Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -687.94 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -813.02 | kJ/mol | Joback Calculated Property |
ΔfusH° | 18.05 | kJ/mol | Joback Calculated Property |
ΔvapH° | 87.64 | kJ/mol | Joback Calculated Property |
log10WS | 0.93 | Crippen Calculated Property | |
logPoct/wat | -1.093 | Crippen Calculated Property | |
McVol | 87.970 | ml/mol | McGowan Calculated Property |
Pc | 7037.97 | kPa | Joback Calculated Property |
Tboil | 674.76 | K | Joback Calculated Property |
Tc | 849.14 | K | Joback Calculated Property |
Tfus | [400.75; 403.15] | K |
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Tfus | 403.15 | K | Thermod... |
Tfus | 400.75 ± 0.60 | K | NIST |
Vc | 0.323 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [222.47; 246.21] | J/mol×K | [674.76; 849.14] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 225 230 235 240 245 700 750 800 850 | ||||
Cp,gas | 222.47 | J/mol×K | 674.76 | Joback Calculated Property |
Cp,gas | 227.04 | J/mol×K | 703.82 | Joback Calculated Property |
Cp,gas | 231.36 | J/mol×K | 732.89 | Joback Calculated Property |
Cp,gas | 235.42 | J/mol×K | 761.95 | Joback Calculated Property |
Cp,gas | 239.25 | J/mol×K | 791.02 | Joback Calculated Property |
Cp,gas | 242.84 | J/mol×K | 820.08 | Joback Calculated Property |
Cp,gas | 246.21 | J/mol×K | 849.14 | Joback Calculated Property |
η | [0.0000080; 0.0048344] | Pa×s | [402.16; 674.76] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 400 500 600 | ||||
η | 0.0048344 | Pa×s | 402.16 | Joback Calculated Property |
η | 0.0009670 | Pa×s | 447.59 | Joback Calculated Property |
η | 0.0002602 | Pa×s | 493.03 | Joback Calculated Property |
η | 0.0000874 | Pa×s | 538.46 | Joback Calculated Property |
η | 0.0000348 | Pa×s | 583.89 | Joback Calculated Property |
η | 0.0000158 | Pa×s | 629.33 | Joback Calculated Property |
η | 0.0000080 | Pa×s | 674.76 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [2.79e-03; 5021.54] | kPa | [403.15; 781.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.51357e+02 | |||
Coefficient B | -2.63327e+04 | |||
Coefficient C | -3.22403e+01 | |||
Coefficient D | 9.21419e-06 | |||
Temperature range, min. | 403.15 | |||
Temperature range, max. | 781.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 400 500 600 700 | ||||
Pvap | 2.79e-03 | kPa | 403.15 | Calculated Property |
Pvap | 0.08 | kPa | 445.13 | Calculated Property |
Pvap | 0.97 | kPa | 487.12 | Calculated Property |
Pvap | 7.26 | kPa | 529.10 | Calculated Property |
Pvap | 36.79 | kPa | 571.08 | Calculated Property |
Pvap | 138.93 | kPa | 613.07 | Calculated Property |
Pvap | 420.70 | kPa | 655.05 | Calculated Property |
Pvap | 1078.61 | kPa | 697.03 | Calculated Property |
Pvap | 2439.33 | kPa | 739.02 | Calculated Property |
Pvap | 5021.54 | kPa | 781.00 | Calculated Property |
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