화학공학소재연구정보센터
Journal of Industrial and Engineering Chemistry, Vol.17, No.4, 667-674, July, 2011
Performance assessment of Tao-Mason equation of state: Results for vapor-liquid equilibrium properties
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The present work evaluates the performance of a molecular-based equation of state in predicting thermodynamic properties of several fluids in a very wide range of temperatures encompassing 100 K < T < 1100 K and pressures ranging from zero to 3200 bar. The theoretical equation of state (EOS) is that of Tao-Mason (TM) which is based on statistical mechanical perturbation theory. The 21 fluids including: argon (Ar), krypton (Kr), xenon (Xe), nitrogen (N2), oxygen (O2), carbon dioxide (CO2), methane (CH4), ethane (C2H6), propane (C3H8), normal butane (n-C4H10), isobutene (i-C4H10), ethene (C2H4), benzene (C6H6), toluene (C7H8) as well as refrigerants consisting of 1,1,1,2 tetra fluoroethane (R134a), tetrafluoromethane (R14), chlorodifluromethane (R22), 1,1,1-trifluoroethane (R143a), 1,1,1-trifluoro,2,2-dichloroethane (R123), octafluoropropane (R218), and 1,1-difluoroethane (R152a) are selected and compared with literature data. The calculations cover the ranges from the dilute vapor or gas to the highly compressed liquid and supercritical regions. The thermodynamic properties are the vapor and liquid densities, the vapor pressure, the internal energy, the enthalpy, the entropy, the heat capacity at constant pressure and constant volume, and the speed of sound. It was found that the overall agreement with literature in all phases especially the vapor/gas phase is remarkable. Furthermore, the Zeno line regularity can be well represented by the TM EOS. Finally, the TM EOS is further assessed through comparing with the Ihm.Song.Mason (ISM) equation of state. In general, the TM EOS outperforms the ISM equation of state.
  1. Song Y, Mason EA, J. Chem. Phys., 91, 7840 (1989)
  2. Weeks JD, Chandler D, Andersen HC, J. Chem. Phys., 54, 5237 (1971)
  3. Carnahan NF, Starling KE, J. Chem. Phys., 51, 635 (1969)
  4. Song Y, Mason EA, Phys. Rev., 41, 3121 (1990)
  5. Song YE, Mason A, Phys. Rev., 42, 4743 (1990)
  6. Song Y, Mason EA, Phys. Rev., 42, 4749 (1990)
  7. Ihm G, Song Y, Mason EA, J. Chem. Phys., 94, 3839 (1991)
  8. Ihm G, Song Y, Mason EA, Fluid Phase Equilib., 75, 117 (1992)
  9. Song Y, Mason EA, Fluid Phase Equilib., 75, 105 (1992)
  10. Tao FM, Mason EA, Int. J. Thermophys., 13, 1053 (1992)
  11. Boushehri A, Mason EA, Int. J. Thermophys., 14, 685 (1993)
  12. Ghatee MH, Boushehri A, Int. J. Thermophys., 17, 945 (1996)
  13. Eslami H, Int. J. Thermophys., 21, 1123 (2000)
  14. Sheikh S, Papari MM, Boushehri A, Ind. Eng. Chem. Res., 41(13), 3274 (2002)
  15. Leila MA, Javanmardi M, Boushehri A, Fluid Phase Equilib., 236(1-2), 237 (2005)
  16. Eslami H, Papari MM, Boushehri A, J. Phys. Soc. Jpn., 69, 1731 (2000)
  17. Eslami H, Papari MM, Boushehri A, J. Phys. Soc. Jpn., 70, 1015 (2001)
  18. Tao FM, Mason EA, J. Chem. Phys., 100(12), 9075 (1994)
  19. Tsonopoulos C, AIChE J., 20, 263 (1974)
  20. Schreiber DR, Pitzer KS, Fluid Phase Equilib., 16, 113 (1989)
  21. Weber LA, Int. J. Thermophys., 15, 461 (1994)
  22. Tsonopoulos C, Fluid Phase Equilib., 211(1), 35 (2003)
  23. Vetere A, Fluid Phase Equilib., 230(1-2), 15 (2005)
  24. Lemmon EW, Mclinden MO, Friend DG, in: Mallard WG, Linstrom PJ (Eds.), Thermophysical Properties of Fluid Systems in NIST Chemistry Webbook, Nat. Inst. Stand. Tech., Gaithersburg, MD, 2005, NIST Standard Reference Database Number 69 http://webbook.nist.gov.
  25. Poling BE, Prausnitz JM, O’Connell JP, The Properties of Gases and Liquids, McGraw Hill, New York (2001)
  26. Riedel LA, Chem. Ing. Tech., 26, 679 (1954)
  27. Liu ZY, Chem. Eng. Commun., 184, 221 (2001)
  28. Majer V, Svoboda V, Pick J, Heat of Vaporization of Fluids, Studies in Modern Thermodynamics, vol. 9, Elsevier, Amsterdam (1989)
  29. Carruth GF, Kobayashi RK, Ind. Eng. Chem. Fundam., 11, 509 (1972)
  30. Chen NH, J. Chem. Eng. Data., 10, 207 (1965)
  31. Watson KM, Ind. Eng. Chem., 35, 398 (1943)
  32. Cachadina I, Mulero A, Fluid Phase Equilib., 240(2), 173 (2006)
  33. Sivaraman A, Magee JW, Kobayashi R, Ind. Eng. Chem. Fundam., 23, 97 (1984)
  34. Kutney MC, Reagan MT, Smith KA, Tester JW, Herschbach DR, J. Phys. Chem. B, 104(40), 9513 (2000)