Xenon
- Formula: Xe
- Molecular weight: 131.293
- IUPAC Standard InChIKey: FHNFHKCVQCLJFQ-UHFFFAOYSA-N
- CAS Registry Number: 7440-63-3
- Chemical structure:
This structure is also available as a 2d Mol file - Other names: Xe; UN 2036; UN 2591; Xenon atom; Xeneisol 133A; Xenomatic
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- Information on this page:
- Other data available:
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- Gas Phase Kinetics Database
- X-ray Photoelectron Spectroscopy Database, version 5.0
- X-ray Photoelectron Spectroscopy Database, version 5.0
- X-ray Photoelectron Spectroscopy Database, version 5.0
- X-ray Photoelectron Spectroscopy Database, version 5.0
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Gas phase thermochemistry data
Go To: Top, Phase change data, Reaction thermochemistry data, Henry's Law data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
S°gas,1 bar | 169.685 ± 0.003 | J/mol*K | Review | Cox, Wagman, et al., 1984 | CODATA Review value |
S°gas,1 bar | 169.68 | J/mol*K | Review | Chase, 1998 | Data last reviewed in March, 1982 |
Gas Phase Heat Capacity (Shomate Equation)
Cp° = A + B*t + C*t2 + D*t3 +
E/t2
H° − H°298.15= A*t + B*t2/2 +
C*t3/3 + D*t4/4 − E/t + F − H
S° = A*ln(t) + B*t + C*t2/2 + D*t3/3 −
E/(2*t2) + G
Cp = heat capacity (J/mol*K)
H° = standard enthalpy (kJ/mol)
S° = standard entropy (J/mol*K)
t = temperature (K) / 1000.
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Temperature (K) | 298. to 6000. |
---|---|
A | 20.78600 |
B | 7.449320×10-7 |
C | -2.049401×10-7 |
D | 1.066661×10-8 |
E | 2.500261×10-8 |
F | -6.197350 |
G | 194.8380 |
H | 0.000000 |
Reference | Chase, 1998 |
Comment | Data last reviewed in March, 1982 |
Phase change data
Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry data, Henry's Law data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 165.02 | K | N/A | Ziegler, Mullins, et al., 1966 | Uncertainty assigned by TRC = 0.05 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 161.38 | K | N/A | Kemp, Kemp, et al., 1985 | Uncertainty assigned by TRC = 0.02 K; studied as possible fixed point for IPTS-68; TRC |
Ttriple | 161.37 | K | N/A | Ziegler, Mullins, et al., 1966 | Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 161.4 | K | N/A | Lahr and Eversole, 1962 | Uncertainty assigned by TRC = 0.3 K; TRC |
Ttriple | 161.36 | K | N/A | Clusius and Weigand, 1940 | Uncertainty assigned by TRC = 0.2 K; See property X for dP/dT for c-l equil.; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 0.81600 | bar | N/A | Fonseca and Lobo, 1989 | Uncertainty assigned by TRC = 0.0001 bar; TRC |
Ptriple | 0.6166 | bar | N/A | Calado, Rebelo, et al., 1986 | Uncertainty assigned by TRC = 0.00007 bar; TRC |
Ptriple | 0.8165 | bar | N/A | Ziegler, Mullins, et al., 1966 | Uncertainty assigned by TRC = 0.0019 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 289.74 | K | N/A | Theeuwes and Bearman, 1970 | Uncertainty assigned by TRC = 0.02 K; PVT, values chosen concordant with vapour pressures measured up to 284 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 8.371 | mol/l | N/A | Theeuwes and Bearman, 1970 | Uncertainty assigned by TRC = 0.00830 mol/l; PVT, values chosen concordant with vapour pressures measured up to 284 K; TRC |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
161.43 to 162.63 | 2.83881 | 326.595 | -49.796 | Chen, Lim, et al., 1975 | Coefficents calculated by NIST from author's data. |
161.70 to 184.70 | 3.80675 | 577.661 | -13.0 | Michels and Wassenaar, 1950 | Coefficents calculated by NIST from author's data. |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
B - John E. Bartmess
MS - José A. Martinho Simões
RCD - Robert C. Dunbar
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.
Individual Reactions
By formula: (Xe+ • Xe) + Xe = (Xe+ • 2Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 28. | kJ/mol | DT | Helm, 1976 | gas phase; corrected for ln T by Keesee and Castleman, 1986; M |
ΔrH° | 28.2 | kJ/mol | DT | Helm, 1976 | gas phase; corrected for ln T by Keesee and Castleman, 1986; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 78.2 | J/mol*K | DT | Helm, 1976 | gas phase; corrected for ln T by Keesee and Castleman, 1986; M |
ΔrS° | 78.2 | J/mol*K | DT | Helm, 1976 | gas phase; corrected for ln T by Keesee and Castleman, 1986; M |
By formula: Cl- + Xe = (Cl- • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 17.6 ± 1.3 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
ΔrH° | 13.0 | kJ/mol | Mobl | Gatland, 1984 | gas phase; B,M |
ΔrH° | 13.0 | kJ/mol | Mobl | Thackston, Eisele, et al., 1980 | gas phase; B,M |
ΔrH° | <13.4 | kJ/mol | Mobl | De Vreugd, Wijnaendts van Resandt, et al., 1979 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | -6.1 ± 1.3 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
By formula: Br- + Xe = (Br- • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15.1 ± 1.3 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
ΔrH° | 12.1 ± 0.42 | kJ/mol | LPES | Yourshaw, Lenzer, et al., 1998 | gas phase; Given: 0.12692(.0005) eV; B |
ΔrH° | 14.2 | kJ/mol | Mobl | Gatland, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | -4.9 ± 1.3 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
By formula: Cs+ + Xe = (Cs+ • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 10.5 | kJ/mol | IMob | Gatland, 1984, 2 | gas phase; M |
ΔrH° | 11.5 | kJ/mol | SCATTERING | Gislason, 1984 | gas phase; M |
ΔrH° | 11.0 | kJ/mol | IMob | Viehland, 1984 | gas phase; M |
ΔrH° | 10.2 | kJ/mol | IMob | Mason and Sharp, 1958 | gas phase; M |
ΔrH° | 14.9 | kJ/mol | IMob | Takebe, 1983 | gas phase; values from this source are too high; M |
By formula: CH3+ + Xe = (CH3+ • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 213. | kJ/mol | PHPMS | McMahon, Heinis, et al., 1988 | gas phase; switching reaction(CH3+)N2, Entropy change calculated or estimated, uses MCA(N2) = 202. kJ/mol; Foster, Williamson, et al., 1974; M |
ΔrH° | 231. ± 10. | kJ/mol | ICR | Hovey and McMahon, 1986 | gas phase; switching reaction(CH3+)CH3F, Entropy change calculated or estimated; M |
By formula: F- + Xe = (F- • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 26.4 ± 1.3 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
ΔrH° | 27.2 ± 3.8 | kJ/mol | Mobl | De Vreugd, Wijnaendts van Resandt, et al., 1979 | gas phase; B |
ΔrH° | 27. | kJ/mol | SCATTERING | De Vrengd, Wijnaendts van Resandt, et al., 1979 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 6.4 ± 1.3 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
+ = IXe-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.69 | kJ/mol | N/A | Lenzer, Furlanetto, et al., 1998 | gas phase; B |
ΔrH° | 11.7 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; Entropy estimated; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | -8.24 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; Entropy estimated; B |
By formula: Xe+ + Xe = (Xe+ • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 99.6 | kJ/mol | PI | Ng, Trevor, et al., 1976 | gas phase; M |
ΔrH° | 95.4 | kJ/mol | SCATTERING | Mittman and Weise, 1974 | gas phase; M |
ΔrH° | 93.7 | kJ/mol | SCATTERING | Lorentz, Olson, et al., 1973 | gas phase; M |
ΔrH° | 95.4 | kJ/mol | PI | Samson, 1966 | gas phase; M |
By formula: K+ + Xe = (K+ • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.0 | kJ/mol | IMob | Gatland, 1984, 2 | gas phase; M |
ΔrH° | 15.8 | kJ/mol | SCATTERING | Gislason, 1984 | gas phase; M |
ΔrH° | 20.3 | kJ/mol | IMob | Viehland, 1984 | gas phase; M |
ΔrH° | 22.3 | kJ/mol | IMob | Takebe, 1983 | gas phase; M |
C5O5WXe (solution) = C5O5W (solution) + (solution)
By formula: C5O5WXe (solution) = C5O5W (solution) + Xe (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 35.1 ± 0.8 | kJ/mol | KinS | Weiller, 1992 | solvent: Liquid Xenon; Temperature range: 173-198 K; MS |
C5MoO5Xe (g) = C5MoO5 (g) + (g)
By formula: C5MoO5Xe (g) = C5MoO5 (g) + Xe (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 33.5 ± 4.2 | kJ/mol | KinG | Wells and Weitz, 1992 | The reaction enthalpy relies on 31.0 ± 4.2 kJ/mol for the activation energy and on the assumption of a negligible barrier for product recombination Wells and Weitz, 1992; MS |
By formula: C5O5WXe (g) = C5O5W (g) + Xe (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 34.3 ± 4.2 | kJ/mol | KinG | Wells and Weitz, 1992 | The reaction enthalpy relies on 31.8 ± 4.2 kJ/mol for the activation energy and on the assumption of a negligible barrier for product recombination Wells and Weitz, 1992; MS |
C5CrO5Xe (g) = C5CrO5 (g) + (g)
By formula: C5CrO5Xe (g) = C5CrO5 (g) + Xe (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 37.7 ± 3.8 | kJ/mol | KinG | Wells and Weitz, 1992 | The reaction enthalpy relies on 35.1 ± 3.8 kJ/mol for the activation energy and assumes a negligible barrier for product recombination Wells and Weitz, 1992; MS |
By formula: Li+ + Xe = (Li+ • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 51.5 | kJ/mol | SCATTERING | Gislason, 1984 | gas phase; M |
ΔrH° | 52.7 | kJ/mol | IMob | Viehland, 1984 | gas phase; M |
ΔrH° | 87.0 | kJ/mol | IMob | Takebe, 1983 | gas phase; M |
By formula: Na+ + Xe = (Na+ • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 25.0 | kJ/mol | SCATTERING | Gislason, 1984 | gas phase; M |
ΔrH° | 24.9 | kJ/mol | IMob | Viehland, 1984 | gas phase; M |
ΔrH° | 39.8 | kJ/mol | IMob | Takebe, 1983 | gas phase; M |
By formula: Rb+ + Xe = (Rb+ • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 11.9 | kJ/mol | IMob | Gatland, 1984, 2 | gas phase; M |
ΔrH° | 17.8 | kJ/mol | IMob | Viehland, 1984 | gas phase; M |
ΔrH° | 15.1 | kJ/mol | IMob | Takebe, 1983 | gas phase; M |
By formula: (Xe+ • 2Xe) + Xe = (Xe+ • 3Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 25.2 ± 0.63 | kJ/mol | PHPMS | Hiraoka and Mori, 1990 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 63.2 | J/mol*K | PHPMS | Hiraoka and Mori, 1990 | gas phase; M |
By formula: (Xe+ • 3Xe) + Xe = (Xe+ • 4Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 11.0 ± 0.63 | kJ/mol | PHPMS | Hiraoka and Mori, 1990 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 54.8 | J/mol*K | PHPMS | Hiraoka and Mori, 1990 | gas phase; M |
By formula: ClXe- + 2Xe = ClXe2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15.5 ± 1.7 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | -9.5 ± 1.7 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
By formula: FXe2- + 3Xe = FXe3-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20.9 ± 1.7 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | -2.8 ± 1.7 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
By formula: FXe- + 2Xe = FXe2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 21.8 ± 1.3 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 0.5 ± 1.3 | kJ/mol | TDAs | Wada, Kikkawa, et al., 2007 | gas phase; B |
By formula: NO- + Xe = (NO- • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16.3 ± 3.8 | kJ/mol | N/A | Hendricks, de Clercq, et al., 2002 | gas phase; B |
ΔrH° | 17.2 ± 2.5 | kJ/mol | N/A | Bowen and Eaton, 1988 | gas phase; B |
By formula: IXe9- + 10Xe = IXe10-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 5.0 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe10- + 11Xe = IXe11-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.8 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe11- + 12Xe = IXe12-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.8 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe- + 2Xe = IXe2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 8.8 ± 2.1 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe2- + 3Xe = IXe3-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 6.7 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe3- + 4Xe = IXe4-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 5.9 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe4- + 5Xe = IXe5-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 5.9 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe5- + 6Xe = IXe6-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 5.0 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe6- + 7Xe = IXe7-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 5.0 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe7- + 8Xe = IXe8-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 5.0 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: IXe8- + 9Xe = IXe9-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 3.8 ± 3.8 | kJ/mol | N/A | Becker, Markovich, et al., 1997 | gas phase; Stated electron affinity is the Vertical Detachment Energy; B |
By formula: V+ + Xe = (V+ • Xe)
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
33. (+5.9,-0.) | CID | Sievers and Armentrout, 1995 | gas phase; guided ion beam CID; M |
By formula: Fe+ + Xe = (Fe+ • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 41.8 ± 5.9 | kJ/mol | CIDT | Rodgers and Armentrout, 2000 | RCD |
By formula: Mg+ + Xe = (Mg+ • Xe)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 31. ± 12. | kJ/mol | CIDT | Andersen, Muntean, et al., 2000 | RCD |
By formula: NOXe- + 2Xe = NOXe2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16.3 | kJ/mol | N/A | Hendricks, de Clercq, et al., 2002 | gas phase; B |
By formula: NOXe2- + 3Xe = NOXe3-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14.6 | kJ/mol | N/A | Hendricks, de Clercq, et al., 2002 | gas phase; B |
By formula: NOXe3- + 4Xe = NOXe4-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1.3 | kJ/mol | N/A | Hendricks, de Clercq, et al., 2002 | gas phase; B |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Rolf Sander
Henry's Law constant (water solution)
kH(T) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
k°H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference |
---|---|---|---|
0.0043 | 2200. | L | N/A |
0.0043 | 1900. | M | N/A |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Cox, Wagman, et al., 1984
Cox, J.D.; Wagman, D.D.; Medvedev, V.A.,
CODATA Key Values for Thermodynamics, Hemisphere Publishing Corp., New York, 1984, 1. [all data]
Chase, 1998
Chase, M.W., Jr.,
NIST-JANAF Themochemical Tables, Fourth Edition,
J. Phys. Chem. Ref. Data, Monograph 9, 1998, 1-1951. [all data]
Ziegler, Mullins, et al., 1966
Ziegler, W.T.; Mullins, J.C.; Berquist, A.R.,
Calculation of the Vapor Pressure and Heats of Vaporization and Sublimation of Liquids and Solids below One Atmosphere Pressure. VIII. Xenon, Ga. Inst. Technol., Eng. Exp. Stn., Proj. A-764, Tech. Rep. No. 3, 1966. [all data]
Kemp, Kemp, et al., 1985
Kemp, R.C.; Kemp, W.R.G.; Smart, P.W.,
The triple point of xenon as a possible defining point on an international temperature scale,
Metrologia, 1985, 21, 43. [all data]
Lahr and Eversole, 1962
Lahr, P.H.; Eversole, W.G.,
Compression Isotherms of Argon, Krypton, and Xenon Through the Freezing Zone,
J. Chem. Eng. Data, 1962, 7, 42-47. [all data]
Clusius and Weigand, 1940
Clusius, K.; Weigand, K.,
Melting Curves of the Gases A, Kr, Xe, CH4, CH3D, CD4, C2H4, C2H6, COS, and PH3 to 200 Atmospheres Pressure. The Chane of Volume on Melting,
Z. Phys. Chem., Abt. B, 1940, 46, 1-37. [all data]
Fonseca and Lobo, 1989
Fonseca, I.M.A.; Lobo, L.Q.,
Thermodynamics of liquid mixtures of xenon and methyl fluoride,
Fluid Phase Equilib., 1989, 47, 249. [all data]
Calado, Rebelo, et al., 1986
Calado, J.C.G.; Rebelo, L.P.N.; Streett, W.B.; Zollweg, J.A.,
Thermodynamics of liquid (dimethylether + xenon),
J. Chem. Thermodyn., 1986, 18, 931. [all data]
Theeuwes and Bearman, 1970
Theeuwes, F.; Bearman, R.J.,
The p,V,T behavior of dense fluids V. The vapor pressure and saturated liquid density of xenon,
J. Chem. Thermodyn., 1970, 2, 507-12. [all data]
Chen, Lim, et al., 1975
Chen, H.H.; Lim, C.C.; Aziz, R.A.,
The Enthalpy of Vaporization and Internal Energy of Liquid Argon, Krypton, and Xenon Determined from Vapor Pressures,
J. Chem. Thermodyn., 1975, 7, 2, 191-199, https://doi.org/10.1016/0021-9614(75)90268-2
. [all data]
Michels and Wassenaar, 1950
Michels, A.; Wassenaar, T.,
Vapour Pressure of Liquid Xenon,
Physica (Amsterdam), 1950, 16, 3, 253-256, https://doi.org/10.1016/0031-8914(50)90023-1
. [all data]
Helm, 1976
Helm, H.,
Formation of Xe3+ Ions in Xenon at Temperatures Between 210 and 293 K,
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Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, References
- Symbols used in this document:
Ptriple Triple point pressure S°gas,1 bar Entropy of gas at standard conditions (1 bar) T Temperature Tboil Boiling point Tc Critical temperature Ttriple Triple point temperature d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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