Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3110 | KDB | |
ΔcH°liquid | -3030.30 ± 0.42 | kJ/mol | NIST |
ΔfH°gas | 103.10 ± 0.54 | kJ/mol | NIST |
ΔfH°liquid | 62.38 ± 0.50 | kJ/mol | NIST |
ΔvapH° | [40.70; 44.60] | kJ/mol | |
ΔvapH° | 44.60 ± 0.02 | kJ/mol | NIST |
ΔvapH° | 40.80 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 40.70 | kJ/mol | NIST |
IE | [7.94; 8.40] | eV | |
IE | 7.99 ± 0.07 | eV | NIST |
IE | 7.94 ± 0.02 | eV | NIST |
IE | 8.40 | eV | NIST |
IE | 8.09 ± 0.01 | eV | NIST |
IE | 7.95 ± 0.05 | eV | NIST |
log10WS | -2.76 | Crippen Calculated Property | |
logPoct/wat | 1.025 | Crippen Calculated Property | |
McVol | 71.830 | ml/mol | McGowan Calculated Property |
Pc | 4850.00 | kPa | KDB |
Inp | [695.00; 769.00] | ||
Inp | 731.00 | NIST | |
Inp | 731.00 | NIST | |
Inp | 710.00 | NIST | |
Inp | 702.00 | NIST | |
Inp | Outlier 695.00 | NIST | |
Inp | 739.00 | NIST | |
Inp | 725.00 | NIST | |
Inp | 710.00 | NIST | |
Inp | 717.00 | NIST | |
Inp | 719.00 | NIST | |
Inp | 730.00 | NIST | |
Inp | 743.00 | NIST | |
Inp | 750.00 | NIST | |
Inp | 741.00 | NIST | |
Inp | 749.00 | NIST | |
Inp | Outlier 769.00 | NIST | |
Inp | 716.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 751.00 | NIST | |
Inp | 737.00 | NIST | |
Inp | 750.00 | NIST | |
Inp | 740.00 | NIST | |
Inp | 741.00 | NIST | |
Inp | 742.00 | NIST | |
Inp | 736.00 | NIST | |
Inp | 743.00 | NIST | |
Inp | 740.00 | NIST | |
Inp | 747.00 | NIST | |
Inp | 750.00 | NIST | |
Inp | 750.00 | NIST | |
Inp | 731.00 | NIST | |
Inp | 715.00 | NIST | |
Inp | 735.00 | NIST | |
Inp | 740.00 | NIST | |
Inp | 738.00 | NIST | |
Inp | 737.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 743.00 | NIST | |
Inp | 744.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 715.00 | NIST | |
Inp | 715.00 | NIST | |
Inp | 717.00 | NIST | |
Inp | 715.00 | NIST | |
Inp | 717.00 | NIST | |
I | [1127.00; 1195.00] | ||
I | 1171.00 | NIST | |
I | 1170.00 | NIST | |
I | 1180.00 | NIST | |
I | 1166.00 | NIST | |
I | 1160.00 | NIST | |
I | Outlier 1195.00 | NIST | |
I | 1154.00 | NIST | |
I | 1148.00 | NIST | |
I | 1140.00 | NIST | |
I | 1149.00 | NIST | |
I | 1134.00 | NIST | |
I | 1155.00 | NIST | |
I | 1137.00 | NIST | |
I | 1142.00 | NIST | |
I | 1153.00 | NIST | |
I | 1129.00 | NIST | |
I | 1157.00 | NIST | |
I | 1145.00 | NIST | |
I | 1168.00 | NIST | |
I | 1157.00 | NIST | |
I | 1149.00 | NIST | |
I | 1149.00 | NIST | |
I | 1149.00 | NIST | |
I | 1127.00 | NIST | |
I | 1180.00 | NIST | |
I | 1140.00 | NIST | |
I | 1147.00 | NIST | |
I | 1139.00 | NIST | |
I | 1139.00 | NIST | |
I | 1139.00 | NIST | |
I | 1132.00 | NIST | |
I | 1134.00 | NIST | |
I | 1144.00 | NIST | |
I | 1139.00 | NIST | |
I | 1142.00 | NIST | |
I | 1139.00 | NIST | |
S°liquid | [200.48; 200.52] | J/mol×K | |
S°liquid | 200.52 | J/mol×K | NIST |
S°liquid | 200.48 | J/mol×K | NIST |
S°liquid | 200.48 | J/mol×K | NIST |
Tboil | 385.80 | K | KDB |
Tc | [596.00; 597.00] | K | |
Tc | 596.00 | K | KDB |
Tc | 597.00 | K | Thermod... |
Tfus | [216.82; 322.11] | K | |
Tfus | 322.11 | K | KDB |
Tfus | 216.91 | K | NIST |
Tfus | 216.82 ± 0.08 | K | NIST |
Tfus | 231.20 ± 0.50 | K | NIST |
Ttriple | [216.87; 216.91] | K | |
Ttriple | 216.91 ± 0.03 | K | NIST |
Ttriple | 216.91 ± 0.02 | K | NIST |
Ttriple | 216.87 ± 0.01 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | [150.06; 150.06] | J/mol×K | [298.15; 298.15] | |
Cp,liquid | 150.06 | J/mol×K | 298.15 | NIST |
Cp,liquid | 150.06 | J/mol×K | 298.15 | NIST |
Cp,liquid | 150.06 | J/mol×K | 298.15 | NIST |
ΔfusH | [7.82; 7.82] | kJ/mol | [216.90; 216.91] | |
ΔfusH | 7.82 | kJ/mol | 216.90 | NIST |
ΔfusH | 7.82 | kJ/mol | 216.90 | NIST |
ΔfusH | 7.82 | kJ/mol | 216.91 | NIST |
ΔfusH | 7.82 | kJ/mol | 216.91 | NIST |
ΔvapH | [38.00; 39.00] | kJ/mol | [353.00; 372.00] | |
ΔvapH | 38.00 | kJ/mol | 353.00 | NIST |
ΔvapH | 39.00 | kJ/mol | 372.00 | NIST |
ΔfusS | 36.07 | J/mol×K | 216.91 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [283.27; 411.86] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40817e+01 | |||
Coefficient B | -3.09648e+03 | |||
Coefficient C | -5.87940e+01 | |||
Temperature range, min. | 283.27 | |||
Temperature range, max. | 411.86 | |||
Pvap | 1.33 | kPa | 283.27 | Calculated Property |
Pvap | 3.04 | kPa | 297.56 | Calculated Property |
Pvap | 6.33 | kPa | 311.85 | Calculated Property |
Pvap | 12.17 | kPa | 326.13 | Calculated Property |
Pvap | 21.91 | kPa | 340.42 | Calculated Property |
Pvap | 37.25 | kPa | 354.71 | Calculated Property |
Pvap | 60.32 | kPa | 369.00 | Calculated Property |
Pvap | 93.61 | kPa | 383.28 | Calculated Property |
Pvap | 139.99 | kPa | 397.57 | Calculated Property |
Pvap | 202.65 | kPa | 411.86 | Calculated Property |
Pvap | [4.07e-03; 4753.96] | kPa | [216.91; 610.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.94030e+01 | |||
Coefficient B | -7.46125e+03 | |||
Coefficient C | -9.43097e+00 | |||
Coefficient D | 4.78467e-06 | |||
Temperature range, min. | 216.91 | |||
Temperature range, max. | 610.00 | |||
Pvap | 4.07e-03 | kPa | 216.91 | Calculated Property |
Pvap | 0.25 | kPa | 260.59 | Calculated Property |
Pvap | 4.05 | kPa | 304.26 | Calculated Property |
Pvap | 28.44 | kPa | 347.94 | Calculated Property |
Pvap | 118.97 | kPa | 391.62 | Calculated Property |
Pvap | 352.89 | kPa | 435.29 | Calculated Property |
Pvap | 827.56 | kPa | 478.97 | Calculated Property |
Pvap | 1646.79 | kPa | 522.65 | Calculated Property |
Pvap | 2916.77 | kPa | 566.32 | Calculated Property |
Pvap | 4753.96 | kPa | 610.00 | Calculated Property |
Find more compounds similar to 1H-Pyrrole, 1-methyl-.
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