Property | Value | Unit | Source |
---|---|---|---|
PAff | 909.30 | kJ/mol | NIST |
BasG | 879.60 | kJ/mol | NIST |
ΔvapH° | 55.70 | kJ/mol | NIST |
IE | [9.79; 12.80] | eV |
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IE | 10.00 | eV | NIST |
IE | 9.79 | eV | NIST |
IE | Outlier 12.80 ± 0.20 | eV | NIST |
IE | 10.06 ± 0.27 | eV | NIST |
IE | 10.69 | eV | NIST |
IE | 10.54 | eV | NIST |
IE | 10.40 | eV | NIST |
log10WS | [0.43; 0.43] |
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|
log10WS | 0.43 | Aq. Sol... | |
log10WS | 0.43 | Estimat... | |
logPoct/wat | 2.204 | Crippen Calculated Property | |
McVol | 139.340 | ml/mol | McGowan Calculated Property |
Inp | [1079.00; 1137.20] |
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|
Inp | 1081.00 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1108.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1090.00 | NIST | |
Inp | 1137.20 | NIST | |
Inp | 1088.00 | NIST | |
Inp | 1120.50 | NIST | |
Inp | 1121.30 | NIST | |
Inp | 1121.50 | NIST | |
Inp | 1090.70 | NIST | |
Inp | 1137.20 | NIST | |
Inp | 1091.00 | NIST | |
Inp | 1091.00 | NIST | |
Inp | 1127.00 | NIST | |
Inp | 1087.00 | NIST | |
Inp | 1090.50 | NIST | |
Inp | 1137.20 | NIST | |
Inp | 1096.00 | NIST | |
Inp | 1091.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1109.00 | NIST | |
I | [1656.00; 1672.10] |
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|
I | 1656.00 | NIST | |
I | 1659.00 | NIST | |
I | 1656.10 | NIST | |
I | 1672.10 | NIST | |
Tboil | [489.00; 489.04] | K |
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Tboil | 489.04 | K | Estimat... |
Tboil | 489.00 ± 2.00 | K | NIST |
Tfus | 216.95 | K | Aq. Sol... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
ΔvapH | [46.30; 55.73] | kJ/mol | [298.15; 398.00] | ![]() |
ΔvapH | 55.73 | kJ/mol | 298.15 | Measure... |
ΔvapH | 46.30 | kJ/mol | 398.00 | NIST |
Pvap | [1.20e-03; 3.82e-03] | kPa | [271.25; 283.15] | ![]() |
T(K) Vapor pressure (kPa) 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 275 280 | ||||
Pvap | 1.20e-03 | kPa | 271.25 | Vapor P... |
Pvap | 1.24e-03 | kPa | 272.25 | Vapor P... |
Pvap | 1.69e-03 | kPa | 275.25 | Vapor P... |
Pvap | 2.22e-03 | kPa | 278.05 | Vapor P... |
Pvap | 3.82e-03 | kPa | 283.15 | Vapor P... |
ρl | [1043.20; 1071.10] | kg/m3 | [293.15; 323.15] | ![]() |
T(K) Liquid Density (kg/m3) 1045 1050 1055 1060 1065 1070 300 310 320 | ||||
ρl | 1071.10 | kg/m3 | 293.15 | Towards... |
ρl | 1067.90 | kg/m3 | 298.15 | Towards... |
ρl | 1063.30 | kg/m3 | 303.15 | Towards... |
ρl | 1058.90 | kg/m3 | 308.15 | Towards... |
ρl | 1053.50 | kg/m3 | 313.15 | Towards... |
ρl | 1048.00 | kg/m3 | 318.15 | Towards... |
ρl | 1043.20 | kg/m3 | 323.15 | Towards... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [361.00; 517.97] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.61069e+01 | |||
Coefficient B | -5.33572e+03 | |||
Coefficient C | -2.37130e+01 | |||
Temperature range, min. | 361.00 | |||
Temperature range, max. | 517.97 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 361.00 | Calculated Property |
Pvap | 2.90 | kPa | 378.44 | Calculated Property |
Pvap | 5.87 | kPa | 395.88 | Calculated Property |
Pvap | 11.15 | kPa | 413.32 | Calculated Property |
Pvap | 20.06 | kPa | 430.76 | Calculated Property |
Pvap | 34.37 | kPa | 448.21 | Calculated Property |
Pvap | 56.45 | kPa | 465.65 | Calculated Property |
Pvap | 89.27 | kPa | 483.09 | Calculated Property |
Pvap | 136.54 | kPa | 500.53 | Calculated Property |
Pvap | 202.65 | kPa | 517.97 | Calculated Property |
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