Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 134.36 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -497.41 | kJ/mol | Joback Calculated Property |
ΔfusH° | 52.74 | kJ/mol | Joback Calculated Property |
ΔvapH° | [111.90; 115.60] | kJ/mol |
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ΔvapH° | 111.90 | kJ/mol | NIST |
ΔvapH° | 114.90 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 115.60 ± 1.90 | kJ/mol | NIST |
ΔvapH° | 115.60 | kJ/mol | NIST |
log10WS | -9.03 | Crippen Calculated Property | |
logPoct/wat | 8.828 | Crippen Calculated Property | |
McVol | 320.840 | ml/mol | McGowan Calculated Property |
Pc | [980.00; 1000.00] | kPa |
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Pc | 980.00 | kPa | KDB |
Pc | 1000.00 ± 200.00 | kPa | NIST |
Pc | 982.00 ± 40.00 | kPa | NIST |
Inp | [356.14; 374.90] |
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|
Inp | 356.14 | NIST | |
Inp | 362.61 | NIST | |
Inp | 374.90 | NIST | |
Inp | 374.90 | NIST | |
Inp | 374.90 | NIST | |
Tboil | 641.80 | K | NIST |
Tc | [763.15; 787.00] | K |
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Tc | 786.00 | K | KDB |
Tc | 787.00 | K | Critica... |
Tc | 786.00 ± 8.00 | K | NIST |
Tc | 785.60 ± 3.00 | K | NIST |
Tc | 763.15 ± 10.00 | K | NIST |
Tfus | 337.70 | K | Joback Calculated Property |
Ttriple | [315.20; 317.22] | K |
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Ttriple | 315.60 | K | Thermal... |
Ttriple | 317.22 | K | Magneti... |
Ttriple | 315.20 ± 1.00 | K | NIST |
Vc | 1.268 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [962.02; 1079.56] | J/mol×K | [702.76; 866.55] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 960 980 1000 1020 1040 1060 1080 700 750 800 850 | ||||
Cp,gas | 962.02 | J/mol×K | 702.76 | Joback Calculated Property |
Cp,gas | 983.83 | J/mol×K | 730.06 | Joback Calculated Property |
Cp,gas | 1004.72 | J/mol×K | 757.36 | Joback Calculated Property |
Cp,gas | 1024.70 | J/mol×K | 784.66 | Joback Calculated Property |
Cp,gas | 1043.81 | J/mol×K | 811.95 | Joback Calculated Property |
Cp,gas | 1062.09 | J/mol×K | 839.25 | Joback Calculated Property |
Cp,gas | 1079.56 | J/mol×K | 866.55 | Joback Calculated Property |
Cp,liquid | 739.00 | J/mol×K | 353.00 | NIST |
Cp,solid | [468.00; 563.60] | J/mol×K | [299.00; 300.00] | ![]() |
Cp,solid | 563.60 | J/mol×K | 299.00 | NIST |
Cp,solid | 468.00 | J/mol×K | 300.00 | NIST |
η | [0.0000755; 0.0029440] | Pa×s | [337.70; 702.76] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 400 500 600 700 | ||||
η | 0.0029440 | Pa×s | 337.70 | Joback Calculated Property |
η | 0.0010030 | Pa×s | 398.54 | Joback Calculated Property |
η | 0.0004545 | Pa×s | 459.39 | Joback Calculated Property |
η | 0.0002478 | Pa×s | 520.23 | Joback Calculated Property |
η | 0.0001534 | Pa×s | 581.07 | Joback Calculated Property |
η | 0.0001040 | Pa×s | 641.92 | Joback Calculated Property |
η | 0.0000755 | Pa×s | 702.76 | Joback Calculated Property |
ΔfusH | [29.51; 78.50] | kJ/mol | [315.20; 316.90] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 30 40 50 60 70 80 315.5 316 316.5 | ||||
ΔfusH | 29.51 | kJ/mol | 315.20 | NIST |
ΔfusH | 47.84 | kJ/mol | 316.10 | NIST |
ΔfusH | 47.84 | kJ/mol | 316.10 | NIST |
ΔfusH | 49.10 | kJ/mol | 316.60 | NIST |
ΔfusH | 78.50 | kJ/mol | 316.90 | NIST |
ΔsubH | 172.60 ± 2.00 | kJ/mol | 391.00 | NIST |
ΔvapH | [84.30; 124.00] | kJ/mol | [298.00; 536.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 90 100 110 120 300 400 500 | ||||
ΔvapH | 110.00 | kJ/mol | 298.00 | A Compa... |
ΔvapH | 111.90 | kJ/mol | 298.15 | Vapor P... |
ΔvapH | 124.00 ± 2.00 | kJ/mol | 391.00 | NIST |
ΔvapH | 100.90 | kJ/mol | 407.50 | NIST |
ΔvapH | 89.90 | kJ/mol | 424.00 | NIST |
ΔvapH | 84.30 | kJ/mol | 513.00 | NIST |
ΔvapH | 91.30 | kJ/mol | 536.50 | NIST |
ΔfusS | [93.62; 151.36] | J/mol×K | [315.20; 316.10] | ![]() |
ΔfusS | 93.62 | J/mol×K | 315.20 | NIST |
ΔfusS | 151.36 | J/mol×K | 316.10 | NIST |
γ | [0.03; 0.03] | N/m | [323.15; 343.15] | ![]() |
γ | 0.03 | N/m | 323.15 | Surface... |
γ | 0.03 | N/m | 333.15 | Surface... |
γ | 0.03 | N/m | 343.15 | Surface... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.11; 101.70] | kPa | [431.15; 649.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.28366e+02 | |||
Coefficient B | -1.54319e+04 | |||
Coefficient C | -1.57784e+01 | |||
Coefficient D | 5.23129e-06 | |||
Temperature range, min. | 431.15 | |||
Temperature range, max. | 649.15 | |||
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 500 600 | ||||
Pvap | 0.11 | kPa | 431.15 | Calculated Property |
Pvap | 0.36 | kPa | 455.37 | Calculated Property |
Pvap | 0.99 | kPa | 479.59 | Calculated Property |
Pvap | 2.43 | kPa | 503.82 | Calculated Property |
Pvap | 5.38 | kPa | 528.04 | Calculated Property |
Pvap | 10.95 | kPa | 552.26 | Calculated Property |
Pvap | 20.75 | kPa | 576.48 | Calculated Property |
Pvap | 37.03 | kPa | 600.71 | Calculated Property |
Pvap | 62.75 | kPa | 624.93 | Calculated Property |
Pvap | 101.70 | kPa | 649.15 | Calculated Property |
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