Property | Value | Unit | Source |
---|---|---|---|
ω | 0.7730 | KDB | |
ΔfG° | 213.09 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -178.32 | kJ/mol | Joback Calculated Property |
ΔfusH° | 36.42 | kJ/mol | Joback Calculated Property |
ΔsubH° | 135.10 | kJ/mol | NIST |
ΔvapH° | 89.60 | kJ/mol | NIST |
IE | 9.10 ± 0.10 | eV | NIST |
log10WS | -6.46 | Crippen Calculated Property | |
logPoct/wat | 6.150 | Crippen Calculated Property | |
McVol | 240.720 | ml/mol | McGowan Calculated Property |
Pc | 1580.00 | kPa | KDB |
Inp | [1866.00; 1878.00] |
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|
Inp | 1878.00 | NIST | |
Inp | 1872.60 | NIST | |
Inp | 1870.00 | NIST | |
Inp | 1866.00 | NIST | |
Inp | 1872.60 | NIST | |
Inp | 1866.00 | NIST | |
Inp | 1878.00 | NIST | |
I | [2141.00; 2180.00] |
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|
I | 2180.00 | NIST | |
I | 2169.00 | NIST | |
I | 2141.00 | NIST | |
I | 2155.00 | NIST | |
Tboil | [590.00; 600.80] | K |
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Tboil | 600.80 | K | KDB |
Tboil | 590.00 ± 5.00 | K | NIST |
Tc | 774.00 | K | KDB |
Tfus | [266.00; 276.00] | K |
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Tfus | 276.00 | K | KDB |
Tfus | 270.00 ± 2.00 | K | NIST |
Tfus | 266.00 ± 2.00 | K | NIST |
Vc | 0.980 | m3/kmol | KDB |
Zc | 0.2406050 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [653.40; 757.49] | J/mol×K | [637.92; 823.44] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 660 680 700 720 740 760 650 700 750 800 | ||||
Cp,gas | 653.40 | J/mol×K | 637.92 | Joback Calculated Property |
Cp,gas | 673.14 | J/mol×K | 668.84 | Joback Calculated Property |
Cp,gas | 691.87 | J/mol×K | 699.76 | Joback Calculated Property |
Cp,gas | 709.62 | J/mol×K | 730.68 | Joback Calculated Property |
Cp,gas | 726.46 | J/mol×K | 761.60 | Joback Calculated Property |
Cp,gas | 742.40 | J/mol×K | 792.52 | Joback Calculated Property |
Cp,gas | 757.49 | J/mol×K | 823.44 | Joback Calculated Property |
η | [0.0001228; 0.0029955] | Pa×s | [319.04; 637.92] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 400 500 600 | ||||
η | 0.0029955 | Pa×s | 319.04 | Joback Calculated Property |
η | 0.0012027 | Pa×s | 372.19 | Joback Calculated Property |
η | 0.0006066 | Pa×s | 425.33 | Joback Calculated Property |
η | 0.0003562 | Pa×s | 478.48 | Joback Calculated Property |
η | 0.0002326 | Pa×s | 531.63 | Joback Calculated Property |
η | 0.0001642 | Pa×s | 584.77 | Joback Calculated Property |
η | 0.0001228 | Pa×s | 637.92 | Joback Calculated Property |
ΔfusH | 43.10 | kJ/mol | 274.60 | NIST |
ΔvapH | [54.39; 92.00] | kJ/mol | [275.00; 600.80] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 60 70 80 90 300 400 500 600 | ||||
ΔvapH | 92.00 | kJ/mol | 275.00 | NIST |
ΔvapH | 83.20 | kJ/mol | 393.00 | NIST |
ΔvapH | 80.60 | kJ/mol | 396.00 | NIST |
ΔvapH | 67.40 | kJ/mol | 552.50 | NIST |
ΔvapH | 54.39 | kJ/mol | 600.80 | KDB |
γ | 0.03 | N/m | 294.30 | Densiti... |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tfus | [269.70; 292.00] | K | [100.00; 100000.00] |
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P(kPa) Melting point (K) 270 275 280 285 290 0 50000 100000 | ||||
Tfus | 269.70 | K | 100.00 | Solid-L... |
Tfus | 274.40 | K | 20200.00 | Solid-L... |
Tfus | 279.00 | K | 40100.00 | Solid-L... |
Tfus | 283.40 | K | 60000.00 | Solid-L... |
Tfus | 287.80 | K | 79900.00 | Solid-L... |
Tfus | 292.00 | K | 100000.00 | Solid-L... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.31; 201.29] | kPa | [456.15; 635.15] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.52577e+01 | |||
Coefficient B | -5.30559e+03 | |||
Coefficient C | -1.02085e+02 | |||
Temperature range, min. | 456.15 | |||
Temperature range, max. | 635.15 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 550 600 | ||||
Pvap | 1.31 | kPa | 456.15 | Calculated Property |
Pvap | 2.92 | kPa | 476.04 | Calculated Property |
Pvap | 5.97 | kPa | 495.93 | Calculated Property |
Pvap | 11.40 | kPa | 515.82 | Calculated Property |
Pvap | 20.54 | kPa | 535.71 | Calculated Property |
Pvap | 35.12 | kPa | 555.59 | Calculated Property |
Pvap | 57.41 | kPa | 575.48 | Calculated Property |
Pvap | 90.21 | kPa | 595.37 | Calculated Property |
Pvap | 136.86 | kPa | 615.26 | Calculated Property |
Pvap | 201.29 | kPa | 635.15 | Calculated Property |
Pvap | [2.55e-07; 1733.22] | kPa | [275.93; 774.26] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.68186e+02 | |||
Coefficient B | -2.21930e+04 | |||
Coefficient C | -3.63255e+01 | |||
Coefficient D | 1.59623e-05 | |||
Temperature range, min. | 275.93 | |||
Temperature range, max. | 774.26 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 400 600 | ||||
Pvap | 2.55e-07 | kPa | 275.93 | Calculated Property |
Pvap | 3.91e-04 | kPa | 331.30 | Calculated Property |
Pvap | 0.04 | kPa | 386.67 | Calculated Property |
Pvap | 0.84 | kPa | 442.04 | Calculated Property |
Pvap | 7.09 | kPa | 497.41 | Calculated Property |
Pvap | 33.84 | kPa | 552.78 | Calculated Property |
Pvap | 113.89 | kPa | 608.15 | Calculated Property |
Pvap | 310.80 | kPa | 663.52 | Calculated Property |
Pvap | 754.21 | kPa | 718.89 | Calculated Property |
Pvap | 1733.22 | kPa | 774.26 | Calculated Property |
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