n-Propane
Synonym: propane
Molecular formula: |
C3H8 |
Molar mass: |
44.10 g·mol-1 |
CAS registry number: |
74-98-6 |
EINECS number: |
200-827-9 |
P. Haimi, P. Uusi-Kyyny, J. -P. Pokki and V. Alopaeus
Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons
Fluid Phase Equilib.
• Year: 2010
• Volume: 295
• Pages: 17-25.
Keywords:
Infinite dilution activity coefficient, Sulphur compounds, VLE
DOI: 10.1016/j.fluid.2010.03.027
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2010.03.027.xml
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S.-X. Hou and Y. -Y. Duan
Vapor-liquid equilibrium measurement and modeling for the difluoromethane + pentafluoroethane + propane ternary mixture
Fluid Phase Equilib.
• Year: 2010
• Volume: 298
• Pages: 106-112.
Keywords:
Vapor liquid equilibrium (VLE), Mixture, Difluoromethane (R32), Pentafluoroethane (R125), Propane (R290)
DOI: 10.1016/j.fluid.2010.07.018
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2010.07.018.xml
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Kim, Y. S., Jang, J. H., Lim, B. D., Kang, J. W., Lee, C. S.
Solubility of mixed gases containing carbon dioxide in ionic liquids: Measurements and predictions
Fluid Phase Equilib.
• Year: 2007
• Volume: 256
• Pages: 70-74.
Keywords:
experiment, calculation, ionic liquids, gases, vapor-liquid equilibria
DOI: 10.1016/j.fluid.2006.11.019
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.11.019.xml
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Gozalpour, F., Al-Saleh, I., Tohidi, B., Danesh, A., Todd, A. C.
Experimental data on binary and ternary mixtures of perfluoro-1,3-dimethylcyclohexane with normal alkanes at 373.15 K
Fluid Phase Equilib.
• Year: 2010
• Volume: 297
• Pages: 138-141.
Keywords:
Tracer, Perfluorocarbons, Fluid sampling, Oil-based mud, Contamination
DOI: 10.1016/j.fluid.2010.06.017
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2010.06.017.xml
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J. S. Lim, J. -Y. Park, j. W. Kang and B. G. Lee
Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
Fluid Phase Equilib.
• Year: 2006
• Volume: 243
• Pages: 57-63.
Keywords:
Propane (R-290), HFC-134a, HFC-143a, Azeotropic mixture, Vapor liquid equilibria (VLE), Carnahan Starling De Santis equation of state (CSD EOS)
DOI: 10.1016/j.fluid.2006.02.016
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.02.016.xml
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J. Gregorowicz
Phase behaviour in the vicinity of the three-phase solid liquid vapour line in asymmetric nonpolar systems at high pressures
Fluid Phase Equilib.
• Year: 2006
• Volume: 240
• Pages: 29-39.
Keywords:
Solid liquid vapour equilibria, Solid liquid equilibria, Liquid vapour equilibria, Asymmetric nonpolar systems, Thermodynamic analysis
DOI: 10.1016/j.fluid.2005.11.031
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2005.11.031.xml
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Y. Miyano, I. Fujihara and K. Sato
Henry s law constants of propane, propene, butane, and 2-methylpropane in methanol at 374-490K
Fluid Phase Equilib.
• Year: 2006
• Volume: 240
• Pages: 56-62.
Keywords:
Experimental data, Henry s law constant, Solubility, Methanol, Propane, Propene, Butane, 2-Methylpropane
DOI: 10.1016/j.fluid.2005.12.001
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2005.12.001.xml
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R. Akasaka, Y. Higashi, K. Tanaka, Y. Kayukawa and K. Fujii
Vapor liquid equilibrium measurements and correlations for the binary mixture of difluoromethane + isobutane and the ternary mixture of propane + isobutane + difluoromethane
Fluid Phase Equilib.
• Year: 2007
• Volume: 261
• Pages: 286-291.
Keywords:
R-32, R-290, R-600a, Vapor liquid equilibrium, Correlation
DOI: 10.1016/j.fluid.2007.06.029
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2007.06.029.xml
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S.-X. Hou and Y. -Y. Duan
Isothermal vapor liquid equilibria for the pentafluoroethane + propane and pentafluoroethane + 1,1,1,2,3,3,3-heptafluoropropane systems
Fluid Phase Equilib.
• Year: 2010
• Volume: 290
• Pages: 121-126.
Keywords:
Vapor liquid equilibrium (VLE), Peng Robinson equation of state (PR Eos), Mixing rules, Pentafluoroethane (R125), 1,1,1,2,3,3,3-Heptafluoropropane (R227ea), Propane (R290)
DOI: 10.1016/j.fluid.2009.09.008
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2009.09.008.xml
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Q. N. N. Ho, K. S. Yoo, B. G. Lee and J. S. Lim
Measurement of vapor liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290)
Fluid Phase Equilib.
• Year: 2006
• Volume: 245
• Pages: 63-70.
Keywords:
Propane (R-290), Propylene (R-1270), Hydrocarbon mixture, Vapor liquid equilibria (VLE), Peng Robinson equation of state (PR-EOS)
DOI: 10.1016/j.fluid.2006.03.009
ThermoML:
http://trc.nist.gov/ThermoML/fpe/j.fluid.2006.03.009.xml
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kitajima, H., Kagawa, N., Tsuruno, S.[Seizou], Wantanabe, K.
Isochoric Heat Capacities of Propane+Isobutane Mixtures at Temperatures from 280 to 420K and at Pressures to 30MPa1
Int. J. Thermophys.
• Year: 2005
• Volume: 26
• Pages: 1733-1742.
Keywords:
critical region, density, heat capacity, isobutane, mixtures, propane, pvTx property.
DOI: 10.1016/2005kitkag0
ThermoML:
http://trc.nist.gov/ThermoML/ijt/2005kitkag0.xml
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Franceschi, E.[Elton], Kunita, M. H.[Marcos H.], Rubira, A. F.[Adley F.], Muniz, E. C.[Edvani Curti], Corazza, M. L.[Marcos L.], Oliveira, J. V., Dariva, C.[Claudio]
Phase Behavior of Binary and Ternary Systems Involving Carbon Dioxide, Propane, and Glycidyl Methacrylate at High Pressure
J. Chem. Eng. Data
• Year: 2006
• Volume: 51
• Pages: 686-690.
Keywords:
phase equilibrium, binary, ternary, carbon dioxide, propane, glycidyl methacrylate,
DOI: 10.1021/je050453p
ThermoML:
http://trc.nist.gov/journals/jced/2006v51/i02/je050453p.xml
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B. G. Lee, W.-J. Yang and J. S. Lim
Vapor-Liquid Equilibria for the Binary System Difluoromethane (HFC-32) + Propane (HC-290) at Seven Temperatures [(268.15, 278.15, 283.15, 288.15, 298.15, 308.15, and 318.15) K]
J. Chem. Eng. Data
• Year: 2003
• Volume: 48
• Pages: 841-846.
Keywords:
VLE, binary system, difluoromethane, propane
DOI: 10.1021/je020154p
ThermoML:
http://trc.nist.gov/journals/jced/2003v48/i04/je020154p.xml
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C. Coquelet, A. Chareton, A. Valtz, A. Baba-Ahmed and D. Richon
Vapor-Liquid Equilibrium Data for the Azeotropic Difluoromethane + Propane System at Temperatures from 294.83 to 343.26 K and Pressures up to 5.4 MPa
J. Chem. Eng. Data
• Year: 2003
• Volume: 48
• Pages: 317-323.
Keywords:
VLE
DOI: 10.1021/je020115d
ThermoML:
http://trc.nist.gov/journals/jced/2003v48/i02/je020115d.xml
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M. Yasumoto, Y. Uchida, K. Ochi, T. Furuya and K. Otake
Critical Properties of Three Dimethyl Ether Binary Systems: Dimethyl Ether (RE-170) + Propane (HC-290), Butane (HC-600), and 2-Methyl Propane (HC-600A)
J. Chem. Eng. Data
• Year: 2005
• Volume: 50
• Pages: 596-602.
Keywords:
critical temperature, critical pressure, critical density, DME, propane, butane, 2-methyl propane
DOI: 10.1021/je0496589
ThermoML:
http://trc.nist.gov/journals/jced/2005v50/i02/je0496589.xml
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Kayukawa, Y.[Yohei], Fujii, K., Higashi, Y.[Yukihiro]
Vapor-Liquid Equilibrium (VLE) Properties for the Binary Systems Propane (1) + n-Butane (2) and Propane (1) + Isobutane (3)
J. Chem. Eng. Data
• Year: 2005
• Volume: 50
• Pages: 579-582.
Keywords:
vapor-liquid equilibrium, propane, butane, isobutane
DOI: 10.1021/je0496701
ThermoML:
http://trc.nist.gov/journals/jced/2005v50/i02/je0496701.xml
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Y. Kayukawa, M. Hasumoto, Y. Kano and K. Watanabe
Liquid-Phase Thermodynamic Properties for the Binary and Ternary Systems of Propane (1), n-Butane (2), and Isobutane (3)
J. Chem. Eng. Data
• Year: 2005
• Volume: 50
• Pages: 565-578.
Keywords:
vapor pressure, density, bubble-point pressure, propane, butane, isobutane
DOI: 10.1021/je049671t
ThermoML:
http://trc.nist.gov/journals/jced/2005v50/i02/je049671t.xml
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Y. Miyano, O. Mitsuoka, H. Ikeda, A. Ouchi, T. Ono, K. Tsuchida and Y. Tateishi
Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methyl-3-buten-2-ol and 3-Methyl-3-buten-1-ol
J. Chem. Eng. Data
• Year: 2005
• Volume: 50
• Pages: 2106-2111.
Keywords:
Henry's Law constants, infinite dilution activity coefficients, Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane 2-Methyl-3-buteno
DOI: 10.1021/je050343i
ThermoML:
http://trc.nist.gov/journals/jced/2005v50/i06/je050343i.xml
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Y. Miyano
Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Propen-1-ol
J. Chem. Eng. Data
• Year: 2005
• Volume: 50
• Pages: 2045-2048.
Keywords:
Experimental data, Mixture, Henry's constant, Activity coefficient, 2-propene-1-ol
DOI: 10.1021/je0502647
ThermoML:
http://trc.nist.gov/journals/jced/2005v50/i06/je0502647.xml
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S. Horstmann, G. Birke and K. Fischer
Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Propane + Dimethyl Ether and Propene + Dimethyl Ether at Temperatures from (298 to 323) K
J. Chem. Eng. Data
• Year: 2004
• Volume: 49
• Pages: 38-42.
Keywords:
vapor-liquid equilibrium, experimental, propane, propene, dimethyl ether
DOI: 10.1021/je0301242
ThermoML:
http://trc.nist.gov/journals/jced/2004v49/i01/je0301242.xml
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Y. Miyano
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 at (250 to 330) K
J. Chem. Eng. Data
• Year: 2004
• Volume: 49
• Pages: 1285-1289.
Keywords:
Henry's constant, Activity coefficients, Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene, 1, 3-Butadiene, 1-Butanol, 2-Butanol
DOI: 10.1021/je034265f
ThermoML:
http://trc.nist.gov/journals/jced/2004v49/i05/je034265f.xml
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P. Tobaly, P. Marteau and V. Ruffier-Meray
High -Pressure Phase Diagrams of Propane + Decahydronaphthalene and Propane + Naphthalene Mixtures
J. Chem. Eng. Data
• Year: 2004
• Volume: 49
• Pages: 795-799.
Keywords:
High-Pressure, Phase equilibria, liquid-vapor, molarity, concentration, mixture, propane, naphthalene, decalin, decahydronaphthalene, spectroscopy, spectrophotometry,
DOI: 10.1021/je0341458
ThermoML:
http://trc.nist.gov/journals/jced/2004v49/i04/je0341458.xml
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Lim, J. S.[Jong Sung], Park, J. -Y.[Ji-Young], Lee, K.-S., Kim, J. -D.[Jae-Duck], Lee, B. G.[Byung Gwon]
Measurement of Vapor-Liquid Equilibria for the Binary Mixture of Pentafluoroethane (HFC-125) + Propane (R-290)
J. Chem. Eng. Data
• Year: 2004
• Volume: 49
• Pages: 750-755.
Keywords:
Vapor-Liquid Equilibria, f Pentafluoroethane (HFC-125), Propane (R-290)
DOI: 10.1021/je030156p
ThermoML:
http://trc.nist.gov/journals/jced/2004v49/i04/je030156p.xml
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Y. Miyano
Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene, and 1,3-butadiene in 2-propanol at 250-330 K
J. Chem. Eng. Data
• Year: 2004
• Volume: 49
• Pages: 368-371.
Keywords:
Henry's Constant, infinite dilution, activity coefficient, alkene, alkane
DOI: 10.1021/je0342116
ThermoML:
http://trc.nist.gov/journals/jced/2004v49/i02/je0342116.xml
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J. S. Lim, Q. N. N. Ho, J. -Y. Park and B. G. Lee
Measurement of Vapor-Liquid Equilibria for the Binary Mixture of Propane (R-290) + Isobutane (R-600a)
J. Chem. Eng. Data
• Year: 2004
• Volume: 49
• Pages: 192-198.
Keywords:
vapor-liquid equilibria, binary mixture, propane, isobutane, Carnahan-Starling-De Santis equation
DOI: 10.1021/je030106k
ThermoML:
http://trc.nist.gov/journals/jced/2004v49/i02/je030106k.xml
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Y. Miyano, S. Ashimori, T. Otuka, T. Dairaku, T. Kitamoto, Y. Kume, Y. Tateishi, Y. Nishiguchi, R. Miura and T. Mitani
Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methylphenol, 3-Methylphenol, and 4-Methylphenol
J. Chem. Eng. Data
• Year: 2010
• Volume: 55
• Pages: 4956-4960.
DOI: 10.1021/je100529s
ThermoML:
http://trc.nist.gov/ThermoML/10.1021/je100529s.xml
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Houssin-Agbomson, D.[Deborah], Coquelet, C.[Christophe], Arpentinier, P., Delcorso, F.[Fabrice], Richon, D.[Dominique]
Equilibrium Data for the Oxygen + Propane Binary System at Temperatures of (110.22, 120.13, 130.58, and 139.95) K
J. Chem. Eng. Data
• Year: 2010
• Volume: 55
• Pages: 4412-4415.
DOI: 10.1021/je100574y
ThermoML:
http://trc.nist.gov/ThermoML/10.1021/je100574y.xml
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P. Naidoo, J. D. Raal and D. Ramjugernath
High-Pressure Vapor-Liquid Equilibrium Data for (Carbon Dioxide + Cyclopentanol) and (Propane + Cyclopentanol)
J. Chem. Eng. Data
• Year: 2010
• Volume: 55
• Pages: 196-200.
Keywords:
VLE data, High-pressures, Supercritical gas solubility, Phase diagram determination
DOI: 10.1021/je900305m
ThermoML:
http://trc.nist.gov/ThermoML/10.1021/je900305m.xml
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B. Breure, E. J. M. Straver, L. J. Florusse, M. P. W. M. Rijkers, I. G. Economou, F. M. Vargas and C. J. Peters
Phase Equilibria in Binary Mixtures of Propane and Phenanthrene: Experimental Data and Modeling with the GC-EoS
J. Chem. Eng. Data
• Year: 2011
• Volume: 56
• Pages: 1407-1413.
Keywords:
Experimental, modeling, propane, phenanthrene, Group Contribution Equation of, State
DOI: 10.1021/je101058b
ThermoML:
http://trc.nist.gov/ThermoML/10.1021/je101058b.xml
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D. Seibt, K. Vob, S. Herrmann, E. Vogel and E. Hassel
Simultaneous Viscosity-Density Measurements on Ethane and Propane over a Wide Range of Temperature and Pressure Including the Near-Critical Region
J. Chem. Eng. Data
• Year: 2011
• Volume: 56
• Pages: 1476-1493.
DOI: 10.1021/je101178u
ThermoML:
http://trc.nist.gov/ThermoML/10.1021/je101178u.xml
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F. Martinez, A. Martin, R. Camarillo and J. Rincon
Measurement and Modeling of the Solubility of 9H-Carbazole in Sub- and Supercritical Propane
J. Chem. Eng. Data
• Year: 2011
• Volume: 56
• Pages: 956-962.
Keywords:
Solubility, propane, carbazole, PAH, Peng-Robinson equation, Chrastil, equation
DOI: 10.1021/je100923d
ThermoML:
http://trc.nist.gov/ThermoML/10.1021/je100923d.xml
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Cristancho, D. E.[Diego E.], Mantilla, I. D.[Ivan D.], Coy, L. A., Tibaduiza, A.[Andrea], Ortiz-Vega, D. O.[Diego O.], Hall, K. R.[Kenneth R.]
Accurate P-rho-T Data and Phase Boundary Determination for a Synthetic Residual Natural Gas Mixture
J. Chem. Eng. Data
• Year: 2011
• Volume: 56
• Pages: 826-832.
DOI: 10.1021/je100500t
ThermoML:
http://trc.nist.gov/ThermoML/10.1021/je100500t.xml
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Y. Miyano, A. Kimura, M. Kuroda, A. Matsushita, A. Yamasaki, Y. Yamaguchi, A. Yoshizawa and Y. Tateishi
Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
J. Chem. Eng. Data
• Year: 2007
• Volume: 52
• Pages: 291-297.
DOI: 10.1021/je060395n
ThermoML:
http://trc.nist.gov/journals/jced/2007v52/i01/je060395n.xml
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M. E. E. ]. Kandil and K. N. Marsh
Determination of the Relative Permittivity and Density within the Gas Phase and Liquid Volume Fraction Formed within the Two-Phase Region for (0.4026 CH4 + 0.5974 C3H8) with a Radio Frequency Re-entrant Cavity
J. Chem. Eng. Data
• Year: 2007
• Volume: 52
• Pages: 1660-1671.
DOI: 10.1021/je700053u
ThermoML:
http://trc.nist.gov/journals/jced/2007v52/i05/je700053u.xml
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Y. Miyano, S. Uno, K. Tochigi, S. Kato and H. Yasuda
Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran
J. Chem. Eng. Data
• Year: 2007
• Volume: 52
• Pages: 2245-2249.
DOI: 10.1021/je700270d
ThermoML:
http://trc.nist.gov/journals/jced/2007v52/i06/je700270d.xml
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Y. Miyano
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.
• Year: 2004
• Volume: 36
• Pages: 865-869.
Keywords:
Data, Mixture, Henry s constant, Activity coefficient, Isobutanol, tert-Butanol
DOI: 10.1016/2004miy2
ThermoML:
http://trc.nist.gov/journals/jct/2004v36/i10/2004miy2.xml
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Y. Miyano
Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutene, 1-butene, isobutane, trans-2-butene and 1,3-butadiene in 1-propanol at T=(260 to 340) K
J. Chem. Thermodyn.
• Year: 2004
• Volume: 36
• Pages: 101-106.
Keywords:
Data, Mixture, Henry's constant, Activity coefficient, 1-propanol, Gas stripping
DOI: 10.1016/2004miy0
ThermoML:
http://trc.nist.gov/journals/jct/2004v36/i02/2004miy0.xml
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S. Glos, R. Kleinrahm and W. Wagner
Measurement of the (p,rho,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
J. Chem. Thermodyn.
• Year: 2004
• Volume: 36
• Pages: 1037-1059.
Keywords:
Propane, Propylene, n-Butane, Isobutane, Density measurements
DOI: 10.1016/j.jct.2004.07.017
ThermoML:
http://trc.nist.gov/journals/jct/2004v36/i12/j.jct.2004.07.017.xml
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Y. Miyano
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-pentanol, 2-pentanol and 3-pentanol
J. Chem. Thermodyn.
• Year: 2005
• Volume: 37
• Pages: 459-465.
Keywords:
Experimental data, Mixture, Henry's constant, Activity coefficient, 1-pentanol, 2-pentanol, 3-pentanol
DOI: 10.1016/j.jct.2004.11.005
ThermoML:
http://trc.nist.gov/journals/jct/2005v37/i05/j.jct.2004.11.005.xml
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X. Dong, M. Gong, J. Liu and J. Wu
Isothermal (vapour + liquid) equilibrium for the binary {1,1,2,2-tetrafluoroethane (R134) + propane (R290)} and {1,1,2,2-tetrafluoroethane (R134) + isobutane (R600a)} systems
J. Chem. Thermodyn.
• Year: 2010
• Volume: 42
• Pages: 1152-1157.
Keywords:
(Vapour + liquid) equilibrium, 1,1,2,2-Tetrafluoroethane, Propane, Isobutane
DOI: 10.1016/j.jct.2010.04.016
ThermoML:
http://trc.nist.gov/ThermoML/10.1016/j.jct.2010.04.016.xml
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X. Dong, M. Gong, J. Liu and J. Wu
Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
J. Chem. Thermodyn.
• Year: 2011
• Volume: 43
• Pages: 505-510.
Keywords:
Saturated vapor pressures, (Vapor + liquid) equilibrium, 1,1,1,2-Tetrafluoroethane, Propane
DOI: 10.1016/j.jct.2010.11.001
ThermoML:
http://trc.nist.gov/ThermoML/10.1016/j.jct.2010.11.001.xml
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R. M. Charin, M. L. Corazza, P. M. Ndiaye, A. A. Rigo, M. A. Mazutti and J. V. Oliveira
Phase equilibrium data and thermodynamic modelling of the system (propane + DMF + methanol) at high pressures
J. Chem. Thermodyn.
• Year: 2011
• Volume: 43
• Pages: 413-419.
Keywords:
Phase equilibrium, High pressure, Propane, DMF, Methanol
DOI: 10.1016/j.jct.2010.10.014
ThermoML:
http://trc.nist.gov/ThermoML/10.1016/j.jct.2010.10.014.xml
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Nagata, Y., Mizutani, K., Miyamoto, H.
The precise measurement of the (vapour + liquid) equilibrium properties for (CO2 + isobutane) binary mixtures
J. Chem. Thermodyn.
• Year: 2011
• Volume: 43
• Pages: 244-247.
Keywords:
Bubble point pressure, Dew point pressure, Measurement, Recirculation method, (Vapour + liquid) equilibrium, (CO2 + isobutane) binary mixture
DOI: 10.1016/j.jct.2010.09.004
ThermoML:
http://trc.nist.gov/ThermoML/10.1016/j.jct.2010.09.004.xml
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Miyamoto, H., Shigetoyo, K., Uematsu, M.
The (p, p, T,x) properties for {x propane + (1 - x) isobutane} with x =(1.0000, 0.2765, 0.5052, and 0.7468) in the temperature range from (280 to 440) K at pressures from (1 to 200) MPa
J. Chem. Thermodyn.
• Year: 2007
• Volume: 39
• Pages: 1423-1431.
Keywords:
Excess molar volume, Measurement, Propane, Propane +isobutane binary mixture, PpTx property
DOI: 10.1016/j.jct.2007.03.012
ThermoML:
http://trc.nist.gov/ThermoML/jct/j.jct.2007.03.012.xml
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