Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -426.85 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -454.35 | kJ/mol | Joback Calculated Property |
ΔfusH° | 6.57 | kJ/mol | Joback Calculated Property |
ΔvapH° | 25.71 | kJ/mol | Joback Calculated Property |
IE | [11.21; 11.83] | eV | |
IE | 11.21 ± 0.02 | eV | NIST |
IE | 11.83 | eV | NIST |
log10WS | -2.13 | Crippen Calculated Property | |
logPoct/wat | 2.170 | Crippen Calculated Property | |
McVol | 58.230 | ml/mol | McGowan Calculated Property |
Pc | 5462.66 | kPa | Joback Calculated Property |
Inp | [398.00; 405.00] | ||
Inp | 398.00 | NIST | |
Inp | 398.00 | NIST | |
Inp | 405.00 | NIST | |
Inp | 405.00 | NIST | |
Tboil | 270.60 | K | NIST |
Tc | 508.13 | K | Joback Calculated Property |
Tfus | 194.35 | K | Joback Calculated Property |
Vc | 0.228 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [75.41; 91.97] | J/mol×K | [321.18; 508.13] | |
T(K) Ideal gas heat capacity (J/mol×K) 75 80 85 90 350 400 450 500 | ||||
Cp,gas | 75.41 | J/mol×K | 321.18 | Joback Calculated Property |
Cp,gas | 79.03 | J/mol×K | 352.34 | Joback Calculated Property |
Cp,gas | 82.28 | J/mol×K | 383.50 | Joback Calculated Property |
Cp,gas | 85.17 | J/mol×K | 414.66 | Joback Calculated Property |
Cp,gas | 87.74 | J/mol×K | 445.82 | Joback Calculated Property |
Cp,gas | 90.00 | J/mol×K | 476.97 | Joback Calculated Property |
Cp,gas | 91.97 | J/mol×K | 508.13 | Joback Calculated Property |
ΔvapH | [18.70; 26.00] | kJ/mol | [230.50; 415.00] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 18 20 22 24 26 250 300 350 400 | ||||
ΔvapH | 26.00 | kJ/mol | 230.50 | NIST |
ΔvapH | 18.70 | kJ/mol | 230.50 | NIST |
ΔvapH | 23.10 | kJ/mol | 240.50 | NIST |
ΔvapH | 23.00 | kJ/mol | 296.00 | NIST |
ΔvapH | 22.40 | kJ/mol | 362.00 | NIST |
ΔvapH | 23.10 | kJ/mol | 415.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [7.33e-06; 4255.61] | kPa | [114.00; 426.15] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.14922e+01 | |||
Coefficient B | -4.38507e+03 | |||
Coefficient C | -7.38664e+00 | |||
Coefficient D | 1.03430e-05 | |||
Temperature range, min. | 114.00 | |||
Temperature range, max. | 426.15 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 300 400 | ||||
Pvap | 7.33e-06 | kPa | 114.00 | Calculated Property |
Pvap | 8.93e-03 | kPa | 148.68 | Calculated Property |
Pvap | 0.57 | kPa | 183.37 | Calculated Property |
Pvap | 8.15 | kPa | 218.05 | Calculated Property |
Pvap | 51.26 | kPa | 252.73 | Calculated Property |
Pvap | 195.29 | kPa | 287.42 | Calculated Property |
Pvap | 541.55 | kPa | 322.10 | Calculated Property |
Pvap | 1219.26 | kPa | 356.78 | Calculated Property |
Pvap | 2387.67 | kPa | 391.47 | Calculated Property |
Pvap | 4255.61 | kPa | 426.15 | Calculated Property |
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