| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6462 | Relay (1.0) Calculated Property | |
| ΔcH°solid | [-3910.00; -3896.70] | kJ/mol |
|
| ΔcH°solid | -3896.70 ± 0.80 | kJ/mol | NIST |
| ΔcH°solid | -3897.00 | kJ/mol | NIST |
| ΔcH°solid | -3905.00 | kJ/mol | NIST |
| ΔcH°solid | -3910.00 | kJ/mol | NIST |
| ΔfG° | -215.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -308.48 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 20.66 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [93.50; 99.00] | kJ/mol |
|
| ΔsubH° | 93.50 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 99.00 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 79.10 ± 0.30 | kJ/mol | NIST |
| IE | [8.26; 9.10] | eV |
|
| IE | 8.26 | eV | NIST |
| IE | 8.26 | eV | NIST |
| IE | 8.26 | eV | NIST |
| IE | 8.72 | eV | NIST |
| IE | 9.10 | eV | NIST |
| log10WS | -0.89 | Aq. Solubility Prediction | |
| logPoct/wat | 1.314 | Crippen Calculated Property | |
| McVol | 107.260 | ml/mol | McGowan Calculated Property |
| Pc | 3950.00 | kPa | Critical-Point Measurements for Phenylethanoic to 7-Phenylheptanoic Acids |
| Inp | [216.16; 1279.00] |
|
|
| Inp | 1269.00 | NIST | |
| Inp | 1254.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1251.00 | NIST | |
| Inp | 1248.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1265.00 | NIST | |
| Inp | 1246.00 | NIST | |
| Inp | 1248.00 | NIST | |
| Inp | 1265.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1265.00 | NIST | |
| Inp | 1240.00 | NIST | |
| Inp | 1246.20 | NIST | |
| Inp | 1265.90 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1256.00 | NIST | |
| Inp | 1267.00 | NIST | |
| Inp | 1265.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1270.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1252.00 | NIST | |
| Inp | 1279.00 | NIST | |
| Inp | 1251.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1252.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1236.00 | NIST | |
| Inp | 1236.00 | NIST | |
| Inp | 1236.00 | NIST | |
| Inp | 1264.00 | NIST | |
| Inp | 1268.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1276.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1249.00 | NIST | |
| Inp | 1233.00 | NIST | |
| Inp | 1230.00 | NIST | |
| Inp | 1212.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | Outlier 216.16 | NIST | |
| Inp | 1254.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1265.00 | NIST | |
| Inp | 1269.00 | NIST | |
| Inp | 1252.00 | NIST | |
| Inp | 1257.00 | NIST | |
| Inp | 1236.00 | NIST | |
| Inp | 1268.00 | NIST | |
| Inp | 1262.00 | NIST | |
| Inp | 1233.00 | NIST | |
| Inp | 1246.20 | NIST | |
| Inp | Outlier 216.16 | NIST | |
| I | [2519.00; 2610.00] |
|
|
| I | 2565.00 | NIST | |
| I | 2561.00 | NIST | |
| I | 2585.00 | NIST | |
| I | 2540.00 | NIST | |
| I | 2543.00 | NIST | |
| I | 2569.00 | NIST | |
| I | 2581.00 | NIST | |
| I | 2556.00 | NIST | |
| I | 2569.00 | NIST | |
| I | 2578.00 | NIST | |
| I | 2581.00 | NIST | |
| I | 2589.00 | NIST | |
| I | 2590.00 | NIST | |
| I | 2548.00 | NIST | |
| I | 2574.00 | NIST | |
| I | Outlier 2519.00 | NIST | |
| I | 2540.00 | NIST | |
| I | 2578.00 | NIST | |
| I | 2555.00 | NIST | |
| I | 2569.00 | NIST | |
| I | 2568.00 | NIST | |
| I | 2573.00 | NIST | |
| I | Outlier 2521.00 | NIST | |
| I | 2568.00 | NIST | |
| I | 2554.00 | NIST | |
| I | 2582.00 | NIST | |
| I | 2561.00 | NIST | |
| I | 2557.00 | NIST | |
| I | 2570.00 | NIST | |
| I | 2570.00 | NIST | |
| I | 2530.00 | NIST | |
| I | 2570.00 | NIST | |
| I | 2569.00 | NIST | |
| I | 2595.00 | NIST | |
| I | 2550.00 | NIST | |
| I | 2550.00 | NIST | |
| I | 2528.00 | NIST | |
| I | 2545.00 | NIST | |
| I | 2553.00 | NIST | |
| I | 2560.00 | NIST | |
| I | 2551.00 | NIST | |
| I | 2539.00 | NIST | |
| I | 2550.00 | NIST | |
| I | 2550.00 | NIST | |
| I | 2578.00 | NIST | |
| I | 2592.00 | NIST | |
| I | 2601.00 | NIST | |
| I | 2601.00 | NIST | |
| I | 2585.00 | NIST | |
| I | 2575.00 | NIST | |
| I | 2597.00 | NIST | |
| I | 2548.00 | NIST | |
| I | 2548.00 | NIST | |
| I | 2585.00 | NIST | |
| I | 2571.00 | NIST | |
| I | 2565.00 | NIST | |
| I | 2571.00 | NIST | |
| I | 2569.00 | NIST | |
| I | 2546.00 | NIST | |
| I | 2534.00 | NIST | |
| I | 2534.00 | NIST | |
| I | 2550.00 | NIST | |
| I | 2568.00 | NIST | |
| I | 2568.00 | NIST | |
| I | 2568.00 | NIST | |
| I | Outlier 2610.00 | NIST | |
| I | 2560.00 | NIST | |
| I | 2574.00 | NIST | |
| I | Outlier 2519.00 | NIST | |
| I | 2566.00 | NIST | |
| I | 2564.00 | NIST | |
| I | 2551.00 | NIST | |
| I | 2577.00 | NIST | |
| I | 2553.00 | NIST | |
| I | 2553.00 | NIST | |
| I | 2548.00 | NIST | |
| I | 2551.00 | NIST | |
| I | 2585.00 | NIST | |
| I | 2538.00 | NIST | |
| I | 2555.00 | NIST | |
| I | 2528.00 | NIST | |
| I | 2539.00 | NIST | |
| I | 2601.00 | NIST | |
| I | 2548.00 | NIST | |
| I | 2571.00 | NIST | |
| I | 2550.00 | NIST | |
| I | 2565.00 | NIST | |
| I | 2569.00 | NIST | |
| I | 2581.00 | NIST | |
| I | Outlier 2519.00 | NIST | |
| I | 2568.00 | NIST | |
| I | 2554.00 | NIST | |
| I | 2570.00 | NIST | |
| I | 2560.00 | NIST | |
| I | 2551.00 | NIST | |
| Tboil | 538.70 | K | NIST |
| Tc | 763.82 | K | Relay (1.0) Calculated Property |
| Tfus | [348.00; 350.32] | K |
|
| Tfus | 350.32 | K | Aq. Solubility Prediction |
| Tfus | 348.00 ± 2.00 | K | NIST |
| Tfus | 349.15 ± 1.00 | K | NIST |
| Tfus | 350.00 ± 2.00 | K | NIST |
| Tfus | 348.05 ± 0.60 | K | NIST |
| Vc | 0.381 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [14.49; 16.50] | kJ/mol | [349.20; 350.80] | |
| ΔfusH | 15.20 | kJ/mol | 349.20 | NIST |
| ΔfusH | 14.49 | kJ/mol | 349.90 | NIST |
| ΔfusH | 14.49 | kJ/mol | 349.90 | NIST |
| ΔfusH | 14.49 | kJ/mol | 349.90 | NIST |
| ΔfusH | 16.50 | kJ/mol | 350.80 | NIST |
| ΔsubH | 98.60 ± 0.40 | kJ/mol | 313.00 | NIST |
| ΔvapH | 65.00 | kJ/mol | 454.50 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [131.56; 324.31] | 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 | -3.36890e+01 | |||
| Coefficient B | 7.35700e-01 | |||
| Coefficient C | -5.15200e-04 | |||
| Coefficient D | 1.37500e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 131.56 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 168.19 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 200.01 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 227.44 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 250.92 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 270.89 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 287.78 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 302.02 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 314.05 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 324.31 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0018037; 0.0002588] | Pa×s | [349.10; 548.22] |
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 | -1.16632e+01 | |||
| Coefficient B | 1.86608e+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. | 349.10 | |||
| Temperature range, max. | 548.22 | |||
| η | 0.0018037 | Pa×s | 349.10 | Calculated Property |
| η | 0.0013116 | Pa×s | 371.23 | Calculated Property |
| η | 0.0009886 | Pa×s | 393.35 | Calculated Property |
| η | 0.0007679 | Pa×s | 415.48 | Calculated Property |
| η | 0.0006119 | Pa×s | 437.60 | Calculated Property |
| η | 0.0004984 | Pa×s | 459.73 | Calculated Property |
| η | 0.0004136 | Pa×s | 481.85 | Calculated Property |
| η | 0.0003490 | Pa×s | 503.98 | Calculated Property |
| η | 0.0002986 | Pa×s | 526.10 | Calculated Property |
| η | 0.0002588 | Pa×s | 548.22 | Calculated Property |
Find more compounds similar to Benzeneacetic acid.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.
These property values are available through the Cheméo API. A free account gives you an access key.