- InChI
- InChI=1S/Xe
- InChI Key
- FHNFHKCVQCLJFQ-UHFFFAOYSA-N
- Formula
- Xe
- SMILES
- [Xe]
- Molecular Weight1
- 131.29
- CAS
- 7440-63-3
- Other Names
-
- UN 2036
- UN 2591
- Xe
- Xeneisol 133A
- Xenomatic
- Xenon atom
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- SProt : Protonation entropy at 298K (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρg : Gas Density (kg/m3).
- ρl : Liquid Density (kg/m3).
- S°gas,1 bar : Molar entropy at standard conditions (1 bar) (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.0020; 0.0080] |
|
|
| ω | 0.0020 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.0060 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.0080 | KDB | |
| PAff | [495.80; 499.60] | kJ/mol |
|
| PAff | 499.60 | kJ/mol | NIST |
| PAff | 495.80 ± 8.40 | kJ/mol | NIST |
| BasG | [474.50; 478.10] | kJ/mol |
|
| BasG | 478.10 | kJ/mol | NIST |
| BasG | 474.50 ± 8.40 | kJ/mol | NIST |
| μ | [0.00; 0.00] | debye |
|
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 0.00 | debye | KDB |
| SProt | 37.00 | J/mol×K | NIST |
| ΔfG° | 0.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [0.00; 0.00] | kJ/mol |
|
| ΔfH°gas | 0.00 | kJ/mol | Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value |
| ΔfH°gas | 0.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| IE | [12.03; 12.17] | eV |
|
| IE | 12.13 | eV | NIST |
| IE | 12.13 | eV | NIST |
| IE | Outlier 12.03 | eV | NIST |
| IE | 12.13 | eV | NIST |
| IE | 12.13 | eV | NIST |
| IE | 12.12 ± 0.02 | eV | NIST |
| IE | 12.13 | eV | NIST |
| IE | 12.13 ± 0.00 | eV | NIST |
| IE | 12.13 | eV | NIST |
| IE | 12.09 ± 0.03 | eV | NIST |
| IE | 12.12 ± 0.00 | eV | NIST |
| IE | 12.15 ± 0.03 | eV | NIST |
| IE | 12.12 ± 0.01 | eV | NIST |
| IE | 12.13 ± 0.00 | eV | NIST |
| IE | 12.13 ± 0.00 | eV | NIST |
| IE | 12.17 | eV | NIST |
| Pc | [5836.32; 5842.00] | kPa |
|
| Pc | 5840.37 | kPa | Mathews (1972), critical constants of inorganic substances Compiled value |
| Pc | 5836.32 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 5840.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 5842.00 | kPa | Air Liquide Gas Encyclopedia |
| Pc | 5840.00 | kPa | KDB |
| Ptriple | [61.66; 81.70] | kPa |
|
| Ptriple | 81.67 ± 0.01 | kPa | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Ptriple | 81.67 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 81.70 | kPa | Air Liquide Gas Encyclopedia |
| Ptriple | 81.59 | kPa | KDB |
| Ptriple | 81.60 ± 0.01 | kPa | NIST |
| Ptriple | Outlier 61.66 ± 0.01 | kPa | NIST |
| Ptriple | 81.65 ± 0.19 | kPa | NIST |
| ρc | [1099.05; 1102.90] | kg/m3 |
|
| ρc | 1102.90 | kg/m3 | Air Liquide Gas Encyclopedia |
| ρc | 1099.05 ± 1.09 | kg/m3 | NIST |
| S°gas,1 bar | 169.69 ± 0.00 | J/mol×K | NIST |
| Tboil | [165.01; 165.11] | K |
|
| Tboil | 165.01 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 165.05 | K | Air Liquide Gas Encyclopedia |
| Tboil | 165.11 | K | KDB |
| Tboil | 165.02 ± 0.05 | K | NIST |
| Tc | [289.70; 289.74] | K |
|
| Tc | 289.73 | K | Mathews (1972), critical constants of inorganic substances Compiled value |
| Tc | Outlier 289.70 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 289.74 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 289.74 | K | Air Liquide Gas Encyclopedia |
| Tc | 289.73 | K | KDB |
| Tc | 289.74 ± 0.02 | K | NIST |
| Tfus | [161.25; 161.40] | K |
|
| Tfus | 161.25 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 161.36 | K | Air Liquide Gas Encyclopedia |
| Tfus | 161.40 | K | KDB |
| Ttriple | [161.25; 161.40] | K |
|
| Ttriple | 161.40 | K | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Ttriple | Outlier 161.25 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 161.40 | K | Air Liquide Gas Encyclopedia |
| Ttriple | 161.40 | K | KDB |
| Ttriple | 161.38 ± 0.02 | K | NIST |
| Ttriple | 161.37 ± 0.05 | K | NIST |
| Ttriple | 161.40 ± 0.30 | K | NIST |
| Ttriple | 161.36 ± 0.20 | K | NIST |
| UQi | 1.13 | ChemSep v8.3 pure component data Compiled value | |
| URi | 1.13 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.118; 0.118] | m3/kmol |
|
| Vc | 0.118 | m3/kmol | Mathews (1972), critical constants of inorganic substances Compiled value |
| Vc | 0.118 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.118 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.118 | m3/kmol | KDB |
| Zc | [0.2860000; 0.2860650] |
|
|
| Zc | 0.2860000 | Mathews (1972), critical constants of inorganic substances Compiled value | |
| Zc | 0.2860000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2860650 | KDB | |
| Zra | [0.28; 0.29] |
|
|
| Zra | 0.29 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.28 | KDB |
Cheméo can also estimate Enthalpy of vaporization at standard conditions, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | 2.29 | kJ/mol | 161.36 | Air Liquide Gas Encyclopedia |
| ΔvapH | [12.55; 15.79] | kJ/mol | [53.50; 165.05] |
|
| ΔvapH | 15.79 | kJ/mol | 53.50 | Measurements of enthalpy of sublimation of Ne, N2, O2, Ar, CO2, Kr, Xe, and H2O using a double paddle oscillator |
| ΔvapH | 12.55 | kJ/mol | 165.05 | Air Liquide Gas Encyclopedia |
| ρg | [5.58; 10.01] | kg/m3 | [165.05; 288.15] |
|
| ρg | 10.01 | kg/m3 | 165.05 | Air Liquide Gas Encyclopedia |
| ρg | 5.58 | kg/m3 | 288.15 | Air Liquide Gas Encyclopedia |
| ρl | [2942.00; 3060.00] | kg/m3 | [165.00; 165.05] |
|
| ρl | 3060.00 | kg/m3 | 165.00 | KDB |
| ρl | 2942.00 | kg/m3 | 165.05 | Air Liquide Gas Encyclopedia |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [20.79; 20.79] | J/mol×K | [10.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.07860e+01 | |||
| Coefficient B | 0.00000e+00 | |||
| Coefficient C | -6.90776e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 10.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 20.79 | J/mol×K | 10.00 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 175.56 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 341.11 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 506.67 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 672.22 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 837.78 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 1003.33 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 1168.89 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 1334.44 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 1500.00 | Calculated Property |
| Cp,gas | [20.79; 20.79] | J/mol×K | [298.00; 6000.00] |
NIST
|
| Equation | Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.07860e+01 | |||
| Coefficient B | 7.44932e-07 | |||
| Coefficient C | -2.04940e-07 | |||
| Coefficient D | 1.06666e-08 | |||
| Coefficient E | 2.50026e-08 | |||
| Reference | Chase, 1998 | |||
| Comment | F=-6.197350, G=194.8380, H=0.000000; Data last reviewed in March, 1982 | |||
| Temperature range, min. | 298.00 | |||
| Temperature range, max. | 6000.00 | |||
| Cp,gas | 20.79 | J/mol×K | 298.00 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 931.56 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 1565.11 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 2198.67 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 2832.22 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 3465.78 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 4099.33 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 4732.89 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 5366.44 | Calculated Property |
| Cp,gas | 20.79 | J/mol×K | 6000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [44.65; 44.66] | J/mol×K | [163.15; 172.65] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 4.46100e+01 | |||
| Coefficient B | -2.21000e+02 | |||
| Coefficient C | -5.82666e+00 | |||
| Coefficient D | 2.65150e-02 | |||
| Coefficient E | -1.32570e-05 | |||
| Temperature range, min. | 163.15 | |||
| Temperature range, max. | 172.65 | |||
| Cp,liquid | 44.65 | J/mol×K | 163.15 | Calculated Property |
| Cp,liquid | 44.65 | J/mol×K | 164.21 | Calculated Property |
| Cp,liquid | 44.65 | J/mol×K | 165.26 | Calculated Property |
| Cp,liquid | 44.65 | J/mol×K | 166.32 | Calculated Property |
| Cp,liquid | 44.66 | J/mol×K | 167.37 | Calculated Property |
| Cp,liquid | 44.66 | J/mol×K | 168.43 | Calculated Property |
| Cp,liquid | 44.66 | J/mol×K | 169.48 | Calculated Property |
| Cp,liquid | 44.66 | J/mol×K | 170.54 | Calculated Property |
| Cp,liquid | 44.66 | J/mol×K | 171.59 | Calculated Property |
| Cp,liquid | 44.66 | J/mol×K | 172.65 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0004310; 0.0004310] | Pa×s | [165.02; 174.52] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -7.74210e+00 | |||
| Coefficient B | -5.37760e-01 | |||
| Coefficient C | -5.01840e-04 | |||
| Coefficient D | -5.29340e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 165.02 | |||
| Temperature range, max. | 174.52 | |||
| η | 0.0004310 | Pa×s | 165.02 | Calculated Property |
| η | 0.0004310 | Pa×s | 166.08 | Calculated Property |
| η | 0.0004310 | Pa×s | 167.13 | Calculated Property |
| η | 0.0004310 | Pa×s | 168.19 | Calculated Property |
| η | 0.0004310 | Pa×s | 169.24 | Calculated Property |
| η | 0.0004310 | Pa×s | 170.30 | Calculated Property |
| η | 0.0004310 | Pa×s | 171.35 | Calculated Property |
| η | 0.0004310 | Pa×s | 172.41 | Calculated Property |
| η | 0.0004310 | Pa×s | 173.46 | Calculated Property |
| η | 0.0004310 | Pa×s | 174.52 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [12.59; 0.00] | kJ/mol | [161.36; 289.74] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 1.74063e+01 | |||
| Coefficient B | -2.33725e-01 | |||
| Coefficient C | 3.14836e+00 | |||
| Coefficient D | -4.99526e+00 | |||
| Coefficient E | 2.47711e+00 | |||
| Critical temperature, Tc (K) | 2.89740e+02 | |||
| Temperature range, min. | 161.36 | |||
| Temperature range, max. | 289.74 | |||
| ΔvapH | 12.59 | kJ/mol | 161.36 | Calculated Property |
| ΔvapH | 12.09 | kJ/mol | 175.62 | Calculated Property |
| ΔvapH | 11.59 | kJ/mol | 189.89 | Calculated Property |
| ΔvapH | 11.07 | kJ/mol | 204.15 | Calculated Property |
| ΔvapH | 10.48 | kJ/mol | 218.42 | Calculated Property |
| ΔvapH | 9.76 | kJ/mol | 232.68 | Calculated Property |
| ΔvapH | 8.83 | kJ/mol | 246.95 | Calculated Property |
| ΔvapH | 7.56 | kJ/mol | 261.21 | Calculated Property |
| ΔvapH | 5.66 | kJ/mol | 275.48 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 289.74 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [81.60; 5820.75] | kPa | [161.40; 289.70] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41675e+01 | |||
| Coefficient B | -1.61435e+03 | |||
| Coefficient C | 3.91000e+00 | |||
| Temperature range, min. | 161.40 | |||
| Temperature range, max. | 289.70 | |||
| Pvap | 81.60 | kPa | 161.40 | Calculated Property |
| Pvap | 177.18 | kPa | 175.66 | Calculated Property |
| Pvap | 343.23 | kPa | 189.91 | Calculated Property |
| Pvap | 607.30 | kPa | 204.17 | Calculated Property |
| Pvap | 998.73 | kPa | 218.42 | Calculated Property |
| Pvap | 1546.88 | kPa | 232.68 | Calculated Property |
| Pvap | 2279.64 | kPa | 246.93 | Calculated Property |
| Pvap | 3222.30 | kPa | 261.19 | Calculated Property |
| Pvap | 4396.68 | kPa | 275.44 | Calculated Property |
| Pvap | 5820.75 | kPa | 289.70 | Calculated Property |
| Pvap | [57.51; 5865.71] | kPa | [155.55; 290.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.45892e+01 | |||
| Coefficient B | -1.75890e+03 | |||
| Coefficient C | -1.87270e+00 | |||
| Coefficient D | 9.16520e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 155.55 | |||
| Temperature range, max. | 290.00 | |||
| Pvap | 57.51 | kPa | 155.55 | Calculated Property |
| Pvap | 136.41 | kPa | 170.49 | Calculated Property |
| Pvap | 280.97 | kPa | 185.43 | Calculated Property |
| Pvap | 519.67 | kPa | 200.37 | Calculated Property |
| Pvap | 884.07 | kPa | 215.31 | Calculated Property |
| Pvap | 1408.05 | kPa | 230.24 | Calculated Property |
| Pvap | 2127.68 | kPa | 245.18 | Calculated Property |
| Pvap | 3081.60 | kPa | 260.12 | Calculated Property |
| Pvap | 4311.96 | kPa | 275.06 | Calculated Property |
| Pvap | 5865.71 | kPa | 290.00 | Calculated Property |
| Pvap | [81.89; 87.97] | kPa | [161.43; 162.63] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.11418e+01 | |||
| Coefficient B | -7.52013e+02 | |||
| Coefficient C | -4.97960e+01 | |||
| Reference | Chen, Lim, et al., 1975 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 161.43 | |||
| Temperature range, max. | 162.63 | |||
| Pvap | 81.89 | kPa | 161.43 | Calculated Property |
| Pvap | 82.55 | kPa | 161.56 | Calculated Property |
| Pvap | 83.21 | kPa | 161.70 | Calculated Property |
| Pvap | 83.88 | kPa | 161.83 | Calculated Property |
| Pvap | 84.55 | kPa | 161.96 | Calculated Property |
| Pvap | 85.23 | kPa | 162.10 | Calculated Property |
| Pvap | 85.91 | kPa | 162.23 | Calculated Property |
| Pvap | 86.59 | kPa | 162.36 | Calculated Property |
| Pvap | 87.28 | kPa | 162.50 | Calculated Property |
| Pvap | 87.97 | kPa | 162.63 | Calculated Property |
| Pvap | [83.56; 276.94] | kPa | [161.70; 184.70] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.33705e+01 | |||
| Coefficient B | -1.33011e+03 | |||
| Coefficient C | -1.30000e+01 | |||
| Reference | Michels and Wassenaar, 1950 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 161.70 | |||
| Temperature range, max. | 184.70 | |||
| Pvap | 83.56 | kPa | 161.70 | Calculated Property |
| Pvap | 97.20 | kPa | 164.26 | Calculated Property |
| Pvap | 112.49 | kPa | 166.81 | Calculated Property |
| Pvap | 129.56 | kPa | 169.37 | Calculated Property |
| Pvap | 148.55 | kPa | 171.92 | Calculated Property |
| Pvap | 169.59 | kPa | 174.48 | Calculated Property |
| Pvap | 192.82 | kPa | 177.03 | Calculated Property |
| Pvap | 218.36 | kPa | 179.59 | Calculated Property |
| Pvap | 246.35 | kPa | 182.14 | Calculated Property |
| Pvap | 276.94 | kPa | 184.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [2978.34; 1106.51] | kg/m3 | [161.36; 289.74] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 3.15930e+02 | |||
| Coefficient B | 2.85520e-01 | |||
| Coefficient C | 2.89740e+02 | |||
| Coefficient D | 2.89670e-01 | |||
| Temperature range, min. | 161.36 | |||
| Temperature range, max. | 289.74 | |||
| ρl | 2978.34 | kg/m3 | 161.36 | Calculated Property |
| ρl | 2881.04 | kg/m3 | 175.62 | Calculated Property |
| ρl | 2778.31 | kg/m3 | 189.89 | Calculated Property |
| ρl | 2668.83 | kg/m3 | 204.15 | Calculated Property |
| ρl | 2550.65 | kg/m3 | 218.42 | Calculated Property |
| ρl | 2420.74 | kg/m3 | 232.68 | Calculated Property |
| ρl | 2273.86 | kg/m3 | 246.95 | Calculated Property |
| ρl | 2099.42 | kg/m3 | 261.21 | Calculated Property |
| ρl | 1868.54 | kg/m3 | 275.48 | Calculated Property |
| ρl | 1106.51 | kg/m3 | 289.74 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.02; 3.41e-06] | N/m | [161.36; 288.58] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -3.28280e-03 | |||
| Coefficient B | 4.98280e+02 | |||
| Coefficient C | -1.14570e+01 | |||
| Coefficient D | 4.66550e-02 | |||
| Coefficient E | -1.13490e-04 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 289.74 K. | |||
| Temperature range, min. | 161.36 | |||
| Temperature range, max. | 288.58 | |||
| γ | 0.02 | N/m | 161.36 | Calculated Property |
| γ | 0.02 | N/m | 175.50 | Calculated Property |
| γ | 0.01 | N/m | 189.63 | Calculated Property |
| γ | 0.01 | N/m | 203.77 | Calculated Property |
| γ | 0.01 | N/m | 217.90 | Calculated Property |
| γ | 0.01 | N/m | 232.04 | Calculated Property |
| γ | 0.00 | N/m | 246.18 | Calculated Property |
| γ | 0.00 | N/m | 260.31 | Calculated Property |
| γ | 0.00 | N/m | 274.45 | Calculated Property |
| γ | 3.41e-06 | N/m | 288.58 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.02] | W/m×K | [150.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 2.67190e-04 | |||
| Coefficient B | 6.20460e-01 | |||
| Coefficient C | 2.15600e+02 | |||
| Coefficient D | -8.14440e+03 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 1500.00 | |||
| λgas | 0.00 | W/m×K | 150.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 300.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 450.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 600.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 750.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 900.00 | Calculated Property |
| λgas | 0.02 | W/m×K | 1050.00 | Calculated Property |
| λgas | 0.02 | W/m×K | 1200.00 | Calculated Property |
| λgas | 0.02 | W/m×K | 1350.00 | Calculated Property |
| λgas | 0.02 | W/m×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.08; 0.03] | W/m×K | [145.90; 270.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -1.21750e-02 | |||
| Coefficient B | 1.43580e+02 | |||
| Coefficient C | -4.26550e+00 | |||
| Coefficient D | 1.10410e-02 | |||
| Coefficient E | -3.29370e-05 | |||
| Temperature range, min. | 145.90 | |||
| Temperature range, max. | 270.00 | |||
| λliquid | 0.08 | W/m×K | 145.90 | Calculated Property |
| λliquid | 0.07 | W/m×K | 159.69 | Calculated Property |
| λliquid | 0.07 | W/m×K | 173.48 | Calculated Property |
| λliquid | 0.06 | W/m×K | 187.27 | Calculated Property |
| λliquid | 0.06 | W/m×K | 201.06 | Calculated Property |
| λliquid | 0.05 | W/m×K | 214.84 | Calculated Property |
| λliquid | 0.05 | W/m×K | 228.63 | Calculated Property |
| λliquid | 0.04 | W/m×K | 242.42 | Calculated Property |
| λliquid | 0.04 | W/m×K | 256.21 | Calculated Property |
| λliquid | 0.03 | W/m×K | 270.00 | Calculated Property |
Mixtures
- 2-PROPANOL, 1,1,1,3,3,3-HEXAFLUORO- + Xenon + Water
- Xenon + Furan, tetrahydro-2,5-dimethyl- + Furan, tetrahydro-2,5-dimethyl-, cis-
- Xenon + Cyclopentane
- Xenon + Argon
- Xenon + 2,5,8,11-Tetraoxadodecane
- Xenon + 2,5,8,11,14-Pentaoxapentadecane
- Xenon + Carbonic acid, dimethyl ester
- Diethyl carbonate + Xenon
Sources
- Air Liquide Gas Encyclopedia
- Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
- Mathews (1972), critical constants of inorganic substances ChEDL chemicals 1.5.2, from Mathews, J. F. Critical Constants of Inorganic Substances. Chem. Rev. 1972, 72, 71-100.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Binary Diffusion Coefficient Data of Various Gas Systems Determined Using a Loschmidt Cell and Holographic Interferometry
- On the behaviour of solutions of xenon in liquid cycloalkanes: Solubility of xenon in cyclopentane
- Physical data for a process to separate krypton from air by selective absorption in an ionic liquid
- Solubility of gases in fluoroorganic alcohols. Part II. Solubilities of noble gases in (water + 1,1,1,3,3,3-hexafluoropropan-2-ol) at 298.15 K and 101.33 kPa
- Measurements of enthalpy of sublimation of Ne, N2, O2, Ar, CO2, Kr, Xe, and H2O using a double paddle oscillator
- Solubilities of gases in cycloethers. The solubility of 13 nonpolar gases in 2,5-dimethyltetrahydrofuran at 273.15 to 303.15 K and 101.32 kPa
- Solubilities of Nonpolar Gases in Triethylene Glycol Dimethyl Ether, Tetraethylene Glycol Dimethyl Ether, Dimethyl Carbonate, and Diethyl Carbonate at 298.15 K and 101.33 kPa Partial Pressure of Gas
- Solubilities of Nonpolar Gases in Dimethyl Carbonate and Diethyl Carbonate
- Solubility of the Single Gases Methane and Xenon in the Ionic Liquid [bmim][CH3SO4]
- KDB
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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