Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2750 | KDB | |
ΔcH°solid | -727.00 ± 8.00 | kJ/mol | NIST |
EA | 1.48 ± 0.10 | eV | NIST |
ΔfG° | -99.94 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-148.20; -143.50] | kJ/mol |
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ΔfH°gas | -148.20 ± 5.70 | kJ/mol | NIST |
ΔfH°gas | -143.50 ± 9.40 | kJ/mol | NIST |
ΔfH°liquid | -199.20 ± 6.10 | kJ/mol | NIST |
ΔfusH° | 11.29 | kJ/mol | Joback Calculated Property |
ΔsubH° | 59.00 ± 0.80 | kJ/mol | NIST |
ΔvapH° | 51.00 ± 2.30 | kJ/mol | NIST |
IE | [11.10; 11.22] | eV |
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IE | 11.10 | eV | NIST |
IE | 11.22 | eV | NIST |
IE | 11.22 | eV | NIST |
log10WS | [-3.67; -3.67] |
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|
log10WS | -3.67 | Aq. Sol... | |
log10WS | -3.67 | Estimat... | |
logPoct/wat | 3.727 | Crippen Calculated Property | |
McVol | 112.480 | ml/mol | McGowan Calculated Property |
Pc | 3940.00 | kPa | KDB |
Inp | [176.00; 1085.00] |
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|
Inp | 1068.00 | NIST | |
Inp | 1081.00 | NIST | |
Inp | 1053.00 | NIST | |
Inp | 1058.00 | NIST | |
Inp | 1057.80 | NIST | |
Inp | 1062.00 | NIST | |
Inp | 1070.00 | NIST | |
Inp | 1070.00 | NIST | |
Inp | 1056.00 | NIST | |
Inp | 1064.00 | NIST | |
Inp | 1062.00 | NIST | |
Inp | 1055.00 | NIST | |
Inp | 1055.00 | NIST | |
Inp | 1057.00 | NIST | |
Inp | 1085.00 | NIST | |
Inp | Outlier 176.00 | NIST | |
Inp | 1068.00 | NIST | |
Inp | 1062.00 | NIST | |
I | [1400.00; 1461.57] |
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|
I | 1444.17 | NIST | |
I | 1461.57 | NIST | |
I | 1426.53 | NIST | |
I | 1400.00 | NIST | |
I | 1400.00 | NIST | |
I | 1444.17 | NIST | |
I | 1400.00 | NIST | |
S°solid,1 bar | 237.30 | J/mol×K | NIST |
Tboil | [458.00; 459.20] | K |
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Tboil | 459.20 | K | KDB |
Tboil | 458.00 ± 1.00 | K | NIST |
Tboil | 458.00 ± 1.00 | K | NIST |
Tc | 704.40 | K | KDB |
Tfus | [458.00; 461.98] | K |
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Tfus | 458.00 | K | KDB |
Tfus | 461.98 | K | Aq. Sol... |
Vc | 0.419 | m3/kmol | KDB |
Zc | 0.2822100 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [157.38; 172.23] | J/mol×K | [463.28; 710.67] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 160 165 170 500 600 700 | ||||
Cp,gas | 157.38 | J/mol×K | 463.28 | Joback Calculated Property |
Cp,gas | 161.53 | J/mol×K | 504.51 | Joback Calculated Property |
Cp,gas | 164.90 | J/mol×K | 545.74 | Joback Calculated Property |
Cp,gas | 167.57 | J/mol×K | 586.98 | Joback Calculated Property |
Cp,gas | 169.62 | J/mol×K | 628.21 | Joback Calculated Property |
Cp,gas | 171.14 | J/mol×K | 669.44 | Joback Calculated Property |
Cp,gas | 172.23 | J/mol×K | 710.67 | Joback Calculated Property |
Cp,solid | [198.24; 218.00] | J/mol×K | [298.15; 298.50] | ![]() |
Cp,solid | 198.24 | J/mol×K | 298.15 | NIST |
Cp,solid | 218.00 | J/mol×K | 298.50 | NIST |
η | [0.0004660; 0.0053154] | Pa×s | [296.66; 463.28] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 300 350 400 450 | ||||
η | 0.0053154 | Pa×s | 296.66 | Joback Calculated Property |
η | 0.0029781 | Pa×s | 324.43 | Joback Calculated Property |
η | 0.0018282 | Pa×s | 352.20 | Joback Calculated Property |
η | 0.0012053 | Pa×s | 379.97 | Joback Calculated Property |
η | 0.0008410 | Pa×s | 407.74 | Joback Calculated Property |
η | 0.0006144 | Pa×s | 435.51 | Joback Calculated Property |
η | 0.0004660 | Pa×s | 463.28 | Joback Calculated Property |
ΔfusH | [2.57; 9.75] | kJ/mol | [318.00; 458.00] | ![]() |
ΔfusH | 2.57 | kJ/mol | 318.00 | NIST |
ΔfusH | 8.22 | kJ/mol | 345.00 | NIST |
ΔfusH | 9.75 | kJ/mol | 458.00 | NIST |
ΔfusH | 9.75 | kJ/mol | 458.00 | NIST |
ΔsubH | [50.50; 59.00] | kJ/mol | [310.50; 394.00] | ![]() |
ΔsubH | 59.00 | kJ/mol | 310.50 | NIST |
ΔsubH | 58.90 | kJ/mol | 331.00 | NIST |
ΔsubH | 50.50 | kJ/mol | 394.00 | NIST |
ΔvapH | [40.30; 53.70] | kJ/mol | [381.50; 486.50] | ![]() |
ΔvapH | 53.70 | kJ/mol | 381.50 | NIST |
ΔvapH | 51.20 | kJ/mol | 402.50 | NIST |
ΔvapH | 49.00 | kJ/mol | 459.20 | KDB |
ΔvapH | 40.30 | kJ/mol | 486.50 | NIST |
ΔfusS | [8.07; 23.83] | J/mol×K | [318.00; 458.00] | ![]() |
ΔfusS | 8.07 | J/mol×K | 318.00 | NIST |
ΔfusS | 23.83 | J/mol×K | 345.00 | NIST |
ΔfusS | 21.29 | J/mol×K | 458.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [344.83; 487.92] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.30211e+01 | |||
Coefficient B | -2.79600e+03 | |||
Coefficient C | -1.25251e+02 | |||
Temperature range, min. | 344.83 | |||
Temperature range, max. | 487.92 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 344.83 | Calculated Property |
Pvap | 3.15 | kPa | 360.73 | Calculated Property |
Pvap | 6.67 | kPa | 376.63 | Calculated Property |
Pvap | 12.94 | kPa | 392.53 | Calculated Property |
Pvap | 23.27 | kPa | 408.43 | Calculated Property |
Pvap | 39.34 | kPa | 424.32 | Calculated Property |
Pvap | 63.06 | kPa | 440.22 | Calculated Property |
Pvap | 96.61 | kPa | 456.12 | Calculated Property |
Pvap | 142.32 | kPa | 472.02 | Calculated Property |
Pvap | 202.67 | kPa | 487.92 | Calculated Property |
Pvap | [0.14; 3043.14] | kPa | [306.15; 698.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.45610e+01 | |||
Coefficient B | -9.86248e+03 | |||
Coefficient C | -1.12902e+01 | |||
Coefficient D | 3.12000e-06 | |||
Temperature range, min. | 306.15 | |||
Temperature range, max. | 698.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 400 600 | ||||
Pvap | 0.14 | kPa | 306.15 | Calculated Property |
Pvap | 1.84 | kPa | 349.69 | Calculated Property |
Pvap | 12.31 | kPa | 393.23 | Calculated Property |
Pvap | 51.31 | kPa | 436.77 | Calculated Property |
Pvap | 153.92 | kPa | 480.31 | Calculated Property |
Pvap | 364.97 | kPa | 523.84 | Calculated Property |
Pvap | 728.77 | kPa | 567.38 | Calculated Property |
Pvap | 1281.11 | kPa | 610.92 | Calculated Property |
Pvap | 2046.94 | kPa | 654.46 | Calculated Property |
Pvap | 3043.14 | kPa | 698.00 | Calculated Property |
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