Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3700 | KDB | |
AP | 345.350 | K | KDB |
ΔcH°liquid | -5468.20 ± 1.30 | kJ/mol | NIST |
ΔfG° | 13.73 | kJ/mol | KDB |
Δc,grossH | 5468.15 | kJ/mol | KDB |
Δc,netH | 5072.012 | kJ/mol | KDB |
ΔfH°gas | [-212.80; -212.60] | kJ/mol | |
ΔfH°gas | -212.80 | kJ/mol | KDB |
ΔfH°gas | -212.60 ± 1.10 | kJ/mol | NIST |
ΔfH°liquid | -252.50 ± 1.10 | kJ/mol | NIST |
ΔfusH° | 12.95 | kJ/mol | Joback Calculated Property |
ΔvapH° | [39.80; 39.88] | kJ/mol | |
ΔvapH° | 39.88 | kJ/mol | NIST |
ΔvapH° | 39.80 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 39.80 | kJ/mol | NIST |
ΔvapH° | 39.80 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 39.83 | kJ/mol | NIST |
log10WS | [-5.16; -5.16] | ||
log10WS | -5.16 | Aq. Sol... | |
log10WS | -5.16 | Estimat... | |
logPoct/wat | 3.223 | Crippen Calculated Property | |
McVol | 123.580 | ml/mol | McGowan Calculated Property |
Pc | [2546.00; 2550.00] | kPa | |
Pc | 2550.00 | kPa | KDB |
Pc | 2550.00 ± 40.00 | kPa | NIST |
Pc | 2546.00 ± 40.53 | kPa | NIST |
ρc | [245.59; 245.59] | kg/m3 | |
ρc | 245.59 ± 4.57 | kg/m3 | NIST |
ρc | 245.59 ± 4.57 | kg/m3 | NIST |
Inp | [762.00; 784.63] | ||
Inp | 773.80 | NIST | |
Inp | 773.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | Outlier 763.50 | NIST | |
Inp | 771.90 | NIST | |
Inp | 776.60 | NIST | |
Inp | 778.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.80 | NIST | |
Inp | 773.30 | NIST | |
Inp | 773.50 | NIST | |
Inp | 773.90 | NIST | |
Inp | 774.10 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 774.20 | NIST | |
Inp | 774.30 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | Outlier 762.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 772.60 | NIST | |
Inp | 773.00 | NIST | |
Inp | 772.80 | NIST | |
Inp | 773.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 775.11 | NIST | |
Inp | 775.75 | NIST | |
Inp | 776.18 | NIST | |
Inp | 774.38 | NIST | |
Inp | 774.76 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 770.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.20 | NIST | |
Inp | 775.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 770.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 773.50 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 769.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 770.00 | NIST | |
Inp | 769.00 | NIST | |
Inp | 769.00 | NIST | |
Inp | 771.70 | NIST | |
Inp | 776.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | Outlier 783.00 | NIST | |
Inp | 774.30 | NIST | |
Inp | 769.27 | NIST | |
Inp | 769.73 | NIST | |
Inp | Outlier 764.58 | NIST | |
Inp | 770.80 | NIST | |
Inp | 772.10 | NIST | |
Inp | 768.70 | NIST | |
Inp | 769.00 | NIST | |
Inp | 770.31 | NIST | |
Inp | 771.67 | NIST | |
Inp | 770.68 | NIST | |
Inp | 770.98 | NIST | |
Inp | 771.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 773.70 | NIST | |
Inp | 773.30 | NIST | |
Inp | 772.90 | NIST | |
Inp | 773.42 | NIST | |
Inp | 773.79 | NIST | |
Inp | 774.07 | NIST | |
Inp | 773.02 | NIST | |
Inp | 773.47 | NIST | |
Inp | 773.76 | NIST | |
Inp | 769.00 | NIST | |
Inp | Outlier 767.00 | NIST | |
Inp | Outlier 784.63 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | Outlier 765.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 772.20 | NIST | |
Inp | 773.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 770.00 | NIST | |
Inp | 777.00 | NIST | |
Inp | Outlier 767.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | Outlier 766.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 769.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 777.00 | NIST | |
Inp | Outlier 779.00 | NIST | |
Inp | 777.00 | NIST | |
Inp | Outlier 779.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | Outlier 764.58 | NIST | |
Inp | 770.31 | NIST | |
Inp | 771.00 | NIST | |
Inp | 773.79 | NIST | |
Inp | 769.00 | NIST | |
I | [764.00; 764.00] | ||
I | 764.00 | NIST | |
I | 764.00 | NIST | |
S°gas | 465.89 ± 0.84 | J/mol×K | NIST |
S°liquid | 362.60 | J/mol×K | NIST |
Tboil | 392.09 | K | KDB |
Tc | [563.60; 563.70] | K | |
Tc | 563.60 | K | KDB |
Tc | 563.60 ± 0.50 | K | NIST |
Tc | 563.70 | K | NIST |
Tc | 563.60 ± 0.40 | K | NIST |
Tfus | 152.60 | K | KDB |
Ttriple | 152.65 ± 0.01 | K | NIST |
Vc | [0.464; 0.464] | m3/kmol | |
Vc | 0.464 | m3/kmol | KDB |
Vc | 0.464 | m3/kmol | NIST |
Zc | 0.2524940 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [232.14; 305.46] | J/mol×K | [382.00; 549.20] | |
Cp,gas | 232.14 | J/mol×K | 382.00 | Joback Calculated Property |
Cp,gas | 245.53 | J/mol×K | 409.87 | Joback Calculated Property |
Cp,gas | 258.44 | J/mol×K | 437.73 | Joback Calculated Property |
Cp,gas | 270.88 | J/mol×K | 465.60 | Joback Calculated Property |
Cp,gas | 282.86 | J/mol×K | 493.46 | Joback Calculated Property |
Cp,gas | 294.38 | J/mol×K | 521.33 | Joback Calculated Property |
Cp,gas | 305.46 | J/mol×K | 549.20 | Joback Calculated Property |
Cp,liquid | [249.66; 250.20] | J/mol×K | [298.15; 298.15] | |
Cp,liquid | 250.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 249.66 | J/mol×K | 298.15 | NIST |
η | [0.0002373; 0.0105616] | Pa×s | [164.92; 382.00] | |
η | 0.0105616 | Pa×s | 164.92 | Joback Calculated Property |
η | 0.0031758 | Pa×s | 201.10 | Joback Calculated Property |
η | 0.0013776 | Pa×s | 237.28 | Joback Calculated Property |
η | 0.0007454 | Pa×s | 273.46 | Joback Calculated Property |
η | 0.0004656 | Pa×s | 309.64 | Joback Calculated Property |
η | 0.0003209 | Pa×s | 345.82 | Joback Calculated Property |
η | 0.0002373 | Pa×s | 382.00 | Joback Calculated Property |
ΔfusH | [11.67; 11.70] | kJ/mol | [152.60; 152.60] | |
ΔfusH | 11.67 | kJ/mol | 152.60 | NIST |
ΔfusH | 11.70 | kJ/mol | 152.60 | NIST |
ΔvapH | [33.66; 41.60] | kJ/mol | [262.00; 392.10] | |
ΔvapH | 41.60 | kJ/mol | 262.00 | NIST |
ΔvapH | 40.10 | kJ/mol | 339.50 | NIST |
ΔvapH | 38.30 | kJ/mol | 354.50 | NIST |
ΔvapH | 33.89 | kJ/mol | 392.10 | KDB |
ΔvapH | 33.66 | kJ/mol | 392.10 | NIST |
n0 | 1.39610 | 298.15 | KDB | |
ρl | 706.00 | kg/m3 | 293.00 | KDB |
γ | 0.02 | N/m | 298.20 | KDB |
λ | [0.11; 0.13] | W/m×K | [259.08; 332.51] | |
λ | 0.13 | W/m×K | 259.08 | Thermal... |
λ | 0.13 | W/m×K | 259.32 | Thermal... |
λ | 0.13 | W/m×K | 259.58 | Thermal... |
λ | 0.12 | W/m×K | 277.99 | Thermal... |
λ | 0.12 | W/m×K | 278.23 | Thermal... |
λ | 0.12 | W/m×K | 278.37 | Thermal... |
λ | 0.12 | W/m×K | 297.36 | Thermal... |
λ | 0.12 | W/m×K | 297.63 | Thermal... |
λ | 0.11 | W/m×K | 297.91 | Thermal... |
λ | 0.11 | W/m×K | 315.56 | Thermal... |
λ | 0.11 | W/m×K | 315.84 | Thermal... |
λ | 0.11 | W/m×K | 316.12 | Thermal... |
λ | 0.11 | W/m×K | 331.93 | Thermal... |
λ | 0.11 | W/m×K | 332.21 | Thermal... |
λ | 0.11 | W/m×K | 332.51 | Thermal... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [285.09; 418.68] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43862e+01 | |||
Coefficient B | -3.40203e+03 | |||
Coefficient C | -4.37910e+01 | |||
Temperature range, min. | 285.09 | |||
Temperature range, max. | 418.68 | |||
Pvap | 1.33 | kPa | 285.09 | Calculated Property |
Pvap | 3.02 | kPa | 299.93 | Calculated Property |
Pvap | 6.25 | kPa | 314.78 | Calculated Property |
Pvap | 11.99 | kPa | 329.62 | Calculated Property |
Pvap | 21.57 | kPa | 344.46 | Calculated Property |
Pvap | 36.73 | kPa | 359.31 | Calculated Property |
Pvap | 59.63 | kPa | 374.15 | Calculated Property |
Pvap | 92.85 | kPa | 388.99 | Calculated Property |
Pvap | 139.39 | kPa | 403.84 | Calculated Property |
Pvap | 202.63 | kPa | 418.68 | Calculated Property |
Pvap | [4.80e-08; 2539.44] | kPa | [152.60; 563.67] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.08909e+01 | |||
Coefficient B | -7.77747e+03 | |||
Coefficient C | -1.13291e+01 | |||
Coefficient D | 7.90061e-06 | |||
Temperature range, min. | 152.60 | |||
Temperature range, max. | 563.67 | |||
Pvap | 4.80e-08 | kPa | 152.60 | Calculated Property |
Pvap | 3.52e-04 | kPa | 198.27 | Calculated Property |
Pvap | 0.06 | kPa | 243.95 | Calculated Property |
Pvap | 1.62 | kPa | 289.62 | Calculated Property |
Pvap | 14.95 | kPa | 335.30 | Calculated Property |
Pvap | 73.51 | kPa | 380.97 | Calculated Property |
Pvap | 242.62 | kPa | 426.65 | Calculated Property |
Pvap | 618.02 | kPa | 472.32 | Calculated Property |
Pvap | 1326.19 | kPa | 518.00 | Calculated Property |
Pvap | 2539.44 | kPa | 563.67 | Calculated Property |
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