| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -5045.40 ± 0.59 | kJ/mol | NIST |
| ΔfH°gas | -59.85 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°liquid | -103.60 ± 0.75 | kJ/mol | NIST |
| ΔfusH° | 7.56 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [42.00; 42.00] | kJ/mol |
|
| ΔvapH° | 42.00 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 42.00 ± 0.20 | kJ/mol | NIST |
| IE | [8.41; 8.47] | eV |
|
| IE | 8.41 | eV | NIST |
| IE | 8.47 ± 0.02 | eV | NIST |
| logPoct/wat | 2.897 | Crippen Calculated Property | |
| McVol | 108.420 | ml/mol | McGowan Calculated Property |
| Inp | [859.00; 899.70] |
|
|
| Inp | 873.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 865.90 | NIST | |
| Inp | 861.80 | NIST | |
| Inp | Outlier 899.70 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 870.00 | NIST | |
| Tboil | [409.00; 411.40] | K |
|
| Tboil | 409.20 | K | NIST |
| Tboil | 410.00 ± 0.50 | K | NIST |
| Tboil | 410.20 ± 0.20 | K | NIST |
| Tboil | 410.32 ± 0.20 | K | NIST |
| Tboil | 410.24 ± 0.20 | K | NIST |
| Tboil | 410.24 ± 0.20 | K | NIST |
| Tboil | 410.22 ± 0.20 | K | NIST |
| Tboil | 410.00 ± 1.00 | K | NIST |
| Tboil | 409.00 ± 4.00 | K | NIST |
| Tboil | 411.40 ± 6.00 | K | NIST |
| Tboil | 411.00 ± 5.00 | K | NIST |
| Tboil | 411.00 ± 5.00 | K | NIST |
| Tboil | 409.00 ± 4.00 | K | NIST |
| Tfus | [179.75; 180.71] | K |
|
| Tfus | 180.71 ± 0.02 | K | NIST |
| Tfus | 180.67 ± 0.05 | K | NIST |
| Tfus | 180.71 ± 0.02 | K | NIST |
| Tfus | 179.75 ± 0.20 | K | NIST |
| Tfus | 180.00 ± 0.50 | K | NIST |
| Tfus | 180.47 ± 0.40 | K | NIST |
| Tfus | 179.93 ± 0.40 | K | NIST |
| Tfus | 180.47 ± 0.10 | K | NIST |
| Tfus | 180.49 ± 0.06 | K | NIST |
| Tfus | 179.93 ± 0.50 | K | NIST |
| Tfus | 180.40 ± 0.30 | K | NIST |
| Tfus | 179.93 ± 0.10 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, 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 |
|---|---|---|---|---|
| Cp,gas | [200.71; 284.49] | J/mol×K | [413.30; 622.66] | |
| Cp,gas | 200.71 | J/mol×K | 413.30 | Joback Calculated Property |
| Cp,gas | 216.71 | J/mol×K | 448.19 | Joback Calculated Property |
| Cp,gas | 231.85 | J/mol×K | 483.09 | Joback Calculated Property |
| Cp,gas | 246.17 | J/mol×K | 517.98 | Joback Calculated Property |
| Cp,gas | 259.69 | J/mol×K | 552.87 | Joback Calculated Property |
| Cp,gas | 272.46 | J/mol×K | 587.76 | Joback Calculated Property |
| Cp,gas | 284.49 | J/mol×K | 622.66 | Joback Calculated Property |
| Cp,liquid | 203.80 | J/mol×K | 298.15 | NIST |
| η | [0.0002403; 0.0068897] | Pa×s | [201.90; 413.30] | |
| η | 0.0068897 | Pa×s | 201.90 | Joback Calculated Property |
| η | 0.0025992 | Pa×s | 237.13 | Joback Calculated Property |
| η | 0.0012618 | Pa×s | 272.37 | Joback Calculated Property |
| η | 0.0007229 | Pa×s | 307.60 | Joback Calculated Property |
| η | 0.0004644 | Pa×s | 342.83 | Joback Calculated Property |
| η | 0.0003239 | Pa×s | 378.07 | Joback Calculated Property |
| η | 0.0002403 | Pa×s | 413.30 | Joback Calculated Property |
Find more compounds similar to Cyclohexane, ethylidene-.
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