Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -9327.70 ± 1.50 | kJ/mol | NIST |
ΔfG° | -190.32 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -617.74 | kJ/mol | Joback Calculated Property |
ΔfusH° | 40.29 | kJ/mol | Joback Calculated Property |
ΔsubH° | 156.00 | kJ/mol | NIST |
ΔvapH° | 72.41 | kJ/mol | Joback Calculated Property |
log10WS | -4.31 | Aq. Sol... | |
logPoct/wat | 5.162 | Crippen Calculated Property | |
McVol | 229.650 | ml/mol | McGowan Calculated Property |
Pc | 1551.34 ± 85.00 | kPa | NIST |
Inp | [306.30; 1890.00] |
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|
Inp | 1865.00 | NIST | |
Inp | 1867.00 | NIST | |
Inp | 1868.00 | NIST | |
Inp | 1840.00 | NIST | |
Inp | 1843.00 | NIST | |
Inp | 1867.00 | NIST | |
Inp | 1869.00 | NIST | |
Inp | 1869.00 | NIST | |
Inp | 1869.00 | NIST | |
Inp | 1869.00 | NIST | |
Inp | 1857.00 | NIST | |
Inp | 1857.00 | NIST | |
Inp | 1868.40 | NIST | |
Inp | 1823.00 | NIST | |
Inp | 1823.00 | NIST | |
Inp | 1863.00 | NIST | |
Inp | 1867.00 | NIST | |
Inp | 1878.00 | NIST | |
Inp | 1857.00 | NIST | |
Inp | 1887.00 | NIST | |
Inp | 1872.00 | NIST | |
Inp | 1869.00 | NIST | |
Inp | 1844.00 | NIST | |
Inp | 1872.00 | NIST | |
Inp | 1845.00 | NIST | |
Inp | 1844.00 | NIST | |
Inp | 1844.00 | NIST | |
Inp | 1865.00 | NIST | |
Inp | 1833.00 | NIST | |
Inp | 1839.00 | NIST | |
Inp | 1867.10 | NIST | |
Inp | 1860.00 | NIST | |
Inp | 1867.00 | NIST | |
Inp | 1848.00 | NIST | |
Inp | 1862.00 | NIST | |
Inp | 1862.00 | NIST | |
Inp | 1843.00 | NIST | |
Inp | 1845.00 | NIST | |
Inp | 1862.00 | NIST | |
Inp | 1878.00 | NIST | |
Inp | 1856.00 | NIST | |
Inp | 1882.00 | NIST | |
Inp | 1868.00 | NIST | |
Inp | 1883.00 | NIST | |
Inp | 1865.00 | NIST | |
Inp | 1873.00 | NIST | |
Inp | 1866.20 | NIST | |
Inp | 1881.00 | NIST | |
Inp | 1865.00 | NIST | |
Inp | 1857.00 | NIST | |
Inp | 1857.00 | NIST | |
Inp | 1869.00 | NIST | |
Inp | 1870.00 | NIST | |
Inp | 1880.00 | NIST | |
Inp | 1858.00 | NIST | |
Inp | 1866.00 | NIST | |
Inp | 1868.00 | NIST | |
Inp | 1858.00 | NIST | |
Inp | 1848.00 | NIST | |
Inp | 1845.00 | NIST | |
Inp | 1851.00 | NIST | |
Inp | 1861.00 | NIST | |
Inp | 1862.00 | NIST | |
Inp | 1877.00 | NIST | |
Inp | 1890.00 | NIST | |
Inp | 1857.00 | NIST | |
Inp | 1845.00 | NIST | |
Inp | 1857.00 | NIST | |
Inp | 1873.00 | NIST | |
Inp | 1876.00 | NIST | |
Inp | 1878.00 | NIST | |
Inp | 1842.00 | NIST | |
Inp | 1859.00 | NIST | |
Inp | 1865.00 | NIST | |
Inp | 1860.00 | NIST | |
Inp | 1881.00 | NIST | |
Inp | 1869.00 | NIST | |
Inp | 1867.00 | NIST | |
Inp | 1855.00 | NIST | |
Inp | 1871.00 | NIST | |
Inp | 1841.00 | NIST | |
Inp | 1850.00 | NIST | |
Inp | 1854.00 | NIST | |
Inp | Outlier 308.82 | NIST | |
Inp | Outlier 319.90 | NIST | |
Inp | Outlier 306.30 | NIST | |
Inp | 1877.00 | NIST | |
Inp | 1873.00 | NIST | |
Inp | 1865.00 | NIST | |
Inp | 1855.00 | NIST | |
I | [2777.00; 2836.00] |
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|
I | 2791.00 | NIST | |
I | Outlier 2779.00 | NIST | |
I | 2791.00 | NIST | |
I | 2819.00 | NIST | |
I | 2821.00 | NIST | |
I | 2809.00 | NIST | |
I | 2819.00 | NIST | |
I | 2836.00 | NIST | |
I | Outlier 2777.00 | NIST | |
I | 2820.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2805.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2809.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2822.00 | NIST | |
I | 2803.00 | NIST | |
Tboil | 688.65 | K | Joback Calculated Property |
Tc | 775.43 ± 3.00 | K | NIST |
Tfus | 325.58 | K | Aq. Sol... |
Ttriple | 325.68 ± 0.02 | K | NIST |
Vc | 0.900 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [663.64; 746.44] | J/mol×K | [688.65; 855.92] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 660 680 700 720 740 700 750 800 850 | ||||
Cp,gas | 663.64 | J/mol×K | 688.65 | Joback Calculated Property |
Cp,gas | 679.08 | J/mol×K | 716.53 | Joback Calculated Property |
Cp,gas | 693.84 | J/mol×K | 744.41 | Joback Calculated Property |
Cp,gas | 707.94 | J/mol×K | 772.28 | Joback Calculated Property |
Cp,gas | 721.39 | J/mol×K | 800.16 | Joback Calculated Property |
Cp,gas | 734.21 | J/mol×K | 828.04 | Joback Calculated Property |
Cp,gas | 746.44 | J/mol×K | 855.92 | Joback Calculated Property |
Cp,solid | 443.28 | J/mol×K | 298.15 | NIST |
η | [0.0000424; 0.0043252] | Pa×s | [369.56; 688.65] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 400 500 600 | ||||
η | 0.0043252 | Pa×s | 369.56 | Joback Calculated Property |
η | 0.0012322 | Pa×s | 422.74 | Joback Calculated Property |
η | 0.0004648 | Pa×s | 475.92 | Joback Calculated Property |
η | 0.0002133 | Pa×s | 529.11 | Joback Calculated Property |
η | 0.0001128 | Pa×s | 582.29 | Joback Calculated Property |
η | 0.0000664 | Pa×s | 635.47 | Joback Calculated Property |
η | 0.0000424 | Pa×s | 688.65 | Joback Calculated Property |
ΔfusH | [8.12; 46.10] | kJ/mol | [318.70; 325.70] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 10 20 30 40 320 322 324 | ||||
ΔfusH | 8.12 | kJ/mol | 318.70 | NIST |
ΔfusH | 46.10 | kJ/mol | 324.90 | NIST |
ΔfusH | 40.40 | kJ/mol | 325.50 | NIST |
ΔfusH | 41.52 | kJ/mol | 325.70 | NIST |
ΔfusH | 41.52 | kJ/mol | 325.70 | NIST |
ΔsubH | [144.30; 178.00] | kJ/mol | [284.00; 294.00] | ![]() |
ΔsubH | 144.30 | kJ/mol | 284.00 | NIST |
ΔsubH | 178.00 | kJ/mol | 294.00 | NIST |
ΔvapH | [94.00; 116.60] | kJ/mol | [298.00; 522.00] | ![]() |
ΔvapH | 116.60 | kJ/mol | 298.00 | Vapor P... |
ΔvapH | 108.50 ± 2.00 | kJ/mol | 357.00 | NIST |
ΔvapH | 94.00 | kJ/mol | 522.00 | NIST |
ΔfusS | [25.48; 127.49] | J/mol×K | [318.70; 325.70] | ![]() |
ΔfusS | 25.48 | J/mol×K | 318.70 | NIST |
ΔfusS | 127.49 | J/mol×K | 325.70 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 530.20 | K | 13.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [471.80; 638.56] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.61706e+01 | |||
Coefficient B | -5.72495e+03 | |||
Coefficient C | -1.11355e+02 | |||
Temperature range, min. | 471.80 | |||
Temperature range, max. | 638.56 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 550 600 | ||||
Pvap | 1.33 | kPa | 471.80 | Calculated Property |
Pvap | 2.90 | kPa | 490.33 | Calculated Property |
Pvap | 5.86 | kPa | 508.86 | Calculated Property |
Pvap | 11.13 | kPa | 527.39 | Calculated Property |
Pvap | 20.02 | kPa | 545.92 | Calculated Property |
Pvap | 34.30 | kPa | 564.44 | Calculated Property |
Pvap | 56.36 | kPa | 582.97 | Calculated Property |
Pvap | 89.17 | kPa | 601.50 | Calculated Property |
Pvap | 136.46 | kPa | 620.03 | Calculated Property |
Pvap | 202.67 | kPa | 638.56 | Calculated Property |
Pvap | [1.18e-06; 1619.87] | kPa | [325.68; 766.40] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 5.78309e+02 | |||
Coefficient B | -4.18615e+04 | |||
Coefficient C | -8.07117e+01 | |||
Coefficient D | 3.36498e-05 | |||
Temperature range, min. | 325.68 | |||
Temperature range, max. | 766.40 | |||
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 1400 1600 400 500 600 700 | ||||
Pvap | 1.18e-06 | kPa | 325.68 | Calculated Property |
Pvap | 9.12e-04 | kPa | 374.65 | Calculated Property |
Pvap | 0.07 | kPa | 423.62 | Calculated Property |
Pvap | 1.23 | kPa | 472.59 | Calculated Property |
Pvap | 9.04 | kPa | 521.56 | Calculated Property |
Pvap | 38.37 | kPa | 570.52 | Calculated Property |
Pvap | 116.97 | kPa | 619.49 | Calculated Property |
Pvap | 297.08 | kPa | 668.46 | Calculated Property |
Pvap | 696.47 | kPa | 717.43 | Calculated Property |
Pvap | 1619.87 | kPa | 766.40 | Calculated Property |
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