| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 965.60 | kJ/mol | NIST |
| BasG | 934.80 | kJ/mol | NIST |
| ΔvapH° | 34.20 ± 0.70 | kJ/mol | NIST |
| IE | [8.41; 8.41] | eV |
|
| IE | 8.41 ± 0.02 | eV | NIST |
| IE | 8.41 ± 0.02 | eV | NIST |
| IE | 8.41 ± 0.05 | eV | NIST |
| IE | 8.41 ± 0.02 | eV | NIST |
| log10WS | 1.07 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.712 | Crippen Calculated Property | |
| McVol | 80.430 | ml/mol | McGowan Calculated Property |
| Inp | [651.00; 697.00] |
|
|
| Inp | 680.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 654.00 | NIST | |
| Inp | Outlier 697.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 673.00 | NIST | |
| I | [839.00; 880.00] |
|
|
| I | 849.00 | NIST | |
| I | 865.00 | NIST | |
| I | 870.00 | NIST | |
| I | 847.00 | NIST | |
| I | 844.00 | NIST | |
| I | 880.00 | NIST | |
| I | 865.00 | NIST | |
| I | 839.00 | NIST | |
| I | 861.00 | NIST | |
| Tboil | [352.45; 353.70] | K |
|
| Tboil | 353.70 | K | NIST |
| Tboil | 352.50 ± 0.15 | K | NIST |
| Tboil | 352.45 ± 0.50 | K | NIST |
| Tc | 548.62 | K | DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development |
| Tfus | 179.15 ± 0.40 | K | NIST |
Cheméo can also estimate Critical Pressure, Critical Volume, Enthalpy of formation at standard conditions, 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 | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [254.31; 378.61] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.41909e+01 | |||
| Coefficient B | -3.05442e+03 | |||
| Coefficient C | -3.46200e+01 | |||
| Temperature range, min. | 254.31 | |||
| Temperature range, max. | 378.61 | |||
| Pvap | 1.33 | kPa | 254.31 | Calculated Property |
| Pvap | 3.03 | kPa | 268.12 | Calculated Property |
| Pvap | 6.30 | kPa | 281.93 | Calculated Property |
| Pvap | 12.11 | kPa | 295.74 | Calculated Property |
| Pvap | 21.79 | kPa | 309.55 | Calculated Property |
| Pvap | 37.06 | kPa | 323.37 | Calculated Property |
| Pvap | 60.07 | kPa | 337.18 | Calculated Property |
| Pvap | 93.34 | kPa | 350.99 | Calculated Property |
| Pvap | 139.78 | kPa | 364.80 | Calculated Property |
| Pvap | 202.66 | kPa | 378.61 | Calculated Property |
| Pvap | [1.56e-03; 4137.60] | kPa | [183.15; 550.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.59271e+01 | |||
| Coefficient B | -5.61155e+03 | |||
| Coefficient C | -6.11939e+00 | |||
| Coefficient D | 4.02154e-06 | |||
| Temperature range, min. | 183.15 | |||
| Temperature range, max. | 550.00 | |||
| Pvap | 1.56e-03 | kPa | 183.15 | Calculated Property |
| Pvap | 0.13 | kPa | 223.91 | Calculated Property |
| Pvap | 2.39 | kPa | 264.67 | Calculated Property |
| Pvap | 18.47 | kPa | 305.43 | Calculated Property |
| Pvap | 83.07 | kPa | 346.19 | Calculated Property |
| Pvap | 261.43 | kPa | 386.96 | Calculated Property |
| Pvap | 644.75 | kPa | 427.72 | Calculated Property |
| Pvap | 1339.77 | kPa | 468.48 | Calculated Property |
| Pvap | 2462.10 | kPa | 509.24 | Calculated Property |
| Pvap | 4137.60 | kPa | 550.00 | Calculated Property |
Find more compounds similar to Pyrrolidine, 1-methyl-.
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