Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1890 | KDB | |
PAff | 784.40 | kJ/mol | NIST |
BasG | 753.60 | kJ/mol | NIST |
ΔcH°gas | -2588.20 ± 1.50 | kJ/mol | NIST |
ΔfG° | 69.12 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 157.00 ± 2.00 | kJ/mol | NIST |
ΔfusH° | 2.30 | kJ/mol | Joback Calculated Property |
ΔvapH° | 25.18 | kJ/mol | Joback Calculated Property |
IE | [9.43; 9.59] | eV | |
IE | 9.43 ± 0.02 | eV | NIST |
IE | 9.43 ± 0.02 | eV | NIST |
IE | 9.43 | eV | NIST |
IE | Outlier 9.59 | eV | NIST |
IE | 9.43 ± 0.03 | eV | NIST |
IE | 9.43 | eV | NIST |
log10WS | -1.25 | Crippen Calculated Property | |
logPoct/wat | 1.336 | Crippen Calculated Property | |
McVol | 52.060 | ml/mol | McGowan Calculated Property |
Pc | 5270.00 | kPa | KDB |
Inp | [432.00; 434.00] | ||
Inp | 432.00 | NIST | |
Inp | 433.00 | NIST | |
Inp | 433.00 | NIST | |
Inp | 434.00 | NIST | |
Tboil | [275.20; 275.80] | K | |
Tboil | 275.80 | K | KDB |
Tboil | 275.20 | K | NIST |
Tc | 446.30 | K | KDB |
Tfus | 154.00 | K | KDB |
Vc | 0.196 | m3/kmol | KDB |
Zc | 0.2776480 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [62.86; 107.27] | J/mol×K | [305.76; 494.92] | |
Cp,gas | 62.86 | J/mol×K | 305.76 | Joback Calculated Property |
Cp,gas | 71.52 | J/mol×K | 337.29 | Joback Calculated Property |
Cp,gas | 79.64 | J/mol×K | 368.81 | Joback Calculated Property |
Cp,gas | 87.25 | J/mol×K | 400.34 | Joback Calculated Property |
Cp,gas | 94.37 | J/mol×K | 431.86 | Joback Calculated Property |
Cp,gas | 101.04 | J/mol×K | 463.39 | Joback Calculated Property |
Cp,gas | 107.27 | J/mol×K | 494.92 | Joback Calculated Property |
η | [0.0002125; 0.0011908] | Pa×s | [154.26; 305.76] | |
η | 0.0011908 | Pa×s | 154.26 | Joback Calculated Property |
η | 0.0007300 | Pa×s | 179.51 | Joback Calculated Property |
η | 0.0005050 | Pa×s | 204.76 | Joback Calculated Property |
η | 0.0003788 | Pa×s | 230.01 | Joback Calculated Property |
η | 0.0003007 | Pa×s | 255.26 | Joback Calculated Property |
η | 0.0002489 | Pa×s | 280.51 | Joback Calculated Property |
η | 0.0002125 | Pa×s | 305.76 | Joback Calculated Property |
ΔvapH | [24.60; 25.81] | kJ/mol | [235.50; 275.80] | |
ΔvapH | 24.60 | kJ/mol | 235.50 | NIST |
ΔvapH | 24.70 | kJ/mol | 240.50 | NIST |
ΔvapH | 25.81 | kJ/mol | 275.80 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.18; 207.71] | kPa | [196.15; 295.08] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.45824e+01 | |||
Coefficient B | -2.55142e+03 | |||
Coefficient C | -1.91380e+01 | |||
Temperature range, min. | 196.15 | |||
Temperature range, max. | 295.08 | |||
Pvap | 1.18 | kPa | 196.15 | Calculated Property |
Pvap | 2.75 | kPa | 207.14 | Calculated Property |
Pvap | 5.82 | kPa | 218.13 | Calculated Property |
Pvap | 11.38 | kPa | 229.13 | Calculated Property |
Pvap | 20.83 | kPa | 240.12 | Calculated Property |
Pvap | 36.00 | kPa | 251.11 | Calculated Property |
Pvap | 59.22 | kPa | 262.10 | Calculated Property |
Pvap | 93.29 | kPa | 273.10 | Calculated Property |
Pvap | 141.54 | kPa | 284.09 | Calculated Property |
Pvap | 207.71 | kPa | 295.08 | Calculated Property |
Pvap | [1.20; 5345.77] | kPa | [196.15; 446.33] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 5.11908e+01 | |||
Coefficient B | -4.13962e+03 | |||
Coefficient C | -5.72351e+00 | |||
Coefficient D | 7.96917e-06 | |||
Temperature range, min. | 196.15 | |||
Temperature range, max. | 446.33 | |||
Pvap | 1.20 | kPa | 196.15 | Calculated Property |
Pvap | 8.44 | kPa | 223.95 | Calculated Property |
Pvap | 36.97 | kPa | 251.75 | Calculated Property |
Pvap | 117.17 | kPa | 279.54 | Calculated Property |
Pvap | 296.00 | kPa | 307.34 | Calculated Property |
Pvap | 635.43 | kPa | 335.14 | Calculated Property |
Pvap | 1210.67 | kPa | 362.94 | Calculated Property |
Pvap | 2111.04 | kPa | 390.73 | Calculated Property |
Pvap | 3444.43 | kPa | 418.53 | Calculated Property |
Pvap | 5345.77 | kPa | 446.33 | Calculated Property |
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