| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2162 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ΔfH°gas | -560.22 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 12.28 | eV | Relay (1.0) Calculated Property |
| logPoct/wat | 2.108 | Crippen Calculated Property | |
| Pc | [3576.77; 3579.81] | kPa |
|
| Pc | 3576.77 | kPa | Mathews (1972), critical constants of inorganic substances Compiled value |
| Pc | 3579.80 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3579.81 ± 5.06 | kPa | NIST |
| Tboil | 285.79 | K | Relay (1.0) Calculated Property |
| Tc | [438.41; 438.60] | K |
|
| Tc | 438.60 | K | Mathews (1972), critical constants of inorganic substances Compiled value |
| Tc | 438.41 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 438.41 ± 0.02 | K | NIST |
| Tfus | 142.55 | K | Relay (1.0) Calculated Property |
Cheméo can also estimate Critical Volume, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, 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.
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [89.59; 108.23] | 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 | 1.04736e+02 | |||
| Coefficient B | 2.80955e+00 | |||
| Coefficient C | -7.53643e-01 | |||
| Coefficient D | 6.39090e-02 | |||
| Coefficient E | -1.41327e+00 | |||
| Reference | Chase, 1998 | |||
| Comment | F=-877.0668, G=453.9431, H=-840.9840; Data last reviewed in December, 1960 | |||
| Temperature range, min. | 298.00 | |||
| Temperature range, max. | 6000.00 | |||
| Cp,gas | 89.59 | J/mol×K | 298.00 | Calculated Property |
| Cp,gas | 105.12 | J/mol×K | 931.56 | Calculated Property |
| Cp,gas | 106.95 | J/mol×K | 1565.11 | Calculated Property |
| Cp,gas | 107.66 | J/mol×K | 2198.67 | Calculated Property |
| Cp,gas | 107.92 | J/mol×K | 2832.22 | Calculated Property |
| Cp,gas | 107.96 | J/mol×K | 3465.78 | Calculated Property |
| Cp,gas | 107.91 | J/mol×K | 4099.33 | Calculated Property |
| Cp,gas | 107.86 | J/mol×K | 4732.89 | Calculated Property |
| Cp,gas | 107.94 | J/mol×K | 5366.44 | Calculated Property |
| Cp,gas | 108.23 | J/mol×K | 6000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.13; 100.25] | kPa | [180.50; 285.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.36436e+01 | |||
| Coefficient B | -2.24325e+03 | |||
| Coefficient C | -3.71390e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 180.50 | |||
| Temperature range, max. | 285.40 | |||
| Pvap | 0.13 | kPa | 180.50 | Calculated Property |
| Pvap | 0.44 | kPa | 192.16 | Calculated Property |
| Pvap | 1.20 | kPa | 203.81 | Calculated Property |
| Pvap | 2.90 | kPa | 215.47 | Calculated Property |
| Pvap | 6.27 | kPa | 227.12 | Calculated Property |
| Pvap | 12.41 | kPa | 238.78 | Calculated Property |
| Pvap | 22.79 | kPa | 250.43 | Calculated Property |
| Pvap | 39.30 | kPa | 262.09 | Calculated Property |
| Pvap | 64.24 | kPa | 273.74 | Calculated Property |
| Pvap | 100.25 | kPa | 285.40 | Calculated Property |
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