| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfH°gas | -239.97 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 16.00 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [50.40; 53.30] | kJ/mol |
|
| ΔvapH° | 53.30 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 50.40 ± 1.30 | kJ/mol | NIST |
| IE | 8.63 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.86 | Aq. Solubility Prediction | |
| logPoct/wat | 1.205 | Crippen Calculated Property | |
| McVol | 93.170 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| Inp | [1003.00; 1074.00] |
|
|
| Inp | 1008.00 | NIST | |
| Inp | 1041.40 | NIST | |
| Inp | 1047.60 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1041.30 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1072.00 | NIST | |
| I | [1628.00; 1705.00] |
|
|
| I | 1699.00 | NIST | |
| I | 1636.00 | NIST | |
| I | 1660.00 | NIST | |
| I | 1633.00 | NIST | |
| I | 1663.00 | NIST | |
| I | 1704.00 | NIST | |
| I | 1658.00 | NIST | |
| I | 1663.00 | NIST | |
| I | 1674.00 | NIST | |
| I | 1674.00 | NIST | |
| I | 1652.00 | NIST | |
| I | 1680.00 | NIST | |
| I | 1701.00 | NIST | |
| I | Outlier 1628.00 | NIST | |
| I | 1653.00 | NIST | |
| I | 1669.00 | NIST | |
| I | 1670.00 | NIST | |
| I | 1675.00 | NIST | |
| I | 1677.00 | NIST | |
| I | 1682.00 | NIST | |
| I | 1682.00 | NIST | |
| I | 1686.00 | NIST | |
| I | 1689.00 | NIST | |
| I | 1670.00 | NIST | |
| I | 1703.00 | NIST | |
| I | 1705.00 | NIST | |
| I | 1703.00 | NIST | |
| I | 1667.00 | NIST | |
| I | 1665.00 | NIST | |
| I | Outlier 1628.00 | NIST | |
| I | 1677.00 | NIST | |
| I | 1670.00 | NIST | |
| I | 1665.00 | NIST | |
| I | 1680.00 | NIST | |
| I | 1633.00 | NIST | |
| I | 1674.00 | NIST | |
| Tboil | [470.15; 470.20] | K |
|
| Tboil | 470.20 | K | NIST |
| Tboil | 470.15 ± 1.00 | K | NIST |
| Tc | 790.07 | K | Relay (1.0) Calculated Property |
| Tfus | [269.65; 272.30] | K |
|
| Tfus | 272.30 | K | Vapor Pressures and Gibbs Energies of Formation of the Three Hydroxybenzaldehydes |
| Tfus | 269.65 | K | Aq. Solubility Prediction |
Cheméo can also estimate Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor 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 | [197.64; 242.09] | J/mol×K | [515.52; 749.54] | |
| Cp,gas | 197.64 | J/mol×K | 515.52 | Joback Calculated Property |
| Cp,gas | 206.73 | J/mol×K | 554.52 | Joback Calculated Property |
| Cp,gas | 215.05 | J/mol×K | 593.53 | Joback Calculated Property |
| Cp,gas | 222.66 | J/mol×K | 632.53 | Joback Calculated Property |
| Cp,gas | 229.65 | J/mol×K | 671.53 | Joback Calculated Property |
| Cp,gas | 236.10 | J/mol×K | 710.54 | Joback Calculated Property |
| Cp,gas | 242.09 | J/mol×K | 749.54 | Joback Calculated Property |
| η | [0.0000996; 0.0031017] | Pa×s | [348.79; 515.52] | |
| η | 0.0031017 | Pa×s | 348.79 | Joback Calculated Property |
| η | 0.0014153 | Pa×s | 376.58 | Joback Calculated Property |
| η | 0.0007194 | Pa×s | 404.37 | Joback Calculated Property |
| η | 0.0003989 | Pa×s | 432.15 | Joback Calculated Property |
| η | 0.0002375 | Pa×s | 459.94 | Joback Calculated Property |
| η | 0.0001500 | Pa×s | 487.73 | Joback Calculated Property |
| η | 0.0000996 | Pa×s | 515.52 | Joback Calculated Property |
| ΔfusH | 13.30 | kJ/mol | 278.70 | NIST |
| ΔvapH | [30.60; 63.30] | kJ/mol | [298.15; 426.50] | |
| ΔvapH | 63.30 | kJ/mol | 298.15 | Thermochemical studies on salicylaldehyde and salicylamide |
| ΔvapH | 49.60 | kJ/mol | 388.00 | NIST |
| ΔvapH | 30.60 | kJ/mol | 426.50 | NIST |
| ρl | 1162.50 | kg/m3 | 298.15 | Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [350.11; 497.57] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.71544e+01 | |||
| Coefficient B | -5.86328e+03 | |||
| Coefficient C | -2.48700e+00 | |||
| Temperature range, min. | 350.11 | |||
| Temperature range, max. | 497.57 | |||
| Pvap | 1.33 | kPa | 350.11 | Calculated Property |
| Pvap | 2.85 | kPa | 366.49 | Calculated Property |
| Pvap | 5.70 | kPa | 382.88 | Calculated Property |
| Pvap | 10.77 | kPa | 399.26 | Calculated Property |
| Pvap | 19.36 | kPa | 415.65 | Calculated Property |
| Pvap | 33.26 | kPa | 432.03 | Calculated Property |
| Pvap | 54.92 | kPa | 448.42 | Calculated Property |
| Pvap | 87.53 | kPa | 464.80 | Calculated Property |
| Pvap | 135.10 | kPa | 481.19 | Calculated Property |
| Pvap | 202.63 | kPa | 497.57 | Calculated Property |
| Pvap | [6.53e-03; 4990.01] | kPa | [266.15; 680.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.31045e+01 | |||
| Coefficient B | -8.28909e+03 | |||
| Coefficient C | -8.49841e+00 | |||
| Coefficient D | 6.54847e-06 | |||
| Temperature range, min. | 266.15 | |||
| Temperature range, max. | 680.00 | |||
| Pvap | 6.53e-03 | kPa | 266.15 | Calculated Property |
| Pvap | 0.20 | kPa | 312.13 | Calculated Property |
| Pvap | 2.27 | kPa | 358.12 | Calculated Property |
| Pvap | 14.25 | kPa | 404.10 | Calculated Property |
| Pvap | 59.96 | kPa | 450.08 | Calculated Property |
| Pvap | 192.31 | kPa | 496.07 | Calculated Property |
| Pvap | 510.73 | kPa | 542.05 | Calculated Property |
| Pvap | 1187.94 | kPa | 588.03 | Calculated Property |
| Pvap | 2516.09 | kPa | 634.02 | Calculated Property |
| Pvap | 4990.01 | kPa | 680.00 | Calculated Property |
Find more compounds similar to BENZALDEHYDE, 2-HYDROXY-.
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