Property | Value | Unit | Source |
---|---|---|---|
PAff | 529.30 | kJ/mol | NIST |
BasG | 503.70 | kJ/mol | NIST |
ΔcH°liquid | [-2222.30; -1519.89] | kJ/mol | |
ΔcH°liquid | -1519.89 | kJ/mol | NIST |
ΔcH°liquid | -2222.30 | kJ/mol | NIST |
ΔfG° | -818.86 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-953.40; -678.00] | kJ/mol | |
ΔfH°gas | -933.00 | kJ/mol | NIST |
ΔfH°gas | -933.20 ± 0.80 | kJ/mol | NIST |
ΔfH°gas | -933.20 ± 0.75 | kJ/mol | NIST |
ΔfH°gas | -953.40 ± 1.60 | kJ/mol | NIST |
ΔfH°gas | -934.00 ± 2.00 | kJ/mol | NIST |
ΔfH°gas | -920.90 ± 5.90 | kJ/mol | NIST |
ΔfH°gas | -917.10 ± 9.60 | kJ/mol | NIST |
ΔfH°gas | -908.80 ± 5.00 | kJ/mol | NIST |
ΔfH°gas | -913.40 | kJ/mol | NIST |
ΔfH°gas | -922.20 | kJ/mol | NIST |
ΔfH°gas | -912.00 ± 8.00 | kJ/mol | NIST |
ΔfH°gas | Outlier -678.00 ± 8.00 | kJ/mol | NIST |
ΔfusH° | 3.25 | kJ/mol | Joback Calculated Property |
ΔvapH° | 13.26 | kJ/mol | Joback Calculated Property |
IE | [14.70; 16.50] | eV | |
IE | 14.70 | eV | NIST |
IE | 16.20 ± 0.10 | eV | NIST |
IE | 15.30 | eV | NIST |
IE | 16.20 | eV | NIST |
IE | 14.70 | eV | NIST |
IE | 16.50 | eV | NIST |
IE | 15.70 | eV | NIST |
IE | 16.20 | eV | NIST |
IE | 16.26 | eV | NIST |
IE | 16.25 ± 0.04 | eV | NIST |
IE | 16.20 | eV | NIST |
log10WS | -1.25 | Crippen Calculated Property | |
logPoct/wat | 1.476 | Crippen Calculated Property | |
McVol | 32.030 | ml/mol | McGowan Calculated Property |
Pc | 3745.00 ± 10.00 | kPa | NIST |
ρc | 629.67 ± 0.88 | kg/m3 | NIST |
Inp | 82.00 | NIST | |
S°liquid | 143.97 | J/mol×K | NIST |
Tboil | 216.13 | K | Joback Calculated Property |
Tc | [227.50; 227.50] | K | |
Tc | 227.50 ± 0.10 | K | NIST |
Tc | 227.50 ± 0.02 | K | NIST |
Tfus | [86.85; 89.50] | K | |
Tfus | 89.00 ± 1.50 | K | NIST |
Tfus | 89.50 ± 0.50 | K | NIST |
Tfus | 86.85 ± 1.00 | K | NIST |
Vc | 0.142 ± 800.000 | m3/kmol | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [49.05; 67.36] | J/mol×K | [216.13; 342.68] | |
T(K) Ideal gas heat capacity (J/mol×K) 50 55 60 65 250 300 | ||||
Cp,gas | 49.05 | J/mol×K | 216.13 | Joback Calculated Property |
Cp,gas | 52.53 | J/mol×K | 237.22 | Joback Calculated Property |
Cp,gas | 55.83 | J/mol×K | 258.31 | Joback Calculated Property |
Cp,gas | 58.96 | J/mol×K | 279.41 | Joback Calculated Property |
Cp,gas | 61.92 | J/mol×K | 300.50 | Joback Calculated Property |
Cp,gas | 64.72 | J/mol×K | 321.59 | Joback Calculated Property |
Cp,gas | 67.36 | J/mol×K | 342.68 | Joback Calculated Property |
Cp,liquid | 80.08 | J/mol×K | 145.00 | NIST |
ΔfusH | [0.69; 1.73] | kJ/mol | [76.10; 89.56] | |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0.6 0.8 1 1.2 1.4 1.6 1.8 80 85 | ||||
ΔfusH | 1.73 | kJ/mol | 76.10 | NIST |
ΔfusH | 1.46 | kJ/mol | 76.10 | NIST |
ΔfusH | 1.71 | kJ/mol | 76.27 | NIST |
ΔfusH | 0.69 | kJ/mol | 88.40 | NIST |
ΔfusH | 0.71 | kJ/mol | 89.50 | NIST |
ΔfusH | 0.71 | kJ/mol | 89.56 | NIST |
ΔfusH | 0.71 | kJ/mol | 89.56 | NIST |
ΔsubH | [14.00; 17.00] | kJ/mol | [76.00; 87.50] | |
ΔsubH | 17.00 | kJ/mol | 76.00 | NIST |
ΔsubH | 14.00 | kJ/mol | 83.00 | NIST |
ΔsubH | 14.70 | kJ/mol | 87.50 | NIST |
ΔvapH | [11.81; 12.80] | kJ/mol | [119.50; 211.00] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 11.8 12 12.2 12.4 12.6 12.8 150 200 | ||||
ΔvapH | 12.80 | kJ/mol | 119.50 | NIST |
ΔvapH | 12.30 | kJ/mol | 126.00 | NIST |
ΔvapH | 12.40 | kJ/mol | 131.00 | NIST |
ΔvapH | 11.81 | kJ/mol | 145.12 | NIST |
ΔvapH | 11.90 | kJ/mol | 178.50 | NIST |
ΔvapH | 12.10 | kJ/mol | 211.00 | NIST |
Pvap | [171.92; 2163.00] | kPa | [153.23; 210.03] | |
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 160 180 200 | ||||
Pvap | 171.92 | kPa | 153.23 | Vapor-l... |
Pvap | 243.00 | kPa | 159.61 | Vapor-L... |
Pvap | 269.00 | kPa | 161.58 | Vapor-L... |
Pvap | 431.00 | kPa | 169.38 | Vapor-L... |
Pvap | 517.00 | kPa | 173.90 | Vapor-L... |
Pvap | 651.00 | kPa | 178.93 | Vapor-L... |
Pvap | 679.00 | kPa | 179.68 | Isother... |
Pvap | 1058.00 | kPa | 190.14 | Isother... |
Pvap | 1205.31 | kPa | 193.43 | Vapor-l... |
Pvap | 1575.00 | kPa | 200.68 | Isother... |
Pvap | 2163.00 | kPa | 210.03 | Isother... |
ΔfusS | [7.70; 22.43] | J/mol×K | [76.10; 89.56] | |
T(K) Entropy of fusion at a given temperature (J/mol×K) 8 10 12 14 16 18 20 22 80 85 | ||||
ΔfusS | 21.40 | J/mol×K | 76.10 | NIST |
ΔfusS | 19.20 | J/mol×K | 76.10 | NIST |
ΔfusS | 22.43 | J/mol×K | 76.27 | NIST |
ΔfusS | 7.70 | J/mol×K | 88.40 | NIST |
ΔfusS | 7.90 | J/mol×K | 89.50 | NIST |
ΔfusS | 7.95 | J/mol×K | 89.56 | NIST |
ΔvapS | 81.41 | J/mol×K | 145.12 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 3735.12] | kPa | [103.48; 227.51] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.39902e+01 | |||
Coefficient B | -1.23425e+03 | |||
Coefficient C | -1.34020e+01 | |||
Temperature range, min. | 103.48 | |||
Temperature range, max. | 227.51 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 150 200 | ||||
Pvap | 1.33 | kPa | 103.48 | Calculated Property |
Pvap | 8.22 | kPa | 117.26 | Calculated Property |
Pvap | 33.06 | kPa | 131.04 | Calculated Property |
Pvap | 99.34 | kPa | 144.82 | Calculated Property |
Pvap | 242.24 | kPa | 158.60 | Calculated Property |
Pvap | 506.11 | kPa | 172.39 | Calculated Property |
Pvap | 940.15 | kPa | 186.17 | Calculated Property |
Pvap | 1593.69 | kPa | 199.95 | Calculated Property |
Pvap | 2512.34 | kPa | 213.73 | Calculated Property |
Pvap | 3735.12 | kPa | 227.51 | Calculated Property |
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