Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4970 | KDB | |
ΔcH°liquid | -4655.50 | kJ/mol | NIST |
ΔfG° | 176.08 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 38.93 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | -88.70 | kJ/mol | NIST |
ΔfusH° | 14.94 | kJ/mol | Joback Calculated Property |
ΔvapH° | 47.64 | kJ/mol | Joback Calculated Property |
IE | [7.40; 7.65] | eV | |
IE | 7.40 ± 0.10 | eV | NIST |
IE | 7.65 ± 0.05 | eV | NIST |
log10WS | -2.06 | Crippen Calculated Property | |
logPoct/wat | 1.886 | Crippen Calculated Property | |
McVol | 109.800 | ml/mol | McGowan Calculated Property |
Pc | 4000.00 | kPa | KDB |
Inp | [196.10; 1167.01] | ||
Inp | 1167.01 | NIST | |
Inp | 1145.70 | NIST | |
Inp | 1160.70 | NIST | |
Inp | 1123.10 | NIST | |
Inp | 1137.70 | NIST | |
Inp | 1167.00 | NIST | |
Inp | 1131.00 | NIST | |
Inp | 1136.00 | NIST | |
Inp | Outlier 196.10 | NIST | |
Inp | Outlier 196.10 | NIST | |
Inp | 1123.10 | NIST | |
I | [1960.00; 1976.00] | ||
I | 1960.00 | NIST | |
I | 1976.00 | NIST | |
I | 1960.00 | NIST | |
Tboil | [487.45; 491.20] | K | |
Tboil | 490.27 | K | KDB |
Tboil | 491.20 | K | NIST |
Tboil | 487.45 ± 0.50 | K | NIST |
Tc | 714.00 | K | KDB |
Tfus | [257.25; 289.00] | K | |
Tfus | Outlier 289.00 | K | KDB |
Tfus | 257.25 ± 1.00 | K | NIST |
Tfus | 259.35 ± 0.35 | K | NIST |
Tfus | 259.32 ± 0.80 | K | NIST |
Tfus | 261.05 ± 0.30 | K | NIST |
Tfus | 258.90 ± 1.00 | K | NIST |
Vc | 0.405 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [228.80; 292.16] | J/mol×K | [491.61; 717.26] | |
Cp,gas | 228.80 | J/mol×K | 491.61 | Joback Calculated Property |
Cp,gas | 240.98 | J/mol×K | 529.22 | Joback Calculated Property |
Cp,gas | 252.48 | J/mol×K | 566.83 | Joback Calculated Property |
Cp,gas | 263.33 | J/mol×K | 604.43 | Joback Calculated Property |
Cp,gas | 273.54 | J/mol×K | 642.04 | Joback Calculated Property |
Cp,gas | 283.15 | J/mol×K | 679.65 | Joback Calculated Property |
Cp,gas | 292.16 | J/mol×K | 717.26 | Joback Calculated Property |
ΔvapH | [55.50; 61.30] | kJ/mol | [317.00; 434.00] | |
ΔvapH | 61.30 ± 0.60 | kJ/mol | 317.00 | NIST |
ΔvapH | 56.90 | kJ/mol | 405.50 | NIST |
ΔvapH | 55.50 | kJ/mol | 434.00 | NIST |
ρl | 969.46 | kg/m3 | 293.10 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [364.72; 522.53] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.44845e+01 | |||
Coefficient B | -4.09072e+03 | |||
Coefficient C | -7.65780e+01 | |||
Temperature range, min. | 364.72 | |||
Temperature range, max. | 522.53 | |||
Pvap | 1.33 | kPa | 364.72 | Calculated Property |
Pvap | 3.01 | kPa | 382.25 | Calculated Property |
Pvap | 6.22 | kPa | 399.79 | Calculated Property |
Pvap | 11.93 | kPa | 417.32 | Calculated Property |
Pvap | 21.47 | kPa | 434.86 | Calculated Property |
Pvap | 36.58 | kPa | 452.39 | Calculated Property |
Pvap | 59.43 | kPa | 469.93 | Calculated Property |
Pvap | 92.62 | kPa | 487.46 | Calculated Property |
Pvap | 139.22 | kPa | 505.00 | Calculated Property |
Pvap | 202.65 | kPa | 522.53 | Calculated Property |
Pvap | [0.01; 65.58] | kPa | [294.15; 473.15] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.53270e+02 | |||
Coefficient B | -1.27469e+04 | |||
Coefficient C | -2.03281e+01 | |||
Coefficient D | 1.36820e-05 | |||
Temperature range, min. | 294.15 | |||
Temperature range, max. | 473.15 | |||
Pvap | 0.01 | kPa | 294.15 | Calculated Property |
Pvap | 0.06 | kPa | 314.04 | Calculated Property |
Pvap | 0.22 | kPa | 333.93 | Calculated Property |
Pvap | 0.71 | kPa | 353.82 | Calculated Property |
Pvap | 1.93 | kPa | 373.71 | Calculated Property |
Pvap | 4.65 | kPa | 393.59 | Calculated Property |
Pvap | 10.09 | kPa | 413.48 | Calculated Property |
Pvap | 20.13 | kPa | 433.37 | Calculated Property |
Pvap | 37.41 | kPa | 453.26 | Calculated Property |
Pvap | 65.58 | kPa | 473.15 | Calculated Property |
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