| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfusH° | 28.32 | kJ/mol | High-pressure phase diagram of the drug mitotane in compressed and/or supercritical CO2 |
| log10WS | [-6.51; -6.51] |
|
|
| log10WS | -6.51 | Aq. Solubility Prediction | |
| log10WS | -6.51 | Estimated Solubility | |
| logPoct/wat | 5.929 | Crippen Calculated Property | |
| McVol | 209.560 | ml/mol | McGowan Calculated Property |
| Inp | [2116.00; 2146.00] |
|
|
| Inp | 2130.00 | NIST | |
| Inp | 2119.00 | NIST | |
| Inp | 2123.00 | NIST | |
| Inp | 2116.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2119.00 | NIST | |
| Inp | 2123.00 | NIST | |
| Inp | 2116.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2118.00 | NIST | |
| Inp | 2118.00 | NIST | |
| Inp | Outlier 2146.00 | NIST | |
| Inp | Outlier 2146.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2118.00 | NIST | |
| Inp | 2119.00 | NIST | |
| Inp | 2123.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Ip | [3104.00; 3120.00] |
|
|
| Ip | 3104.00 | NIST | |
| Ip | 3120.00 | NIST | |
| Ip | 3120.00 | NIST | |
| Ip | 3104.00 | NIST | |
| Tboil | 624.48 | K | Relay (1.0) Calculated Property |
| Tfus | 349.40 ± 0.20 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Enthalpy of formation at standard conditions, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, Ionization energy 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 | [246.05; 532.63] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -8.50000e-01 | |||
| Coefficient B | 1.09600e+00 | |||
| Coefficient C | -7.54120e-04 | |||
| Coefficient D | 1.91600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 246.05 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 300.99 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 348.74 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 389.91 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 425.10 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 454.92 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 479.98 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 500.88 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 518.23 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 532.63 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0039011; 0.0001358] | Pa×s | [349.40; 696.61] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.22835e+01 | |||
| Coefficient B | 2.35392e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 349.40 | |||
| Temperature range, max. | 696.61 | |||
| η | 0.0039011 | Pa×s | 349.40 | Calculated Property |
| η | 0.0019964 | Pa×s | 387.98 | Calculated Property |
| η | 0.0011533 | Pa×s | 426.56 | Calculated Property |
| η | 0.0007297 | Pa×s | 465.14 | Calculated Property |
| η | 0.0004953 | Pa×s | 503.72 | Calculated Property |
| η | 0.0003552 | Pa×s | 542.30 | Calculated Property |
| η | 0.0002662 | Pa×s | 580.88 | Calculated Property |
| η | 0.0002068 | Pa×s | 619.46 | Calculated Property |
| η | 0.0001655 | Pa×s | 658.03 | Calculated Property |
| η | 0.0001358 | Pa×s | 696.61 | Calculated Property |
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