| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 747.90 | kJ/mol | NIST |
| BasG | 712.00 | kJ/mol | NIST |
| IE | [9.89; 10.58] | eV |
|
| IE | 9.89 | eV | NIST |
| IE | 10.06 ± 0.03 | eV | NIST |
| IE | 10.03 | eV | NIST |
| IE | 10.58 ± 0.05 | eV | NIST |
| logPoct/wat | -1.184 | Crippen Calculated Property | |
| Pc | 6600.00 | kPa | Air Liquide Gas Encyclopedia |
| Ptriple | 2.98 | kPa | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Tboil | 210.67 | K | Air Liquide Gas Encyclopedia |
| Tc | [373.00; 373.05] | K |
|
| Tc | 373.00 | K | Mathews (1972), critical constants of inorganic substances Compiled value |
| Tc | 373.05 | K | Air Liquide Gas Encyclopedia |
| Tfus | 156.15 | K | Air Liquide Gas Encyclopedia |
| Ttriple | 156.24 | K | Staveley, Lobo and Calado (1981), triple points Compiled value |
Cheméo can also estimate Critical Volume, Enthalpy of formation at standard conditions, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, 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 |
|---|---|---|---|---|
| ΔvapH | [16.68; 16.70] | kJ/mol | [210.00; 210.67] | |
| ΔvapH | 16.70 | kJ/mol | 210.00 | NIST |
| ΔvapH | 16.68 | kJ/mol | 210.67 | Air Liquide Gas Encyclopedia |
| ρg | 3.29 | kg/m3 | 288.15 | Air Liquide Gas Encyclopedia |
| ρl | 1634.00 | kg/m3 | 210.67 | Air Liquide Gas Encyclopedia |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [3.00; 6541.68] | kPa | [156.23; 373.00] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.38469e+01 | |||
| Coefficient B | -1.81915e+03 | |||
| Coefficient C | -1.35500e+01 | |||
| Temperature range, min. | 156.23 | |||
| Temperature range, max. | 373.00 | |||
| Pvap | 3.00 | kPa | 156.23 | Calculated Property |
| Pvap | 18.89 | kPa | 180.32 | Calculated Property |
| Pvap | 74.82 | kPa | 204.40 | Calculated Property |
| Pvap | 217.72 | kPa | 228.49 | Calculated Property |
| Pvap | 510.85 | kPa | 252.57 | Calculated Property |
| Pvap | 1025.35 | kPa | 276.66 | Calculated Property |
| Pvap | 1831.04 | kPa | 300.74 | Calculated Property |
| Pvap | 2989.19 | kPa | 324.83 | Calculated Property |
| Pvap | 4548.16 | kPa | 348.91 | Calculated Property |
| Pvap | 6541.68 | kPa | 373.00 | Calculated Property |
| Pvap | [0.13; 100.63] | kPa | [130.50; 211.10] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.25119e+01 | |||
| Coefficient B | -1.39674e+03 | |||
| Coefficient C | -3.43060e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 130.50 | |||
| Temperature range, max. | 211.10 | |||
| Pvap | 0.13 | kPa | 130.50 | Calculated Property |
| Pvap | 0.46 | kPa | 139.46 | Calculated Property |
| Pvap | 1.31 | kPa | 148.41 | Calculated Property |
| Pvap | 3.20 | kPa | 157.37 | Calculated Property |
| Pvap | 6.90 | kPa | 166.32 | Calculated Property |
| Pvap | 13.52 | kPa | 175.28 | Calculated Property |
| Pvap | 24.43 | kPa | 184.23 | Calculated Property |
| Pvap | 41.30 | kPa | 193.19 | Calculated Property |
| Pvap | 66.02 | kPa | 202.14 | Calculated Property |
| Pvap | 100.63 | kPa | 211.10 | Calculated Property |
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