Isothermal Properties for Xenon

Fluid Data

Isothermal Data for T = 0.0000 C

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Auxiliary Data

Reference States, Normal Boiling Point Convention

Additional fluid properties

References and Notes

Equation of state

Lemmon, E.W.; Span, R., Short Fundamental Equations of State for 20 Industrial Fluids, J. Chem. Eng. Data, 2006, 51, 3, 785-850, https://doi.org/10.1021/je050186n . [all data]

The uncertainties in the equation of state are 0.2% in density up to 100 MPa, rising to 1% at higher pressures, 0.2% in vapor pressure, 1% in the speed of sound, and 2% in heat capacities.

Auxillary model, Cp0

Lemmon, E.W. and Span, R., 2006.

Auxillary model, PX0

Lemmon, E.W. and Span, R., 2006.

Auxillary model, PH0

Lemmon, E.W. and Span, R., 2006.

Transport model

Huber, M.L., Models for the Viscosity, Thermal Conductivity, and Surface Tension of Selected Pure Fluids as Implemented in REFPROP v10.0, NIST Interagency/Internal Report (NISTIR) - 8209, NIST, Boulder, Colorado, 2018, https://doi.org/10.6028/NIST.IR.8209 . [all data]

Estimated uncertainty for gas-phase viscosity is 1%, for liquid to 60 MPa and temperatures above 170 K is 5%. Estimated uncertainty for gas-phase thermal conductivity is 5%, and 3% for the liquid at pressures to 50 MPa at temperatures 170 K to 235 K.

The Lennard-Jones parameters were obtained by fitting data in Vogel, E., Ber. Bunsen-Ges. Phys. Chem., 88:997-1002, 1984.

Auxillary model, the thermal conductivity critical enhancement

Perkins, R.A.; Sengers, J.V.; Abdulagatov, I.M.; Huber, M.L., Simplified Model for the Critical Thermal-Conductivity Enhancement in Molecular Fluids, Int. J. Thermophys., 2013, 34, 2, 191-212, https://doi.org/10.1007/s10765-013-1409-z . [all data]

Surface tension

Mulero, A.; Cachadiña, I.; Parra, M.I., Recommended Correlations for the Surface Tension of Common Fluids, J. Phys. Chem. Ref. Data, 2012, 41, 4, 043105, https://doi.org/10.1063/1.4768782 . [all data]

Dielectric constant

Harvey, A.H.; Lemmon, E.W., Method for Estimating the Dielectric Constant of Natural Gas Mixtures, Int. J. Thermophys., 2005, 26, 1, 31-46, https://doi.org/10.1007/s10765-005-2351-5 . [all data]

Metling line

Michels, A.; Prins, C., The Melting Lines of Argon, Krypton and Xenon up to 1500 atm; Representation of the Results by a Law of Corresponding States, Physica (Amsterdam), 1962, 28, 2, 101-116, https://doi.org/10.1016/0031-8914(62)90096-4 . [all data]

Michels, A. and Prins, C., "The Melting Lines of Argon, Krypton and Xenon up to 1500 Atm; Representation of the Results by a Law of Corresponding States," Physica, 28:101-116, 1962.

Sublimation line

Lemmon, E.W., 2003.

Vapor pressure

Cullimore, I.D., 2010.

Functional Form: P=Pc*EXP[SUM(Ni*Theta^ti)*Tc/T] where Theta=1-T/Tc, Tc and Pc are the reducing parameters below, which are followed by rows containing Ni and ti.

Saturated liquid density

Cullimore, I.D., 2010.

Functional Form: D=Dc*[1+SUM(Ni*Theta^ti)] where Theta=1-T/Tc, Tc and Dc are the reducing parameters below, which are followed by rows containing Ni and ti.

Saturated liquid volume

Cullimore, I.D., 2010.

Functional Form: D=Dc*EXP[SUM(Ni*Theta^ti)] where Theta=1-T/Tc, Tc and Dc are the reducing parameters below, which are followed by rows containing Ni and ti.

The fluid data above is also available from the NIST Reference Fluid Thermodynamic and Transport Properties Database. This product includes additional features not available from this web site.

Notes