Property | Value | Unit | Source |
---|---|---|---|
PAff | 571.30 | kJ/mol | NIST |
BasG | 541.50 | kJ/mol | NIST |
ΔfG° | -635.98 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-739.50; -695.40] | kJ/mol | |
ΔfH°gas | -708.80 ± 4.20 | kJ/mol | NIST |
ΔfH°gas | -705.00 ± 3.40 | kJ/mol | NIST |
ΔfH°gas | Outlier -739.50 ± 5.00 | kJ/mol | NIST |
ΔfH°gas | -695.40 ± 9.20 | kJ/mol | NIST |
ΔfH°gas | -699.00 | kJ/mol | NIST |
ΔfH°gas | -715.00 ± 4.00 | kJ/mol | NIST |
ΔfusH° | 4.37 | kJ/mol | Joback Calculated Property |
ΔvapH° | 18.46 | kJ/mol | Joback Calculated Property |
IE | [12.39; 13.10] | eV | |
IE | 12.60 ± 0.40 | eV | NIST |
IE | 13.00 ± 1.00 | eV | NIST |
IE | 13.08 ± 0.02 | eV | NIST |
IE | 12.60 ± 0.02 | eV | NIST |
IE | 12.45 | eV | NIST |
IE | 12.39 | eV | NIST |
IE | 12.39 | eV | NIST |
IE | 12.91 ± 0.03 | eV | NIST |
IE | 13.08 ± 0.01 | eV | NIST |
IE | 13.10 | eV | NIST |
IE | 13.00 | eV | NIST |
IE | 13.08 ± 0.02 | eV | NIST |
log10WS | -1.55 | Crippen Calculated Property | |
logPoct/wat | 1.745 | Crippen Calculated Property | |
McVol | 42.500 | ml/mol | McGowan Calculated Property |
Pc | [3867.94; 3885.00] | kPa | |
Pc | 3885.00 ± 6.00 | kPa | NIST |
Pc | 3868.00 ± 10.00 | kPa | NIST |
Pc | 3879.00 ± 9.80 | kPa | NIST |
Pc | 3867.94 | kPa | NIST |
ρc | [577.66; 598.86] | kg/m3 | |
ρc | 598.86 ± 0.52 | kg/m3 | NIST |
ρc | 577.66 ± 3.13 | kg/m3 | NIST |
ρc | 582.36 ± 3.13 | kg/m3 | NIST |
ρc | 579.75 | kg/m3 | NIST |
Inp | [190.00; 209.00] | ||
Inp | 209.00 | NIST | |
Inp | 190.00 | NIST | |
Inp | 190.00 | NIST | |
Inp | 209.00 | NIST | |
Tboil | [191.65; 191.80] | K | |
Tboil | 191.70 | K | NIST |
Tboil | 191.65 ± 0.05 | K | NIST |
Tboil | 191.80 ± 0.30 | K | NIST |
Tboil | 191.80 ± 0.30 | K | NIST |
Tc | [301.54; 301.98] | K | |
Tc | 301.92 ± 0.08 | K | NIST |
Tc | 301.90 ± 0.10 | K | NIST |
Tc | Outlier 301.54 ± 0.20 | K | NIST |
Tc | 301.92 ± 0.30 | K | NIST |
Tc | 301.88 ± 0.05 | K | NIST |
Tc | 301.98 | K | NIST |
Tc | 301.80 | K | NIST |
Tfus | [92.03; 92.20] | K | |
Tfus | 92.20 ± 0.30 | K | NIST |
Tfus | 92.03 | K | NIST |
Ttriple | 92.00 ± 2.00 | K | NIST |
Vc | 0.183 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [60.54; 78.50] | J/mol×K | [254.29; 403.52] | |
Cp,gas | 60.54 | J/mol×K | 254.29 | Joback Calculated Property |
Cp,gas | 64.09 | J/mol×K | 279.16 | Joback Calculated Property |
Cp,gas | 67.41 | J/mol×K | 304.03 | Joback Calculated Property |
Cp,gas | 70.50 | J/mol×K | 328.90 | Joback Calculated Property |
Cp,gas | 73.37 | J/mol×K | 353.78 | Joback Calculated Property |
Cp,gas | 76.04 | J/mol×K | 378.65 | Joback Calculated Property |
Cp,gas | 78.50 | J/mol×K | 403.52 | Joback Calculated Property |
ΔvapH | [15.70; 17.10] | kJ/mol | [157.50; 285.00] | |
ΔvapH | 17.10 | kJ/mol | 157.50 | NIST |
ΔvapH | 17.00 | kJ/mol | 159.00 | NIST |
ΔvapH | 16.80 | kJ/mol | 168.50 | NIST |
ΔvapH | 15.70 | kJ/mol | 215.00 | NIST |
ΔvapH | 15.70 | kJ/mol | 257.00 | NIST |
ΔvapH | 16.00 | kJ/mol | 285.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [5.74e-04; 3825.19] | kPa | [92.15; 302.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 4.10990e+01 | |||
Coefficient B | -2.65987e+03 | |||
Coefficient C | -4.37378e+00 | |||
Coefficient D | 1.02412e-05 | |||
Temperature range, min. | 92.15 | |||
Temperature range, max. | 302.00 | |||
Pvap | 5.74e-04 | kPa | 92.15 | Calculated Property |
Pvap | 0.08 | kPa | 115.47 | Calculated Property |
Pvap | 1.74 | kPa | 138.78 | Calculated Property |
Pvap | 14.95 | kPa | 162.10 | Calculated Property |
Pvap | 71.04 | kPa | 185.42 | Calculated Property |
Pvap | 230.83 | kPa | 208.73 | Calculated Property |
Pvap | 580.67 | kPa | 232.05 | Calculated Property |
Pvap | 1222.20 | kPa | 255.37 | Calculated Property |
Pvap | 2264.79 | kPa | 278.68 | Calculated Property |
Pvap | 3825.19 | kPa | 302.00 | Calculated Property |
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