| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3690 | KDB | |
| ΔfH°gas | 133.82 | kJ/mol | Relay (1.0) Calculated Property |
| ΔvapH° | 68.44 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.28 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.94 | Aq. Solubility Prediction | |
| logPoct/wat | 2.852 | Crippen Calculated Property | |
| McVol | 132.610 | ml/mol | McGowan Calculated Property |
| Pc | 3900.00 | kPa | KDB |
| Inp | [247.38; 1497.00] |
|
|
| Inp | 1417.00 | NIST | |
| Inp | 1434.00 | NIST | |
| Inp | 1417.00 | NIST | |
| Inp | 1434.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1446.00 | NIST | |
| Inp | 1454.00 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1497.00 | NIST | |
| Inp | 1446.00 | NIST | |
| Inp | Outlier 247.38 | NIST | |
| Inp | Outlier 247.96 | NIST | |
| Inp | 1472.00 | NIST | |
| Inp | 1446.00 | NIST | |
| Inp | 1417.00 | NIST | |
| Inp | Outlier 247.38 | NIST | |
| I | [2063.00; 2088.00] |
|
|
| I | 2063.00 | NIST | |
| I | 2088.00 | NIST | |
| I | 2063.00 | NIST | |
| I | 2088.00 | NIST | |
| I | 2063.00 | NIST | |
| I | 2088.00 | NIST | |
| I | 2086.00 | NIST | |
| Tboil | [532.00; 540.40] | K |
|
| Tboil | 540.40 | K | KDB |
| Tboil | 538.20 | K | NIST |
| Tboil | 540.35 ± 0.06 | K | NIST |
| Tboil | 532.00 ± 7.00 | K | NIST |
| Tc | 807.00 | K | KDB |
| Tfus | [288.00; 330.00] | K |
|
| Tfus | 330.00 | K | KDB |
| Tfus | 288.00 ± 0.10 | K | NIST |
| Vc | 0.500 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Standard Gibbs free energy of formation 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 |
|---|---|---|---|---|
| ΔvapH | 56.30 | kJ/mol | 500.50 | NIST |
| ρl | 1053.34 | kg/m3 | 293.10 | KDB |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 416.20 | K | 2.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [398.79; 573.17] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41680e+01 | |||
| Coefficient B | -4.26710e+03 | |||
| Coefficient C | -9.13700e+01 | |||
| Temperature range, min. | 398.79 | |||
| Temperature range, max. | 573.17 | |||
| Pvap | 1.33 | kPa | 398.79 | Calculated Property |
| Pvap | 3.04 | kPa | 418.17 | Calculated Property |
| Pvap | 6.31 | kPa | 437.54 | Calculated Property |
| Pvap | 12.12 | kPa | 456.92 | Calculated Property |
| Pvap | 21.81 | kPa | 476.29 | Calculated Property |
| Pvap | 37.10 | kPa | 495.67 | Calculated Property |
| Pvap | 60.12 | kPa | 515.04 | Calculated Property |
| Pvap | 93.39 | kPa | 534.42 | Calculated Property |
| Pvap | 139.82 | kPa | 553.79 | Calculated Property |
| Pvap | 202.65 | kPa | 573.17 | Calculated Property |
| Pvap | [11.59; 106.13] | kPa | [458.50; 542.60] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40758e+01 | |||
| Coefficient B | -4.15501e+03 | |||
| Coefficient C | -1.01103e+02 | |||
| Reference | Malanowska and Wecsile, 1964, 2 | |||
| Temperature range, min. | 458.50 | |||
| Temperature range, max. | 542.60 | |||
| Pvap | 11.59 | kPa | 458.50 | Calculated Property |
| Pvap | 15.58 | kPa | 467.84 | Calculated Property |
| Pvap | 20.65 | kPa | 477.19 | Calculated Property |
| Pvap | 26.99 | kPa | 486.53 | Calculated Property |
| Pvap | 34.84 | kPa | 495.88 | Calculated Property |
| Pvap | 44.44 | kPa | 505.22 | Calculated Property |
| Pvap | 56.07 | kPa | 514.57 | Calculated Property |
| Pvap | 70.01 | kPa | 523.91 | Calculated Property |
| Pvap | 86.59 | kPa | 533.26 | Calculated Property |
| Pvap | 106.13 | kPa | 542.60 | Calculated Property |
| Pvap | [11.59; 106.13] | kPa | [458.50; 542.60] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40758e+01 | |||
| Coefficient B | -4.15501e+03 | |||
| Coefficient C | -1.01103e+02 | |||
| Reference | Malanowska and Wecsile, 1964 | |||
| Temperature range, min. | 458.50 | |||
| Temperature range, max. | 542.60 | |||
| Pvap | 11.59 | kPa | 458.50 | Calculated Property |
| Pvap | 15.58 | kPa | 467.84 | Calculated Property |
| Pvap | 20.65 | kPa | 477.19 | Calculated Property |
| Pvap | 26.99 | kPa | 486.53 | Calculated Property |
| Pvap | 34.84 | kPa | 495.88 | Calculated Property |
| Pvap | 44.44 | kPa | 505.22 | Calculated Property |
| Pvap | 56.07 | kPa | 514.57 | Calculated Property |
| Pvap | 70.01 | kPa | 523.91 | Calculated Property |
| Pvap | 86.59 | kPa | 533.26 | Calculated Property |
| Pvap | 106.13 | kPa | 542.60 | Calculated Property |
Find more compounds similar to Quinoline, 2,4-dimethyl-.
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