Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4040.00 ± 2.00 | kJ/mol | NIST |
ΔfG° | 118.00 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 187.00 | kJ/mol | NIST |
ΔfusH° | 6.22 | kJ/mol | Joback Calculated Property |
ΔvapH° | [38.70; 38.70] | kJ/mol | |
ΔvapH° | 38.70 ± 0.21 | kJ/mol | NIST |
ΔvapH° | 38.70 ± 0.20 | kJ/mol | NIST |
IE | [8.03; 8.52] | eV | |
IE | 8.29 | eV | NIST |
IE | 8.03 | eV | NIST |
IE | 8.52 | eV | NIST |
IE | 8.40 | eV | NIST |
IE | 8.20 ± 0.05 | eV | NIST |
IE | 8.28 | eV | NIST |
IE | 8.50 | eV | NIST |
log10WS | -2.15 | Aq. Sol... | |
logPoct/wat | 2.059 | Crippen Calculated Property | |
McVol | 85.730 | ml/mol | McGowan Calculated Property |
Pc | 4333.96 | kPa | Joback Calculated Property |
Inp | [108.90; 807.00] | ||
Inp | 807.00 | NIST | |
Inp | 794.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 784.00 | NIST | |
Inp | 782.60 | NIST | |
Inp | 786.60 | NIST | |
Inp | 774.00 | NIST | |
Inp | 756.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 769.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 776.00 | NIST | |
Inp | 787.00 | NIST | |
Inp | 758.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 784.00 | NIST | |
Inp | 784.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | Outlier 108.90 | NIST | |
Inp | Outlier 108.90 | NIST | |
I | [1056.00; 1089.00] | ||
I | 1089.00 | NIST | |
I | 1056.00 | NIST | |
I | 1089.00 | NIST | |
I | 1089.00 | NIST | |
I | 1089.00 | NIST | |
S°gas | 315.60 ± 1.10 | J/mol×K | NIST |
S°liquid | 214.64 | J/mol×K | NIST |
Tboil | 389.70 | K | NIST |
Tc | 604.64 | K | Joback Calculated Property |
Tfus | 193.40 | K | Aq. Sol... |
Ttriple | [197.91; 197.92] | K | |
Ttriple | 197.92 ± 0.07 | K | NIST |
Ttriple | 197.91 ± 0.07 | K | NIST |
Ttriple | 197.92 ± 0.05 | K | NIST |
Vc | 0.311 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [134.40; 201.05] | J/mol×K | [385.53; 604.64] | |
Cp,gas | 134.40 | J/mol×K | 385.53 | Joback Calculated Property |
Cp,gas | 147.36 | J/mol×K | 422.05 | Joback Calculated Property |
Cp,gas | 159.55 | J/mol×K | 458.57 | Joback Calculated Property |
Cp,gas | 170.98 | J/mol×K | 495.08 | Joback Calculated Property |
Cp,gas | 181.69 | J/mol×K | 531.60 | Joback Calculated Property |
Cp,gas | 191.71 | J/mol×K | 568.12 | Joback Calculated Property |
Cp,gas | 201.05 | J/mol×K | 604.64 | Joback Calculated Property |
Cp,liquid | 162.76 | J/mol×K | 298.15 | NIST |
η | [0.0002247; 0.0099693] | Pa×s | [179.03; 385.53] | |
η | 0.0099693 | Pa×s | 179.03 | Joback Calculated Property |
η | 0.0031831 | Pa×s | 213.45 | Joback Calculated Property |
η | 0.0013955 | Pa×s | 247.86 | Joback Calculated Property |
η | 0.0007480 | Pa×s | 282.28 | Joback Calculated Property |
η | 0.0004592 | Pa×s | 316.70 | Joback Calculated Property |
η | 0.0003102 | Pa×s | 351.11 | Joback Calculated Property |
η | 0.0002247 | Pa×s | 385.53 | Joback Calculated Property |
ΔfusH | [1.16; 2.35] | kJ/mol | [154.00; 198.00] | |
ΔfusH | 2.35 | kJ/mol | 154.00 | NIST |
ΔfusH | 1.16 | kJ/mol | 198.00 | NIST |
ΔfusH | 1.16 | kJ/mol | 198.00 | NIST |
ΔvapH | [39.40; 40.80] | kJ/mol | [305.50; 344.50] | |
ΔvapH | 40.80 | kJ/mol | 305.50 | NIST |
ΔvapH | 39.40 | kJ/mol | 344.50 | NIST |
ΔfusS | [5.86; 15.24] | J/mol×K | [154.00; 198.00] | |
ΔfusS | 15.24 | J/mol×K | 154.00 | NIST |
ΔfusS | 5.86 | J/mol×K | 198.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [333.70; 390.20] | K | [16.30; 99.90] | |
Tboilr | 333.70 | K | 16.30 | NIST |
Tboilr | 390.20 | K | 99.90 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [280.70; 416.14] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.50540e+01 | |||
Coefficient B | -3.87828e+03 | |||
Coefficient C | -1.80620e+01 | |||
Temperature range, min. | 280.70 | |||
Temperature range, max. | 416.14 | |||
Pvap | 1.33 | kPa | 280.70 | Calculated Property |
Pvap | 2.97 | kPa | 295.75 | Calculated Property |
Pvap | 6.08 | kPa | 310.80 | Calculated Property |
Pvap | 11.63 | kPa | 325.85 | Calculated Property |
Pvap | 20.92 | kPa | 340.90 | Calculated Property |
Pvap | 35.72 | kPa | 355.94 | Calculated Property |
Pvap | 58.28 | kPa | 370.99 | Calculated Property |
Pvap | 91.34 | kPa | 386.04 | Calculated Property |
Pvap | 138.20 | kPa | 401.09 | Calculated Property |
Pvap | 202.65 | kPa | 416.14 | Calculated Property |
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