| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.8416 | Relay (1.0) Calculated Property | |
| ΔfH°gas | -541.58 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 41.40 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 98.46 | kJ/mol | Relay (1.0) Calculated Property |
| log10WS | -5.65 | Aq. Solubility Prediction | |
| logPoct/wat | 4.000 | Crippen Calculated Property | |
| McVol | 245.930 | ml/mol | McGowan Calculated Property |
| Pc | 1758.02 | kPa | Joback Calculated Property |
| Inp | [378.40; 2358.90] |
|
|
| Inp | 2327.00 | NIST | |
| Inp | 2358.90 | NIST | |
| Inp | 2271.00 | NIST | |
| Inp | 2350.00 | NIST | |
| Inp | 2287.00 | NIST | |
| Inp | 2287.00 | NIST | |
| Inp | 2290.00 | NIST | |
| Inp | 2290.00 | NIST | |
| Inp | 2327.00 | NIST | |
| Inp | Outlier 378.40 | NIST | |
| Inp | 2327.00 | NIST | |
| Inp | 2358.90 | NIST | |
| Inp | Outlier 378.40 | NIST | |
| Tboil | 642.60 | K | Relay (1.0) Calculated Property |
| Tc | 889.27 | K | Relay (1.0) Calculated Property |
| Tfus | 503.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.908 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Standard Gibbs free energy of formation, 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 |
|---|---|---|---|---|
| ΔvapH | [89.00; 109.80] | kJ/mol | [298.00; 466.00] | |
| ΔvapH | 109.80 | kJ/mol | 298.00 | A Comparison of Results by Correlation Gas Chromatography with Another Gas Chromatographic Retention Time Technique. The Effects of Retention Time Coincidence on Vaporization Enthalpy and Vapor Pressure |
| ΔvapH | 89.00 | kJ/mol | 466.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [329.26; 775.68] | 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 | -1.70760e+01 | |||
| Coefficient B | 1.48192e+00 | |||
| Coefficient C | -8.15960e-04 | |||
| Coefficient D | 1.26800e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 329.26 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 410.68 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 483.22 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 547.27 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 603.22 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 651.49 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 692.47 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 726.56 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 754.16 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 775.68 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0004377; 0.0000765] | Pa×s | [503.15; 722.00] |
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 | -1.34868e+01 | |||
| Coefficient B | 2.89450e+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. | 503.15 | |||
| Temperature range, max. | 722.00 | |||
| η | 0.0004377 | Pa×s | 503.15 | Calculated Property |
| η | 0.0003357 | Pa×s | 527.47 | Calculated Property |
| η | 0.0002636 | Pa×s | 551.78 | Calculated Property |
| η | 0.0002112 | Pa×s | 576.10 | Calculated Property |
| η | 0.0001723 | Pa×s | 600.42 | Calculated Property |
| η | 0.0001429 | Pa×s | 624.74 | Calculated Property |
| η | 0.0001201 | Pa×s | 649.05 | Calculated Property |
| η | 0.0001022 | Pa×s | 673.37 | Calculated Property |
| η | 0.0000880 | Pa×s | 697.69 | Calculated Property |
| η | 0.0000765 | Pa×s | 722.00 | Calculated Property |
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