Property | Value | Unit | Source |
---|---|---|---|
PAff | [905.50; 908.30] | kJ/mol |
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PAff | 905.50 | kJ/mol | NIST |
PAff | 908.30 | kJ/mol | NIST |
BasG | [876.50; 884.10] | kJ/mol |
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BasG | 876.50 | kJ/mol | NIST |
BasG | 884.10 | kJ/mol | NIST |
ΔcH°solid | -8956.90 ± 1.30 | kJ/mol | NIST |
EA | [0.88; 1.07] | eV |
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EA | 1.06 ± 0.01 | eV | NIST |
EA | 1.07 ± 0.04 | eV | NIST |
EA | 0.88 ± 0.04 | eV | NIST |
ΔfG° | 513.78 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 342.60 ± 5.90 | kJ/mol | NIST |
ΔfH°solid | 206.70 ± 3.00 | kJ/mol | NIST |
ΔfusH° | 36.80 | kJ/mol | Heat Ca... |
ΔsubH° | [125.00; 144.00] | kJ/mol |
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ΔsubH° | 136.10 ± 0.30 | kJ/mol | NIST |
ΔsubH° | 144.00 ± 5.00 | kJ/mol | NIST |
ΔsubH° | 143.70 ± 0.50 | kJ/mol | NIST |
ΔsubH° | 125.00 | kJ/mol | NIST |
ΔvapH° | 106.20 ± 3.70 | kJ/mol | NIST |
IE | [6.64; 7.04] | eV |
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IE | 6.97 ± 0.05 | eV | NIST |
IE | 6.97 | eV | NIST |
IE | 6.90 ± 0.30 | eV | NIST |
IE | 6.97 | eV | NIST |
IE | 7.04 | eV | NIST |
IE | 7.04 ± 0.04 | eV | NIST |
IE | 7.01 | eV | NIST |
IE | 7.00 ± 0.30 | eV | NIST |
IE | 6.94 | eV | NIST |
IE | 6.95 | eV | NIST |
IE | 6.90 | eV | NIST |
IE | 7.00 | eV | NIST |
IE | 7.00 | eV | NIST |
IE | Outlier 6.64 | eV | NIST |
IE | 6.97 ± 0.02 | eV | NIST |
IE | 7.01 | eV | NIST |
log10WS | [-8.60; -8.60] |
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|
log10WS | -8.60 | Aq. Sol... | |
log10WS | -8.60 | Estimat... | |
logPoct/wat | 5.146 | Crippen Calculated Property | |
McVol | 182.340 | ml/mol | McGowan Calculated Property |
Pc | 2511.00 | kPa | KDB |
Inp | [401.28; 2436.00] |
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|
Inp | 2426.00 | NIST | |
Inp | 2425.00 | NIST | |
Inp | 2395.00 | NIST | |
Inp | 2425.00 | NIST | |
Inp | 2386.00 | NIST | |
Inp | 2436.00 | NIST | |
Inp | 403.90 | NIST | |
Inp | 405.00 | NIST | |
Inp | 403.50 | NIST | |
Inp | 403.15 | NIST | |
Inp | 402.86 | NIST | |
Inp | 407.30 | NIST | |
Inp | 403.52 | NIST | |
Inp | 408.30 | NIST | |
Inp | 401.28 | NIST | |
Inp | 405.70 | NIST | |
Inp | 403.51 | NIST | |
Inp | 403.70 | NIST | |
Inp | 403.89 | NIST | |
Inp | 408.30 | NIST | |
Inp | 2395.00 | NIST | |
S°solid,1 bar | 215.40 | J/mol×K | NIST |
Tboil | 704.82 | K | Joback Calculated Property |
Tc | 987.20 | K | KDB |
Tfus | [608.00; 625.55] | K |
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Tfus | 608.00 | K | KDB |
Tfus | 625.55 | K | Aq. Sol... |
Tfus | 613.15 ± 2.00 | K | NIST |
Tfus | 613.15 ± 2.00 | K | NIST |
Ttriple | 623.75 | K | Solubil... |
Vc | 0.700 | m3/kmol | KDB |
Zc | 0.2141430 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [468.00; 543.24] | J/mol×K | [704.82; 968.39] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 480 500 520 540 700 800 900 | ||||
Cp,gas | 468.00 | J/mol×K | 704.82 | Joback Calculated Property |
Cp,gas | 482.86 | J/mol×K | 748.75 | Joback Calculated Property |
Cp,gas | 496.51 | J/mol×K | 792.68 | Joback Calculated Property |
Cp,gas | 509.15 | J/mol×K | 836.61 | Joback Calculated Property |
Cp,gas | 521.02 | J/mol×K | 880.54 | Joback Calculated Property |
Cp,gas | 532.31 | J/mol×K | 924.47 | Joback Calculated Property |
Cp,gas | 543.24 | J/mol×K | 968.39 | Joback Calculated Property |
Cp,solid | 236.60 | J/mol×K | 298.15 | NIST |
η | [0.0007153; 0.0017235] | Pa×s | [442.18; 704.82] | ![]() |
T(K) Dynamic viscosity (Pa×s) 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 1.80e-3 500 600 700 | ||||
η | 0.0017235 | Pa×s | 442.18 | Joback Calculated Property |
η | 0.0013935 | Pa×s | 485.95 | Joback Calculated Property |
η | 0.0011669 | Pa×s | 529.73 | Joback Calculated Property |
η | 0.0010040 | Pa×s | 573.50 | Joback Calculated Property |
η | 0.0008825 | Pa×s | 617.27 | Joback Calculated Property |
η | 0.0007890 | Pa×s | 661.05 | Joback Calculated Property |
η | 0.0007153 | Pa×s | 704.82 | Joback Calculated Property |
ΔsubH | [117.20; 132.60] | kJ/mol | [293.00; 463.00] | ![]() |
T(K) Enthalpy of sublimation at a given temperature (kJ/mol) 120 125 130 300 350 400 450 | ||||
ΔsubH | 124.00 | kJ/mol | 293.00 | NIST |
ΔsubH | 126.50 | kJ/mol | 383.00 | NIST |
ΔsubH | 124.80 ± 2.60 | kJ/mol | 414.50 | NIST |
ΔsubH | 125.00 ± 4.00 | kJ/mol | 422.00 | NIST |
ΔsubH | 126.10 ± 9.00 | kJ/mol | 429.00 | NIST |
ΔsubH | 132.60 | kJ/mol | 458.00 | NIST |
ΔsubH | 117.20 | kJ/mol | 459.00 | NIST |
ΔsubH | 128.80 | kJ/mol | 463.00 | NIST |
Psub | [1.46e-05; 2.15e-04] | kPa | [399.00; 430.10] | ![]() |
T(K) Sublimation pressure (kPa) 0 5.00e-5 1.00e-4 1.50e-4 2.00e-4 400 410 420 430 | ||||
Psub | 1.46e-05 | kPa | 399.00 | Sublima... |
Psub | 2.10e-05 | kPa | 404.40 | Sublima... |
Psub | 2.55e-05 | kPa | 405.60 | Sublima... |
Psub | 3.39e-05 | kPa | 409.50 | Sublima... |
Psub | 4.22e-05 | kPa | 410.60 | Sublima... |
Psub | 5.42e-05 | kPa | 414.60 | Sublima... |
Psub | 6.67e-05 | kPa | 415.80 | Sublima... |
Psub | 6.39e-05 | kPa | 416.60 | Sublima... |
Psub | 7.84e-05 | kPa | 418.60 | Sublima... |
Psub | 8.46e-05 | kPa | 419.60 | Sublima... |
Psub | 1.03e-04 | kPa | 420.80 | Sublima... |
Psub | 1.28e-04 | kPa | 424.70 | Sublima... |
Psub | 2.15e-04 | kPa | 430.10 | Sublima... |
Pvap | [1.24e-07; 0.85] | kPa | [298.15; 510.00] | ![]() |
T(K) Vapor pressure (kPa) 0 0.2 0.4 0.6 0.8 300 400 500 | ||||
Pvap | 1.24e-07 | kPa | 298.15 | Hypothe... |
Pvap | 1.62e-07 | kPa | 300.00 | Hypothe... |
Pvap | 6.39e-07 | kPa | 310.00 | Hypothe... |
Pvap | 2.28e-06 | kPa | 320.00 | Hypothe... |
Pvap | 7.39e-06 | kPa | 330.00 | Hypothe... |
Pvap | 2.20e-05 | kPa | 340.00 | Hypothe... |
Pvap | 6.05e-05 | kPa | 350.00 | Hypothe... |
Pvap | 1.55e-04 | kPa | 360.00 | Hypothe... |
Pvap | 3.72e-04 | kPa | 370.00 | Hypothe... |
Pvap | 8.40e-04 | kPa | 380.00 | Hypothe... |
Pvap | 1.80e-03 | kPa | 390.00 | Hypothe... |
Pvap | 3.66e-03 | kPa | 400.00 | Hypothe... |
Pvap | 7.11e-03 | kPa | 410.00 | Hypothe... |
Pvap | 0.01 | kPa | 420.00 | Hypothe... |
Pvap | 0.02 | kPa | 430.00 | Hypothe... |
Pvap | 0.04 | kPa | 440.00 | Hypothe... |
Pvap | 0.07 | kPa | 450.00 | Hypothe... |
Pvap | 0.11 | kPa | 460.00 | Hypothe... |
Pvap | 0.18 | kPa | 470.00 | Hypothe... |
Pvap | 0.27 | kPa | 480.00 | Hypothe... |
Pvap | 0.40 | kPa | 490.00 | Hypothe... |
Pvap | 0.59 | kPa | 500.00 | Hypothe... |
Pvap | 0.85 | kPa | 510.00 | Hypothe... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [9.10e-05; 9.79e-04] | kPa | [420.15; 449.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.74648e+01 | |||
Coefficient B | -1.54566e+04 | |||
Coefficient C | 3.15863e-03 | |||
Coefficient D | -2.56685e-09 | |||
Temperature range, min. | 420.15 | |||
Temperature range, max. | 449.15 | |||
T(K) Vapor pressure (kPa) 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 420 430 440 | ||||
Pvap | 9.10e-05 | kPa | 420.15 | Calculated Property |
Pvap | 1.20e-04 | kPa | 423.37 | Calculated Property |
Pvap | 1.59e-04 | kPa | 426.59 | Calculated Property |
Pvap | 2.08e-04 | kPa | 429.82 | Calculated Property |
Pvap | 2.72e-04 | kPa | 433.04 | Calculated Property |
Pvap | 3.54e-04 | kPa | 436.26 | Calculated Property |
Pvap | 4.59e-04 | kPa | 439.48 | Calculated Property |
Pvap | 5.93e-04 | kPa | 442.71 | Calculated Property |
Pvap | 7.63e-04 | kPa | 445.93 | Calculated Property |
Pvap | 9.79e-04 | kPa | 449.15 | Calculated Property |
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