Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | [-2462.70; -2458.50] | kJ/mol |
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ΔcH°liquid | -2458.50 ± 0.40 | kJ/mol | NIST |
ΔcH°liquid | -2462.70 ± 0.60 | kJ/mol | NIST |
ΔfG° | 10.98 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -69.50 ± 0.56 | kJ/mol | NIST |
ΔfH°liquid | [-116.00; -111.70] | kJ/mol |
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ΔfH°liquid | -116.00 ± 0.50 | kJ/mol | NIST |
ΔfH°liquid | -111.70 ± 0.60 | kJ/mol | NIST |
ΔfusH° | 8.81 | kJ/mol | Joback Calculated Property |
ΔvapH° | [46.48; 46.50] | kJ/mol |
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ΔvapH° | 46.48 ± 0.25 | kJ/mol | NIST |
ΔvapH° | 46.50 ± 0.30 | kJ/mol | NIST |
log10WS | -0.45 | Crippen Calculated Property | |
logPoct/wat | 0.546 | Crippen Calculated Property | |
McVol | 74.470 | ml/mol | McGowan Calculated Property |
Pc | 3699.95 | kPa | Joback Calculated Property |
Tboil | 415.42 | K | Joback Calculated Property |
Tc | 607.19 | K | Joback Calculated Property |
Tfus | 222.06 | K | Joback Calculated Property |
Vc | 0.303 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [137.15; 172.21] | J/mol×K | [415.42; 607.19] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 140 150 160 170 450 500 550 600 | ||||
Cp,gas | 137.15 | J/mol×K | 415.42 | Joback Calculated Property |
Cp,gas | 143.44 | J/mol×K | 447.38 | Joback Calculated Property |
Cp,gas | 149.56 | J/mol×K | 479.34 | Joback Calculated Property |
Cp,gas | 155.51 | J/mol×K | 511.31 | Joback Calculated Property |
Cp,gas | 161.26 | J/mol×K | 543.27 | Joback Calculated Property |
Cp,gas | 166.84 | J/mol×K | 575.23 | Joback Calculated Property |
Cp,gas | 172.21 | J/mol×K | 607.19 | Joback Calculated Property |
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