| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3630 | KDB | |
| PAff | 952.40 | kJ/mol | NIST |
| BasG | 920.60 | kJ/mol | NIST |
| ΔcH°liquid | -4042.30 | kJ/mol | NIST |
| ΔfG° | 173.77 | kJ/mol | Relay (1.0-beta) Calculated Property |
| ΔfH°gas | 69.11 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°liquid | 1.50 | kJ/mol | NIST |
| ΔvapH° | 44.70 ± 0.80 | kJ/mol | NIST |
| IE | 9.14 | eV | Relay (1.0) Calculated Property |
| log10WS | [0.51; 0.51] |
|
|
| log10WS | 0.51 | Aq. Solubility Prediction | |
| log10WS | 0.51 | Estimated Solubility | |
| logPoct/wat | 1.644 | Crippen Calculated Property | |
| McVol | 95.710 | ml/mol | McGowan Calculated Property |
| Pc | 4100.00 | kPa | KDB |
| Inp | [140.78; 951.00] |
|
|
| Inp | 886.90 | NIST | |
| Inp | 886.90 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 871.80 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 884.40 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 879.40 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 905.70 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 912.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | Outlier 140.78 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 951.00 | NIST | |
| I | [1267.00; 1311.00] |
|
|
| I | 1288.00 | NIST | |
| I | 1290.00 | NIST | |
| I | 1284.00 | NIST | |
| I | Outlier 1311.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1277.00 | NIST | |
| I | 1286.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1279.00 | NIST | |
| I | 1284.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1282.00 | NIST | |
| I | 1275.00 | NIST | |
| Tboil | [417.00; 423.15] | K |
|
| Tboil | 421.80 | K | KDB |
| Tboil | 421.80 | K | NIST |
| Tboil | 423.15 ± 1.50 | K | NIST |
| Tboil | 422.05 ± 0.40 | K | NIST |
| Tboil | 422.00 ± 3.00 | K | NIST |
| Tboil | Outlier 417.00 ± 4.00 | K | NIST |
| Tc | [628.00; 634.00] | K |
|
| Tc | 634.00 | K | KDB |
| Tc | 628.00 | K | Critical point measurements of four pyridines |
| Tfus | [210.00; 210.10] | K |
|
| Tfus | 210.00 | K | KDB |
| Tfus | 210.10 | K | Aq. Solubility Prediction |
| Tfus | 210.05 ± 0.50 | K | NIST |
| Vc | 0.353 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 43.70 | kJ/mol | 348.00 | NIST |
| ρl | 932.25 | kg/m3 | 293.10 | KDB |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [313.04; 448.47] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47492e+01 | |||
| Coefficient B | -3.67933e+03 | |||
| Coefficient C | -5.86190e+01 | |||
| Temperature range, min. | 313.04 | |||
| Temperature range, max. | 448.47 | |||
| Pvap | 1.33 | kPa | 313.04 | Calculated Property |
| Pvap | 2.99 | kPa | 328.09 | Calculated Property |
| Pvap | 6.16 | kPa | 343.14 | Calculated Property |
| Pvap | 11.79 | kPa | 358.18 | Calculated Property |
| Pvap | 21.21 | kPa | 373.23 | Calculated Property |
| Pvap | 36.17 | kPa | 388.28 | Calculated Property |
| Pvap | 58.87 | kPa | 403.33 | Calculated Property |
| Pvap | 92.01 | kPa | 418.37 | Calculated Property |
| Pvap | 138.72 | kPa | 433.42 | Calculated Property |
| Pvap | 202.63 | kPa | 448.47 | Calculated Property |
| Pvap | [1.41e-03; 3940.30] | kPa | [225.15; 631.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.84456e+01 | |||
| Coefficient B | -7.49816e+03 | |||
| Coefficient C | -7.73720e+00 | |||
| Coefficient D | 4.01534e-06 | |||
| Temperature range, min. | 225.15 | |||
| Temperature range, max. | 631.15 | |||
| Pvap | 1.41e-03 | kPa | 225.15 | Calculated Property |
| Pvap | 0.10 | kPa | 270.26 | Calculated Property |
| Pvap | 1.74 | kPa | 315.37 | Calculated Property |
| Pvap | 13.66 | kPa | 360.48 | Calculated Property |
| Pvap | 63.73 | kPa | 405.59 | Calculated Property |
| Pvap | 209.38 | kPa | 450.71 | Calculated Property |
| Pvap | 539.80 | kPa | 495.82 | Calculated Property |
| Pvap | 1171.94 | kPa | 540.93 | Calculated Property |
| Pvap | 2248.04 | kPa | 586.04 | Calculated Property |
| Pvap | 3940.30 | kPa | 631.15 | Calculated Property |
Find more compounds similar to Pyridine, 2-ethyl-.
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