Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -2937.00 ± 4.00 | kJ/mol | NIST |
ΔcH°solid | [-2939.90; -2934.10] | kJ/mol |
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ΔcH°solid | -2939.90 | kJ/mol | NIST |
ΔcH°solid | -2934.10 ± 1.00 | kJ/mol | NIST |
ΔfG° | 78.56 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 24.60 | kJ/mol | NIST |
ΔfH°(+) ion | 883.20 | kJ/mol | NIST |
ΔfH(+) ion,0K | 895.80 | kJ/mol | NIST |
ΔfH°solid | -42.30 ± 1.00 | kJ/mol | NIST |
ΔfusH° | 17.91 | kJ/mol | Low-Tem... |
ΔsubH° | [64.75; 65.20] | kJ/mol |
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ΔsubH° | 64.75 ± 0.15 | kJ/mol | NIST |
ΔsubH° | 65.20 ± 2.00 | kJ/mol | NIST |
ΔvapH° | [47.80; 54.80] | kJ/mol |
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ΔvapH° | 54.80 | kJ/mol | NIST |
ΔvapH° | 47.80 | kJ/mol | NIST |
IE | [8.89; 9.00] | eV |
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IE | 8.92 ± 0.03 | eV | NIST |
IE | 8.95 | eV | NIST |
IE | 8.92 ± 0.02 | eV | NIST |
IE | 8.97 ± 0.03 | eV | NIST |
IE | 8.94 | eV | NIST |
IE | 8.98 ± 0.02 | eV | NIST |
IE | 8.89 ± 0.01 | eV | NIST |
IE | 8.94 ± 0.01 | eV | NIST |
IE | 8.95 | eV | NIST |
IE | 8.99 | eV | NIST |
IE | 9.00 | eV | NIST |
log10WS | [-3.29; -3.27] |
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|
log10WS | -3.29 | Aq. Sol... | |
log10WS | -3.27 | Estimat... | |
logPoct/wat | 2.993 | Crippen Calculated Property | |
McVol | 96.120 | ml/mol | McGowan Calculated Property |
NFPA Fire | 2 | KDB | |
NFPA Health | 2 | KDB | |
Pc | 4151.61 | kPa | Joback Calculated Property |
Inp | [162.00; 1057.00] |
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|
Inp | 1023.15 | NIST | |
Inp | 1023.18 | NIST | |
Inp | 1032.51 | NIST | |
Inp | 1032.76 | NIST | |
Inp | 1016.00 | NIST | |
Inp | 1037.40 | NIST | |
Inp | 1037.40 | NIST | |
Inp | 1046.00 | NIST | |
Inp | 1012.00 | NIST | |
Inp | 993.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 1016.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 1015.00 | NIST | |
Inp | 1016.00 | NIST | |
Inp | 1016.00 | NIST | |
Inp | 1000.00 | NIST | |
Inp | 1021.24 | NIST | |
Inp | 1021.56 | NIST | |
Inp | 1024.00 | NIST | |
Inp | 1025.03 | NIST | |
Inp | 1014.90 | NIST | |
Inp | 991.21 | NIST | |
Inp | 990.60 | NIST | |
Inp | 989.50 | NIST | |
Inp | 1014.00 | NIST | |
Inp | 1009.00 | NIST | |
Inp | 996.00 | NIST | |
Inp | 991.00 | NIST | |
Inp | 987.00 | NIST | |
Inp | 1009.00 | NIST | |
Inp | 1024.00 | NIST | |
Inp | 1010.00 | NIST | |
Inp | 998.00 | NIST | |
Inp | 1013.00 | NIST | |
Inp | 1004.00 | NIST | |
Inp | 1004.00 | NIST | |
Inp | 960.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 974.00 | NIST | |
Inp | 1008.00 | NIST | |
Inp | 1015.00 | NIST | |
Inp | 1024.00 | NIST | |
Inp | 1007.00 | NIST | |
Inp | 1014.00 | NIST | |
Inp | 1016.00 | NIST | |
Inp | 1057.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 1009.00 | NIST | |
Inp | 1050.00 | NIST | |
Inp | 986.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 1047.00 | NIST | |
Inp | 1029.00 | NIST | |
Inp | 987.00 | NIST | |
Inp | 985.00 | NIST | |
Inp | 1000.00 | NIST | |
Inp | 985.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 995.00 | NIST | |
Inp | 994.00 | NIST | |
Inp | 1023.00 | NIST | |
Inp | Outlier 163.00 | NIST | |
Inp | Outlier 162.00 | NIST | |
Inp | Outlier 163.15 | NIST | |
Inp | Outlier 164.81 | NIST | |
Inp | 1013.00 | NIST | |
Inp | 974.00 | NIST | |
I | [1420.00; 1495.00] |
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|
I | 1483.20 | NIST | |
I | 1438.00 | NIST | |
I | 1438.00 | NIST | |
I | 1471.00 | NIST | |
I | 1438.00 | NIST | |
I | 1449.00 | NIST | |
I | 1449.00 | NIST | |
I | 1450.00 | NIST | |
I | 1446.09 | NIST | |
I | 1450.00 | NIST | |
I | 1446.00 | NIST | |
I | 1453.00 | NIST | |
I | 1420.00 | NIST | |
I | 1434.00 | NIST | |
I | 1436.00 | NIST | |
I | 1436.00 | NIST | |
I | Outlier 1495.00 | NIST | |
I | 1420.00 | NIST | |
S°solid,1 bar | 175.41 | J/mol×K | NIST |
Tboil | [446.85; 447.75] | K |
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Tboil | 446.85 | K | KDB |
Tboil | 447.20 | K | NIST |
Tboil | 447.27 ± 0.07 | K | NIST |
Tboil | 447.60 ± 0.50 | K | NIST |
Tboil | 447.75 ± 0.30 | K | NIST |
Tboil | 447.30 ± 0.50 | K | NIST |
Tboil | 446.85 ± 0.70 | K | NIST |
Tc | 674.86 | K | Joback Calculated Property |
Tfus | [326.35; 326.41] | K |
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Tfus | 326.35 | K | KDB |
Tfus | 326.41 | K | Aq. Sol... |
Ttriple | [326.15; 326.16] | K |
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Ttriple | 326.16 | K | KDB |
Ttriple | 326.15 ± 0.01 | K | NIST |
Vc | 0.361 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [149.05; 190.77] | J/mol×K | [443.20; 674.86] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 150 160 170 180 190 500 600 | ||||
Cp,gas | 149.05 | J/mol×K | 443.20 | Joback Calculated Property |
Cp,gas | 157.36 | J/mol×K | 481.81 | Joback Calculated Property |
Cp,gas | 165.09 | J/mol×K | 520.42 | Joback Calculated Property |
Cp,gas | 172.26 | J/mol×K | 559.03 | Joback Calculated Property |
Cp,gas | 178.92 | J/mol×K | 597.64 | Joback Calculated Property |
Cp,gas | 185.08 | J/mol×K | 636.25 | Joback Calculated Property |
Cp,gas | 190.77 | J/mol×K | 674.86 | Joback Calculated Property |
Cp,liquid | [177.09; 183.21] | J/mol×K | [327.15; 353.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 177 178 179 180 181 182 183 330 340 350 | ||||
Cp,liquid | 177.09 | J/mol×K | 327.15 | Heat Ca... |
Cp,liquid | 177.53 | J/mol×K | 329.15 | Heat Ca... |
Cp,liquid | 177.98 | J/mol×K | 331.15 | Heat Ca... |
Cp,liquid | 178.43 | J/mol×K | 333.15 | Heat Ca... |
Cp,liquid | 178.89 | J/mol×K | 335.15 | Heat Ca... |
Cp,liquid | 179.35 | J/mol×K | 337.15 | Heat Ca... |
Cp,liquid | 179.81 | J/mol×K | 339.15 | Heat Ca... |
Cp,liquid | 180.28 | J/mol×K | 341.15 | Heat Ca... |
Cp,liquid | 180.76 | J/mol×K | 343.15 | Heat Ca... |
Cp,liquid | 181.24 | J/mol×K | 345.15 | Heat Ca... |
Cp,liquid | 181.73 | J/mol×K | 347.15 | Heat Ca... |
Cp,liquid | 182.22 | J/mol×K | 349.15 | Heat Ca... |
Cp,liquid | 182.71 | J/mol×K | 351.15 | Heat Ca... |
Cp,liquid | 183.21 | J/mol×K | 353.15 | Heat Ca... |
Cp,solid | [98.00; 172.00] | J/mol×K | [180.00; 299.80] | ![]() |
T(K) Solid phase heat capacity (J/mol×K) 100 110 120 130 140 150 160 170 200 250 300 | ||||
Cp,solid | 98.00 | J/mol×K | 180.00 | NIST |
Cp,solid | 147.60 | J/mol×K | 298.00 | NIST |
Cp,solid | 147.76 | J/mol×K | 298.15 | NIST |
Cp,solid | 142.70 | J/mol×K | 298.15 | NIST |
Cp,solid | 172.00 | J/mol×K | 299.80 | NIST |
η | [0.0002989; 0.0021588] | Pa×s | [256.16; 443.20] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 300 350 400 | ||||
η | 0.0021588 | Pa×s | 256.16 | Joback Calculated Property |
η | 0.0012985 | Pa×s | 287.33 | Joback Calculated Property |
η | 0.0008628 | Pa×s | 318.51 | Joback Calculated Property |
η | 0.0006166 | Pa×s | 349.68 | Joback Calculated Property |
η | 0.0004656 | Pa×s | 380.85 | Joback Calculated Property |
η | 0.0003668 | Pa×s | 412.03 | Joback Calculated Property |
η | 0.0002989 | Pa×s | 443.20 | Joback Calculated Property |
ΔfusH | [17.91; 18.19] | kJ/mol | [192.50; 326.20] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 17.9 17.95 18 18.05 18.1 18.15 18.2 200 250 300 | ||||
ΔfusH | 17.91 | kJ/mol | 192.50 | NIST |
ΔfusH | 18.16 | kJ/mol | 326.00 | NIST |
ΔfusH | 18.16 | kJ/mol | 326.00 | NIST |
ΔfusH | 18.16 | kJ/mol | 326.00 | NIST |
ΔfusH | 18.14 | kJ/mol | 326.05 | NIST |
ΔfusH | 18.05 | kJ/mol | 326.15 | NIST |
ΔfusH | 18.19 | kJ/mol | 326.20 | NIST |
ΔsubH | [53.10; 65.40] | kJ/mol | [275.50; 363.00] | ![]() |
T(K) Enthalpy of sublimation at a given temperature (kJ/mol) 52 54 56 58 60 62 64 66 300 350 | ||||
ΔsubH | 56.90 | kJ/mol | 275.50 | NIST |
ΔsubH | 53.10 | kJ/mol | 285.50 | NIST |
ΔsubH | 64.80 ± 0.80 | kJ/mol | 302.00 | NIST |
ΔsubH | 64.80 ± 0.40 | kJ/mol | 303.00 | NIST |
ΔsubH | 63.00 ± 0.40 | kJ/mol | 318.00 | NIST |
ΔsubH | 65.40 | kJ/mol | 363.00 | NIST |
ΔvapH | [44.20; 46.40] | kJ/mol | [326.00; 403.00] | ![]() |
ΔvapH | 46.40 | kJ/mol | 326.00 | NIST |
ΔvapH | 45.00 | kJ/mol | 394.50 | NIST |
ΔvapH | 44.20 | kJ/mol | 403.00 | NIST |
ΔfusS | [55.30; 55.70] | J/mol×K | [326.00; 326.15] | ![]() |
ΔfusS | 55.70 | J/mol×K | 326.00 | NIST |
ΔfusS | 55.60 | J/mol×K | 326.05 | NIST |
ΔfusS | 55.30 | J/mol×K | 326.15 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [323.57; 477.69] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.47073e+01 | |||
Coefficient B | -4.15642e+03 | |||
Coefficient C | -3.53240e+01 | |||
Temperature range, min. | 323.57 | |||
Temperature range, max. | 477.69 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 323.57 | Calculated Property |
Pvap | 2.99 | kPa | 340.69 | Calculated Property |
Pvap | 6.17 | kPa | 357.82 | Calculated Property |
Pvap | 11.81 | kPa | 374.94 | Calculated Property |
Pvap | 21.25 | kPa | 392.07 | Calculated Property |
Pvap | 36.23 | kPa | 409.19 | Calculated Property |
Pvap | 58.96 | kPa | 426.32 | Calculated Property |
Pvap | 92.11 | kPa | 443.44 | Calculated Property |
Pvap | 138.80 | kPa | 460.57 | Calculated Property |
Pvap | 202.64 | kPa | 477.69 | Calculated Property |
Pvap | [1.25; 4077.90] | kPa | [326.14; 684.75] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.13197e+01 | |||
Coefficient B | -8.43460e+03 | |||
Coefficient C | -9.63023e+00 | |||
Coefficient D | 4.66574e-06 | |||
Temperature range, min. | 326.14 | |||
Temperature range, max. | 684.75 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 400 500 600 | ||||
Pvap | 1.25 | kPa | 326.14 | Calculated Property |
Pvap | 7.81 | kPa | 365.99 | Calculated Property |
Pvap | 32.01 | kPa | 405.83 | Calculated Property |
Pvap | 97.57 | kPa | 445.68 | Calculated Property |
Pvap | 240.38 | kPa | 485.52 | Calculated Property |
Pvap | 506.82 | kPa | 525.37 | Calculated Property |
Pvap | 952.11 | kPa | 565.21 | Calculated Property |
Pvap | 1640.81 | kPa | 605.06 | Calculated Property |
Pvap | 2650.32 | kPa | 644.90 | Calculated Property |
Pvap | 4077.90 | kPa | 684.75 | Calculated Property |
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