Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1800 | KDB | |
ΔcH°liquid | -747.80 ± 0.60 | kJ/mol | NIST |
ΔfG° | 73.78 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [118.00; 122.00] | kJ/mol |
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ΔfH°gas | 118.00 ± 4.20 | kJ/mol | NIST |
ΔfH°gas | 122.00 ± 4.20 | kJ/mol | NIST |
ΔfH°liquid | 68.50 ± 0.80 | kJ/mol | NIST |
ΔfusH° | 7.16 | kJ/mol | Joback Calculated Property |
ΔvapH° | [45.60; 49.00] | kJ/mol |
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ΔvapH° | 45.60 | kJ/mol | NIST |
ΔvapH° | 45.60 | kJ/mol | NIST |
ΔvapH° | 49.00 | kJ/mol | NIST |
IE | [9.46; 9.46] | eV |
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IE | 9.46 ± 0.02 | eV | NIST |
IE | 9.46 ± 0.02 | eV | NIST |
IE | 9.46 | eV | NIST |
IE | 9.46 | eV | NIST |
log10WS | [-2.34; -2.34] |
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|
log10WS | -2.34 | Aq. Sol... | |
log10WS | -2.34 | Estimat... | |
logPoct/wat | 1.814 | Crippen Calculated Property | |
McVol | 76.590 | ml/mol | McGowan Calculated Property |
Pc | 5420.00 | kPa | KDB |
Inp | [876.00; 911.00] |
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|
Inp | 903.00 | NIST | |
Inp | 911.00 | NIST | |
Inp | 895.00 | NIST | |
Inp | 876.00 | NIST | |
Inp | 878.00 | NIST | |
I | [1510.47; 1522.18] |
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|
I | 1510.47 | NIST | |
I | 1522.18 | NIST | |
Tboil | 455.20 | K | KDB |
Tc | 740.90 | K | KDB |
Tfus | [278.93; 279.00] | K |
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Tfus | 279.00 | K | KDB |
Tfus | 278.93 | K | Aq. Sol... |
Vc | 0.268 | m3/kmol | KDB |
Zc | 0.2353570 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [70.80; 81.08] | J/mol×K | [408.56; 665.08] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 70 72 74 76 78 80 82 500 600 | ||||
Cp,gas | 70.80 | J/mol×K | 408.56 | Joback Calculated Property |
Cp,gas | 73.16 | J/mol×K | 451.31 | Joback Calculated Property |
Cp,gas | 75.21 | J/mol×K | 494.07 | Joback Calculated Property |
Cp,gas | 76.99 | J/mol×K | 536.82 | Joback Calculated Property |
Cp,gas | 78.54 | J/mol×K | 579.57 | Joback Calculated Property |
Cp,gas | 79.89 | J/mol×K | 622.32 | Joback Calculated Property |
Cp,gas | 81.08 | J/mol×K | 665.08 | Joback Calculated Property |
Cp,liquid | [112.80; 133.90] | J/mol×K | [298.00; 298.15] | ![]() |
Cp,liquid | 133.90 | J/mol×K | 298.00 | NIST |
Cp,liquid | 133.81 | J/mol×K | 298.15 | NIST |
Cp,liquid | 112.80 | J/mol×K | 298.15 | NIST |
η | [0.0005376; 0.0059647] | Pa×s | [217.15; 408.56] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 250 300 350 400 | ||||
η | 0.0059647 | Pa×s | 217.15 | Joback Calculated Property |
η | 0.0030891 | Pa×s | 249.05 | Joback Calculated Property |
η | 0.0018577 | Pa×s | 280.95 | Joback Calculated Property |
η | 0.0012392 | Pa×s | 312.86 | Joback Calculated Property |
η | 0.0008910 | Pa×s | 344.76 | Joback Calculated Property |
η | 0.0006774 | Pa×s | 376.66 | Joback Calculated Property |
η | 0.0005376 | Pa×s | 408.56 | Joback Calculated Property |
ΔfusH | [12.05; 12.10] | kJ/mol | [279.20; 279.20] | ![]() |
ΔfusH | 12.10 | kJ/mol | 279.20 | NIST |
ΔfusH | 12.05 | kJ/mol | 279.20 | NIST |
ΔvapH | [45.40; 48.80] | kJ/mol | [374.00; 430.50] | ![]() |
ΔvapH | 48.80 | kJ/mol | 374.00 | NIST |
ΔvapH | 45.40 | kJ/mol | 430.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 208.42] | kPa | [332.29; 486.28] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40015e+01 | |||
Coefficient B | -3.62073e+03 | |||
Coefficient C | -6.82730e+01 | |||
Temperature range, min. | 332.29 | |||
Temperature range, max. | 486.28 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 332.29 | Calculated Property |
Pvap | 3.07 | kPa | 349.40 | Calculated Property |
Pvap | 6.43 | kPa | 366.51 | Calculated Property |
Pvap | 12.42 | kPa | 383.62 | Calculated Property |
Pvap | 22.43 | kPa | 400.73 | Calculated Property |
Pvap | 38.23 | kPa | 417.84 | Calculated Property |
Pvap | 61.99 | kPa | 434.95 | Calculated Property |
Pvap | 96.28 | kPa | 452.06 | Calculated Property |
Pvap | 144.01 | kPa | 469.17 | Calculated Property |
Pvap | 208.42 | kPa | 486.28 | Calculated Property |
Pvap | [0.04; 5401.79] | kPa | [279.25; 747.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.24639e+01 | |||
Coefficient B | -9.19799e+03 | |||
Coefficient C | -1.12077e+01 | |||
Coefficient D | 4.65037e-06 | |||
Temperature range, min. | 279.25 | |||
Temperature range, max. | 747.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 400 600 | ||||
Pvap | 0.04 | kPa | 279.25 | Calculated Property |
Pvap | 1.18 | kPa | 331.22 | Calculated Property |
Pvap | 11.87 | kPa | 383.19 | Calculated Property |
Pvap | 61.11 | kPa | 435.17 | Calculated Property |
Pvap | 205.65 | kPa | 487.14 | Calculated Property |
Pvap | 522.33 | kPa | 539.11 | Calculated Property |
Pvap | 1096.75 | kPa | 591.08 | Calculated Property |
Pvap | 2021.37 | kPa | 643.06 | Calculated Property |
Pvap | 3406.50 | kPa | 695.03 | Calculated Property |
Pvap | 5401.79 | kPa | 747.00 | Calculated Property |
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