Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 178.59 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 127.30 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | 53.00 ± 2.00 | kJ/mol | NIST |
ΔfusH° | 12.33 | kJ/mol | Joback Calculated Property |
ΔvapH° | [50.60; 57.70] | kJ/mol | |
ΔvapH° | 57.40 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 57.70 | kJ/mol | NIST |
ΔvapH° | 50.60 ± 1.40 | kJ/mol | NIST |
IE | [8.73; 8.91] | eV | |
IE | 8.73 ± 0.02 | eV | NIST |
IE | 8.80 | eV | NIST |
IE | 8.91 | eV | NIST |
log10WS | -3.30 | Crippen Calculated Property | |
logPoct/wat | 2.622 | Crippen Calculated Property | |
McVol | 111.550 | ml/mol | McGowan Calculated Property |
Pc | 4000.70 | kPa | Joback Calculated Property |
Inp | 1174.00 | NIST | |
Tboil | 479.38 | K | Joback Calculated Property |
Tc | 731.20 | K | Joback Calculated Property |
Tfus | [297.60; 299.45] | K | |
Tfus | 297.60 | K | NIST |
Tfus | 299.45 ± 0.50 | K | NIST |
Vc | 0.407 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [183.02; 236.84] | J/mol×K | [479.38; 731.20] | |
Cp,gas | 183.02 | J/mol×K | 479.38 | Joback Calculated Property |
Cp,gas | 194.03 | J/mol×K | 521.35 | Joback Calculated Property |
Cp,gas | 204.14 | J/mol×K | 563.32 | Joback Calculated Property |
Cp,gas | 213.42 | J/mol×K | 605.29 | Joback Calculated Property |
Cp,gas | 221.92 | J/mol×K | 647.26 | Joback Calculated Property |
Cp,gas | 229.71 | J/mol×K | 689.23 | Joback Calculated Property |
Cp,gas | 236.84 | J/mol×K | 731.20 | Joback Calculated Property |
η | [0.0003339; 0.0042031] | Pa×s | [253.13; 479.38] | |
η | 0.0042031 | Pa×s | 253.13 | Joback Calculated Property |
η | 0.0020961 | Pa×s | 290.84 | Joback Calculated Property |
η | 0.0012263 | Pa×s | 328.55 | Joback Calculated Property |
η | 0.0008012 | Pa×s | 366.25 | Joback Calculated Property |
η | 0.0005667 | Pa×s | 403.96 | Joback Calculated Property |
η | 0.0004253 | Pa×s | 441.67 | Joback Calculated Property |
η | 0.0003339 | Pa×s | 479.38 | Joback Calculated Property |
ΔfusH | [13.20; 13.20] | kJ/mol | [299.50; 299.50] | |
ΔfusH | 13.20 | kJ/mol | 299.50 | NIST |
ΔfusH | 13.20 | kJ/mol | 299.50 | NIST |
ΔvapH | 46.80 | kJ/mol | 380.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [366.00; 366.20] | K | [1.30; 1.30] | |
Tboilr | 366.20 | K | 1.30 | NIST |
Tboilr | 366.00 | K | 1.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [354.99; 519.29] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.38427e+01 | |||
Coefficient B | -3.78202e+03 | |||
Coefficient C | -7.59750e+01 | |||
Temperature range, min. | 354.99 | |||
Temperature range, max. | 519.29 | |||
Pvap | 1.33 | kPa | 354.99 | Calculated Property |
Pvap | 3.07 | kPa | 373.25 | Calculated Property |
Pvap | 6.40 | kPa | 391.50 | Calculated Property |
Pvap | 12.33 | kPa | 409.76 | Calculated Property |
Pvap | 22.19 | kPa | 428.01 | Calculated Property |
Pvap | 37.68 | kPa | 446.27 | Calculated Property |
Pvap | 60.88 | kPa | 464.52 | Calculated Property |
Pvap | 94.23 | kPa | 482.78 | Calculated Property |
Pvap | 140.48 | kPa | 501.03 | Calculated Property |
Pvap | 202.64 | kPa | 519.29 | Calculated Property |
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