Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3130 | KDB | |
ΔcH°liquid | -6121.90 ± 1.60 | kJ/mol | NIST |
ΔfG° | 34.12 | kJ/mol | KDB |
Δc,grossH | 6121.95 | kJ/mol | KDB |
Δc,netH | 5681.830 | kJ/mol | KDB |
ΔfH°gas | -236.40 | kJ/mol | KDB |
ΔfusH° | 4.61 | kJ/mol | Joback Calculated Property |
ΔvapH° | 41.80 | kJ/mol | NIST |
log10WS | -2.86 | Crippen Calculated Property | |
logPoct/wat | 3.325 | Crippen Calculated Property | |
McVol | 137.670 | ml/mol | McGowan Calculated Property |
Pc | [2716.00; 2720.00] | kPa | |
Pc | 2720.00 | kPa | KDB |
Pc | 2720.00 ± 40.00 | kPa | NIST |
Pc | 2716.00 ± 20.00 | kPa | NIST |
Inp | [851.00; 870.00] | ||
Inp | 861.00 | NIST | |
Inp | 852.00 | NIST | |
Inp | 857.90 | NIST | |
Inp | 864.20 | NIST | |
Inp | 854.50 | NIST | |
Inp | 854.70 | NIST | |
Inp | 861.00 | NIST | |
Inp | 861.10 | NIST | |
Inp | 860.90 | NIST | |
Inp | 858.00 | NIST | |
Inp | 863.00 | NIST | |
Inp | 858.90 | NIST | |
Inp | 861.00 | NIST | |
Inp | 854.00 | NIST | |
Inp | 859.00 | NIST | |
Inp | 865.00 | NIST | |
Inp | Outlier 870.00 | NIST | |
Inp | 851.00 | NIST | |
Inp | 856.00 | NIST | |
Inp | 858.00 | NIST | |
Inp | 861.00 | NIST | |
Inp | 861.00 | NIST | |
Inp | 858.00 | NIST | |
Inp | 851.00 | NIST | |
Tboil | [405.00; 414.72] | K | |
Tboil | 414.72 | K | KDB |
Tboil | 414.70 | K | NIST |
Tboil | 414.70 ± 0.03 | K | NIST |
Tboil | 414.55 ± 0.40 | K | NIST |
Tboil | 414.35 ± 0.50 | K | NIST |
Tboil | 414.69 ± 0.10 | K | NIST |
Tboil | 414.55 ± 0.50 | K | NIST |
Tboil | 414.69 ± 0.20 | K | NIST |
Tboil | Outlier 405.00 ± 1.50 | K | NIST |
Tc | [607.50; 607.55] | K | |
Tc | 607.50 | K | KDB |
Tc | 607.50 ± 0.50 | K | NIST |
Tc | 607.55 ± 0.20 | K | NIST |
Tfus | [171.00; 171.02] | K | |
Tfus | 171.00 | K | KDB |
Tfus | 171.01 ± 0.10 | K | NIST |
Tfus | 171.02 ± 0.02 | K | NIST |
Tfus | 171.02 ± 0.05 | K | NIST |
Vc | 0.516 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [273.79; 361.94] | J/mol×K | [401.21; 582.85] | |
Cp,gas | 273.79 | J/mol×K | 401.21 | Joback Calculated Property |
Cp,gas | 290.35 | J/mol×K | 431.48 | Joback Calculated Property |
Cp,gas | 306.13 | J/mol×K | 461.76 | Joback Calculated Property |
Cp,gas | 321.15 | J/mol×K | 492.03 | Joback Calculated Property |
Cp,gas | 335.44 | J/mol×K | 522.31 | Joback Calculated Property |
Cp,gas | 349.03 | J/mol×K | 552.58 | Joback Calculated Property |
Cp,gas | 361.94 | J/mol×K | 582.85 | Joback Calculated Property |
η | [0.0002468; 0.0512340] | Pa×s | [163.61; 401.21] | |
η | 0.0512340 | Pa×s | 163.61 | Joback Calculated Property |
η | 0.0088523 | Pa×s | 203.21 | Joback Calculated Property |
η | 0.0027119 | Pa×s | 242.81 | Joback Calculated Property |
η | 0.0011576 | Pa×s | 282.41 | Joback Calculated Property |
η | 0.0006093 | Pa×s | 322.01 | Joback Calculated Property |
η | 0.0003691 | Pa×s | 361.61 | Joback Calculated Property |
η | 0.0002468 | Pa×s | 401.21 | Joback Calculated Property |
ΔvapH | [34.94; 39.30] | kJ/mol | [373.50; 414.70] | |
ΔvapH | 39.30 | kJ/mol | 373.50 | NIST |
ΔvapH | 34.94 | kJ/mol | 414.70 | KDB |
n0 | 1.42003 | 298.15 | KDB | |
ρl | 755.00 | kg/m3 | 293.00 | KDB |
γ | 0.02 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [301.17; 443.29] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40767e+01 | |||
Coefficient B | -3.41898e+03 | |||
Coefficient C | -5.32210e+01 | |||
Temperature range, min. | 301.17 | |||
Temperature range, max. | 443.29 | |||
Pvap | 1.33 | kPa | 301.17 | Calculated Property |
Pvap | 3.04 | kPa | 316.96 | Calculated Property |
Pvap | 6.33 | kPa | 332.75 | Calculated Property |
Pvap | 12.18 | kPa | 348.54 | Calculated Property |
Pvap | 21.91 | kPa | 364.33 | Calculated Property |
Pvap | 37.26 | kPa | 380.13 | Calculated Property |
Pvap | 60.34 | kPa | 395.92 | Calculated Property |
Pvap | 93.63 | kPa | 411.71 | Calculated Property |
Pvap | 140.02 | kPa | 427.50 | Calculated Property |
Pvap | 202.67 | kPa | 443.29 | Calculated Property |
Pvap | [1.32; 2717.64] | kPa | [300.15; 607.50] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.24133e+01 | |||
Coefficient B | -7.67624e+03 | |||
Coefficient C | -1.00145e+01 | |||
Coefficient D | 6.27762e-06 | |||
Temperature range, min. | 300.15 | |||
Temperature range, max. | 607.50 | |||
Pvap | 1.32 | kPa | 300.15 | Calculated Property |
Pvap | 7.01 | kPa | 334.30 | Calculated Property |
Pvap | 25.86 | kPa | 368.45 | Calculated Property |
Pvap | 73.51 | kPa | 402.60 | Calculated Property |
Pvap | 172.93 | kPa | 436.75 | Calculated Property |
Pvap | 353.58 | kPa | 470.90 | Calculated Property |
Pvap | 650.96 | kPa | 505.05 | Calculated Property |
Pvap | 1107.31 | kPa | 539.20 | Calculated Property |
Pvap | 1774.29 | kPa | 573.35 | Calculated Property |
Pvap | 2717.64 | kPa | 607.50 | Calculated Property |
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