Property | Value | Unit | Source |
---|---|---|---|
PAff | 904.00 | kJ/mol | NIST |
BasG | 872.10 | kJ/mol | NIST |
Cp,liquid | 122.10 | J/mol×K | Thermop... |
IE | 9.50 | eV | NIST |
log10WS | -0.99 | Crippen Calculated Property | |
logPoct/wat | 1.143 | Crippen Calculated Property | |
McVol | 60.000 | ml/mol | McGowan Calculated Property |
Inp | [686.00; 760.00] | ||
Inp | 760.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 729.00 | NIST | |
Inp | 735.00 | NIST | |
Inp | 705.00 | NIST | |
Inp | 709.00 | NIST | |
Inp | 739.00 | NIST | |
Inp | 730.00 | NIST | |
Inp | 730.00 | NIST | |
Inp | 706.00 | NIST | |
Inp | 686.00 | NIST | |
Inp | 707.00 | NIST | |
Inp | 707.00 | NIST | |
Inp | 707.00 | NIST | |
Inp | 707.00 | NIST | |
Inp | 694.00 | NIST | |
Inp | 740.00 | NIST | |
Inp | 735.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 711.00 | NIST | |
Inp | 728.00 | NIST | |
Inp | 726.00 | NIST | |
Inp | 709.00 | NIST | |
Inp | 703.00 | NIST | |
Inp | 716.00 | NIST | |
Inp | 742.00 | NIST | |
Inp | 745.00 | NIST | |
Inp | 707.00 | NIST | |
Inp | 705.00 | NIST | |
Inp | 709.00 | NIST | |
Inp | 715.00 | NIST | |
Inp | 735.00 | NIST | |
Inp | 740.00 | NIST | |
Inp | 688.00 | NIST | |
Inp | 760.00 | NIST | |
I | [1210.00; 1270.00] | ||
I | 1259.00 | NIST | |
I | 1238.00 | NIST | |
I | Outlier 1210.00 | NIST | |
I | 1244.00 | NIST | |
I | 1252.00 | NIST | |
I | 1265.00 | NIST | |
I | 1249.00 | NIST | |
I | 1262.00 | NIST | |
I | 1229.00 | NIST | |
I | 1270.00 | NIST | |
I | 1270.00 | NIST | |
I | 1270.00 | NIST | |
I | 1239.00 | NIST | |
I | 1248.00 | NIST | |
I | 1247.00 | NIST | |
I | 1240.00 | NIST | |
I | 1235.00 | NIST | |
I | 1239.00 | NIST | |
I | 1235.00 | NIST | |
I | 1240.00 | NIST | |
I | 1262.00 | NIST | |
I | 1260.00 | NIST | |
I | 1246.00 | NIST | |
I | 1246.00 | NIST | |
I | 1262.00 | NIST | |
S°liquid | [169.95; 169.95] | J/mol×K | |
S°liquid | 169.95 | J/mol×K | NIST |
S°liquid | 169.95 | J/mol×K | NIST |
Tboil | [390.70; 391.39] | K | |
Tboil | 390.70 | K | NIST |
Tboil | 391.39 ± 0.20 | K | NIST |
Tfus | 239.58 ± 0.05 | K | NIST |
Ttriple | [239.48; 239.53] | K | |
Ttriple | 239.53 ± 0.02 | K | NIST |
Ttriple | 239.48 ± 0.02 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | [121.00; 121.00] | J/mol×K | [298.15; 298.15] | |
Cp,liquid | 121.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 121.00 | J/mol×K | 298.15 | NIST |
ΔfusH | [9.54; 9.59] | kJ/mol | [239.40; 239.53] | |
ΔfusH | 9.58 | kJ/mol | 239.40 | NIST |
ΔfusH | 9.59 | kJ/mol | 239.48 | NIST |
ΔfusH | 9.54 | kJ/mol | 239.53 | NIST |
ΔvapH | [38.90; 39.70] | kJ/mol | [363.00; 363.50] | |
ΔvapH | 39.70 | kJ/mol | 363.00 | NIST |
ΔvapH | 38.90 | kJ/mol | 363.50 | NIST |
ΔfusS | [40.04; 40.04] | J/mol×K | [239.48; 239.53] | |
ΔfusS | 40.04 | J/mol×K | 239.48 | NIST |
ΔfusS | 40.04 | J/mol×K | 239.53 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [288.81; 416.27] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.47286e+01 | |||
Coefficient B | -3.45024e+03 | |||
Coefficient C | -4.98900e+01 | |||
Temperature range, min. | 288.81 | |||
Temperature range, max. | 416.27 | |||
Pvap | 1.33 | kPa | 288.81 | Calculated Property |
Pvap | 2.99 | kPa | 302.97 | Calculated Property |
Pvap | 6.16 | kPa | 317.13 | Calculated Property |
Pvap | 11.80 | kPa | 331.30 | Calculated Property |
Pvap | 21.23 | kPa | 345.46 | Calculated Property |
Pvap | 36.20 | kPa | 359.62 | Calculated Property |
Pvap | 58.92 | kPa | 373.78 | Calculated Property |
Pvap | 92.06 | kPa | 387.95 | Calculated Property |
Pvap | 138.77 | kPa | 402.11 | Calculated Property |
Pvap | 202.65 | kPa | 416.27 | Calculated Property |
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