| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | [-3053.00; -3024.70] | kJ/mol |
|
| ΔcH°solid | -3053.00 | kJ/mol | NIST |
| ΔcH°solid | -3045.70 | kJ/mol | NIST |
| ΔcH°solid | -3025.00 ± 2.00 | kJ/mol | NIST |
| ΔcH°solid | -3024.70 ± 1.80 | kJ/mol | NIST |
| ΔfH°gas | -1019.23 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | [-1337.50; -1337.20] | kJ/mol |
|
| ΔfH°solid | -1337.50 | kJ/mol | NIST |
| ΔfH°solid | -1337.20 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 54.69 | kJ/mol | Heat Capacities and Nonisothermal Thermal Decomposition Reaction Kinetics of d-Mannitol |
| ΔsubH° | 202.00 | kJ/mol | NIST |
| ΔvapH° | 112.41 | kJ/mol | Relay (1.0) Calculated Property |
| log10WS | 0.06 | Estimated Solubility | |
| logPoct/wat | -3.585 | Crippen Calculated Property | |
| McVol | 130.620 | ml/mol | McGowan Calculated Property |
| Pc | 6830.13 | kPa | Joback Calculated Property |
| S°solid,1 bar | [238.50; 253.10] | J/mol×K |
|
| S°solid,1 bar | 238.50 | J/mol×K | NIST |
| S°solid,1 bar | 253.10 | J/mol×K | NIST |
| Tboil | 678.50 | K | Relay (1.0) Calculated Property |
| Tc | 956.29 | K | Relay (1.0) Calculated Property |
| Tfus | [435.00; 440.62] | K |
|
| Tfus | 440.62 | K | Heat capacities of some sugar alcohols as phase change materials for thermal energy storage applications |
| Tfus | Outlier 435.00 | K | Nanocalorimetry measurements of metastable states |
| Tfus | 438.88 | K | Cycling stability of D-mannitol when used as phase change material for thermal storage applications |
| Tfus | 439.13 | K | KDB |
| Tfus | 439.10 ± 0.10 | K | NIST |
| Tfus | 439.00 ± 1.00 | K | NIST |
| Tfus | 439.20 ± 0.20 | K | NIST |
| Tfus | 439.13 ± 0.20 | K | NIST |
| Tfus | 439.20 ± 0.20 | K | NIST |
| Vc | 0.511 | 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 | [423.52; 456.48] | J/mol×K | [888.20; 1093.15] | |
| Cp,gas | 423.52 | J/mol×K | 888.20 | Joback Calculated Property |
| Cp,gas | 429.94 | J/mol×K | 922.36 | Joback Calculated Property |
| Cp,gas | 435.95 | J/mol×K | 956.52 | Joback Calculated Property |
| Cp,gas | 441.58 | J/mol×K | 990.67 | Joback Calculated Property |
| Cp,gas | 446.86 | J/mol×K | 1024.83 | Joback Calculated Property |
| Cp,gas | 451.81 | J/mol×K | 1058.99 | Joback Calculated Property |
| Cp,gas | 456.48 | J/mol×K | 1093.15 | Joback Calculated Property |
| Cp,solid | [236.00; 244.80] | J/mol×K | [294.10; 303.00] | |
| Cp,solid | 236.00 | J/mol×K | 294.10 | NIST |
| Cp,solid | 239.00 | J/mol×K | 298.15 | NIST |
| Cp,solid | 244.80 | J/mol×K | 303.00 | NIST |
| η | [4.5102972e-09; 0.0005812] | Pa×s | [462.30; 888.20] | |
| η | 0.0005812 | Pa×s | 462.30 | Joback Calculated Property |
| η | 0.0000222 | Pa×s | 533.28 | Joback Calculated Property |
| η | 0.0000018 | Pa×s | 604.27 | Joback Calculated Property |
| η | 0.0000003 | Pa×s | 675.25 | Joback Calculated Property |
| η | 5.1223146e-08 | Pa×s | 746.23 | Joback Calculated Property |
| η | 1.3677470e-08 | Pa×s | 817.22 | Joback Calculated Property |
| η | 4.5102972e-09 | Pa×s | 888.20 | Joback Calculated Property |
| ΔfusH | [53.58; 56.10] | kJ/mol | [433.20; 439.10] | |
| ΔfusH | 53.58 | kJ/mol | 433.20 | NIST |
| ΔfusH | 53.58 | kJ/mol | 433.20 | NIST |
| ΔfusH | 54.69 | kJ/mol | 437.30 | NIST |
| ΔfusH | 56.10 | kJ/mol | 439.10 | NIST |
| ΔfusH | 56.10 | kJ/mol | 439.10 | NIST |
| ΔvapH | 135.60 ± 1.10 | kJ/mol | 479.50 | NIST |
| ΔfusS | [123.70; 127.80] | J/mol×K | [433.20; 439.10] | |
| ΔfusS | 123.70 | J/mol×K | 433.20 | NIST |
| ΔfusS | 123.70 | J/mol×K | 433.20 | NIST |
| ΔfusS | 127.80 | J/mol×K | 439.10 | NIST |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 568.20 | K | 0.50 | NIST |
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