Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3610 | KDB | |
AP | 341.850 | K | KDB |
ΔcH°liquid | [-5470.12; -5262.00] | kJ/mol | |
ΔcH°liquid | -5470.12 ± 0.96 | kJ/mol | NIST |
ΔcH°liquid | -5432.10 | kJ/mol | NIST |
ΔcH°liquid | -5262.00 | kJ/mol | NIST |
ΔfG° | 16.94 | kJ/mol | KDB |
Δc,grossH | 5470.12 | kJ/mol | KDB |
Δc,netH | 5073.979 | kJ/mol | KDB |
ΔfH°gas | [-211.00; -210.90] | kJ/mol | |
ΔfH°gas | -211.00 | kJ/mol | KDB |
ΔfH°gas | -210.90 ± 1.20 | kJ/mol | NIST |
ΔfH°liquid | -250.50 ± 1.10 | kJ/mol | NIST |
ΔfusH° | 12.95 | kJ/mol | Joback Calculated Property |
ΔvapH° | [33.00; 39.70] | kJ/mol | |
ΔvapH° | 39.69 | kJ/mol | NIST |
ΔvapH° | 39.70 | kJ/mol | NIST |
ΔvapH° | 39.60 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 39.69 | kJ/mol | NIST |
ΔvapH° | 33.00 | kJ/mol | NIST |
log10WS | -2.93 | Crippen Calculated Property | |
logPoct/wat | 3.223 | Crippen Calculated Property | |
McVol | 123.580 | ml/mol | McGowan Calculated Property |
Pc | [2607.90; 2610.00] | kPa | |
Pc | 2610.00 | kPa | KDB |
Pc | 2610.00 ± 40.00 | kPa | NIST |
Pc | 2607.90 ± 40.53 | kPa | NIST |
ρc | [251.30; 251.30] | kg/m3 | |
ρc | 251.30 ± 4.57 | kg/m3 | NIST |
ρc | 251.30 ± 4.57 | kg/m3 | NIST |
Inp | [763.00; 777.00] | ||
Inp | 775.70 | NIST | |
Inp | 771.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.80 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 775.30 | NIST | |
Inp | 775.30 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 776.90 | NIST | |
Inp | 772.00 | NIST | |
Inp | 770.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 772.20 | NIST | |
Inp | 776.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 770.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 772.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 770.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 773.40 | NIST | |
Inp | 772.90 | NIST | |
Inp | 775.00 | NIST | |
Inp | 769.70 | NIST | |
Inp | 770.10 | NIST | |
Inp | 771.44 | NIST | |
Inp | 773.69 | NIST | |
Inp | 772.00 | NIST | |
Inp | 774.01 | NIST | |
Inp | 774.57 | NIST | |
Inp | 774.94 | NIST | |
Inp | 773.78 | NIST | |
Inp | 774.37 | NIST | |
Inp | 774.75 | NIST | |
Inp | 770.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | Outlier 765.00 | NIST | |
Inp | 777.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | Outlier 763.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 775.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 769.00 | NIST | |
Inp | 770.00 | NIST | |
Inp | 775.70 | NIST | |
Inp | 775.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | 775.30 | NIST | |
Inp | 770.00 | NIST | |
Inp | 772.20 | NIST | |
Inp | 773.40 | NIST | |
Inp | 774.00 | NIST | |
Tboil | [391.55; 391.97] | K | |
Tboil | 391.70 | K | KDB |
Tboil | 391.70 | K | NIST |
Tboil | 391.70 | K | NIST |
Tboil | 391.68 ± 0.20 | K | NIST |
Tboil | Outlier 391.97 ± 0.20 | K | NIST |
Tboil | 391.55 ± 0.20 | K | NIST |
Tboil | 391.69 ± 0.20 | K | NIST |
Tboil | 391.80 ± 0.40 | K | NIST |
Tboil | 391.85 ± 0.50 | K | NIST |
Tboil | 391.65 ± 0.50 | K | NIST |
Tboil | 391.70 ± 0.15 | K | NIST |
Tboil | 391.90 ± 0.00 | K | NIST |
Tboil | 391.68 ± 0.02 | K | NIST |
Tboil | 391.68 ± 0.10 | K | NIST |
Tboil | 391.85 ± 0.20 | K | NIST |
Tboil | 391.85 ± 0.30 | K | NIST |
Tc | [565.40; 565.50] | K | |
Tc | 565.50 | K | KDB |
Tc | 565.50 ± 0.50 | K | NIST |
Tc | 565.40 | K | NIST |
Tc | 565.42 ± 0.40 | K | NIST |
Tfus | 164.92 | K | Joback Calculated Property |
Vc | [0.455; 0.455] | m3/kmol | |
Vc | 0.455 | m3/kmol | KDB |
Vc | 0.455 | m3/kmol | NIST |
Zc | 0.2525710 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [241.42; 298.74] | J/mol×K | [397.10; 522.70] | |
Cp,gas | 241.42 | J/mol×K | 397.10 | NIST |
Cp,gas | 269.87 | J/mol×K | 462.70 | NIST |
Cp,gas | 298.74 | J/mol×K | 522.70 | NIST |
η | [0.0002373; 0.0105616] | Pa×s | [164.92; 382.00] | |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 200 250 300 350 | ||||
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 |
ΔvapH | [33.59; 42.40] | kJ/mol | [321.00; 391.70] | |
ΔvapH | 42.40 | kJ/mol | 321.00 | NIST |
ΔvapH | 38.20 | kJ/mol | 353.50 | NIST |
ΔvapH | 33.61 | kJ/mol | 391.70 | KDB |
ΔvapH | 33.59 | kJ/mol | 391.70 | NIST |
n0 | 1.39919 | 298.15 | KDB | |
ρl | 718.00 | kg/m3 | 289.00 | KDB |
γ | 0.02 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [286.01; 418.13] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42298e+01 | |||
Coefficient B | -3.26994e+03 | |||
Coefficient C | -5.14790e+01 | |||
Temperature range, min. | 286.01 | |||
Temperature range, max. | 418.13 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 286.01 | Calculated Property |
Pvap | 3.03 | kPa | 300.69 | Calculated Property |
Pvap | 6.29 | kPa | 315.37 | Calculated Property |
Pvap | 12.08 | kPa | 330.05 | Calculated Property |
Pvap | 21.74 | kPa | 344.73 | Calculated Property |
Pvap | 36.99 | kPa | 359.41 | Calculated Property |
Pvap | 59.98 | kPa | 374.09 | Calculated Property |
Pvap | 93.23 | kPa | 388.77 | Calculated Property |
Pvap | 139.70 | kPa | 403.45 | Calculated Property |
Pvap | 202.64 | kPa | 418.13 | Calculated Property |
Pvap | [0.11; 2592.05] | kPa | [250.00; 565.40] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.99778e+01 | |||
Coefficient B | -7.73243e+03 | |||
Coefficient C | -1.11883e+01 | |||
Coefficient D | 7.70935e-06 | |||
Temperature range, min. | 250.00 | |||
Temperature range, max. | 565.40 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 300 400 500 | ||||
Pvap | 0.11 | kPa | 250.00 | Calculated Property |
Pvap | 1.26 | kPa | 285.04 | Calculated Property |
Pvap | 7.92 | kPa | 320.09 | Calculated Property |
Pvap | 32.26 | kPa | 355.13 | Calculated Property |
Pvap | 97.30 | kPa | 390.18 | Calculated Property |
Pvap | 237.23 | kPa | 425.22 | Calculated Property |
Pvap | 496.10 | kPa | 460.27 | Calculated Property |
Pvap | 927.58 | kPa | 495.31 | Calculated Property |
Pvap | 1597.80 | kPa | 530.36 | Calculated Property |
Pvap | 2592.05 | kPa | 565.40 | Calculated Property |
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