| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | -3009.40 ± 1.40 | kJ/mol | NIST |
| ΔfH°gas | -1033.24 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | -1353.70 ± 1.40 | kJ/mol | NIST |
| ΔfusH° | 21.73 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 186.00 | kJ/mol | NIST |
| ΔvapH° | 113.18 | kJ/mol | Relay (1.0) Calculated Property |
| log10WS | [1.09; 1.09] |
|
|
| log10WS | 1.09 | Aq. Solubility Prediction | |
| log10WS | 1.09 | Estimated Solubility | |
| logPoct/wat | -3.585 | Crippen Calculated Property | |
| McVol | 130.620 | ml/mol | McGowan Calculated Property |
| Pc | 6830.13 | kPa | Joback Calculated Property |
| Tboil | 681.00 | K | Relay (1.0) Calculated Property |
| Tc | 979.66 | K | Relay (1.0) Calculated Property |
| Tfus | [361.25; 434.05] | K |
|
| Tfus | 371.70 | K | Solid-liquid phase equilibria in binary mixtures of functionalized ionic liquids with sugar alcohols: New experimental data and modelling |
| Tfus | 371.70 | K | Solubility data and modeling for sugar alcohols in ionic liquids |
| Tfus | 372.85 | K | Artificial neural networks as a supporting tool for compatibility study based on thermogravimetric data |
| Tfus | Outlier 434.05 | K | Aq. Solubility Prediction |
| Tfus | 366.50 ± 0.60 | K | NIST |
| Tfus | 371.85 ± 0.50 | K | NIST |
| Tfus | 361.25 ± 0.50 | K | NIST |
| Tfus | 367.45 ± 1.00 | K | NIST |
| Vc | 0.523 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate 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 | [423.48; 456.45] | J/mol×K | [888.00; 1092.90] | |
| Cp,gas | 423.48 | J/mol×K | 888.00 | Joback Calculated Property |
| Cp,gas | 429.90 | J/mol×K | 922.15 | Joback Calculated Property |
| Cp,gas | 435.91 | J/mol×K | 956.30 | Joback Calculated Property |
| Cp,gas | 441.54 | J/mol×K | 990.45 | Joback Calculated Property |
| Cp,gas | 446.82 | J/mol×K | 1024.60 | Joback Calculated Property |
| Cp,gas | 451.78 | J/mol×K | 1058.75 | Joback Calculated Property |
| Cp,gas | 456.45 | J/mol×K | 1092.90 | Joback Calculated Property |
| Cp,solid | 241.43 | J/mol×K | 298.15 | NIST |
| η | [4.5232902e-09; 0.0005812] | Pa×s | [462.30; 888.00] | |
| η | 0.0005812 | Pa×s | 462.30 | Joback Calculated Property |
| η | 0.0000222 | Pa×s | 533.25 | Joback Calculated Property |
| η | 0.0000018 | Pa×s | 604.20 | Joback Calculated Property |
| η | 0.0000003 | Pa×s | 675.15 | Joback Calculated Property |
| η | 5.1362493e-08 | Pa×s | 746.10 | Joback Calculated Property |
| η | 1.3716255e-08 | Pa×s | 817.05 | Joback Calculated Property |
| η | 4.5232902e-09 | Pa×s | 888.00 | Joback Calculated Property |
| ΔfusH | [30.20; 30.35] | kJ/mol | [235.00; 366.50] | |
| ΔfusH | 30.35 | kJ/mol | 235.00 | NIST |
| ΔfusH | 30.20 | kJ/mol | 366.50 | NIST |
| ΔfusH | 30.20 | kJ/mol | 366.50 | NIST |
| ΔvapH | 132.40 ± 2.00 | kJ/mol | 479.00 | NIST |
| Pvap | [1.31; 65.00] | kPa | [523.15; 623.15] | |
| Pvap | 1.31 | kPa | 523.15 | Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols |
| Pvap | 4.49 | kPa | 548.15 | Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols |
| Pvap | 12.30 | kPa | 573.15 | Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols |
| Pvap | 30.00 | kPa | 598.15 | Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols |
| Pvap | 65.00 | kPa | 623.15 | Vapor Pressures and Evaporation Studies of Sugars and Sugar Alcohols |
| ΔfusS | 82.50 | J/mol×K | 366.50 | NIST |
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