Property | Value | Unit | Source |
---|---|---|---|
ω | 0.7700 | KDB | |
ΔcH°liquid | -11351.20 ± 2.20 | kJ/mol | NIST |
ΔfG° | 92.15 | kJ/mol | KDB |
ΔfH°gas | [-394.20; -393.90] | kJ/mol |
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ΔfH°gas | -394.20 | kJ/mol | KDB |
ΔfH°gas | -393.90 ± 2.40 | kJ/mol | NIST |
ΔfH°liquid | -479.50 ± 2.40 | kJ/mol | NIST |
ΔfusH° | 39.79 | kJ/mol | Joback Calculated Property |
ΔsubH° | 125.10 | kJ/mol | NIST |
ΔvapH° | [86.00; 86.50] | kJ/mol |
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ΔvapH° | 86.02 | kJ/mol | NIST |
ΔvapH° | 86.50 | kJ/mol | NIST |
ΔvapH° | 86.00 ± 0.80 | kJ/mol | NIST |
ΔvapH° | 86.20 | kJ/mol | NIST |
log10WS | -6.94 | Crippen Calculated Property | |
logPoct/wat | 6.878 | Crippen Calculated Property | |
McVol | 250.390 | ml/mol | McGowan Calculated Property |
Pc | [1300.00; 1342.00] | kPa |
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Pc | 1340.00 | kPa | KDB |
Pc | 1300.00 ± 200.00 | kPa | NIST |
Pc | 1320.00 ± 40.00 | kPa | NIST |
Pc | 1342.00 ± 160.00 | kPa | NIST |
ρc | [216.42; 218.10] | kg/m3 |
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ρc | 216.42 ± 48.09 | kg/m3 | NIST |
ρc | 218.10 ± 4.81 | kg/m3 | NIST |
Inp | [282.99; 287.19] |
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|
Inp | 282.99 | NIST | |
Inp | 287.19 | NIST | |
S°liquid | 652.24 | J/mol×K | NIST |
Tboil | [561.65; 575.10] | K |
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Tboil | 575.10 | K | KDB |
Tboil | 575.00 | K | NIST |
Tboil | 574.25 ± 0.70 | K | NIST |
Tboil | 563.15 ± 2.00 | K | NIST |
Tboil | 561.65 ± 1.50 | K | NIST |
Tboil | 561.65 ± 2.00 | K | NIST |
Tc | [725.30; 736.00] | K |
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Tc | 736.00 | K | KDB |
Tc | 736.00 ± 2.00 | K | NIST |
Tc | 731.10 ± 3.00 | K | NIST |
Tc | Outlier 725.30 ± 1.60 | K | NIST |
Tc | 735.90 ± 1.00 | K | NIST |
Tc | 735.60 | K | NIST |
Tc | 736.00 ± 3.00 | K | NIST |
Tc | 736.00 ± 5.00 | K | NIST |
Tfus | [294.00; 301.00] | K |
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Tfus | 295.00 | K | KDB |
Tfus | 295.35 | K | High pr... |
Tfus | 294.95 ± 0.50 | K | NIST |
Tfus | 295.00 ± 2.00 | K | NIST |
Tfus | Outlier 301.00 ± 5.00 | K | NIST |
Tfus | 294.90 ± 0.30 | K | NIST |
Tfus | 295.11 ± 0.02 | K | NIST |
Tfus | 295.11 ± 0.02 | K | NIST |
Tfus | 295.13 ± 0.01 | K | NIST |
Tfus | 295.13 ± 0.01 | K | NIST |
Tfus | 295.15 ± 1.00 | K | NIST |
Tfus | 295.11 ± 0.06 | K | NIST |
Tfus | 295.13 ± 0.03 | K | NIST |
Tfus | 295.10 ± 0.10 | K | NIST |
Tfus | 295.01 ± 0.15 | K | NIST |
Tfus | 295.08 ± 0.20 | K | NIST |
Tfus | 295.00 ± 0.20 | K | NIST |
Tfus | 295.00 ± 0.20 | K | NIST |
Tfus | 294.87 ± 0.20 | K | NIST |
Tfus | 294.40 ± 0.50 | K | NIST |
Tfus | 294.40 ± 0.20 | K | NIST |
Tfus | 294.39 ± 0.20 | K | NIST |
Tfus | 295.09 ± 0.20 | K | NIST |
Tfus | 294.00 ± 2.00 | K | NIST |
Tfus | 295.00 ± 3.00 | K | NIST |
Tfus | 296.00 ± 2.00 | K | NIST |
Tfus | 296.00 ± 2.00 | K | NIST |
Tfus | 295.40 ± 2.00 | K | NIST |
Tfus | 295.70 ± 2.00 | K | NIST |
Tfus | 295.00 ± 4.00 | K | NIST |
Tfus | 295.70 ± 2.00 | K | NIST |
Ttriple | 295.14 ± 0.04 | K | NIST |
Vc | [1.103; 1.103] | m3/kmol |
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Vc | 1.103 | m3/kmol | KDB |
Vc | 1.103 | m3/kmol | NIST |
Zc | 0.2415270 | KDB | |
Zra | 0.23 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [666.92; 773.60] | J/mol×K | [588.36; 747.00] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 660 680 700 720 740 760 780 600 650 700 750 | ||||
Cp,gas | 666.92 | J/mol×K | 588.36 | Joback Calculated Property |
Cp,gas | 686.55 | J/mol×K | 614.80 | Joback Calculated Property |
Cp,gas | 705.41 | J/mol×K | 641.24 | Joback Calculated Property |
Cp,gas | 723.52 | J/mol×K | 667.68 | Joback Calculated Property |
Cp,gas | 740.91 | J/mol×K | 694.12 | Joback Calculated Property |
Cp,gas | 757.59 | J/mol×K | 720.56 | Joback Calculated Property |
Cp,gas | 773.60 | J/mol×K | 747.00 | Joback Calculated Property |
Cp,liquid | 534.34 | J/mol×K | 298.15 | NIST |
η | [0.0001372; 0.0047502] | Pa×s | [281.35; 588.36] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 300 400 500 | ||||
η | 0.0047502 | Pa×s | 281.35 | Joback Calculated Property |
η | 0.0016701 | Pa×s | 332.52 | Joback Calculated Property |
η | 0.0007760 | Pa×s | 383.69 | Joback Calculated Property |
η | 0.0004318 | Pa×s | 434.86 | Joback Calculated Property |
η | 0.0002719 | Pa×s | 486.02 | Joback Calculated Property |
η | 0.0001869 | Pa×s | 537.19 | Joback Calculated Property |
η | 0.0001372 | Pa×s | 588.36 | Joback Calculated Property |
ΔfusH | [10.96; 40.17] | kJ/mol | [284.30; 295.10] | ![]() |
ΔfusH | 10.96 | kJ/mol | 284.30 | NIST |
ΔfusH | 39.40 | kJ/mol | 294.70 | NIST |
ΔfusH | 40.17 | kJ/mol | 295.10 | NIST |
ΔfusH | 40.17 | kJ/mol | 295.10 | NIST |
ΔsubH | [131.00; 131.50] | kJ/mol | [288.00; 290.50] | ![]() |
ΔsubH | 131.50 ± 4.60 | kJ/mol | 288.00 | NIST |
ΔsubH | 131.00 ± 13.00 | kJ/mol | 290.50 | NIST |
ΔvapH | [52.89; 91.10] | kJ/mol | [304.50; 576.00] | ![]() |
ΔvapH | 91.10 | kJ/mol | 304.50 | NIST |
ΔvapH | 71.60 | kJ/mol | 457.50 | NIST |
ΔvapH | 62.90 | kJ/mol | 532.50 | NIST |
ΔvapH | 52.89 | kJ/mol | 576.00 | KDB |
n0 | [1.42680; 1.43620] | [293.10; 318.15] | ![]() |
|
n0 | 1.43620 | 293.10 | Liquid ... | |
n0 | 1.43620 | 293.10 | Extract... | |
n0 | 1.42680 | 318.15 | Thermod... | |
ρl | [723.00; 778.00] | kg/m3 | [298.00; 373.15] | ![]() |
T(K) Liquid Density (kg/m3) 720 730 740 750 760 770 780 300 320 340 360 | ||||
ρl | 778.00 | kg/m3 | 298.00 | KDB |
ρl | 771.02 | kg/m3 | 303.15 | Density... |
ρl | 764.16 | kg/m3 | 313.15 | Density... |
ρl | 757.30 | kg/m3 | 323.15 | Density... |
ρl | 750.45 | kg/m3 | 333.15 | Density... |
ρl | 743.70 | kg/m3 | 343.15 | Density... |
ρl | 736.80 | kg/m3 | 353.15 | Density... |
ρl | 729.80 | kg/m3 | 363.15 | Density... |
ρl | 723.00 | kg/m3 | 373.15 | Density... |
ΔfusS | [38.56; 136.11] | J/mol×K | [284.30; 295.10] | ![]() |
ΔfusS | 38.56 | J/mol×K | 284.30 | NIST |
ΔfusS | 136.11 | J/mol×K | 295.10 | NIST |
γ | 0.03 | N/m | 303.20 | KDB |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 434.90 | K | 1.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [436.10; 609.50] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.46994e+01 | |||
Coefficient B | -4.66990e+03 | |||
Coefficient C | -1.12064e+02 | |||
Temperature range, min. | 436.10 | |||
Temperature range, max. | 609.50 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
Pvap | 1.33 | kPa | 436.10 | Calculated Property |
Pvap | 2.99 | kPa | 455.37 | Calculated Property |
Pvap | 6.17 | kPa | 474.63 | Calculated Property |
Pvap | 11.81 | kPa | 493.90 | Calculated Property |
Pvap | 21.26 | kPa | 513.17 | Calculated Property |
Pvap | 36.25 | kPa | 532.43 | Calculated Property |
Pvap | 58.98 | kPa | 551.70 | Calculated Property |
Pvap | 92.12 | kPa | 570.97 | Calculated Property |
Pvap | 138.82 | kPa | 590.23 | Calculated Property |
Pvap | 202.64 | kPa | 609.50 | Calculated Property |
Pvap | [2.11e-05; 1370.81] | kPa | [295.13; 733.37] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.59113e+02 | |||
Coefficient B | -2.12295e+04 | |||
Coefficient C | -3.50392e+01 | |||
Coefficient D | 1.53105e-05 | |||
Temperature range, min. | 295.13 | |||
Temperature range, max. | 733.37 | |||
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 1400 400 600 | ||||
Pvap | 2.11e-05 | kPa | 295.13 | Calculated Property |
Pvap | 4.27e-03 | kPa | 343.82 | Calculated Property |
Pvap | 0.15 | kPa | 392.52 | Calculated Property |
Pvap | 1.83 | kPa | 441.21 | Calculated Property |
Pvap | 11.17 | kPa | 489.90 | Calculated Property |
Pvap | 43.71 | kPa | 538.60 | Calculated Property |
Pvap | 128.05 | kPa | 587.29 | Calculated Property |
Pvap | 311.38 | kPa | 635.98 | Calculated Property |
Pvap | 674.90 | kPa | 684.68 | Calculated Property |
Pvap | 1370.81 | kPa | 733.37 | Calculated Property |
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