Isothermal Properties for Xenon
- Fluid Data
- Auxiliary Data
- References and Notes
- Notes
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Fluid Data
Isothermal Data for T = 273.16 K
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Auxiliary Data
Reference States, Normal Boiling Point Convention
Enthalpy | H = 0 at the normal boiling point for saturated liquid. |
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Entropy | S = 0 at the normal boiling point for saturated liquid. |
Additional fluid properties
Critical temperature (Tc) | 289.733 K |
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Critical pressure (Pc) | 5.8420 MPa |
Critical density (Dc) | 8.4 mol/l |
Acentric factor | 0.00363 |
Normal boiling point | 165.05 K |
Dipole moment | 0.0 Debye |
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.
Notes
- Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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