Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4120 | KDB | |
PAff | 845.60 | kJ/mol | NIST |
BasG | 816.50 | kJ/mol | NIST |
ΔcH°liquid | [-5839.60; -5815.30] | kJ/mol | |
ΔcH°liquid | -5839.60 ± 1.10 | kJ/mol | NIST |
ΔcH°liquid | -5837.50 ± 3.00 | kJ/mol | NIST |
ΔcH°liquid | -5815.30 ± 5.90 | kJ/mol | NIST |
EA | 0.11 ± 0.01 | eV | NIST |
ΔfG° | 118.80 | kJ/mol | KDB |
ΔfH°gas | [-46.50; -43.20] | kJ/mol | |
ΔfH°gas | -44.84 | kJ/mol | KDB |
ΔfH°gas | -43.20 ± 1.30 | kJ/mol | NIST |
ΔfH°gas | -44.40 ± 1.20 | kJ/mol | NIST |
ΔfH°gas | -46.50 ± 3.00 | kJ/mol | NIST |
ΔfH°liquid | [-98.50; -96.40] | kJ/mol | |
ΔfH°liquid | -96.40 ± 1.20 | kJ/mol | NIST |
ΔfH°liquid | -98.50 ± 3.00 | kJ/mol | NIST |
ΔfusH° | 14.53 | kJ/mol | Joback Calculated Property |
ΔvapH° | [51.98; 55.80] | kJ/mol | |
ΔvapH° | 53.20 | kJ/mol | NIST |
ΔvapH° | 51.98 ± 0.17 | kJ/mol | NIST |
ΔvapH° | 52.00 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 55.80 | kJ/mol | NIST |
IE | [8.07; 8.47] | eV | |
IE | 8.47 ± 0.05 | eV | NIST |
IE | 8.07 | eV | NIST |
IE | 8.30 ± 0.03 | eV | NIST |
log10WS | -3.37 | Crippen Calculated Property | |
logPoct/wat | 2.920 | Crippen Calculated Property | |
McVol | 128.000 | ml/mol | McGowan Calculated Property |
Pc | 2870.00 | kPa | KDB |
Inp | [1096.00; 1154.00] | ||
Inp | 1129.00 | NIST | |
Inp | 1137.00 | NIST | |
Inp | 1113.50 | NIST | |
Inp | 1121.30 | NIST | |
Inp | 1096.00 | NIST | |
Inp | 1096.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1110.00 | NIST | |
Inp | 1099.50 | NIST | |
Inp | 1104.00 | NIST | |
Inp | 1110.00 | NIST | |
Inp | 1118.00 | NIST | |
Inp | 1125.00 | NIST | |
Inp | 1108.40 | NIST | |
Inp | 1111.40 | NIST | |
Inp | 1110.50 | NIST | |
Inp | 1117.50 | NIST | |
Inp | 1125.00 | NIST | |
Inp | 1108.00 | NIST | |
Inp | 1108.40 | NIST | |
Inp | 1111.40 | NIST | |
Inp | 1113.00 | NIST | |
Inp | 1105.05 | NIST | |
Inp | 1137.00 | NIST | |
Inp | 1140.00 | NIST | |
Inp | Outlier 1145.00 | NIST | |
Inp | 1139.00 | NIST | |
Inp | Outlier 1144.00 | NIST | |
Inp | Outlier 1149.00 | NIST | |
Inp | Outlier 1150.00 | NIST | |
Inp | 1097.70 | NIST | |
Inp | Outlier 1151.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1118.10 | NIST | |
Inp | 1103.00 | NIST | |
Inp | Outlier 1154.00 | NIST | |
Inp | 1108.80 | NIST | |
Inp | 1112.00 | NIST | |
Inp | 1133.00 | NIST | |
Inp | 1105.00 | NIST | |
Inp | 1113.00 | NIST | |
Inp | 1113.00 | NIST | |
Inp | 1104.26 | NIST | |
Inp | 1104.97 | NIST | |
Inp | 1104.00 | NIST | |
Inp | 1102.00 | NIST | |
Inp | 1102.00 | NIST | |
Inp | 1103.00 | NIST | |
Inp | 1112.85 | NIST | |
Inp | 1110.00 | NIST | |
Inp | 1110.00 | NIST | |
Inp | 1117.00 | NIST | |
Inp | 1118.00 | NIST | |
Inp | 1122.00 | NIST | |
Inp | 1116.00 | NIST | |
Inp | 1107.00 | NIST | |
Inp | 1116.00 | NIST | |
Inp | 1122.00 | NIST | |
Inp | 1113.00 | NIST | |
Inp | 1114.00 | NIST | |
Inp | 1115.00 | NIST | |
Inp | 1113.00 | NIST | |
Inp | 1119.00 | NIST | |
Inp | 1121.00 | NIST | |
Inp | 1115.00 | NIST | |
Inp | 1104.00 | NIST | |
Inp | 1108.00 | NIST | |
Inp | 1103.00 | NIST | |
Inp | 1127.90 | NIST | |
Inp | 1116.00 | NIST | |
Inp | 1100.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1137.00 | NIST | |
Inp | 1100.00 | NIST | |
Inp | 1107.00 | NIST | |
Inp | 1104.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1106.00 | NIST | |
Inp | 1114.00 | NIST | |
Inp | 1115.00 | NIST | |
Inp | 1116.00 | NIST | |
Inp | 1129.00 | NIST | |
Inp | 1096.00 | NIST | |
Inp | 1110.00 | NIST | |
Inp | 1125.00 | NIST | |
Inp | 1105.05 | NIST | |
Inp | Outlier 1144.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1112.85 | NIST | |
Inp | 1108.80 | NIST | |
I | [1395.00; 1474.50] | ||
I | 1456.30 | NIST | |
I | 1474.50 | NIST | |
I | 1395.00 | NIST | |
I | 1416.50 | NIST | |
I | 1410.50 | NIST | |
I | 1455.80 | NIST | |
I | 1430.00 | NIST | |
I | 1447.00 | NIST | |
I | 1441.00 | NIST | |
I | 1443.00 | NIST | |
I | 1422.00 | NIST | |
I | 1416.00 | NIST | |
I | 1422.00 | NIST | |
I | 1456.30 | NIST | |
I | 1455.80 | NIST | |
S°liquid | 310.00 | J/mol×K | NIST |
Tboil | 471.30 | K | KDB |
Tc | 679.00 | K | KDB |
Tfus | [245.78; 249.95] | K | |
Tfus | 249.00 | K | KDB |
Tfus | 249.42 ± 0.03 | K | NIST |
Tfus | 249.45 ± 0.02 | K | NIST |
Tfus | 249.46 ± 0.01 | K | NIST |
Tfus | 249.34 ± 0.20 | K | NIST |
Tfus | 249.38 ± 0.20 | K | NIST |
Tfus | 249.04 ± 0.30 | K | NIST |
Tfus | 248.94 ± 0.40 | K | NIST |
Tfus | 249.95 ± 0.20 | K | NIST |
Tfus | 249.03 ± 0.50 | K | NIST |
Tfus | 249.30 ± 0.30 | K | NIST |
Tfus | Outlier 245.78 ± 0.50 | K | NIST |
Tfus | 249.20 ± 1.00 | K | NIST |
Tfus | 249.00 ± 0.20 | K | NIST |
Ttriple | 248.60 ± 0.30 | K | NIST |
Vc | 0.487 | m3/kmol | KDB |
Zc | 0.2478280 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [258.77; 332.37] | J/mol×K | [469.82; 678.39] | |
Cp,gas | 258.77 | J/mol×K | 469.82 | Joback Calculated Property |
Cp,gas | 272.57 | J/mol×K | 504.58 | Joback Calculated Property |
Cp,gas | 285.73 | J/mol×K | 539.34 | Joback Calculated Property |
Cp,gas | 298.28 | J/mol×K | 574.11 | Joback Calculated Property |
Cp,gas | 310.23 | J/mol×K | 608.87 | Joback Calculated Property |
Cp,gas | 321.58 | J/mol×K | 643.63 | Joback Calculated Property |
Cp,gas | 332.37 | J/mol×K | 678.39 | Joback Calculated Property |
Cp,liquid | 240.20 | J/mol×K | 297.10 | NIST |
η | [0.0001983; 0.0012469] | Pa×s | [266.44; 469.82] | |
η | 0.0012469 | Pa×s | 266.44 | Joback Calculated Property |
η | 0.0007720 | Pa×s | 300.34 | Joback Calculated Property |
η | 0.0005268 | Pa×s | 334.23 | Joback Calculated Property |
η | 0.0003857 | Pa×s | 368.13 | Joback Calculated Property |
η | 0.0002977 | Pa×s | 402.03 | Joback Calculated Property |
η | 0.0002391 | Pa×s | 435.92 | Joback Calculated Property |
η | 0.0001983 | Pa×s | 469.82 | Joback Calculated Property |
ΔfusH | [12.93; 12.93] | kJ/mol | [248.60; 248.60] | |
ΔfusH | 12.93 | kJ/mol | 248.60 | NIST |
ΔfusH | 12.93 | kJ/mol | 248.60 | NIST |
ΔvapH | [43.81; 58.90] | kJ/mol | [392.50; 471.30] | |
ΔvapH | 58.90 | kJ/mol | 392.50 | NIST |
ΔvapH | 50.00 | kJ/mol | 425.00 | NIST |
ΔvapH | 43.81 | kJ/mol | 471.30 | KDB |
n0 | 1.51070 | 298.15 | KDB | |
ρl | 890.00 | kg/m3 | 293.00 | KDB |
γ | 0.03 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [346.93; 501.64] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.47275e+01 | |||
Coefficient B | -4.18697e+03 | |||
Coefficient C | -5.69750e+01 | |||
Temperature range, min. | 346.93 | |||
Temperature range, max. | 501.64 | |||
Pvap | 1.33 | kPa | 346.93 | Calculated Property |
Pvap | 2.99 | kPa | 364.12 | Calculated Property |
Pvap | 6.16 | kPa | 381.31 | Calculated Property |
Pvap | 11.80 | kPa | 398.50 | Calculated Property |
Pvap | 21.23 | kPa | 415.69 | Calculated Property |
Pvap | 36.20 | kPa | 432.88 | Calculated Property |
Pvap | 58.92 | kPa | 450.07 | Calculated Property |
Pvap | 92.06 | kPa | 467.26 | Calculated Property |
Pvap | 138.77 | kPa | 484.45 | Calculated Property |
Pvap | 202.65 | kPa | 501.64 | Calculated Property |
Pvap | [8.69e-04; 2905.67] | kPa | [249.46; 679.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.52013e+01 | |||
Coefficient B | -9.20614e+03 | |||
Coefficient C | -1.00776e+01 | |||
Coefficient D | 4.43237e-06 | |||
Temperature range, min. | 249.46 | |||
Temperature range, max. | 679.00 | |||
Pvap | 8.69e-04 | kPa | 249.46 | Calculated Property |
Pvap | 0.06 | kPa | 297.19 | Calculated Property |
Pvap | 1.16 | kPa | 344.91 | Calculated Property |
Pvap | 9.45 | kPa | 392.64 | Calculated Property |
Pvap | 45.01 | kPa | 440.37 | Calculated Property |
Pvap | 149.99 | kPa | 488.09 | Calculated Property |
Pvap | 390.35 | kPa | 535.82 | Calculated Property |
Pvap | 853.35 | kPa | 583.55 | Calculated Property |
Pvap | 1646.90 | kPa | 631.27 | Calculated Property |
Pvap | 2905.67 | kPa | 679.00 | Calculated Property |
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