Property | Value | Unit | Source |
---|---|---|---|
PAff | 856.40 | kJ/mol | NIST |
ΔcH°solid | [-2867.00; -2847.90] | kJ/mol | |
ΔcH°solid | -2847.90 ± 1.10 | kJ/mol | NIST |
ΔcH°solid | -2850.60 ± 0.42 | kJ/mol | NIST |
ΔcH°solid | -2867.00 | kJ/mol | NIST |
ΔcH°solid | -2861.00 | kJ/mol | NIST |
SProt | -15.00 | J/mol×K | NIST |
ΔfG° | -187.56 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-284.70; -265.20] | kJ/mol | |
ΔfH°gas | -284.70 ± 1.20 | kJ/mol | NIST |
ΔfH°gas | -275.00 | kJ/mol | NIST |
ΔfH°gas | -265.20 | kJ/mol | NIST |
ΔfH°solid | [-370.70; -351.20] | kJ/mol | |
ΔfH°solid | -370.70 ± 1.10 | kJ/mol | NIST |
ΔfH°solid | -368.00 ± 0.50 | kJ/mol | NIST |
ΔfH°solid | -351.20 | kJ/mol | NIST |
ΔfusH° | 17.29 | kJ/mol | Joback Calculated Property |
ΔsubH° | [86.00; 93.00] | kJ/mol | |
ΔsubH° | 86.00 ± 0.52 | kJ/mol | NIST |
ΔsubH° | 86.00 | kJ/mol | NIST |
ΔsubH° | 87.50 ± 0.50 | kJ/mol | NIST |
ΔsubH° | 93.00 | kJ/mol | NIST |
ΔvapH° | 78.40 ± 1.30 | kJ/mol | NIST |
IE | [8.20; 8.63] | eV | |
IE | 8.20 | eV | NIST |
IE | 8.63 | eV | NIST |
log10WS | [0.81; 0.81] | ||
log10WS | 0.81 | Aq. Sol... | |
log10WS | 0.81 | Estimat... | |
logPoct/wat | 1.098 | Crippen Calculated Property | |
McVol | 83.380 | ml/mol | McGowan Calculated Property |
NFPA Fire | 1 | KDB | |
Pc | 6240.00 | kPa | Critica... |
Inp | [213.50; 1379.00] | ||
Inp | 1379.00 | NIST | |
Inp | 1376.00 | NIST | |
Inp | 1368.00 | NIST | |
Inp | 1368.00 | NIST | |
Inp | 213.50 | NIST | |
Inp | 216.79 | NIST | |
Inp | 219.64 | NIST | |
Inp | 1376.00 | NIST | |
Inp | 213.50 | NIST | |
Inp | 1368.00 | NIST | |
Tboil | [549.05; 554.55] | K | |
Tboil | 549.05 | K | KDB |
Tboil | 550.00 | K | NIST |
Tboil | 549.10 ± 0.40 | K | NIST |
Tboil | 554.55 ± 0.50 | K | NIST |
Tc | 766.85 | K | Joback Calculated Property |
Tfus | [382.00; 383.90] | K | |
Tfus | 382.85 | K | KDB |
Tfus | 383.90 | K | Aq. Sol... |
Tfus | 383.15 | K | Liquid ... |
Tfus | 382.00 | K | Enthalp... |
Tfus | 383.65 | K | Thermal... |
Ttriple | [382.70; 383.54] | K | |
Ttriple | 383.54 ± 0.02 | K | NIST |
Ttriple | 382.70 ± 0.20 | K | NIST |
Ttriple | 382.80 ± 0.25 | K | NIST |
Vc | 0.196 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [186.33; 226.33] | J/mol×K | [519.62; 766.85] | |
T(K) Ideal gas heat capacity (J/mol×K) 190 200 210 220 230 600 700 | ||||
Cp,gas | 186.33 | J/mol×K | 519.62 | Joback Calculated Property |
Cp,gas | 194.85 | J/mol×K | 560.83 | Joback Calculated Property |
Cp,gas | 202.41 | J/mol×K | 602.03 | Joback Calculated Property |
Cp,gas | 209.18 | J/mol×K | 643.24 | Joback Calculated Property |
Cp,gas | 215.32 | J/mol×K | 684.44 | Joback Calculated Property |
Cp,gas | 220.99 | J/mol×K | 725.65 | Joback Calculated Property |
Cp,gas | 226.33 | J/mol×K | 766.85 | Joback Calculated Property |
Cp,solid | [131.00; 151.00] | J/mol×K | [297.90; 323.00] | |
T(K) Solid phase heat capacity (J/mol×K) 130 135 140 145 150 300 310 320 | ||||
Cp,solid | 131.40 | J/mol×K | 297.90 | NIST |
Cp,solid | 131.00 | J/mol×K | 298.00 | NIST |
Cp,solid | 135.53 | J/mol×K | 298.15 | NIST |
Cp,solid | 139.30 | J/mol×K | 298.15 | NIST |
Cp,solid | 151.00 | J/mol×K | 323.00 | NIST |
η | [0.0000251; 0.0009603] | Pa×s | [394.72; 519.62] | |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 400 450 500 | ||||
η | 0.0009603 | Pa×s | 394.72 | Joback Calculated Property |
η | 0.0004493 | Pa×s | 415.54 | Joback Calculated Property |
η | 0.0002260 | Pa×s | 436.35 | Joback Calculated Property |
η | 0.0001210 | Pa×s | 457.17 | Joback Calculated Property |
η | 0.0000684 | Pa×s | 477.99 | Joback Calculated Property |
η | 0.0000406 | Pa×s | 498.80 | Joback Calculated Property |
η | 0.0000251 | Pa×s | 519.62 | Joback Calculated Property |
ΔfusH | [1.20; 21.30] | kJ/mol | [366.80; 382.90] | |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0 5 10 15 20 370 375 380 | ||||
ΔfusH | 1.20 | kJ/mol | 366.80 | NIST |
ΔfusH | 20.50 | kJ/mol | 381.00 | NIST |
ΔfusH | 18.90 | kJ/mol | 382.60 | NIST |
ΔfusH | 18.90 | kJ/mol | 382.60 | NIST |
ΔfusH | 21.30 | kJ/mol | 382.80 | NIST |
ΔfusH | 21.30 | kJ/mol | 382.90 | NIST |
ΔsubH | [85.30; 95.00] | kJ/mol | [303.00; 353.50] | |
T(K) Enthalpy of sublimation at a given temperature (kJ/mol) 86 88 90 92 94 320 340 | ||||
ΔsubH | 93.40 | kJ/mol | 303.00 | NIST |
ΔsubH | 95.00 ± 1.00 | kJ/mol | 329.00 | NIST |
ΔsubH | 93.00 ± 21.00 | kJ/mol | 329.50 | NIST |
ΔsubH | 85.30 ± 0.50 | kJ/mol | 334.00 | NIST |
ΔsubH | 92.30 | kJ/mol | 353.50 | NIST |
ΔvapH | [74.30; 74.30] | kJ/mol | [427.50; 484.50] | |
ΔvapH | 74.30 | kJ/mol | 427.50 | NIST |
ΔvapH | 74.30 | kJ/mol | 484.50 | NIST |
Psub | [4.00e-04; 0.02] | kPa | [323.10; 364.30] | |
T(K) Sublimation pressure (kPa) 0 5.00e-3 0.01 0.02 0.02 0.03 330 340 350 360 | ||||
Psub | 4.00e-04 | kPa | 323.10 | Di-Hydr... |
Psub | 5.48e-04 | kPa | 326.10 | Di-Hydr... |
Psub | 6.17e-04 | kPa | 326.70 | Di-Hydr... |
Psub | 7.74e-04 | kPa | 329.10 | Di-Hydr... |
Psub | 8.81e-04 | kPa | 330.10 | Di-Hydr... |
Psub | 9.66e-04 | kPa | 331.20 | Di-Hydr... |
Psub | 1.06e-03 | kPa | 332.10 | Di-Hydr... |
Psub | 1.24e-03 | kPa | 333.30 | Di-Hydr... |
Psub | 1.34e-03 | kPa | 334.20 | Di-Hydr... |
Psub | 1.47e-03 | kPa | 335.20 | Di-Hydr... |
Psub | 1.86e-03 | kPa | 337.10 | Di-Hydr... |
Psub | 2.23e-03 | kPa | 339.30 | Di-Hydr... |
Psub | 2.54e-03 | kPa | 340.30 | Di-Hydr... |
Psub | 2.72e-03 | kPa | 341.20 | Di-Hydr... |
Psub | 2.71e-03 | kPa | 341.30 | Di-Hydr... |
Psub | 3.40e-03 | kPa | 343.30 | Di-Hydr... |
Psub | 3.41e-03 | kPa | 343.50 | Di-Hydr... |
Psub | 3.54e-03 | kPa | 344.30 | Di-Hydr... |
Psub | 3.67e-03 | kPa | 344.40 | Di-Hydr... |
Psub | 4.58e-03 | kPa | 346.20 | Di-Hydr... |
Psub | 4.68e-03 | kPa | 346.40 | Di-Hydr... |
Psub | 5.53e-03 | kPa | 348.30 | Di-Hydr... |
Psub | 5.56e-03 | kPa | 348.40 | Di-Hydr... |
Psub | 5.69e-03 | kPa | 349.30 | Di-Hydr... |
Psub | 6.49e-03 | kPa | 350.20 | Di-Hydr... |
Psub | 6.43e-03 | kPa | 350.30 | Di-Hydr... |
Psub | 7.32e-03 | kPa | 351.30 | Di-Hydr... |
Psub | 7.73e-03 | kPa | 352.20 | Di-Hydr... |
Psub | 8.71e-03 | kPa | 353.30 | Di-Hydr... |
Psub | 9.84e-03 | kPa | 354.30 | Di-Hydr... |
Psub | 0.01 | kPa | 355.20 | Di-Hydr... |
Psub | 0.01 | kPa | 356.30 | Di-Hydr... |
Psub | 0.01 | kPa | 357.40 | Di-Hydr... |
Psub | 0.01 | kPa | 358.20 | Di-Hydr... |
Psub | 0.01 | kPa | 358.60 | Di-Hydr... |
Psub | 0.02 | kPa | 360.20 | Di-Hydr... |
Psub | 0.02 | kPa | 360.40 | Di-Hydr... |
Psub | 0.02 | kPa | 361.30 | Di-Hydr... |
Psub | 0.02 | kPa | 364.30 | Di-Hydr... |
ΔfusS | [3.27; 55.60] | J/mol×K | [366.80; 382.80] | |
ΔfusS | 3.27 | J/mol×K | 366.80 | NIST |
ΔfusS | 53.80 | J/mol×K | 381.00 | NIST |
ΔfusS | 49.41 | J/mol×K | 382.60 | NIST |
ΔfusS | 55.60 | J/mol×K | 382.80 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboil | [444.70; 456.80] | K | [2.95; 4.93] | |
Tboil | 444.70 | K | 2.95 | Vapour ... |
Tboil | 451.30 | K | 3.93 | Vapour ... |
Tboil | 456.80 | K | 4.93 | Vapour ... |
Tboilr | 451.20 | K | 2.10 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.09; 7618.13] | kPa | [382.00; 810.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.64521e+02 | |||
Coefficient B | -1.68432e+04 | |||
Coefficient C | -2.08308e+01 | |||
Coefficient D | 7.18739e-06 | |||
Temperature range, min. | 382.00 | |||
Temperature range, max. | 810.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 8000 400 600 800 | ||||
Pvap | 0.09 | kPa | 382.00 | Calculated Property |
Pvap | 1.41 | kPa | 429.56 | Calculated Property |
Pvap | 10.76 | kPa | 477.11 | Calculated Property |
Pvap | 51.35 | kPa | 524.67 | Calculated Property |
Pvap | 176.66 | kPa | 572.22 | Calculated Property |
Pvap | 481.64 | kPa | 619.78 | Calculated Property |
Pvap | 1111.85 | kPa | 667.33 | Calculated Property |
Pvap | 2278.49 | kPa | 714.89 | Calculated Property |
Pvap | 4290.69 | kPa | 762.44 | Calculated Property |
Pvap | 7618.13 | kPa | 810.00 | Calculated Property |
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