Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -13130.00 ± 10.00 | kJ/mol | NIST |
ΔfG° | -19.43 | kJ/mol | KDB |
ΔfH°gas | -608.10 | kJ/mol | KDB |
ΔfusH° | 51.64 | kJ/mol | Joback Calculated Property |
ΔsubH° | [218.00; 223.00] | kJ/mol |
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ΔsubH° | 218.00 ± 4.00 | kJ/mol | NIST |
ΔsubH° | 223.00 ± 3.80 | kJ/mol | NIST |
ΔvapH° | 125.90 ± 0.80 | kJ/mol | NIST |
log10WS | -7.46 | Crippen Calculated Property | |
logPoct/wat | 7.020 | Crippen Calculated Property | |
McVol | 298.530 | ml/mol | McGowan Calculated Property |
Pc | 1300.00 | kPa | KDB |
Inp | [371.04; 2296.00] |
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|
Inp | 2276.40 | NIST | |
Inp | 2275.00 | NIST | |
Inp | 2276.00 | NIST | |
Inp | 2273.00 | NIST | |
Inp | 2292.00 | NIST | |
Inp | 2252.00 | NIST | |
Inp | 2271.00 | NIST | |
Inp | 2281.00 | NIST | |
Inp | 2290.00 | NIST | |
Inp | 2252.00 | NIST | |
Inp | 2278.00 | NIST | |
Inp | 2267.00 | NIST | |
Inp | 2252.00 | NIST | |
Inp | 2296.00 | NIST | |
Inp | 2282.00 | NIST | |
Inp | Outlier 371.04 | NIST | |
Inp | Outlier 374.80 | NIST | |
Inp | Outlier 374.56 | NIST | |
Inp | 2273.00 | NIST | |
I | [2717.00; 2755.00] |
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|
I | 2755.00 | NIST | |
I | 2717.00 | NIST | |
I | 2755.00 | NIST | |
I | 2717.00 | NIST | |
Tboil | 629.00 | K | KDB |
Tc | 809.00 | K | KDB |
Tfus | [336.90; 344.70] | K |
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Tfus | 339.20 | K | KDB |
Tfus | 337.67 | K | Phase d... |
Tfus | 336.90 | K | Solid-l... |
Tfus | 337.00 | K | Evaluat... |
Tfus | 338.00 ± 0.25 | K | NIST |
Tfus | 338.30 ± 0.80 | K | NIST |
Tfus | 339.20 ± 2.00 | K | NIST |
Tfus | Outlier 344.70 ± 2.00 | K | NIST |
Tfus | 338.50 ± 1.50 | K | NIST |
Vc | 1.175 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [926.90; 1029.83] | J/mol×K | [749.18; 918.60] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 920 940 960 980 1000 1020 1040 750 800 850 900 | ||||
Cp,gas | 926.90 | J/mol×K | 749.18 | Joback Calculated Property |
Cp,gas | 946.11 | J/mol×K | 777.42 | Joback Calculated Property |
Cp,gas | 964.46 | J/mol×K | 805.65 | Joback Calculated Property |
Cp,gas | 981.97 | J/mol×K | 833.89 | Joback Calculated Property |
Cp,gas | 998.68 | J/mol×K | 862.13 | Joback Calculated Property |
Cp,gas | 1014.62 | J/mol×K | 890.36 | Joback Calculated Property |
Cp,gas | 1029.83 | J/mol×K | 918.60 | Joback Calculated Property |
η | [0.0000197; 0.0035106] | Pa×s | [375.98; 749.18] | ![]() |
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 3.50e-3 400 500 600 700 | ||||
η | 0.0035106 | Pa×s | 375.98 | Joback Calculated Property |
η | 0.0008012 | Pa×s | 438.18 | Joback Calculated Property |
η | 0.0002640 | Pa×s | 500.38 | Joback Calculated Property |
η | 0.0001112 | Pa×s | 562.58 | Joback Calculated Property |
η | 0.0000556 | Pa×s | 624.78 | Joback Calculated Property |
η | 0.0000316 | Pa×s | 686.98 | Joback Calculated Property |
η | 0.0000197 | Pa×s | 749.18 | Joback Calculated Property |
ΔfusH | [43.60; 73.72] | kJ/mol | [336.60; 338.20] | ![]() |
ΔfusH | 43.60 | kJ/mol | 336.60 | NIST |
ΔfusH | 43.60 | kJ/mol | 336.60 | NIST |
ΔfusH | 73.72 | kJ/mol | 338.20 | NIST |
ΔsubH | 218.00 ± 3.80 | kJ/mol | 334.00 | NIST |
ΔvapH | [83.40; 118.90] | kJ/mol | [348.50; 570.50] | ![]() |
ΔvapH | 118.90 | kJ/mol | 348.50 | NIST |
ΔvapH | 83.50 | kJ/mol | 570.50 | NIST |
ΔvapH | 83.40 | kJ/mol | 570.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [503.40; 675.51] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.64855e+01 | |||
Coefficient B | -6.20057e+03 | |||
Coefficient C | -1.20599e+02 | |||
Temperature range, min. | 503.40 | |||
Temperature range, max. | 675.51 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 550 600 650 | ||||
Pvap | 1.33 | kPa | 503.40 | Calculated Property |
Pvap | 2.88 | kPa | 522.52 | Calculated Property |
Pvap | 5.81 | kPa | 541.65 | Calculated Property |
Pvap | 11.01 | kPa | 560.77 | Calculated Property |
Pvap | 19.79 | kPa | 579.89 | Calculated Property |
Pvap | 33.95 | kPa | 599.02 | Calculated Property |
Pvap | 55.87 | kPa | 618.14 | Calculated Property |
Pvap | 88.62 | kPa | 637.26 | Calculated Property |
Pvap | 136.00 | kPa | 656.39 | Calculated Property |
Pvap | 202.65 | kPa | 675.51 | Calculated Property |
Pvap | [7.51e-06; 1234.95] | kPa | [338.55; 792.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.53036e+02 | |||
Coefficient B | -2.53640e+04 | |||
Coefficient C | -3.27535e+01 | |||
Coefficient D | 7.52974e-06 | |||
Temperature range, min. | 338.55 | |||
Temperature range, max. | 792.00 | |||
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 400 600 800 | ||||
Pvap | 7.51e-06 | kPa | 338.55 | Calculated Property |
Pvap | 1.73e-03 | kPa | 388.93 | Calculated Property |
Pvap | 0.08 | kPa | 439.32 | Calculated Property |
Pvap | 1.20 | kPa | 489.70 | Calculated Property |
Pvap | 8.97 | kPa | 540.08 | Calculated Property |
Pvap | 40.78 | kPa | 590.47 | Calculated Property |
Pvap | 130.41 | kPa | 640.85 | Calculated Property |
Pvap | 324.42 | kPa | 691.23 | Calculated Property |
Pvap | 674.60 | kPa | 741.62 | Calculated Property |
Pvap | 1234.95 | kPa | 792.00 | Calculated Property |
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