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Volumn 50, Issue 1, 2005, Pages 44-48

Vapor-liquid equilibrium for the difluoromethane (R32) + n-butane (R600) system

Author keywords

[No Author keywords available]

Indexed keywords

COMPUTER SOFTWARE; GAS CHROMATOGRAPHY; MATHEMATICAL MODELS; METHANE; PHASE EQUILIBRIA; REFRIGERANTS; REGRESSION ANALYSIS; SOLUBILITY; THERMAL CONDUCTIVITY;

EID: 12344289530     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je049874h     Document Type: Article
Times cited : (14)

References (17)
  • 1
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    • VLLE measurements and their correlation for the R32 + R600 system
    • Bobbo, S.; Fedele, L.; Camporese, R.; Stryjek, R. VLLE measurements and their correlation for the R32 + R600 system. Fluid Phase Equilib. 2003, 210, 45-56.
    • (2003) Fluid Phase Equilib. , vol.210 , pp. 45-56
    • Bobbo, S.1    Fedele, L.2    Camporese, R.3    Stryjek, R.4
  • 4
    • 0037198851 scopus 로고    scopus 로고
    • VLE measurements and modeling for the strongly positive azeotropic R32 + propane system
    • Bobbo, S.; Fedele, L.; Camporese, R.; Stryjek, R. VLE measurements and modeling for the strongly positive azeotropic R32 + propane system. Fluid Phase Equilib. 2002, 199, 175-183.
    • (2002) Fluid Phase Equilib. , vol.199 , pp. 175-183
    • Bobbo, S.1    Fedele, L.2    Camporese, R.3    Stryjek, R.4
  • 6
    • 0347132560 scopus 로고    scopus 로고
    • Vapor-liquid equilibria of HFC-32/n-butane mixtures
    • Shimawaki S.; Fujii K. Vapor-Liquid Equilibria of HFC-32/n-Butane Mixtures. Int. J. Thermodyn. 2003, 24, 1033-1042.
    • (2003) Int. J. Thermodyn. , vol.24 , pp. 1033-1042
    • Shimawaki, S.1    Fujii, K.2
  • 7
    • 0032173064 scopus 로고    scopus 로고
    • A recirculation apparatus for vapor-liquid equilibrium measurements of refrigerants. Binary mixtures of R600a, R134a and R236fa
    • Bobbo, S.; Stryjek, R.; Elvassore, N.; Bertucco, A. A recirculation apparatus for vapor-liquid equilibrium measurements of refrigerants. Binary mixtures of R600a, R134a and R236fa. Fluid Phase Equilib. 1998, 150-151, 343-352.
    • (1998) Fluid Phase Equilib. , vol.150-151 , pp. 343-352
    • Bobbo, S.1    Stryjek, R.2    Elvassore, N.3    Bertucco, A.4
  • 9
    • 0016984146 scopus 로고
    • Vapor-liquid equilibrium from a hard sphere equation of state
    • De Santis, R.; Gironi, F.; Marrelli, L. Vapor-liquid equilibrium from a hard sphere equation of state. Ind. Eng. Chem. Fundam. 1976, 15, 183-189.
    • (1976) Ind. Eng. Chem. Fundam. , vol.15 , pp. 183-189
    • De Santis, R.1    Gironi, F.2    Marrelli, L.3
  • 11
    • 47649111276 scopus 로고
    • Equilibrium constants from a modified Redlich-Kwong equation of state
    • Soave, G. Equilibrium constants from a modified Redlich-Kwong equation of state. Chem. Eng. Sci. 1972, 27, 1197-1203.
    • (1972) Chem. Eng. Sci. , vol.27 , pp. 1197-1203
    • Soave, G.1
  • 13
    • 0018544434 scopus 로고
    • New mixing rules in simple equations of state for representing vapor-liquid equilibria of strongly non-Ideal mixtures
    • Huron, M. J.; Vidal, J. New Mixing Rules in Simple Equations of State for Representing Vapor-Liquid Equilibria of Strongly Non-Ideal Mixtures. Fluid Phase Equilib. 1979, 3, 255-272.
    • (1979) Fluid Phase Equilib. , vol.3 , pp. 255-272
    • Huron, M.J.1    Vidal, J.2
  • 14
    • 84984084157 scopus 로고
    • Local compositions in thermodynamic excess functions for liquid mixtures
    • Renon, H.; Prausnitz, J. M. Local Compositions in Thermodynamic Excess Functions for Liquid Mixtures. AIChE J. 1968, 14, 135-144.
    • (1968) AIChE J. , vol.14 , pp. 135-144
    • Renon, H.1    Prausnitz, J.M.2
  • 15
    • 0026867521 scopus 로고
    • A theoretically correct mixing rule for cubic equations of state
    • Wong, D. S. H.; Sandier S. I. A Theoretically Correct Mixing Rule for Cubic Equations of State. AIChE J. 1992, 38, 671-680.
    • (1992) AIChE J. , vol.38 , pp. 671-680
    • Wong, D.S.H.1    Sandier, S.I.2
  • 16
    • 0026906172 scopus 로고
    • Equation of state mixing rule for nonideal mixtures using available activity coefficient model parameters and that allows extrapolation over large ranges of temperature or pressure
    • Wong D. S. H.; Obey H.; Sandier S. I. Equation of State Mixing Rule for Nonideal Mixtures using Available Activity Coefficient Model Parameters and that Allows Extrapolation over Large Ranges of Temperature or Pressure. Ind. Eng. Chem. Res. 1992, 31, 2033-2039.
    • (1992) Ind. Eng. Chem. Res. , vol.31 , pp. 2033-2039
    • Wong, D.S.H.1    Obey, H.2    Sandier, S.I.3
  • 17
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    • A helmholtz energy equation of state for calculating the thermodynamic properties of fluid mixtures
    • Lemmon, E. W.; Tillner-Roth, R. A Helmholtz energy equation of state for calculating the thermodynamic properties of fluid mixtures. Fluid Phase Equilib. 1999, 165, 1-21.
    • (1999) Fluid Phase Equilib. , vol.165 , pp. 1-21
    • Lemmon, E.W.1    Tillner-Roth, R.2


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.