Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -1451.00 | kJ/mol | NIST |
ΔfG° | -271.47 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -444.00 ± 10.00 | kJ/mol | NIST |
ΔfH°liquid | -487.00 ± 8.80 | kJ/mol | NIST |
ΔfusH° | 10.51 | kJ/mol | Joback Calculated Property |
ΔvapH° | [43.40; 46.74] | kJ/mol | |
ΔvapH° | 46.74 | kJ/mol | NIST |
ΔvapH° | 43.40 ± 4.20 | kJ/mol | NIST |
ΔvapH° | 46.73 ± 0.06 | kJ/mol | NIST |
ΔvapH° | 46.70 ± 0.10 | kJ/mol | NIST |
IE | [10.30; 10.70] | eV | |
IE | 10.30 | eV | NIST |
IE | 10.53 ± 0.05 | eV | NIST |
IE | 10.70 | eV | NIST |
log10WS | -0.09 | Crippen Calculated Property | |
logPoct/wat | 0.398 | Crippen Calculated Property | |
McVol | 72.810 | ml/mol | McGowan Calculated Property |
Pc | 4462.28 | kPa | Joback Calculated Property |
Inp | [679.00; 731.00] | ||
Inp | 708.00 | NIST | |
Inp | 691.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 705.00 | NIST | |
Inp | 729.40 | NIST | |
Inp | 731.00 | NIST | |
I | [1270.00; 1345.00] | ||
I | 1270.00 | NIST | |
I | 1314.00 | NIST | |
I | 1345.00 | NIST | |
I | 1318.00 | NIST | |
Tboil | [400.00; 404.70] | K | |
Tboil | 402.60 | K | NIST |
Tboil | 404.00 ± 3.00 | K | NIST |
Tboil | Outlier 400.00 ± 3.00 | K | NIST |
Tboil | 403.10 ± 0.50 | K | NIST |
Tboil | 403.20 ± 0.50 | K | NIST |
Tboil | 403.10 ± 0.50 | K | NIST |
Tboil | 404.70 ± 0.50 | K | NIST |
Tc | 570.48 | K | Joback Calculated Property |
Tfus | [240.50; 241.00] | K | |
Tfus | 241.00 ± 0.02 | K | NIST |
Tfus | 240.50 ± 0.20 | K | NIST |
Vc | 0.277 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [117.88; 147.10] | J/mol×K | [381.76; 570.48] | |
Cp,gas | 117.88 | J/mol×K | 381.76 | Joback Calculated Property |
Cp,gas | 123.10 | J/mol×K | 413.21 | Joback Calculated Property |
Cp,gas | 128.19 | J/mol×K | 444.67 | Joback Calculated Property |
Cp,gas | 133.14 | J/mol×K | 476.12 | Joback Calculated Property |
Cp,gas | 137.95 | J/mol×K | 507.57 | Joback Calculated Property |
Cp,gas | 142.60 | J/mol×K | 539.02 | Joback Calculated Property |
Cp,gas | 147.10 | J/mol×K | 570.48 | Joback Calculated Property |
η | [0.0003300; 0.0025693] | Pa×s | [225.65; 381.76] | |
η | 0.0025693 | Pa×s | 225.65 | Joback Calculated Property |
η | 0.0015292 | Pa×s | 251.67 | Joback Calculated Property |
η | 0.0010031 | Pa×s | 277.69 | Joback Calculated Property |
η | 0.0007073 | Pa×s | 303.70 | Joback Calculated Property |
η | 0.0005270 | Pa×s | 329.72 | Joback Calculated Property |
η | 0.0004099 | Pa×s | 355.74 | Joback Calculated Property |
η | 0.0003300 | Pa×s | 381.76 | Joback Calculated Property |
ΔvapH | [39.23; 46.70] | kJ/mol | [350.50; 402.60] | |
ΔvapH | 46.70 | kJ/mol | 350.50 | NIST |
ΔvapH | 45.50 | kJ/mol | 360.00 | NIST |
ΔvapH | 39.23 | kJ/mol | 402.60 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 403.20 | K | 98.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [301.98; 427.49] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.50317e+01 | |||
Coefficient B | -3.58037e+03 | |||
Coefficient C | -5.91440e+01 | |||
Temperature range, min. | 301.98 | |||
Temperature range, max. | 427.49 | |||
Pvap | 1.33 | kPa | 301.98 | Calculated Property |
Pvap | 2.97 | kPa | 315.93 | Calculated Property |
Pvap | 6.09 | kPa | 329.87 | Calculated Property |
Pvap | 11.64 | kPa | 343.82 | Calculated Property |
Pvap | 20.94 | kPa | 357.76 | Calculated Property |
Pvap | 35.76 | kPa | 371.71 | Calculated Property |
Pvap | 58.33 | kPa | 385.65 | Calculated Property |
Pvap | 91.40 | kPa | 399.60 | Calculated Property |
Pvap | 138.25 | kPa | 413.54 | Calculated Property |
Pvap | 202.66 | kPa | 427.49 | Calculated Property |
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