Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4411.27 ± 0.79 | kJ/mol | NIST |
ΔfG° | 72.65 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-25.00; -19.90] | kJ/mol |
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ΔfH°gas | -25.00 | kJ/mol | NIST |
ΔfH°gas | -19.90 ± 0.90 | kJ/mol | NIST |
ΔfH°liquid | -58.37 ± 0.88 | kJ/mol | NIST |
ΔfusH° | 7.58 | kJ/mol | Joback Calculated Property |
ΔvapH° | [38.50; 38.50] | kJ/mol |
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ΔvapH° | 38.50 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 38.50 ± 0.30 | kJ/mol | NIST |
IE | 8.53 ± 0.01 | eV | NIST |
log10WS | -2.50 | Crippen Calculated Property | |
logPoct/wat | 2.507 | Crippen Calculated Property | |
McVol | 94.330 | ml/mol | McGowan Calculated Property |
Pc | 3646.53 | kPa | Joback Calculated Property |
Inp | [744.00; 779.00] |
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|
Inp | 751.00 | NIST | |
Inp | 751.00 | NIST | |
Inp | 746.10 | NIST | |
Inp | 747.40 | NIST | |
Inp | 752.00 | NIST | |
Inp | 744.00 | NIST | |
Inp | 744.00 | NIST | |
Inp | 747.00 | NIST | |
Inp | 748.00 | NIST | |
Inp | 748.00 | NIST | |
Inp | 749.00 | NIST | |
Inp | 749.00 | NIST | |
Inp | 751.00 | NIST | |
Inp | 753.00 | NIST | |
Inp | 752.00 | NIST | |
Inp | 750.00 | NIST | |
Inp | Outlier 775.00 | NIST | |
Inp | Outlier 779.00 | NIST | |
Inp | 747.40 | NIST | |
Inp | 748.40 | NIST | |
Inp | 750.90 | NIST | |
Inp | 747.00 | NIST | |
Inp | 748.00 | NIST | |
Inp | 751.00 | NIST | |
Inp | 744.00 | NIST | |
Inp | 747.00 | NIST | |
Inp | 749.00 | NIST | |
Inp | 751.00 | NIST | |
Inp | 749.00 | NIST | |
Inp | 750.00 | NIST | |
Inp | 753.00 | NIST | |
Inp | 751.00 | NIST | |
Inp | 754.00 | NIST | |
Inp | 752.00 | NIST | |
Inp | 755.00 | NIST | |
Inp | 744.00 | NIST | |
Inp | 744.00 | NIST | |
I | [880.00; 891.10] |
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|
I | 891.00 | NIST | |
I | 880.00 | NIST | |
I | 886.00 | NIST | |
I | 891.00 | NIST | |
I | 891.10 | NIST | |
I | 880.50 | NIST | |
I | 885.90 | NIST | |
I | 891.10 | NIST | |
I | 880.50 | NIST | |
I | 885.90 | NIST | |
I | 891.00 | NIST | |
I | 880.50 | NIST | |
Tboil | [376.15; 382.00] | K |
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Tboil | 379.50 | K | NIST |
Tboil | 380.00 ± 1.00 | K | NIST |
Tboil | 379.70 ± 0.40 | K | NIST |
Tboil | 379.70 ± 0.50 | K | NIST |
Tboil | 379.50 ± 0.30 | K | NIST |
Tboil | 378.00 ± 2.00 | K | NIST |
Tboil | 380.50 ± 1.00 | K | NIST |
Tboil | 379.70 ± 3.00 | K | NIST |
Tboil | 380.00 ± 3.00 | K | NIST |
Tboil | 377.00 ± 3.00 | K | NIST |
Tboil | 377.00 ± 3.00 | K | NIST |
Tboil | 379.48 ± 0.30 | K | NIST |
Tboil | 379.35 ± 0.30 | K | NIST |
Tboil | 382.00 ± 4.00 | K | NIST |
Tboil | Outlier 376.15 ± 0.50 | K | NIST |
Tboil | 379.90 ± 2.00 | K | NIST |
Tboil | 381.00 ± 3.00 | K | NIST |
Tc | 582.00 | K | Joback Calculated Property |
Tfus | [149.80; 154.35] | K |
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Tfus | 149.80 ± 0.50 | K | NIST |
Tfus | 154.35 ± 0.30 | K | NIST |
Vc | 0.355 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [164.17; 233.94] | J/mol×K | [383.65; 582.00] | ![]() |
Cp,gas | 164.17 | J/mol×K | 383.65 | Joback Calculated Property |
Cp,gas | 177.41 | J/mol×K | 416.71 | Joback Calculated Property |
Cp,gas | 189.97 | J/mol×K | 449.77 | Joback Calculated Property |
Cp,gas | 201.88 | J/mol×K | 482.82 | Joback Calculated Property |
Cp,gas | 213.16 | J/mol×K | 515.88 | Joback Calculated Property |
Cp,gas | 223.84 | J/mol×K | 548.94 | Joback Calculated Property |
Cp,gas | 233.94 | J/mol×K | 582.00 | Joback Calculated Property |
Cp,liquid | 188.30 | J/mol×K | 298.15 | NIST |
η | [0.0002801; 0.0031534] | Pa×s | [197.07; 383.65] | ![]() |
η | 0.0031534 | Pa×s | 197.07 | Joback Calculated Property |
η | 0.0015999 | Pa×s | 228.17 | Joback Calculated Property |
η | 0.0009552 | Pa×s | 259.26 | Joback Calculated Property |
η | 0.0006369 | Pa×s | 290.36 | Joback Calculated Property |
η | 0.0004593 | Pa×s | 321.46 | Joback Calculated Property |
η | 0.0003509 | Pa×s | 352.55 | Joback Calculated Property |
η | 0.0002801 | Pa×s | 383.65 | Joback Calculated Property |
ΔvapH | 36.50 | kJ/mol | 363.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.68] | kPa | [275.85; 404.91] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41400e+01 | |||
Coefficient B | -3.14169e+03 | |||
Coefficient C | -4.90480e+01 | |||
Temperature range, min. | 275.85 | |||
Temperature range, max. | 404.91 | |||
Pvap | 1.33 | kPa | 275.85 | Calculated Property |
Pvap | 3.04 | kPa | 290.19 | Calculated Property |
Pvap | 6.31 | kPa | 304.53 | Calculated Property |
Pvap | 12.14 | kPa | 318.87 | Calculated Property |
Pvap | 21.85 | kPa | 333.21 | Calculated Property |
Pvap | 37.16 | kPa | 347.55 | Calculated Property |
Pvap | 60.20 | kPa | 361.89 | Calculated Property |
Pvap | 93.48 | kPa | 376.23 | Calculated Property |
Pvap | 139.90 | kPa | 390.57 | Calculated Property |
Pvap | 202.68 | kPa | 404.91 | Calculated Property |
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