Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4837.10 | kJ/mol | NIST |
ΔfG° | -219.88 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -458.53 | kJ/mol | Joback Calculated Property |
ΔfusH° | 15.74 | kJ/mol | Joback Calculated Property |
ΔvapH° | 42.17 | kJ/mol | Joback Calculated Property |
log10WS | -1.79 | Crippen Calculated Property | |
logPoct/wat | 1.986 | Crippen Calculated Property | |
McVol | 131.020 | ml/mol | McGowan Calculated Property |
Pc | 2450.00 | kPa | KDB |
Inp | [915.00; 961.00] |
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|
Inp | 940.30 | NIST | |
Inp | 930.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 956.00 | NIST | |
Inp | 946.00 | NIST | |
Inp | 940.00 | NIST | |
Inp | 939.00 | NIST | |
Inp | Outlier 915.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 929.00 | NIST | |
Inp | 938.00 | NIST | |
Inp | 937.00 | NIST | |
Inp | 939.00 | NIST | |
Inp | 937.00 | NIST | |
Inp | 937.00 | NIST | |
Inp | 945.00 | NIST | |
Inp | 945.00 | NIST | |
Inp | 945.00 | NIST | |
Inp | 946.00 | NIST | |
Inp | 935.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 920.00 | NIST | |
Inp | 961.00 | NIST | |
Inp | 939.00 | NIST | |
Inp | 958.00 | NIST | |
Inp | 961.00 | NIST | |
Inp | 953.00 | NIST | |
Inp | 955.00 | NIST | |
Inp | 946.00 | NIST | |
Inp | 961.00 | NIST | |
Inp | 938.00 | NIST | |
Inp | 935.00 | NIST | |
Inp | 935.00 | NIST | |
Inp | 935.00 | NIST | |
Inp | 939.00 | NIST | |
Inp | 939.00 | NIST | |
Inp | 955.00 | NIST | |
Inp | 958.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 941.00 | NIST | |
Inp | 940.00 | NIST | |
Inp | 939.00 | NIST | |
Inp | 920.00 | NIST | |
Inp | 933.00 | NIST | |
Inp | 946.00 | NIST | |
I | [1139.00; 1185.00] |
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I | Outlier 1185.00 | NIST | |
I | 1171.00 | NIST | |
I | 1165.00 | NIST | |
I | 1139.00 | NIST | |
I | 1157.00 | NIST | |
I | 1170.00 | NIST | |
I | 1160.00 | NIST | |
I | 1162.00 | NIST | |
I | 1152.00 | NIST | |
I | 1174.00 | NIST | |
I | 1158.00 | NIST | |
I | 1159.00 | NIST | |
I | 1161.00 | NIST | |
I | 1152.00 | NIST | |
I | 1156.00 | NIST | |
I | 1152.00 | NIST | |
I | 1156.00 | NIST | |
I | 1146.00 | NIST | |
I | 1152.00 | NIST | |
I | 1139.00 | NIST | |
I | 1162.00 | NIST | |
I | Outlier 1185.00 | NIST | |
I | 1170.00 | NIST | |
I | 1158.00 | NIST | |
Tboil | 430.10 | K | KDB |
Tc | [611.00; 611.40] | K |
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Tc | 611.00 | K | KDB |
Tc | 611.40 ± 6.00 | K | NIST |
Tfus | 237.08 | K | Joback Calculated Property |
Vc | 0.501 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [279.83; 348.57] | J/mol×K | [458.29; 637.16] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 280 290 300 310 320 330 340 350 500 550 600 | ||||
Cp,gas | 279.83 | J/mol×K | 458.29 | Joback Calculated Property |
Cp,gas | 292.41 | J/mol×K | 488.10 | Joback Calculated Property |
Cp,gas | 304.54 | J/mol×K | 517.91 | Joback Calculated Property |
Cp,gas | 316.22 | J/mol×K | 547.72 | Joback Calculated Property |
Cp,gas | 327.44 | J/mol×K | 577.53 | Joback Calculated Property |
Cp,gas | 338.23 | J/mol×K | 607.34 | Joback Calculated Property |
Cp,gas | 348.57 | J/mol×K | 637.16 | Joback Calculated Property |
η | [0.0002420; 0.0048246] | Pa×s | [237.08; 458.29] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 300 400 | ||||
η | 0.0048246 | Pa×s | 237.08 | Joback Calculated Property |
η | 0.0020946 | Pa×s | 273.95 | Joback Calculated Property |
η | 0.0011084 | Pa×s | 310.82 | Joback Calculated Property |
η | 0.0006713 | Pa×s | 347.69 | Joback Calculated Property |
η | 0.0004476 | Pa×s | 384.55 | Joback Calculated Property |
η | 0.0003204 | Pa×s | 421.42 | Joback Calculated Property |
η | 0.0002420 | Pa×s | 458.29 | Joback Calculated Property |
ΔvapH | 41.70 | kJ/mol | 353.50 | NIST |
ρl | 863.00 | kg/m3 | 291.00 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [321.04; 456.38] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.49752e+01 | |||
Coefficient B | -3.82371e+03 | |||
Coefficient C | -6.07040e+01 | |||
Temperature range, min. | 321.04 | |||
Temperature range, max. | 456.38 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 321.04 | Calculated Property |
Pvap | 2.97 | kPa | 336.08 | Calculated Property |
Pvap | 6.10 | kPa | 351.12 | Calculated Property |
Pvap | 11.67 | kPa | 366.15 | Calculated Property |
Pvap | 20.99 | kPa | 381.19 | Calculated Property |
Pvap | 35.84 | kPa | 396.23 | Calculated Property |
Pvap | 58.43 | kPa | 411.27 | Calculated Property |
Pvap | 91.51 | kPa | 426.30 | Calculated Property |
Pvap | 138.33 | kPa | 441.34 | Calculated Property |
Pvap | 202.64 | kPa | 456.38 | Calculated Property |
Pvap | [0.14; 2071.57] | kPa | [277.15; 603.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | -2.82579e+01 | |||
Coefficient B | -3.31903e+03 | |||
Coefficient C | 6.90926e+00 | |||
Coefficient D | -7.79519e-06 | |||
Temperature range, min. | 277.15 | |||
Temperature range, max. | 603.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 300 400 500 600 | ||||
Pvap | 0.14 | kPa | 277.15 | Calculated Property |
Pvap | 1.10 | kPa | 313.36 | Calculated Property |
Pvap | 5.81 | kPa | 349.56 | Calculated Property |
Pvap | 22.75 | kPa | 385.77 | Calculated Property |
Pvap | 70.43 | kPa | 421.97 | Calculated Property |
Pvap | 180.65 | kPa | 458.18 | Calculated Property |
Pvap | 396.91 | kPa | 494.38 | Calculated Property |
Pvap | 765.75 | kPa | 530.59 | Calculated Property |
Pvap | 1321.86 | kPa | 566.79 | Calculated Property |
Pvap | 2071.57 | kPa | 603.00 | Calculated Property |
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