Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2730 | KDB | |
AP | 318.150 | K | KDB |
ΔcH°liquid | -4583.30 ± 1.00 | kJ/mol | NIST |
ΔfG° | 39.06 | kJ/mol | KDB |
Δc,grossH | 4583.32 | kJ/mol | KDB |
Δc,netH | 4275.253 | kJ/mol | KDB |
ΔfH°gas | [-138.40; -138.30] | kJ/mol | |
ΔfH°gas | -138.40 | kJ/mol | KDB |
ΔfH°gas | -138.30 ± 1.20 | kJ/mol | NIST |
ΔfH°liquid | -172.10 ± 1.10 | kJ/mol | NIST |
ΔfusH° | 1.52 | kJ/mol | Joback Calculated Property |
ΔvapH° | [33.80; 33.80] | kJ/mol | |
ΔvapH° | 33.80 | kJ/mol | NIST |
ΔvapH° | 33.80 | kJ/mol | NIST |
IE | 9.46 ± 0.05 | eV | NIST |
log10WS | -2.41 | Crippen Calculated Property | |
logPoct/wat | 2.587 | Crippen Calculated Property | |
McVol | 98.630 | ml/mol | McGowan Calculated Property |
Pc | 3440.00 | kPa | KDB |
Inp | [662.30; 684.00] | ||
Inp | 665.00 | NIST | |
Inp | 675.50 | NIST | |
Inp | 669.00 | NIST | |
Inp | 675.90 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.80 | NIST | |
Inp | 676.10 | NIST | |
Inp | 675.80 | NIST | |
Inp | 673.30 | NIST | |
Inp | 677.40 | NIST | |
Inp | 671.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 672.40 | NIST | |
Inp | 676.50 | NIST | |
Inp | 675.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 671.70 | NIST | |
Inp | 673.60 | NIST | |
Inp | 675.40 | NIST | |
Inp | 676.90 | NIST | |
Inp | 669.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 675.90 | NIST | |
Inp | 676.10 | NIST | |
Inp | 674.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 673.20 | NIST | |
Inp | 673.20 | NIST | |
Inp | Outlier 684.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 680.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | Outlier 683.00 | NIST | |
Inp | 669.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 671.10 | NIST | |
Inp | 669.70 | NIST | |
Inp | Outlier 662.30 | NIST | |
Inp | Outlier 663.04 | NIST | |
Inp | 668.50 | NIST | |
Inp | 665.52 | NIST | |
Inp | 665.59 | NIST | |
Inp | 665.48 | NIST | |
Inp | 665.63 | NIST | |
Inp | 666.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 666.00 | NIST | |
Inp | 670.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 669.00 | NIST | |
Inp | 669.00 | NIST | |
Inp | Outlier 683.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 665.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 669.70 | NIST | |
Inp | 665.59 | NIST | |
Inp | 669.00 | NIST | |
Inp | 665.00 | NIST | |
Inp | 676.80 | NIST | |
Inp | 671.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 675.40 | NIST | |
Inp | 674.00 | NIST | |
Inp | Outlier 684.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 677.00 | NIST | |
S°gas | 359.28 | J/mol×K | NIST |
S°liquid | 265.01 | J/mol×K | NIST |
Tboil | [360.00; 361.35] | K | |
Tboil | 361.00 | K | KDB |
Tboil | 360.70 | K | NIST |
Tboil | 361.00 ± 0.20 | K | NIST |
Tboil | 361.05 ± 0.30 | K | NIST |
Tboil | 360.99 ± 0.02 | K | NIST |
Tboil | 361.35 ± 0.30 | K | NIST |
Tboil | 360.65 ± 0.20 | K | NIST |
Tboil | 361.20 ± 0.30 | K | NIST |
Tboil | 360.65 ± 0.50 | K | NIST |
Tboil | 360.70 ± 0.30 | K | NIST |
Tboil | 361.30 ± 0.60 | K | NIST |
Tboil | Outlier 360.00 ± 1.00 | K | NIST |
Tc | 547.00 | K | KDB |
Tfus | [196.00; 203.42] | K | |
Tfus | 203.40 | K | KDB |
Tfus | 203.27 ± 0.20 | K | NIST |
Tfus | 203.24 ± 0.20 | K | NIST |
Tfus | 203.42 ± 0.06 | K | NIST |
Tfus | 203.34 ± 0.08 | K | NIST |
Tfus | 203.34 ± 0.07 | K | NIST |
Tfus | 203.35 ± 0.05 | K | NIST |
Tfus | 203.24 ± 0.30 | K | NIST |
Tfus | 203.24 ± 0.30 | K | NIST |
Tfus | 203.42 ± 0.10 | K | NIST |
Tfus | 197.28 ± 4.00 | K | NIST |
Tfus | 203.16 ± 1.00 | K | NIST |
Tfus | 196.75 ± 0.40 | K | NIST |
Tfus | 196.75 ± 5.00 | K | NIST |
Tfus | 196.00 ± 5.00 | K | NIST |
Ttriple | [203.67; 203.68] | K | |
Ttriple | 203.68 ± 0.05 | K | NIST |
Ttriple | 203.67 ± 0.02 | K | NIST |
Ttriple | 203.67 ± 0.03 | K | NIST |
Ttriple | 203.67 ± 0.02 | K | NIST |
Vc | 0.360 | m3/kmol | KDB |
Zc | 0.2722930 | KDB | |
Zra | 0.28 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [174.34; 256.90] | J/mol×K | [375.08; 578.27] | |
Cp,gas | 174.34 | J/mol×K | 375.08 | Joback Calculated Property |
Cp,gas | 190.73 | J/mol×K | 408.95 | Joback Calculated Property |
Cp,gas | 205.94 | J/mol×K | 442.81 | Joback Calculated Property |
Cp,gas | 220.07 | J/mol×K | 476.68 | Joback Calculated Property |
Cp,gas | 233.21 | J/mol×K | 510.54 | Joback Calculated Property |
Cp,gas | 245.45 | J/mol×K | 544.41 | Joback Calculated Property |
Cp,gas | 256.90 | J/mol×K | 578.27 | Joback Calculated Property |
Cp,liquid | 187.36 | J/mol×K | 299.81 | NIST |
ΔfusH | [1.09; 6.49] | kJ/mol | [146.80; 203.70] | |
ΔfusH | 6.49 | kJ/mol | 146.80 | NIST |
ΔfusH | 1.09 | kJ/mol | 203.70 | NIST |
ΔfusH | 1.09 | kJ/mol | 203.70 | NIST |
ΔvapH | [30.29; 34.00] | kJ/mol | [323.50; 361.00] | |
ΔvapH | 34.00 | kJ/mol | 323.50 | NIST |
ΔvapH | 33.80 | kJ/mol | 325.50 | NIST |
ΔvapH | 30.29 | kJ/mol | 361.00 | KDB |
n0 | 1.41091 | 298.15 | KDB | |
ρl | 759.00 | kg/m3 | 289.00 | KDB |
ΔfusS | [5.34; 44.18] | J/mol×K | [146.80; 203.70] | |
ΔfusS | 44.18 | J/mol×K | 146.80 | NIST |
ΔfusS | 5.34 | J/mol×K | 203.70 | NIST |
γ | 0.02 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [261.51; 385.78] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42167e+01 | |||
Coefficient B | -3.06828e+03 | |||
Coefficient C | -4.12340e+01 | |||
Temperature range, min. | 261.51 | |||
Temperature range, max. | 385.78 | |||
Pvap | 1.33 | kPa | 261.51 | Calculated Property |
Pvap | 3.03 | kPa | 275.32 | Calculated Property |
Pvap | 6.29 | kPa | 289.13 | Calculated Property |
Pvap | 12.09 | kPa | 302.93 | Calculated Property |
Pvap | 21.76 | kPa | 316.74 | Calculated Property |
Pvap | 37.02 | kPa | 330.55 | Calculated Property |
Pvap | 60.01 | kPa | 344.36 | Calculated Property |
Pvap | 93.27 | kPa | 358.16 | Calculated Property |
Pvap | 139.72 | kPa | 371.97 | Calculated Property |
Pvap | 202.64 | kPa | 385.78 | Calculated Property |
Pvap | [9.19e-03; 3463.34] | kPa | [203.36; 547.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.87017e+01 | |||
Coefficient B | -6.92875e+03 | |||
Coefficient C | -1.12381e+01 | |||
Coefficient D | 9.90988e-06 | |||
Temperature range, min. | 203.36 | |||
Temperature range, max. | 547.00 | |||
Pvap | 9.19e-03 | kPa | 203.36 | Calculated Property |
Pvap | 0.34 | kPa | 241.54 | Calculated Property |
Pvap | 4.03 | kPa | 279.72 | Calculated Property |
Pvap | 23.50 | kPa | 317.91 | Calculated Property |
Pvap | 87.75 | kPa | 356.09 | Calculated Property |
Pvap | 244.22 | kPa | 394.27 | Calculated Property |
Pvap | 557.63 | kPa | 432.45 | Calculated Property |
Pvap | 1112.54 | kPa | 470.64 | Calculated Property |
Pvap | 2024.61 | kPa | 508.82 | Calculated Property |
Pvap | 3463.34 | kPa | 547.00 | Calculated Property |
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