| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5580 | Relay (1.0) Calculated Property | |
| ΔfG° | -133.67 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -223.60 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 16.00 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [98.20; 102.50] | kJ/mol |
|
| ΔsubH° | 102.50 ± 0.50 | kJ/mol | NIST |
| ΔsubH° | 99.70 ± 0.40 | kJ/mol | NIST |
| ΔsubH° | 98.20 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | 70.00 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.32 ± 0.02 | eV | NIST |
| log10WS | [-0.96; -0.96] |
|
|
| log10WS | -0.96 | Aq. Solubility Prediction | |
| log10WS | -0.96 | Estimated Solubility | |
| logPoct/wat | 1.205 | Crippen Calculated Property | |
| McVol | 93.170 | ml/mol | McGowan Calculated Property |
| Pc | 5602.57 | kPa | Joback Calculated Property |
| Inp | [1302.00; 1324.00] |
|
|
| Inp | 1318.60 | NIST | |
| Inp | 1320.80 | NIST | |
| Inp | 1320.00 | NIST | |
| Inp | 1320.00 | NIST | |
| Inp | 1318.00 | NIST | |
| Inp | Outlier 1302.00 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1317.00 | NIST | |
| Inp | 1324.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1318.00 | NIST | |
| Inp | 1323.00 | NIST | |
| Inp | 1320.00 | NIST | |
| Inp | 1323.00 | NIST | |
| Inp | 1318.60 | NIST | |
| Inp | Outlier 1302.00 | NIST | |
| Ip | [2958.00; 2958.00] |
|
|
| Ip | 2958.00 | NIST | |
| Ip | 2958.00 | NIST | |
| Tboil | 530.64 | K | Relay (1.0) Calculated Property |
| Tc | 786.50 | K | Relay (1.0) Calculated Property |
| Tfus | [387.00; 390.48] | K |
|
| Tfus | 387.00 | K | Measurement and modeling for solubility of 3-hydroxybenzaldehyde and its mixture with 4-hydroxybenzaldehyde in supercritical carbon dioxide |
| Tfus | 390.20 | K | Vapor Pressures and Gibbs Energies of Formation of the Three Hydroxybenzaldehydes |
| Tfus | 390.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 390.48 | K | Aq. Solubility Prediction |
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 | [118.52; 275.14] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -3.49000e+01 | |||
| Coefficient B | 7.19000e-01 | |||
| Coefficient C | -6.37560e-04 | |||
| Coefficient D | 2.28600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 118.52 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 149.79 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 175.91 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 197.59 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 215.57 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 230.56 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 243.29 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 254.48 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 264.86 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 275.14 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0010220; 0.0000876] | Pa×s | [389.46; 524.88] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.64080e+01 | |||
| Coefficient B | 3.70839e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 389.46 | |||
| Temperature range, max. | 524.88 | |||
| η | 0.0010220 | Pa×s | 389.46 | Calculated Property |
| η | 0.0007171 | Pa×s | 404.50 | Calculated Property |
| η | 0.0005162 | Pa×s | 419.55 | Calculated Property |
| η | 0.0003801 | Pa×s | 434.60 | Calculated Property |
| η | 0.0002857 | Pa×s | 449.65 | Calculated Property |
| η | 0.0002187 | Pa×s | 464.69 | Calculated Property |
| η | 0.0001703 | Pa×s | 479.74 | Calculated Property |
| η | 0.0001346 | Pa×s | 494.79 | Calculated Property |
| η | 0.0001079 | Pa×s | 509.83 | Calculated Property |
| η | 0.0000876 | Pa×s | 524.88 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.10; 4998.66] | kPa | [390.15; 844.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 6.33034e+01 | |||
| Coefficient B | -1.08755e+04 | |||
| Coefficient C | -6.35445e+00 | |||
| Coefficient D | 1.28665e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 390.15 | |||
| Temperature range, max. | 844.00 | |||
| Pvap | 0.10 | kPa | 390.15 | Calculated Property |
| Pvap | 1.20 | kPa | 440.58 | Calculated Property |
| Pvap | 8.08 | kPa | 491.01 | Calculated Property |
| Pvap | 36.51 | kPa | 541.43 | Calculated Property |
| Pvap | 123.56 | kPa | 591.86 | Calculated Property |
| Pvap | 336.94 | kPa | 642.29 | Calculated Property |
| Pvap | 779.67 | kPa | 692.72 | Calculated Property |
| Pvap | 1589.01 | kPa | 743.14 | Calculated Property |
| Pvap | 2931.68 | kPa | 793.57 | Calculated Property |
| Pvap | 4998.66 | kPa | 844.00 | Calculated Property |
| Pvap | [0.13; 101.63] | kPa | [394.30; 583.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.68576e+01 | |||
| Coefficient B | -6.56685e+03 | |||
| Coefficient C | -4.63290e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 394.30 | |||
| Temperature range, max. | 583.00 | |||
| Pvap | 0.13 | kPa | 394.30 | Calculated Property |
| Pvap | 0.39 | kPa | 415.27 | Calculated Property |
| Pvap | 1.02 | kPa | 436.23 | Calculated Property |
| Pvap | 2.40 | kPa | 457.20 | Calculated Property |
| Pvap | 5.21 | kPa | 478.17 | Calculated Property |
| Pvap | 10.54 | kPa | 499.13 | Calculated Property |
| Pvap | 20.02 | kPa | 520.10 | Calculated Property |
| Pvap | 36.02 | kPa | 541.07 | Calculated Property |
| Pvap | 61.80 | kPa | 562.03 | Calculated Property |
| Pvap | 101.63 | kPa | 583.00 | Calculated Property |
Find more compounds similar to Benzaldehyde, 4-hydroxy-.
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