Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3460 | KDB | |
PAff | 747.30 | kJ/mol | NIST |
BasG | 719.60 | kJ/mol | NIST |
ΔfG° | -696.08 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -749.49 | kJ/mol | Joback Calculated Property |
ΔfusH° | 16.49 | kJ/mol | Joback Calculated Property |
ΔvapH° | [35.40; 36.00] | kJ/mol | |
ΔvapH° | 36.00 | kJ/mol | NIST |
ΔvapH° | 35.40 | kJ/mol | NIST |
IE | [9.53; 9.56] | eV | |
IE | 9.55 ± 0.01 | eV | NIST |
IE | 9.53 ± 0.00 | eV | NIST |
IE | 9.55 | eV | NIST |
IE | 9.56 | eV | NIST |
log10WS | -2.31 | Aq. Sol... | |
logPoct/wat | 2.243 | Crippen Calculated Property | |
McVol | 78.720 | ml/mol | McGowan Calculated Property |
Pc | [3747.00; 3747.00] | kPa | |
Pc | 3747.00 | kPa | KDB |
Pc | 3747.00 ± 6.00 | kPa | NIST |
S°liquid | 257.30 | J/mol×K | NIST |
Tboil | [356.20; 357.61] | K | |
Tboil | 357.61 | K | KDB |
Tboil | 356.20 | K | NIST |
Tc | [535.25; 535.25] | K | |
Tc | 535.25 | K | KDB |
Tc | 535.25 ± 0.20 | K | NIST |
Tfus | 225.00 | K | KDB |
Ttriple | 226.90 ± 0.02 | K | NIST |
Vc | 0.336 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [141.11; 176.14] | J/mol×K | [375.38; 548.84] | |
Cp,gas | 141.11 | J/mol×K | 375.38 | Joback Calculated Property |
Cp,gas | 147.59 | J/mol×K | 404.29 | Joback Calculated Property |
Cp,gas | 153.81 | J/mol×K | 433.20 | Joback Calculated Property |
Cp,gas | 159.77 | J/mol×K | 462.11 | Joback Calculated Property |
Cp,gas | 165.47 | J/mol×K | 491.02 | Joback Calculated Property |
Cp,gas | 170.93 | J/mol×K | 519.93 | Joback Calculated Property |
Cp,gas | 176.14 | J/mol×K | 548.84 | Joback Calculated Property |
Cp,liquid | 190.30 | J/mol×K | 298.15 | NIST |
ΔfusH | [10.67; 10.67] | kJ/mol | [226.90; 226.90] | |
ΔfusH | 10.67 | kJ/mol | 226.90 | NIST |
ΔfusH | 10.67 | kJ/mol | 226.90 | NIST |
ΔvapH | [32.40; 36.00] | kJ/mol | [301.00; 400.50] | |
ΔvapH | 36.00 | kJ/mol | 301.00 | NIST |
ΔvapH | 36.00 | kJ/mol | 334.50 | NIST |
ΔvapH | 32.40 | kJ/mol | 400.50 | NIST |
ρl | [1352.00; 1403.00] | kg/m3 | [296.30; 325.90] | |
ρl | 1403.00 | kg/m3 | 296.30 | Liquid-... |
ρl | 1352.00 | kg/m3 | 325.90 | Liquid-... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [263.09; 356.95] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.66435e+01 | |||
Coefficient B | -3.46280e+03 | |||
Coefficient C | -5.13750e+01 | |||
Temperature range, min. | 263.09 | |||
Temperature range, max. | 356.95 | |||
Pvap | 1.33 | kPa | 263.09 | Calculated Property |
Pvap | 2.87 | kPa | 273.52 | Calculated Property |
Pvap | 5.78 | kPa | 283.95 | Calculated Property |
Pvap | 10.95 | kPa | 294.38 | Calculated Property |
Pvap | 19.68 | kPa | 304.81 | Calculated Property |
Pvap | 33.78 | kPa | 315.23 | Calculated Property |
Pvap | 55.63 | kPa | 325.66 | Calculated Property |
Pvap | 88.34 | kPa | 336.09 | Calculated Property |
Pvap | 135.77 | kPa | 346.52 | Calculated Property |
Pvap | 202.63 | kPa | 356.95 | Calculated Property |
Pvap | [3.63; 3714.84] | kPa | [279.15; 535.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.97998e+01 | |||
Coefficient B | -6.81695e+03 | |||
Coefficient C | -9.70897e+00 | |||
Coefficient D | 7.53476e-06 | |||
Temperature range, min. | 279.15 | |||
Temperature range, max. | 535.00 | |||
Pvap | 3.63 | kPa | 279.15 | Calculated Property |
Pvap | 15.32 | kPa | 307.58 | Calculated Property |
Pvap | 48.61 | kPa | 336.01 | Calculated Property |
Pvap | 124.96 | kPa | 364.43 | Calculated Property |
Pvap | 274.38 | kPa | 392.86 | Calculated Property |
Pvap | 534.58 | kPa | 421.29 | Calculated Property |
Pvap | 950.43 | kPa | 449.72 | Calculated Property |
Pvap | 1574.63 | kPa | 478.14 | Calculated Property |
Pvap | 2470.18 | kPa | 506.57 | Calculated Property |
Pvap | 3714.84 | kPa | 535.00 | Calculated Property |
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