS; PARAMETER ESTIMATION; POLYNOMIALS;

ACTIVITY COEFFICIENT MODEL; LEGENDRE POLYNOMIALS; WILSON BINARY INTERACTION;

PHASE EQUILIBRIA;

EID: 43449117801     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je800021r     Document Type: Article

References (26)

1. Ouni, T.; Zaytseva, A.; Uusi-Kyyny, P.; Pokki, J.-P.; Aittamaa, J. Vapour-liquid equilibrium for the 2-methylpropane + methanol, +ethanol, + 2-propanol, + 2-butanol and + 2-methyl-2-propanol systems at 313.15 K. Fluid Phase Equilib. 2005, 232, 90-99.
2. Leu, A.-D.; Robinson, D. B. Equilibrium phase properties of the methanol-isobutane binary system. J. Chem. Eng. Data 1992, 37, 10-13.
3. Zabaloy, M. S.; Mabe, G. D. B.; Bottini, S. B.; Brignole, E. A. Vapor liquid equilibria in ternary mixtures of water-alcohol-non polar gases. Fluid Phase Equilib. 1993, 83, 159-166.
4. Miyano, Y.; Nakanishi, K.; Fukuchi, K. Henry's constants of butane, isobutane, 1-butene and isobutene in methanol at 255-320 K. Fluid Phase Equilib. 2003, 208, 223-238.
5. Miyano, Y.; Fujihara, I.; Sato, K. Henry's law constants of propane, propene, butane, and 2-methylpropane in methanol at 374-490 K. Fluid Phase Equilib. 2006, 240, 56-62.
6. Miyano, Y. Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2butene, and 1,3-butadiene in 2-propanol at 250-330 K. J. Chem. Eng. Data 2004, 49, 368-371.
7. Miyano, Y. Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-butanol and 2-butanol from (250-330) K. J. Chem. Eng. Data 2004, 49, 1285-1289.
8. Miyano, Y. Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in isobutanol and tert-butanol. J. Chem. Thermodyn. 2004, 36, 865-869.
9. Moore, J. D.; Brown, P R.; Ott, J. B. Excess molar enthalpies and excess molar volumes for the binary mixtures of 2-methylpropane, 2-methylpropene, and propan-2-ol at the temperatures (298.15 and 323.15) K and the pressures (5, 10, and 15) MPa. J. Chem. Thermodyn. 1997, 29, 179-195.
10. Van Ness, H. C.; Abbott, M. M. A procedure for rapid degassing of liquids. Ind. Eng. Chem. Fundam. 1978, 17:1, 66-67.
11. ∞ data for the different binary butanol-water systems at 50°C. J. Chem. Eng. Data 1994, 39, 309-315.
12. Yaws, C. L. Chemical properties handbook: physical, thermodynamic, environmental, transport, safety, and health related properties for organic and inorganic chemicals; McGraw-Hill: New York, 1999.
13. Perry, R. H.; Green, D. W. Perry's chemical engineers' handbook, 7th ed.; McGraw-Hill: New York, 1997.
14. Daubert, T. E.; Danner, R. P. Physical and thermodynamic properties of pure chemicals: Data compilation; Hemisphere: New York, 1989.
15. Reid, R. C.; Prausnitz, J. M.; Poling, B. E. The properties of gases & liquids, 4th ed.; McGraw-Hill: New York, 1987.
16. Uusi-Kyyny, P.; Pokki, J.-P.; Laakkonen, M.; Aittamaa, J.; Liukkonen, S. Vapor liquid equilibrium for the binary systems 2-methylpentane + 2-butanol at 329.2 K and n-hexane + 2-butanol at 329.2 and 363.2 K with a static apparatus. Fluid Phase Equilib. 2002, 201, 343-358.
17. Hynynen, K.; Uusi-Kyyny, P.; Pokki, J.-P.; Pakkanen, M.; Aittamaa, J. Isothermal vapor liquid equilibrium for 2-methylpropene + methanol, + 1-propanol, + 2-propanol, + 2-butanol, and + 2-methyl-2propanol binary systems at 364.5 K. J. Chem. Eng. Data 2006, 51, 562-568.
18. Barker, J. A. Determination of activity coefficients from total pressure measurements. Aust. J. Chem. 1953, 6, 207-210.
19. Aittamaa, J.; Pokki, J.-P. VLEFFT A Program package to obtain parameters in models of activity coefficient from VLE data (Manual); Helsinki University of Technology, Laboratory of chemical engineering: Espoo, 2004.
20. Gmehling, J.; Onken, U. Vapor-liquid equilibrium data collection. Aqueousorganic systems, DECHEMA Chemistry Data Series; DECHEMA: Frankfurt/Main, 1977; Vol. 1, Part 1.
21. Soave, G. Equilibrium constants from a modified Redlich-Kwong equation of state. Chem. Eng. Sci. 1972, 27, 1192-1203.
22. Rackett, H. G. Equation of state for saturated liquids. J. Chem. Eng. Data 1970, 15 (4), 514-517.
23. Pokki, J.-P. Development of Vapour Liquid Equilibrium Calculation Methods for Chemical Engineering Design, Dissertation, Chemical Engineering Report Series No. 46; Espoo, 2004.
24. Poling, B. E.; Prausnitz, J. M.; O'Connell, J. P. The properties of gases & liquids, 5th ed.; McGraw-Hill: NY, 2000.
25. Laakkonen, M.; Pokki, J.-P.; Uusi-Kyyny, P.; Aittamaa, J. Vapour liquid equilibrium for the 1-butene + methanol, + ethanol, + 2-propanol, + 2-butanol and + 2-methyl-2-propanol systems at 326 K. Fluid Phase Equilib. 2003, 206, 237-252.
26. 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.