Property | Value | Unit | Source |
---|---|---|---|
ΔcH°gas | [-3296.00; -3258.00] | kJ/mol | |
ΔcH°gas | -3296.00 ± 0.71 | kJ/mol | NIST |
ΔcH°gas | -3258.00 ± 1.30 | kJ/mol | NIST |
ΔfG° | 127.04 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 185.10 ± 0.75 | kJ/mol | NIST |
ΔfusH° | -0.29 | kJ/mol | Joback Calculated Property |
ΔvapH° | [27.50; 27.70] | kJ/mol | |
ΔvapH° | 27.70 | kJ/mol | NIST |
ΔvapH° | 27.50 ± 0.10 | kJ/mol | NIST |
IE | [9.26; 9.73] | eV | |
IE | 9.26 | eV | NIST |
IE | 9.26 | eV | NIST |
IE | 9.26 | eV | NIST |
IE | 9.26 | eV | NIST |
IE | 9.37 ± 0.05 | eV | NIST |
IE | Outlier 9.73 | eV | NIST |
IE | 9.45 | eV | NIST |
log10WS | -1.46 | Crippen Calculated Property | |
logPoct/wat | 1.560 | Crippen Calculated Property | |
McVol | 59.590 | ml/mol | McGowan Calculated Property |
Pc | 5213.15 | kPa | Joback Calculated Property |
S°liquid | 193.68 | J/mol×K | NIST |
Tboil | [303.18; 312.18] | K | |
Tboil | 312.10 | K | NIST |
Tboil | 303.18 ± 0.10 | K | NIST |
Tboil | 312.18 ± 0.10 | K | NIST |
Tc | 506.40 | K | NIST |
Tfus | [166.10; 166.10] | K | |
Tfus | 166.10 ± 0.10 | K | NIST |
Tfus | 166.10 ± 0.10 | K | NIST |
Ttriple | 166.14 ± 0.05 | K | NIST |
Vc | 0.236 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [277.69; 286.35] | J/mol×K | [283.16; 312.14] | |
Cp,gas | 277.69 ± 0.63 | J/mol×K | 283.16 | NIST |
Cp,gas | 282.21 ± 0.63 | J/mol×K | 298.16 | NIST |
Cp,gas | 286.35 ± 0.63 | J/mol×K | 312.14 | NIST |
Cp,liquid | 134.52 | J/mol×K | 298.15 | NIST |
ΔfusH | [6.43; 6.43] | kJ/mol | [166.10; 166.14] | |
ΔfusH | 6.43 | kJ/mol | 166.10 | NIST |
ΔfusH | 6.43 | kJ/mol | 166.10 | NIST |
ΔfusH | 6.43 | kJ/mol | 166.14 | NIST |
ΔvapH | [26.70; 28.60] | kJ/mol | [283.00; 312.13] | |
ΔvapH | 28.30 ± 0.10 | kJ/mol | 283.00 | NIST |
ΔvapH | 28.60 | kJ/mol | 310.00 | NIST |
ΔvapH | 26.70 ± 0.10 | kJ/mol | 312.00 | NIST |
ΔvapH | 26.76 | kJ/mol | 312.10 | NIST |
ΔvapH | 26.75 | kJ/mol | 312.13 | NIST |
ΔfusS | 38.72 | J/mol×K | 166.14 | NIST |
ΔvapS | 85.70 | J/mol×K | 312.13 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [227.42; 333.14] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.44024e+01 | |||
Coefficient B | -2.70023e+03 | |||
Coefficient C | -3.61160e+01 | |||
Temperature range, min. | 227.42 | |||
Temperature range, max. | 333.14 | |||
Pvap | 1.33 | kPa | 227.42 | Calculated Property |
Pvap | 3.02 | kPa | 239.17 | Calculated Property |
Pvap | 6.24 | kPa | 250.91 | Calculated Property |
Pvap | 11.98 | kPa | 262.66 | Calculated Property |
Pvap | 21.56 | kPa | 274.41 | Calculated Property |
Pvap | 36.71 | kPa | 286.15 | Calculated Property |
Pvap | 59.60 | kPa | 297.90 | Calculated Property |
Pvap | 92.81 | kPa | 309.65 | Calculated Property |
Pvap | 139.36 | kPa | 321.39 | Calculated Property |
Pvap | 202.64 | kPa | 333.14 | Calculated Property |
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