Property | Value | Unit | Source |
---|---|---|---|
PAff | 826.40 | kJ/mol | NIST |
BasG | 797.60 | kJ/mol | NIST |
ΔcH°gas | -3186.60 ± 0.96 | kJ/mol | NIST |
ΔcH°liquid | -3158.20 ± 1.60 | kJ/mol | NIST |
ΔfG° | 158.35 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 75.70 ± 1.00 | kJ/mol | NIST |
ΔfusH° | 4.84 | kJ/mol | Joback Calculated Property |
ΔvapH° | 26.40 | kJ/mol | NIST |
ΔvapH° | 26.80 ± 0.30 | kJ/mol | NIST |
IE | [8.84; 9.04] | eV | ![]() |
IE | 8.86 ± 0.02 | eV | NIST |
IE | 8.85 ± 0.02 | eV | NIST |
IE | 8.85 | eV | NIST |
IE | 8.90 ± 0.10 | eV | NIST |
IE | 8.89 | eV | NIST |
IE | 8.85 ± 0.01 | eV | NIST |
IE | 8.84 ± 0.01 | eV | NIST |
IE | 8.85 | eV | NIST |
IE | 8.85 | eV | NIST |
IE | 8.87 | eV | NIST |
IE | Outlier 9.04 | eV | NIST |
logPoct/wat | 1.748 | Crippen Calculated Property | |
Pc | 3862.67 | kPa | Joback Calculated Property |
S°gas | 314.76 | J/mol×K | NIST |
S°liquid | 228.28 | J/mol×K | NIST |
S°liquid | 229.20 | J/mol×K | NIST |
S°liquid | 229.30 | J/mol×K | NIST |
Tboil | [306.00; 309.65] | K | ![]() |
Tboil | 307.30 | K | NIST |
Tboil | 307.20 ± 2.00 | K | NIST |
Tboil | 307.20 ± 1.00 | K | NIST |
Tboil | 307.30 ± 0.50 | K | NIST |
Tboil | 307.00 ± 1.50 | K | NIST |
Tboil | 306.00 ± 2.00 | K | NIST |
Tboil | 307.00 ± 0.60 | K | NIST |
Tboil | 307.20 ± 0.50 | K | NIST |
Tboil | 307.50 ± 0.50 | K | NIST |
Tboil | 307.02 ± 0.60 | K | NIST |
Tboil | 307.22 ± 0.20 | K | NIST |
Tboil | 307.55 ± 1.50 | K | NIST |
Tboil | 306.40 ± 1.00 | K | NIST |
Tboil | 306.30 ± 1.00 | K | NIST |
Tboil | 307.30 ± 0.50 | K | NIST |
Tboil | Outlier 309.65 ± 1.00 | K | NIST |
Tboil | 309.00 ± 2.00 | K | NIST |
Tc | 480.20 | K | Joback Calculated Property |
Tfus | [126.40; 153.00] | K | ![]() |
Tfus | 127.18 ± 0.05 | K | NIST |
Tfus | 127.20 ± 0.03 | K | NIST |
Tfus | 127.10 ± 0.40 | K | NIST |
Tfus | 126.96 ± 0.20 | K | NIST |
Tfus | 127.01 ± 0.10 | K | NIST |
Tfus | 126.40 ± 0.40 | K | NIST |
Tfus | Outlier 153.00 ± 10.00 | K | NIST |
Ttriple | 127.27 ± 0.05 | K | NIST |
Ttriple | 126.40 ± 0.20 | K | NIST |
Vc | 0.279 | m3/kg-mol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | 101.90 | J/mol×K | 307.04 | Joback Calculated Property |
Cp,liquid | 151.08 | J/mol×K | 298.15 | NIST |
Cp,liquid | 152.50 | J/mol×K | 298.15 | NIST |
Cp,liquid | 152.60 | J/mol×K | 298.2 | NIST |
ΔfusH | [4.83; 4.92] | kJ/mol | [126.40; 127.30] | ![]() |
ΔfusH | 4.83 | kJ/mol | 126.4 | NIST |
ΔfusH | 4.83 | kJ/mol | 126.4 | NIST |
ΔfusH | 4.92 | kJ/mol | 127.27 | NIST |
ΔfusH | 4.92 | kJ/mol | 127.3 | NIST |
ΔfusH | 4.92 | kJ/mol | 127.3 | NIST |
ΔvapH | [25.80; 31.50] | kJ/mol | [225.50; 307.20] | ![]() |
ΔvapH | 31.50 | kJ/mol | 225.5 | NIST |
ΔvapH | 29.40 | kJ/mol | 237.5 | NIST |
ΔvapH | 28.30 | kJ/mol | 285.0 | NIST |
ΔvapH | 27.40 | kJ/mol | 288.0 | NIST |
ΔvapH | 27.30 | kJ/mol | 299.0 | NIST |
ΔvapH | 25.80 | kJ/mol | 307.2 | NIST |
ΔfusS | 38.21 | J/mol×K | 126.4 | NIST |
ΔfusS | 38.21 | J/mol×K | 126.4 | NIST |
ΔfusS | 38.69 | J/mol×K | 127.27 | NIST |
Joback and Reid Groups | |
---|---|
=CH2 | 2 |
-CH3 | 1 |
=C< | 1 |
=CH- | 1 |
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