Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1220 | KDB | |
Tig | 745.37 | K | KDB |
μ | 1.45 | debye | KDB |
LFL | 4.00 | % in Air | KDB |
UFL | 26.00 | % in Air | KDB |
Tflash,cc | 194.26 | K | KDB |
ΔfG° | 51.54 | kJ/mol | KDB |
ΔfH°gas | [21.00; 38.10] | kJ/mol | |
ΔfH°gas | 35.17 | kJ/mol | KDB |
ΔfH°gas | 22.00 ± 3.00 | kJ/mol | NIST |
ΔfH°gas | 29.00 | kJ/mol | NIST |
ΔfH°gas | 21.00 | kJ/mol | NIST |
ΔfH°gas | 35.30 ± 1.40 | kJ/mol | NIST |
ΔfH°gas | 38.10 ± 0.84 | kJ/mol | NIST |
ΔfH°liquid | 0.90 ± 3.20 | kJ/mol | NIST |
ΔfusH° | 3.85 | kJ/mol | Joback Calculated Property |
ΔvapH° | 21.00 ± 1.00 | kJ/mol | NIST |
IE | [9.98; 10.20] | eV | |
IE | 9.99 ± 0.02 | eV | NIST |
IE | 9.98 ± 0.02 | eV | NIST |
IE | 9.99 ± 0.02 | eV | NIST |
IE | 10.01 | eV | NIST |
IE | 10.00 | eV | NIST |
IE | 10.00 ± 0.01 | eV | NIST |
IE | 10.00 ± 0.01 | eV | NIST |
IE | 10.00 ± 0.02 | eV | NIST |
IE | 10.00 ± 0.01 | eV | NIST |
IE | 9.99 | eV | NIST |
IE | 10.00 ± 0.01 | eV | NIST |
IE | Outlier 10.20 | eV | NIST |
IE | Outlier 10.20 | eV | NIST |
IE | 10.15 | eV | NIST |
log10WS | [-1.75; -1.75] | ||
log10WS | -1.75 | Aq. Sol... | |
log10WS | -1.75 | Estimat... | |
logPoct/wat | 1.369 | Crippen Calculated Property | |
McVol | 46.980 | ml/mol | McGowan Calculated Property |
NFPA Fire | 4 | KDB | |
NFPA Health | 2 | KDB | |
NFPA Safety | 2 | KDB | |
Pc | 5155.00 | kPa | KDB |
Inp | [353.00; 378.00] | ||
Inp | 362.00 | NIST | |
Inp | 363.00 | NIST | |
Inp | 364.00 | NIST | |
Inp | 366.00 | NIST | |
Inp | 366.00 | NIST | |
Inp | Outlier 378.00 | NIST | |
Inp | 353.00 | NIST | |
Inp | 366.00 | NIST | |
I | [505.00; 603.00] | ||
I | 603.00 | NIST | |
I | 505.00 | NIST | |
S°liquid | 118.00 | J/mol×K | NIST |
Tboil | [259.05; 259.45] | K | |
Tboil | 259.35 | K | KDB |
Tboil | 259.35 | K | NIST |
Tboil | 259.45 ± 0.20 | K | NIST |
Tboil | 259.05 ± 0.40 | K | NIST |
Tboil | 259.30 ± 0.20 | K | NIST |
Tc | 424.61 | K | KDB |
Tfus | [94.43; 119.45] | K | |
Tfus | 119.40 | K | KDB |
Tfus | 119.45 | K | Aq. Sol... |
Tfus | 119.35 | K | NIST |
Tfus | Outlier 94.43 ± 0.10 | K | NIST |
Tfus | 119.36 ± 0.02 | K | NIST |
Tfus | 113.50 ± 0.20 | K | NIST |
Ttriple | 119.31 ± 0.02 | K | NIST |
Vc | 0.177 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [52.25; 70.09] | J/mol×K | [279.27; 453.15] | |
Cp,gas | 52.25 | J/mol×K | 279.27 | Joback Calculated Property |
Cp,gas | 55.59 | J/mol×K | 308.25 | Joback Calculated Property |
Cp,gas | 58.78 | J/mol×K | 337.23 | Joback Calculated Property |
Cp,gas | 61.82 | J/mol×K | 366.21 | Joback Calculated Property |
Cp,gas | 64.71 | J/mol×K | 395.19 | Joback Calculated Property |
Cp,gas | 67.47 | J/mol×K | 424.17 | Joback Calculated Property |
Cp,gas | 70.09 | J/mol×K | 453.15 | Joback Calculated Property |
Cp,liquid | 89.45 | J/mol×K | 298.15 | NIST |
η | [0.0002043; 0.0017378] | Pa×s | [140.46; 279.27] | |
η | 0.0017378 | Pa×s | 140.46 | Joback Calculated Property |
η | 0.0009451 | Pa×s | 163.59 | Joback Calculated Property |
η | 0.0005978 | Pa×s | 186.73 | Joback Calculated Property |
η | 0.0004183 | Pa×s | 209.87 | Joback Calculated Property |
η | 0.0003142 | Pa×s | 233.00 | Joback Calculated Property |
η | 0.0002485 | Pa×s | 256.13 | Joback Calculated Property |
η | 0.0002043 | Pa×s | 279.27 | Joback Calculated Property |
ΔfusH | [4.92; 4.92] | kJ/mol | [119.30; 119.31] | |
ΔfusH | 4.92 | kJ/mol | 119.30 | NIST |
ΔfusH | 4.92 | kJ/mol | 119.30 | NIST |
ΔfusH | 4.92 | kJ/mol | 119.31 | NIST |
ΔvapH | [22.26; 23.30] | kJ/mol | [234.50; 265.50] | |
ΔvapH | 23.30 | kJ/mol | 234.50 | NIST |
ΔvapH | 22.90 | kJ/mol | 243.00 | NIST |
ΔvapH | 22.26 | kJ/mol | 259.40 | KDB |
ΔvapH | 22.70 | kJ/mol | 265.50 | NIST |
Pvap | [172.00; 601.50] | kPa | [273.10; 313.15] | |
Pvap | 172.00 | kPa | 273.10 | Vapor-L... |
Pvap | 601.50 | kPa | 313.15 | Vapor-L... |
ρl | 969.00 | kg/m3 | 259.00 | KDB |
ΔfusS | 41.20 | J/mol×K | 119.31 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.69] | kPa | [187.41; 277.61] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.38927e+01 | |||
Coefficient B | -2.09601e+03 | |||
Coefficient C | -3.33500e+01 | |||
Temperature range, min. | 187.41 | |||
Temperature range, max. | 277.61 | |||
Pvap | 1.33 | kPa | 187.41 | Calculated Property |
Pvap | 3.06 | kPa | 197.43 | Calculated Property |
Pvap | 6.38 | kPa | 207.45 | Calculated Property |
Pvap | 12.30 | kPa | 217.48 | Calculated Property |
Pvap | 22.13 | kPa | 227.50 | Calculated Property |
Pvap | 37.59 | kPa | 237.52 | Calculated Property |
Pvap | 60.77 | kPa | 247.54 | Calculated Property |
Pvap | 94.12 | kPa | 257.57 | Calculated Property |
Pvap | 140.40 | kPa | 267.59 | Calculated Property |
Pvap | 202.69 | kPa | 277.61 | Calculated Property |
Pvap | [1.65e-05; 5873.76] | kPa | [119.36; 432.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.48913e+01 | |||
Coefficient B | -5.42760e+03 | |||
Coefficient C | -1.26907e+01 | |||
Coefficient D | 1.80238e-05 | |||
Temperature range, min. | 119.36 | |||
Temperature range, max. | 432.00 | |||
Pvap | 1.65e-05 | kPa | 119.36 | Calculated Property |
Pvap | 0.02 | kPa | 154.10 | Calculated Property |
Pvap | 1.32 | kPa | 188.84 | Calculated Property |
Pvap | 17.50 | kPa | 223.57 | Calculated Property |
Pvap | 99.05 | kPa | 258.31 | Calculated Property |
Pvap | 340.45 | kPa | 293.05 | Calculated Property |
Pvap | 862.76 | kPa | 327.79 | Calculated Property |
Pvap | 1809.24 | kPa | 362.52 | Calculated Property |
Pvap | 3375.42 | kPa | 397.26 | Calculated Property |
Pvap | 5873.76 | kPa | 432.00 | Calculated Property |
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