| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4758 | Relay (1.0) Calculated Property | |
| ΔfG° | -120.09 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -325.81 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 8.20 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 71.66 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.63 | eV | Relay (1.0) Calculated Property |
| log10WS | [-1.29; -1.29] |
|
|
| log10WS | -1.29 | Aq. Solubility Prediction | |
| log10WS | -1.29 | Estimated Solubility | |
| logPoct/wat | 2.092 | Crippen Calculated Property | |
| McVol | 118.590 | ml/mol | McGowan Calculated Property |
| Pc | 3722.56 | kPa | Joback Calculated Property |
| Inp | [1131.40; 1155.00] |
|
|
| Inp | 1131.40 | NIST | |
| Inp | 1147.30 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1133.00 | NIST | |
| Inp | 1133.00 | NIST | |
| I | [1640.80; 1700.00] |
|
|
| I | 1640.80 | NIST | |
| I | 1700.00 | NIST | |
| I | 1640.80 | NIST | |
| Tboil | 477.18 | K | Relay (1.0) Calculated Property |
| Tc | 698.90 | K | Relay (1.0) Calculated Property |
| Tfus | 291.52 | K | Aq. Solubility Prediction |
| Ttriple | 263.56 | K | Heat capacities of selected cycloalcohols |
Cheméo can also estimate Critical Volume for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [274.72; 362.56] | J/mol×K | [502.71; 707.64] | |
| Cp,gas | 274.72 | J/mol×K | 502.71 | Joback Calculated Property |
| Cp,gas | 291.42 | J/mol×K | 536.87 | Joback Calculated Property |
| Cp,gas | 307.29 | J/mol×K | 571.02 | Joback Calculated Property |
| Cp,gas | 322.32 | J/mol×K | 605.18 | Joback Calculated Property |
| Cp,gas | 336.54 | J/mol×K | 639.33 | Joback Calculated Property |
| Cp,gas | 349.95 | J/mol×K | 673.49 | Joback Calculated Property |
| Cp,gas | 362.56 | J/mol×K | 707.64 | Joback Calculated Property |
| η | [0.0001108; 0.1481500] | Pa×s | [241.08; 502.71] | |
| η | 0.1481500 | Pa×s | 241.08 | Joback Calculated Property |
| η | 0.0178103 | Pa×s | 284.69 | Joback Calculated Property |
| η | 0.0037588 | Pa×s | 328.29 | Joback Calculated Property |
| η | 0.0011425 | Pa×s | 371.89 | Joback Calculated Property |
| η | 0.0004459 | Pa×s | 415.50 | Joback Calculated Property |
| η | 0.0002081 | Pa×s | 459.10 | Joback Calculated Property |
| η | 0.0001108 | Pa×s | 502.71 | Joback Calculated Property |
| ΔfusH | [1.97; 2.12] | kJ/mol | [261.30; 297.10] | |
| ΔfusH | 2.12 | kJ/mol | 261.30 | NIST |
| ΔfusH | 2.02 | kJ/mol | 291.20 | NIST |
| ΔfusH | 2.06 | kJ/mol | 295.00 | NIST |
| ΔfusH | 2.06 | kJ/mol | 295.00 | NIST |
| ΔfusH | 1.97 | kJ/mol | 297.10 | NIST |
| ΔfusS | [6.98; 8.11] | J/mol×K | [261.30; 295.00] | |
| ΔfusS | 8.11 | J/mol×K | 261.30 | NIST |
| ΔfusS | 6.98 | J/mol×K | 295.00 | NIST |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 380.20 | K | 2.90 | NIST |
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