Property | Value | Unit | Source |
---|---|---|---|
PAff | 816.40 | kJ/mol | NIST |
BasG | 785.10 | kJ/mol | NIST |
ΔcH°liquid | -3465.00 ± 0.71 | kJ/mol | NIST |
ΔfG° | 15.03 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -108.70 ± 0.88 | kJ/mol | NIST |
ΔfH°liquid | -140.50 ± 0.88 | kJ/mol | NIST |
ΔfusH° | 2.74 | kJ/mol | Joback Calculated Property |
ΔvapH° | [30.80; 31.80] | kJ/mol | |
ΔvapH° | 30.93 | kJ/mol | NIST |
ΔvapH° | 30.80 | kJ/mol | NIST |
ΔvapH° | 30.90 ± 0.08 | kJ/mol | NIST |
ΔvapH° | 31.80 | kJ/mol | NIST |
IE | 9.03 | eV | NIST |
log10WS | -1.68 | Crippen Calculated Property | |
logPoct/wat | 1.715 | Crippen Calculated Property | |
McVol | 83.570 | ml/mol | McGowan Calculated Property |
Pc | 4333.96 | kPa | Joback Calculated Property |
Inp | [574.00; 617.00] | ||
Inp | 605.50 | NIST | |
Inp | Outlier 617.00 | NIST | |
Inp | 599.20 | NIST | |
Inp | 602.50 | NIST | |
Inp | 602.00 | NIST | |
Inp | 586.00 | NIST | |
Inp | Outlier 574.00 | NIST | |
Inp | 577.00 | NIST | |
Inp | 603.00 | NIST | |
Inp | 602.00 | NIST | |
Inp | 606.00 | NIST | |
Inp | 599.00 | NIST | |
Inp | 602.00 | NIST | |
Inp | 584.00 | NIST | |
Inp | 594.00 | NIST | |
Inp | 600.00 | NIST | |
Inp | 595.00 | NIST | |
Inp | 587.00 | NIST | |
Inp | 589.00 | NIST | |
Inp | 602.00 | NIST | |
Inp | 584.00 | NIST | |
I | [779.00; 779.00] | ||
I | 779.00 | NIST | |
I | 779.00 | NIST | |
S°liquid | 246.44 | J/mol×K | NIST |
Tboil | [334.50; 339.00] | K | |
Tboil | 334.75 | K | KDB |
Tboil | 337.40 | K | NIST |
Tboil | 337.00 | K | NIST |
Tboil | 337.40 | K | NIST |
Tboil | 339.00 ± 2.00 | K | NIST |
Tboil | 336.00 ± 3.00 | K | NIST |
Tboil | 334.50 ± 0.35 | K | NIST |
Tboil | 337.90 ± 0.60 | K | NIST |
Tboil | 337.00 ± 2.00 | K | NIST |
Tc | 530.10 | K | NIST |
Tfus | [273.97; 274.41] | K | |
Tfus | 274.41 | K | KDB |
Tfus | 273.97 ± 0.20 | K | NIST |
Ttriple | 274.42 ± 0.02 | K | NIST |
Vc | 0.302 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [135.13; 187.65] | J/mol×K | [350.55; 555.05] | |
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 170 180 190 400 500 | ||||
Cp,gas | 135.13 | J/mol×K | 350.55 | Joback Calculated Property |
Cp,gas | 145.28 | J/mol×K | 384.63 | Joback Calculated Property |
Cp,gas | 154.84 | J/mol×K | 418.72 | Joback Calculated Property |
Cp,gas | 163.83 | J/mol×K | 452.80 | Joback Calculated Property |
Cp,gas | 172.28 | J/mol×K | 486.88 | Joback Calculated Property |
Cp,gas | 180.21 | J/mol×K | 520.97 | Joback Calculated Property |
Cp,gas | 187.65 | J/mol×K | 555.05 | Joback Calculated Property |
Cp,liquid | 175.06 | J/mol×K | 298.15 | NIST |
ΔfusH | [0.65; 4.07] | kJ/mol | [151.60; 274.40] | |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0.5 1 1.5 2 2.5 3 3.5 4 150 200 250 | ||||
ΔfusH | 4.07 | kJ/mol | 151.60 | NIST |
ΔfusH | 0.65 | kJ/mol | 157.00 | NIST |
ΔfusH | 0.97 | kJ/mol | 199.40 | NIST |
ΔfusH | 2.48 | kJ/mol | 274.40 | NIST |
ΔfusH | 2.48 | kJ/mol | 274.40 | NIST |
ΔvapH | [28.45; 30.90] | kJ/mol | [284.00; 337.40] | |
ΔvapH | 30.10 | kJ/mol | 284.00 | NIST |
ΔvapH | 30.90 | kJ/mol | 333.00 | NIST |
ΔvapH | 28.45 | kJ/mol | 337.40 | NIST |
n0 | [1.42000; 1.42000] | [293.10; 298.15] | ||
n0 | 1.42000 | 293.10 | Isother... | |
n0 | 1.42000 | 298.15 | Vapor L... | |
ΔfusS | [4.13; 26.83] | J/mol×K | [151.60; 274.40] | |
ΔfusS | 26.83 | J/mol×K | 151.60 | NIST |
ΔfusS | 4.13 | J/mol×K | 157.00 | NIST |
ΔfusS | 4.87 | J/mol×K | 199.40 | NIST |
ΔfusS | 9.04 | J/mol×K | 274.40 | NIST |
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