Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4910 | KDB | |
Tig | 508.15 | K | KDB |
ΔcH°liquid | -6619.60 ± 1.80 | kJ/mol | NIST |
Tflash,cc | 326.48 | K | KDB |
ΔfG° | 121.10 | kJ/mol | KDB |
ΔfH°gas | [-124.60; -123.40] | kJ/mol | |
ΔfH°gas | -124.20 | kJ/mol | KDB |
ΔfH°gas | -124.60 | kJ/mol | NIST |
ΔfH°gas | -123.40 | kJ/mol | NIST |
ΔfH°liquid | -173.80 ± 1.90 | kJ/mol | NIST |
ΔfusH° | 20.38 | kJ/mol | Joback Calculated Property |
ΔvapH° | [50.40; 50.50] | kJ/mol | |
ΔvapH° | 50.44 | kJ/mol | NIST |
ΔvapH° | 50.43 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 50.40 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 50.50 | kJ/mol | NIST |
IE | [9.42; 9.59] | eV | |
IE | 9.42 ± 0.01 | eV | NIST |
IE | 9.48 | eV | NIST |
IE | 9.42 ± 0.01 | eV | NIST |
IE | 9.59 ± 0.01 | eV | NIST |
log10WS | [-5.51; -5.51] | ||
log10WS | -5.51 | Aq. Sol... | |
log10WS | -5.51 | Estimat... | |
logPoct/wat | 3.923 | Crippen Calculated Property | |
McVol | 147.460 | ml/mol | McGowan Calculated Property |
NFPA Fire | 2 | KDB | |
Pc | [2220.00; 2220.00] | kPa | |
Pc | 2220.00 | kPa | KDB |
Pc | 2220.00 ± 100.00 | kPa | NIST |
ρc | 238.45 ± 14.03 | kg/m3 | NIST |
Inp | [153.90; 997.00] | ||
Inp | 985.00 | NIST | |
Inp | 982.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 990.00 | NIST | |
Inp | 985.10 | NIST | |
Inp | 985.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 988.60 | NIST | |
Inp | 990.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 982.00 | NIST | |
Inp | 983.00 | NIST | |
Inp | 982.00 | NIST | |
Inp | 990.00 | NIST | |
Inp | 989.20 | NIST | |
Inp | 990.10 | NIST | |
Inp | 982.70 | NIST | |
Inp | 982.20 | NIST | |
Inp | 987.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 990.00 | NIST | |
Inp | 992.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 992.50 | NIST | |
Inp | 993.00 | NIST | |
Inp | 992.00 | NIST | |
Inp | 987.00 | NIST | |
Inp | 993.00 | NIST | |
Inp | 993.00 | NIST | |
Inp | 989.20 | NIST | |
Inp | 989.50 | NIST | |
Inp | 990.70 | NIST | |
Inp | 985.00 | NIST | |
Inp | 989.20 | NIST | |
Inp | 989.50 | NIST | |
Inp | 990.70 | NIST | |
Inp | 988.00 | NIST | |
Inp | 988.74 | NIST | |
Inp | 988.81 | NIST | |
Inp | 988.83 | NIST | |
Inp | 991.63 | NIST | |
Inp | 991.76 | NIST | |
Inp | 991.73 | NIST | |
Inp | 988.00 | NIST | |
Inp | 991.00 | NIST | |
Inp | 982.00 | NIST | |
Inp | 997.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 991.00 | NIST | |
Inp | 991.00 | NIST | |
Inp | 992.00 | NIST | |
Inp | 992.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 988.80 | NIST | |
Inp | 988.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 997.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 987.00 | NIST | |
Inp | 986.00 | NIST | |
Inp | 990.00 | NIST | |
Inp | 991.00 | NIST | |
Inp | 982.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | Outlier 157.60 | NIST | |
Inp | Outlier 153.90 | NIST | |
I | [1020.00; 1061.00] | ||
I | 1052.00 | NIST | |
I | 1054.00 | NIST | |
I | 1055.00 | NIST | |
I | 1048.00 | NIST | |
I | 1050.00 | NIST | |
I | 1046.00 | NIST | |
I | 1047.00 | NIST | |
I | 1046.00 | NIST | |
I | 1051.70 | NIST | |
I | 1055.30 | NIST | |
I | 1048.50 | NIST | |
I | 1049.80 | NIST | |
I | 1051.70 | NIST | |
I | 1055.30 | NIST | |
I | 1048.50 | NIST | |
I | 1049.80 | NIST | |
I | 1047.00 | NIST | |
I | 1061.00 | NIST | |
I | Outlier 1020.00 | NIST | |
I | 1054.00 | NIST | |
I | 1043.00 | NIST | |
I | 1035.00 | NIST | |
I | 1039.00 | NIST | |
S°liquid | 425.01 | J/mol×K | NIST |
Tboil | 443.60 | K | KDB |
Tc | [617.00; 617.00] | K | |
Tc | 617.00 | K | KDB |
Tc | 617.00 ± 2.00 | K | NIST |
Tfus | [206.90; 207.06] | K | |
Tfus | 206.90 | K | KDB |
Tfus | 207.06 | K | Aq. Sol... |
Ttriple | [206.47; 206.89] | K | |
Ttriple | 206.89 ± 0.05 | K | NIST |
Ttriple | 206.89 ± 0.06 | K | NIST |
Ttriple | 206.88 ± 0.06 | K | NIST |
Ttriple | 206.47 ± 0.20 | K | NIST |
Vc | [0.584; 0.584] | m3/kmol | |
Vc | 0.584 | m3/kmol | KDB |
Vc | 0.584 | m3/kmol | NIST |
Zc | 0.2527230 | KDB | |
Zra | 0.25 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [299.13; 378.63] | J/mol×K | [424.88; 590.50] | |
Cp,gas | 299.13 | J/mol×K | 424.88 | Joback Calculated Property |
Cp,gas | 313.75 | J/mol×K | 452.48 | Joback Calculated Property |
Cp,gas | 327.80 | J/mol×K | 480.09 | Joback Calculated Property |
Cp,gas | 341.30 | J/mol×K | 507.69 | Joback Calculated Property |
Cp,gas | 354.26 | J/mol×K | 535.29 | Joback Calculated Property |
Cp,gas | 366.70 | J/mol×K | 562.90 | Joback Calculated Property |
Cp,gas | 378.63 | J/mol×K | 590.50 | Joback Calculated Property |
Cp,liquid | 300.83 | J/mol×K | 298.15 | NIST |
η | [0.0002345; 0.0053123] | Pa×s | [200.70; 424.88] | |
η | 0.0053123 | Pa×s | 200.70 | Joback Calculated Property |
η | 0.0020999 | Pa×s | 238.06 | Joback Calculated Property |
η | 0.0010678 | Pa×s | 275.43 | Joback Calculated Property |
η | 0.0006382 | Pa×s | 312.79 | Joback Calculated Property |
η | 0.0004257 | Pa×s | 350.15 | Joback Calculated Property |
η | 0.0003070 | Pa×s | 387.52 | Joback Calculated Property |
η | 0.0002345 | Pa×s | 424.88 | Joback Calculated Property |
ΔfusH | [7.95; 13.81] | kJ/mol | [198.30; 206.90] | |
ΔfusH | 7.95 | kJ/mol | 198.30 | NIST |
ΔfusH | 13.81 | kJ/mol | 206.90 | NIST |
ΔfusH | 13.81 | kJ/mol | 206.90 | NIST |
ΔvapH | [38.66; 45.10] | kJ/mol | [402.50; 443.70] | |
ΔvapH | 45.10 | kJ/mol | 402.50 | NIST |
ΔvapH | 43.80 | kJ/mol | 414.00 | NIST |
ΔvapH | 38.66 | kJ/mol | 443.70 | KDB |
n0 | [1.42139; 1.42140] | [293.15; 293.15] | ||
n0 | 1.42139 | 293.15 | Excess ... | |
n0 | 1.42140 | 293.15 | Isobari... | |
ρl | 741.00 | kg/m3 | 293.00 | KDB |
ΔfusS | [40.09; 66.73] | J/mol×K | [198.30; 206.90] | |
ΔfusS | 40.09 | J/mol×K | 198.30 | NIST |
ΔfusS | 66.73 | J/mol×K | 206.90 | NIST |
γ | 0.02 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [326.18; 467.83] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.48286e+01 | |||
Coefficient B | -3.90202e+03 | |||
Coefficient C | -5.78340e+01 | |||
Temperature range, min. | 326.18 | |||
Temperature range, max. | 467.83 | |||
Pvap | 1.33 | kPa | 326.18 | Calculated Property |
Pvap | 2.98 | kPa | 341.92 | Calculated Property |
Pvap | 6.14 | kPa | 357.66 | Calculated Property |
Pvap | 11.74 | kPa | 373.40 | Calculated Property |
Pvap | 21.13 | kPa | 389.14 | Calculated Property |
Pvap | 36.05 | kPa | 404.87 | Calculated Property |
Pvap | 58.72 | kPa | 420.61 | Calculated Property |
Pvap | 91.83 | kPa | 436.35 | Calculated Property |
Pvap | 138.58 | kPa | 452.09 | Calculated Property |
Pvap | 202.63 | kPa | 467.83 | Calculated Property |
Pvap | [1.46e-05; 2193.34] | kPa | [206.89; 617.05] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.10936e+02 | |||
Coefficient B | -9.75380e+03 | |||
Coefficient C | -1.41204e+01 | |||
Coefficient D | 8.63327e-06 | |||
Temperature range, min. | 206.89 | |||
Temperature range, max. | 617.05 | |||
Pvap | 1.46e-05 | kPa | 206.89 | Calculated Property |
Pvap | 5.24e-03 | kPa | 252.46 | Calculated Property |
Pvap | 0.23 | kPa | 298.04 | Calculated Property |
Pvap | 3.04 | kPa | 343.61 | Calculated Property |
Pvap | 19.43 | kPa | 389.18 | Calculated Property |
Pvap | 77.82 | kPa | 434.76 | Calculated Property |
Pvap | 229.39 | kPa | 480.33 | Calculated Property |
Pvap | 550.65 | kPa | 525.90 | Calculated Property |
Pvap | 1151.02 | kPa | 571.48 | Calculated Property |
Pvap | 2193.34 | kPa | 617.05 | Calculated Property |
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