Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -25.94 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -153.32 | kJ/mol | Joback Calculated Property |
ΔfusH° | 8.61 | kJ/mol | Joback Calculated Property |
ΔvapH° | 28.46 | kJ/mol | Joback Calculated Property |
log10WS | -1.35 | Crippen Calculated Property | |
logPoct/wat | 1.556 | Crippen Calculated Property | |
McVol | 82.880 | ml/mol | McGowan Calculated Property |
Pc | 3572.80 | kPa | Joback Calculated Property |
Tboil | 332.90 | K | Joback Calculated Property |
Tc | 500.59 | K | Joback Calculated Property |
Tfus | 166.58 | K | Joback Calculated Property |
Vc | 0.315 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [135.21; 180.14] | J/mol×K | [332.90; 500.59] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 140 150 160 170 180 350 400 450 500 | ||||
Cp,gas | 135.21 | J/mol×K | 332.90 | Joback Calculated Property |
Cp,gas | 143.28 | J/mol×K | 360.85 | Joback Calculated Property |
Cp,gas | 151.11 | J/mol×K | 388.80 | Joback Calculated Property |
Cp,gas | 158.71 | J/mol×K | 416.74 | Joback Calculated Property |
Cp,gas | 166.08 | J/mol×K | 444.69 | Joback Calculated Property |
Cp,gas | 173.22 | J/mol×K | 472.64 | Joback Calculated Property |
Cp,gas | 180.14 | J/mol×K | 500.59 | Joback Calculated Property |
η | [0.0002010; 0.0024826] | Pa×s | [166.58; 332.90] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 200 250 300 | ||||
η | 0.0024826 | Pa×s | 166.58 | Joback Calculated Property |
η | 0.0012110 | Pa×s | 194.30 | Joback Calculated Property |
η | 0.0007067 | Pa×s | 222.02 | Joback Calculated Property |
η | 0.0004648 | Pa×s | 249.74 | Joback Calculated Property |
η | 0.0003324 | Pa×s | 277.46 | Joback Calculated Property |
η | 0.0002526 | Pa×s | 305.18 | Joback Calculated Property |
η | 0.0002010 | Pa×s | 332.90 | Joback Calculated Property |
Pvap | [20.00; 101.70] | kPa | [296.02; 337.90] | ![]() |
T(K) Vapor pressure (kPa) 20 40 60 80 100 300 310 320 330 | ||||
Pvap | 20.00 | kPa | 296.02 | Isother... |
Pvap | 25.00 | kPa | 301.62 | Isother... |
Pvap | 30.00 | kPa | 305.44 | Isother... |
Pvap | 35.00 | kPa | 309.37 | Isother... |
Pvap | 40.00 | kPa | 312.65 | Isother... |
Pvap | 45.00 | kPa | 315.13 | Isother... |
Pvap | 50.00 | kPa | 317.88 | Isother... |
Pvap | 55.00 | kPa | 320.29 | Isother... |
Pvap | 60.00 | kPa | 322.72 | Isother... |
Pvap | 65.00 | kPa | 324.90 | Isother... |
Pvap | 70.00 | kPa | 326.95 | Isother... |
Pvap | 75.00 | kPa | 328.89 | Isother... |
Pvap | 80.00 | kPa | 330.76 | Isother... |
Pvap | 85.00 | kPa | 332.86 | Isother... |
Pvap | 90.00 | kPa | 334.22 | Isother... |
Pvap | 95.00 | kPa | 336.28 | Isother... |
Pvap | 100.00 | kPa | 337.38 | Isother... |
Pvap | 101.70 | kPa | 337.90 | Isother... |
n0 | 1.39094 ± 0.00005 | 298.15 | Binary ... | |
ρl | [762.69; 768.97] | kg/m3 | [293.15; 298.15] | ![]() |
ρl | 768.97 ± 0.01 | kg/m3 | 293.15 | Isother... |
ρl | 762.98 ± 0.01 | kg/m3 | 298.15 | Binary ... |
ρl | 762.96 | kg/m3 | 298.15 | Liquid ... |
ρl | 762.69 ± 0.01 | kg/m3 | 298.15 | Binary ... |
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