Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -1663.80 | kJ/mol | NIST |
ΔfG° | -193.09 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -446.30 | kJ/mol | NIST |
ΔfH°liquid | -497.30 | kJ/mol | NIST |
ΔfH°solid | -517.10 | kJ/mol | NIST |
ΔfusH° | 11.51 | kJ/mol | Joback Calculated Property |
ΔsubH° | 76.30 | kJ/mol | NIST |
ΔvapH° | 51.00 ± 2.50 | kJ/mol | NIST |
IE | [10.20; 10.62] | eV |
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IE | 10.20 | eV | NIST |
IE | 10.62 | eV | NIST |
log10WS | [0.85; 0.85] |
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|
log10WS | 0.85 | Aq. Sol... | |
log10WS | 0.85 | Estimat... | |
logPoct/wat | 0.102 | Crippen Calculated Property | |
McVol | 70.550 | ml/mol | McGowan Calculated Property |
Pc | 5080.25 | kPa | Joback Calculated Property |
Inp | 838.00 | NIST | |
Tboil | [456.20; 458.40] | K |
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Tboil | 458.40 | K | KDB |
Tboil | 456.20 | K | NIST |
Tboil | 458.40 ± 0.60 | K | NIST |
Tc | 613.38 | K | Joback Calculated Property |
Tfus | [321.34; 321.90] | K |
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Tfus | 321.34 | K | KDB |
Tfus | 321.90 | K | Aq. Sol... |
Ttriple | 321.41 ± 0.02 | K | NIST |
Vc | 0.257 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [136.41; 172.18] | J/mol×K | [416.86; 613.38] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 140 150 160 170 450 500 550 600 | ||||
Cp,gas | 136.41 | J/mol×K | 416.86 | Joback Calculated Property |
Cp,gas | 142.88 | J/mol×K | 449.61 | Joback Calculated Property |
Cp,gas | 149.16 | J/mol×K | 482.37 | Joback Calculated Property |
Cp,gas | 155.23 | J/mol×K | 515.12 | Joback Calculated Property |
Cp,gas | 161.10 | J/mol×K | 547.87 | Joback Calculated Property |
Cp,gas | 166.75 | J/mol×K | 580.63 | Joback Calculated Property |
Cp,gas | 172.18 | J/mol×K | 613.38 | Joback Calculated Property |
Cp,solid | 156.43 | J/mol×K | 300.00 | NIST |
ΔfusH | [15.23; 20.90] | kJ/mol | [321.41; 321.90] | ![]() |
ΔfusH | 16.79 | kJ/mol | 321.41 | NIST |
ΔfusH | 20.90 | kJ/mol | 321.70 | NIST |
ΔfusH | 15.23 | kJ/mol | 321.90 | NIST |
ΔsubH | [71.90; 89.10] | kJ/mol | [264.50; 322.00] | ![]() |
ΔsubH | 77.70 | kJ/mol | 264.50 | NIST |
ΔsubH | 89.10 ± 0.80 | kJ/mol | 299.50 | NIST |
ΔsubH | 71.90 | kJ/mol | 322.00 | NIST |
ΔvapH | [56.60; 77.70] | kJ/mol | [298.15; 397.50] | ![]() |
ΔvapH | 77.70 | kJ/mol | 298.15 | The ent... |
ΔvapH | 56.60 | kJ/mol | 397.50 | NIST |
Pvap | [0.88; 2.95] | kPa | [322.60; 371.70] | ![]() |
T(K) Vapor pressure (kPa) 1 1.5 2 2.5 3 340 360 | ||||
Pvap | 0.88 | kPa | 322.60 | Vapor-L... |
Pvap | 1.29 | kPa | 337.20 | Vapor-L... |
Pvap | 1.49 | kPa | 342.30 | Vapor-L... |
Pvap | 1.96 | kPa | 352.50 | Vapor-L... |
Pvap | 2.38 | kPa | 362.60 | Vapor-L... |
Pvap | 2.95 | kPa | 371.70 | Vapor-L... |
ΔfusS | [52.25; 64.80] | J/mol×K | [321.41; 321.70] | ![]() |
ΔfusS | 52.25 | J/mol×K | 321.41 | NIST |
ΔfusS | 64.80 | J/mol×K | 321.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.62; 101.21] | kPa | [338.15; 457.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.20583e+01 | |||
Coefficient B | -1.00894e+04 | |||
Coefficient C | -1.08907e+01 | |||
Coefficient D | 6.38522e-06 | |||
Temperature range, min. | 338.15 | |||
Temperature range, max. | 457.15 | |||
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 350 400 450 | ||||
Pvap | 0.62 | kPa | 338.15 | Calculated Property |
Pvap | 1.34 | kPa | 351.37 | Calculated Property |
Pvap | 2.70 | kPa | 364.59 | Calculated Property |
Pvap | 5.13 | kPa | 377.82 | Calculated Property |
Pvap | 9.29 | kPa | 391.04 | Calculated Property |
Pvap | 16.09 | kPa | 404.26 | Calculated Property |
Pvap | 26.77 | kPa | 417.48 | Calculated Property |
Pvap | 43.00 | kPa | 430.71 | Calculated Property |
Pvap | 66.91 | kPa | 443.93 | Calculated Property |
Pvap | 101.21 | kPa | 457.15 | Calculated Property |
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