| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5800 | KDB | |
| ΔfG° | -79.77 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -329.99 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 21.07 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 65.45 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.18 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.48 | Aq. Solubility Prediction | |
| logPoct/wat | 2.643 | Crippen Calculated Property | |
| McVol | 149.530 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [2400.00; 2600.00] | kPa |
|
| Pc | 2600.00 | kPa | KDB |
| Pc | 2400.00 | kPa | Critical Point Measurements for n-Alkyl Benzoates (C8 to C13) |
| Inp | [1324.00; 1389.00] |
|
|
| Inp | 1383.13 | NIST | |
| Inp | 1356.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1353.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1386.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1367.00 | NIST | |
| Inp | 1373.00 | NIST | |
| Inp | 1365.00 | NIST | |
| Inp | 1344.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | 1358.00 | NIST | |
| Inp | 1332.00 | NIST | |
| Inp | 1351.00 | NIST | |
| Inp | 1341.00 | NIST | |
| Inp | Outlier 1389.00 | NIST | |
| Inp | 1377.00 | NIST | |
| Inp | 1352.00 | NIST | |
| Inp | Outlier 1324.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1348.00 | NIST | |
| Inp | 1353.00 | NIST | |
| Inp | 1358.00 | NIST | |
| Inp | 1346.00 | NIST | |
| Inp | 1355.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1361.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1349.00 | NIST | |
| Inp | 1362.00 | NIST | |
| Inp | 1339.00 | NIST | |
| Inp | 1338.00 | NIST | |
| Inp | 1344.00 | NIST | |
| Inp | 1343.00 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | Outlier 1389.00 | NIST | |
| Inp | 1348.00 | NIST | |
| Inp | 1360.00 | NIST | |
| Inp | 1341.00 | NIST | |
| I | [1839.00; 1913.00] |
|
|
| I | 1879.00 | NIST | |
| I | 1901.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1884.00 | NIST | |
| I | 1913.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1856.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1839.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1903.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1841.00 | NIST | |
| Tboil | [521.50; 523.45] | K |
|
| Tboil | 523.00 | K | KDB |
| Tboil | 522.20 | K | NIST |
| Tboil | 521.50 ± 0.50 | K | NIST |
| Tboil | 523.45 ± 0.60 | K | NIST |
| Tboil | 522.15 ± 1.00 | K | NIST |
| Tc | 723.00 | K | KDB |
| Tfus | [250.75; 254.35] | K |
|
| Tfus | 251.00 | K | KDB |
| Tfus | 254.35 | K | Aq. Solubility Prediction |
| Tfus | 250.75 ± 0.30 | K | NIST |
| Vc | 0.561 | m3/kmol | KDB |
| Zc | 0.2426390 | KDB |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [346.39; 421.37] | J/mol×K | [554.05; 763.32] | |
| Cp,gas | 346.39 | J/mol×K | 554.05 | Joback Calculated Property |
| Cp,gas | 360.84 | J/mol×K | 588.93 | Joback Calculated Property |
| Cp,gas | 374.48 | J/mol×K | 623.81 | Joback Calculated Property |
| Cp,gas | 387.33 | J/mol×K | 658.68 | Joback Calculated Property |
| Cp,gas | 399.42 | J/mol×K | 693.56 | Joback Calculated Property |
| Cp,gas | 410.76 | J/mol×K | 728.44 | Joback Calculated Property |
| Cp,gas | 421.37 | J/mol×K | 763.32 | Joback Calculated Property |
| η | [0.0002006; 0.0023060] | Pa×s | [312.31; 554.05] | |
| η | 0.0023060 | Pa×s | 312.31 | Joback Calculated Property |
| η | 0.0012165 | Pa×s | 352.60 | Joback Calculated Property |
| η | 0.0007317 | Pa×s | 392.89 | Joback Calculated Property |
| η | 0.0004838 | Pa×s | 433.18 | Joback Calculated Property |
| η | 0.0003432 | Pa×s | 473.47 | Joback Calculated Property |
| η | 0.0002569 | Pa×s | 513.76 | Joback Calculated Property |
| η | 0.0002006 | Pa×s | 554.05 | Joback Calculated Property |
| ΔvapH | [54.40; 60.40] | kJ/mol | [295.50; 424.00] | |
| ΔvapH | 58.10 | kJ/mol | 295.50 | NIST |
| ΔvapH | 60.40 | kJ/mol | 418.50 | NIST |
| ΔvapH | 54.40 | kJ/mol | 418.50 | NIST |
| ΔvapH | 57.10 | kJ/mol | 424.00 | NIST |
| ρl | 1006.00 | kg/m3 | 293.00 | KDB |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [4.15e-05; 2492.76] | kPa | [251.65; 724.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.83166e+01 | |||
| Coefficient B | -9.10652e+03 | |||
| Coefficient C | -5.84030e+00 | |||
| Coefficient D | 1.02964e-06 | |||
| Temperature range, min. | 251.65 | |||
| Temperature range, max. | 724.00 | |||
| Pvap | 4.15e-05 | kPa | 251.65 | Calculated Property |
| Pvap | 7.28e-03 | kPa | 304.13 | Calculated Property |
| Pvap | 0.24 | kPa | 356.62 | Calculated Property |
| Pvap | 3.02 | kPa | 409.10 | Calculated Property |
| Pvap | 19.67 | kPa | 461.58 | Calculated Property |
| Pvap | 82.84 | kPa | 514.07 | Calculated Property |
| Pvap | 256.86 | kPa | 566.55 | Calculated Property |
| Pvap | 637.76 | kPa | 619.03 | Calculated Property |
| Pvap | 1342.34 | kPa | 671.52 | Calculated Property |
| Pvap | 2492.76 | kPa | 724.00 | Calculated Property |
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