Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -15196.00 ± 1.00 | kJ/mol | NIST |
ΔfG° | -82.72 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -783.49 | kJ/mol | Joback Calculated Property |
ΔfusH° | 60.70 | kJ/mol | Joback Calculated Property |
ΔvapH° | 78.17 | kJ/mol | Joback Calculated Property |
log10WS | -8.73 | Crippen Calculated Property | |
logPoct/wat | 8.371 | Crippen Calculated Property | |
McVol | 356.460 | ml/mol | McGowan Calculated Property |
Pc | 827.64 | kPa | Joback Calculated Property |
Inp | [2573.00; 2596.00] |
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Inp | 2576.00 | NIST | |
Inp | 2596.00 | NIST | |
Inp | 2596.00 | NIST | |
Inp | 2593.50 | NIST | |
Inp | 2576.00 | NIST | |
Inp | 2573.00 | NIST | |
Inp | 2593.50 | NIST | |
I | [2883.00; 2883.00] |
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I | 2883.00 | NIST | |
I | 2883.00 | NIST | |
Tboil | 824.81 | K | Joback Calculated Property |
Tc | 1009.81 | K | Joback Calculated Property |
Tfus | 432.40 | K | Joback Calculated Property |
Vc | 1.403 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [1156.81; 1270.08] | J/mol×K | [824.81; 1009.81] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 1160 1180 1200 1220 1240 1260 1280 850 900 950 1000 | ||||
Cp,gas | 1156.81 | J/mol×K | 824.81 | Joback Calculated Property |
Cp,gas | 1178.47 | J/mol×K | 855.64 | Joback Calculated Property |
Cp,gas | 1198.97 | J/mol×K | 886.48 | Joback Calculated Property |
Cp,gas | 1218.34 | J/mol×K | 917.31 | Joback Calculated Property |
Cp,gas | 1236.63 | J/mol×K | 948.14 | Joback Calculated Property |
Cp,gas | 1253.86 | J/mol×K | 978.97 | Joback Calculated Property |
Cp,gas | 1270.08 | J/mol×K | 1009.81 | Joback Calculated Property |
η | [0.0000418; 0.0010603] | Pa×s | [432.40; 824.81] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 500 600 700 800 | ||||
η | 0.0010603 | Pa×s | 432.40 | Joback Calculated Property |
η | 0.0004342 | Pa×s | 497.80 | Joback Calculated Property |
η | 0.0002188 | Pa×s | 563.20 | Joback Calculated Property |
η | 0.0001271 | Pa×s | 628.61 | Joback Calculated Property |
η | 0.0000818 | Pa×s | 694.01 | Joback Calculated Property |
η | 0.0000568 | Pa×s | 759.41 | Joback Calculated Property |
η | 0.0000418 | Pa×s | 824.81 | Joback Calculated Property |
ΔfusH | [19.16; 77.82] | kJ/mol | [321.00; 321.00] | ![]() |
ΔfusH | 19.16 | kJ/mol | 321.00 | NIST |
ΔfusH | 77.82 | kJ/mol | 321.00 | NIST |
ΔsubH | 196.50 | kJ/mol | 315.50 | NIST |
ΔvapH | 127.50 | kJ/mol | 335.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 514.20 | K | 1.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.61] | kPa | [596.00; 686.82] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 2.91277e+01 | |||
Coefficient B | -1.24178e+04 | |||
Coefficient C | -1.65424e+02 | |||
Temperature range, min. | 596.00 | |||
Temperature range, max. | 686.82 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 600 650 | ||||
Pvap | 1.33 | kPa | 596.00 | Calculated Property |
Pvap | 2.58 | kPa | 606.09 | Calculated Property |
Pvap | 4.85 | kPa | 616.18 | Calculated Property |
Pvap | 8.87 | kPa | 626.27 | Calculated Property |
Pvap | 15.79 | kPa | 636.36 | Calculated Property |
Pvap | 27.46 | kPa | 646.46 | Calculated Property |
Pvap | 46.68 | kPa | 656.55 | Calculated Property |
Pvap | 77.66 | kPa | 666.64 | Calculated Property |
Pvap | 126.63 | kPa | 676.73 | Calculated Property |
Pvap | 202.61 | kPa | 686.82 | Calculated Property |
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