| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | -6109.10 | kJ/mol | NIST |
| ΔfH°gas | -334.97 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 27.66 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 85.99 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 7.97 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.15 | Aq. Solubility Prediction | |
| logPoct/wat | 2.611 | Crippen Calculated Property | |
| McVol | 159.820 | ml/mol | McGowan Calculated Property |
| Pc | 3673.09 | kPa | Joback Calculated Property |
| Inp | [1650.00; 1702.00] |
|
|
| Inp | 1702.00 | NIST | |
| Inp | 1650.00 | NIST | |
| Inp | 1650.00 | NIST | |
| Inp | 1650.00 | NIST | |
| Inp | 1655.00 | NIST | |
| Inp | 1650.00 | NIST | |
| Inp | 1660.00 | NIST | |
| Inp | 1655.00 | NIST | |
| Inp | 1702.00 | NIST | |
| Tboil | 582.78 | K | Relay (1.0) Calculated Property |
| Tc | 886.56 | K | Relay (1.0) Calculated Property |
| Tfus | [314.49; 315.35] | K |
|
| Tfus | 314.90 | K | The use of organic calibration standards in the enthalpy calibration of differential scanning calorimeters |
| Tfus | Outlier 315.35 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 314.83 ± 0.25 | K | NIST |
| Tfus | 314.84 ± 0.20 | K | NIST |
| Tfus | 314.82 ± 0.20 | K | NIST |
| Tfus | 314.49 ± 0.20 | K | NIST |
| Tfus | 314.53 ± 1.00 | K | NIST |
| Tfus | 315.00 ± 1.50 | K | NIST |
| Ttriple | 314.75 | K | Investigation of the melting behavior of the reference materials biphenyl and phenyl salicylate by a new type adiabatic scanning calorimeter |
Cheméo can also estimate 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 | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 446.20 | K | 1.60 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [199.97; 483.49] | 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 | -6.02500e+01 | |||
| Coefficient B | 1.18080e+00 | |||
| Coefficient C | -9.07560e-04 | |||
| Coefficient D | 2.70500e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 199.97 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 255.88 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 303.69 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 344.26 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 378.44 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 407.09 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 431.06 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 451.22 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 468.41 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 483.49 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0337522; 0.0000189] | Pa×s | [314.77; 660.42] |
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 | -1.76970e+01 | |||
| Coefficient B | 4.50386e+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. | 314.77 | |||
| Temperature range, max. | 660.42 | |||
| η | 0.0337522 | Pa×s | 314.77 | Calculated Property |
| η | 0.0071216 | Pa×s | 353.18 | Calculated Property |
| η | 0.0020389 | Pa×s | 391.58 | Calculated Property |
| η | 0.0007299 | Pa×s | 429.99 | Calculated Property |
| η | 0.0003092 | Pa×s | 468.39 | Calculated Property |
| η | 0.0001492 | Pa×s | 506.80 | Calculated Property |
| η | 0.0000798 | Pa×s | 545.20 | Calculated Property |
| η | 0.0000463 | Pa×s | 583.61 | Calculated Property |
| η | 0.0000288 | Pa×s | 622.02 | Calculated Property |
| η | 0.0000189 | Pa×s | 660.42 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.03] | N/m | [317.15; 446.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 7.18594e-02 | |||
| Coefficient B | -9.76000e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 317.15 | |||
| Temperature range, max. | 446.15 | |||
| γ | 0.04 | N/m | 317.15 | Calculated Property |
| γ | 0.04 | N/m | 331.48 | Calculated Property |
| γ | 0.04 | N/m | 345.82 | Calculated Property |
| γ | 0.04 | N/m | 360.15 | Calculated Property |
| γ | 0.04 | N/m | 374.48 | Calculated Property |
| γ | 0.03 | N/m | 388.82 | Calculated Property |
| γ | 0.03 | N/m | 403.15 | Calculated Property |
| γ | 0.03 | N/m | 417.48 | Calculated Property |
| γ | 0.03 | N/m | 431.82 | Calculated Property |
| γ | 0.03 | N/m | 446.15 | Calculated Property |
Find more compounds similar to Benzoic acid, 2-hydroxy-, phenyl ester.
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