Property | Value | Unit | Source |
---|---|---|---|
PAff | 580.00 | kJ/mol | NIST |
BasG | 550.30 | kJ/mol | NIST |
EA | 0.91 ± 0.20 | eV | NIST |
ΔfG° | -609.73 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-649.40; -647.30] | kJ/mol |
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ΔfH°gas | -647.30 ± 2.90 | kJ/mol | NIST |
ΔfH°gas | -649.40 ± 3.20 | kJ/mol | NIST |
ΔfusH° | 5.46 | kJ/mol | Joback Calculated Property |
ΔvapH° | 20.51 | kJ/mol | Joback Calculated Property |
IE | [11.40; 12.40] | eV |
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IE | 11.40 ± 0.01 | eV | NIST |
IE | 11.40 ± 0.01 | eV | NIST |
IE | 11.76 ± 0.02 | eV | NIST |
IE | 11.70 | eV | NIST |
IE | 11.82 ± 0.02 | eV | NIST |
IE | 11.89 ± 0.10 | eV | NIST |
IE | 12.30 ± 0.30 | eV | NIST |
IE | 12.40 | eV | NIST |
IE | 12.08 ± 0.05 | eV | NIST |
IE | 12.10 | eV | NIST |
IE | 12.00 | eV | NIST |
IE | 12.12 ± 0.02 | eV | NIST |
log10WS | -1.83 | Crippen Calculated Property | |
logPoct/wat | 1.901 | Crippen Calculated Property | |
McVol | 47.760 | ml/mol | McGowan Calculated Property |
Pc | 3956.00 ± 3.00 | kPa | NIST |
ρc | 763.91 ± 4.47 | kg/m3 | NIST |
Inp | [222.00; 222.00] |
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|
Inp | 222.00 | NIST | |
Inp | 222.00 | NIST | |
Tboil | 215.30 | K | NIST |
Tc | 340.08 ± 0.02 | K | NIST |
Tfus | [98.47; 98.72] | K |
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Tfus | 98.47 ± 0.05 | K | NIST |
Tfus | 98.72 ± 0.05 | K | NIST |
Vc | 0.197 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [65.29; 83.79] | J/mol×K | [283.02; 447.40] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 65 70 75 80 85 300 350 400 450 | ||||
Cp,gas | 65.29 | J/mol×K | 283.02 | Joback Calculated Property |
Cp,gas | 69.11 | J/mol×K | 310.42 | Joback Calculated Property |
Cp,gas | 72.61 | J/mol×K | 337.81 | Joback Calculated Property |
Cp,gas | 75.81 | J/mol×K | 365.21 | Joback Calculated Property |
Cp,gas | 78.73 | J/mol×K | 392.60 | Joback Calculated Property |
Cp,gas | 81.39 | J/mol×K | 420.00 | Joback Calculated Property |
Cp,gas | 83.79 | J/mol×K | 447.40 | Joback Calculated Property |
Cp,liquid | 163.80 | J/mol×K | 293.00 | NIST |
ΔvapH | [17.70; 19.10] | kJ/mol | [190.50; 308.00] | ![]() |
ΔvapH | 19.10 | kJ/mol | 190.50 | NIST |
ΔvapH | 17.70 | kJ/mol | 213.50 | NIST |
ΔvapH | 17.80 | kJ/mol | 308.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [5.90e-04; 4288.50] | kPa | [105.15; 340.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.46449e+01 | |||
Coefficient B | -3.96443e+03 | |||
Coefficient C | -1.17615e+01 | |||
Coefficient D | 3.40177e-05 | |||
Temperature range, min. | 105.15 | |||
Temperature range, max. | 340.15 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 100 200 300 | ||||
Pvap | 5.90e-04 | kPa | 105.15 | Calculated Property |
Pvap | 0.10 | kPa | 131.26 | Calculated Property |
Pvap | 2.22 | kPa | 157.37 | Calculated Property |
Pvap | 17.84 | kPa | 183.48 | Calculated Property |
Pvap | 78.05 | kPa | 209.59 | Calculated Property |
Pvap | 236.84 | kPa | 235.71 | Calculated Property |
Pvap | 573.08 | kPa | 261.82 | Calculated Property |
Pvap | 1205.20 | kPa | 287.93 | Calculated Property |
Pvap | 2328.41 | kPa | 314.04 | Calculated Property |
Pvap | 4288.50 | kPa | 340.15 | Calculated Property |
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