Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | [-3394.20; -3389.00] | kJ/mol |
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ΔcH°liquid | -3394.20 ± 2.60 | kJ/mol | NIST |
ΔcH°liquid | -3389.00 | kJ/mol | NIST |
ΔcH°liquid | -3390.00 ± 2.00 | kJ/mol | NIST |
ΔfG° | -249.69 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -636.00 ± 3.00 | kJ/mol | NIST |
ΔfH°liquid | -681.80 ± 2.60 | kJ/mol | NIST |
ΔfusH° | 29.21 | kJ/mol | Joback Calculated Property |
ΔvapH° | [41.00; 45.80] | kJ/mol |
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ΔvapH° | 45.80 | kJ/mol | NIST |
ΔvapH° | 41.00 ± 0.40 | kJ/mol | NIST |
log10WS | -1.31 | Crippen Calculated Property | |
logPoct/wat | 1.088 | Crippen Calculated Property | |
McVol | 102.150 | ml/mol | McGowan Calculated Property |
Pc | 3534.66 | kPa | Joback Calculated Property |
Inp | [729.00; 786.00] |
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|
Inp | 755.00 | NIST | |
Inp | 729.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 786.00 | NIST | |
Inp | 781.00 | NIST | |
Inp | 776.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 767.00 | NIST | |
Inp | 767.00 | NIST | |
Inp | 771.00 | NIST | |
Inp | 786.00 | NIST | |
I | [1069.00; 1070.00] |
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|
I | 1070.00 | NIST | |
I | 1069.00 | NIST | |
I | 1069.00 | NIST | |
I | 1069.00 | NIST | |
I | 1070.00 | NIST | |
S°gas | 374.40 ± 5.00 | J/mol×K | NIST |
S°liquid | 289.40 | J/mol×K | NIST |
Tboil | [395.00; 401.15] | K |
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Tboil | 397.15 | K | NIST |
Tboil | Outlier 401.15 ± 0.50 | K | NIST |
Tboil | 397.15 ± 1.00 | K | NIST |
Tboil | 395.00 ± 1.00 | K | NIST |
Tboil | 397.20 ± 1.50 | K | NIST |
Tboil | 396.50 ± 1.00 | K | NIST |
Tc | 563.00 ± 4.00 | K | NIST |
Tfus | [284.15; 286.00] | K |
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Tfus | 285.75 | K | NIST |
Tfus | 284.15 ± 1.00 | K | NIST |
Tfus | 285.65 ± 0.20 | K | NIST |
Tfus | 286.00 ± 0.50 | K | NIST |
Tfus | 285.70 ± 0.10 | K | NIST |
Ttriple | 285.70 ± 0.10 | K | NIST |
Vc | 0.365 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [223.56; 300.83] | J/mol×K | [427.74; 632.02] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 220 240 260 280 300 450 500 550 600 | ||||
Cp,gas | 223.56 | J/mol×K | 427.74 | Joback Calculated Property |
Cp,gas | 237.89 | J/mol×K | 461.79 | Joback Calculated Property |
Cp,gas | 251.64 | J/mol×K | 495.83 | Joback Calculated Property |
Cp,gas | 264.82 | J/mol×K | 529.88 | Joback Calculated Property |
Cp,gas | 277.41 | J/mol×K | 563.93 | Joback Calculated Property |
Cp,gas | 289.41 | J/mol×K | 597.97 | Joback Calculated Property |
Cp,gas | 300.83 | J/mol×K | 632.02 | Joback Calculated Property |
Cp,liquid | [250.20; 257.30] | J/mol×K | [298.00; 306.60] | ![]() |
Cp,liquid | 250.20 | J/mol×K | 298.00 | NIST |
Cp,liquid | 257.30 | J/mol×K | 298.15 | NIST |
Cp,liquid | 254.00 | J/mol×K | 306.60 | NIST |
η | [0.0009070; 0.0013740] | Pa×s | [288.15; 308.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 9.00e-4 1.00e-3 1.10e-3 1.20e-3 1.30e-3 1.40e-3 290 295 300 305 | ||||
η | 0.0013740 | Pa×s | 288.15 | Densiti... |
η | 0.0012240 | Pa×s | 293.15 | Densiti... |
η | 0.0011070 | Pa×s | 298.15 | Densiti... |
η | 0.0011070 | Pa×s | 298.15 | Excess ... |
η | 0.0011070 | Pa×s | 298.15 | Molecul... |
η | 0.0010010 | Pa×s | 303.15 | Excess ... |
η | 0.0010010 | Pa×s | 303.15 | Molecul... |
η | 0.0010010 | Pa×s | 303.15 | Densiti... |
η | 0.0009070 | Pa×s | 308.15 | Excess ... |
η | 0.0009070 | Pa×s | 308.15 | Molecul... |
η | 0.0009070 | Pa×s | 308.15 | Densiti... |
ΔfusH | [0.26; 13.52] | kJ/mol | [142.70; 285.70] | ![]() |
ΔfusH | 0.26 | kJ/mol | 142.70 | NIST |
ΔfusH | 0.77 | kJ/mol | 147.50 | NIST |
ΔfusH | 13.52 | kJ/mol | 285.70 | NIST |
ΔfusH | 13.52 | kJ/mol | 285.70 | NIST |
ΔvapH | 41.50 | kJ/mol | 359.50 | NIST |
n0 | 1.40290 | 298.15 | Viscosi... | |
ΔfusS | [1.81; 47.32] | J/mol×K | [142.70; 285.70] | ![]() |
ΔfusS | 1.81 | J/mol×K | 142.70 | NIST |
ΔfusS | 5.24 | J/mol×K | 147.50 | NIST |
ΔfusS | 47.32 | J/mol×K | 285.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.68; 202.63] | kPa | [285.75; 421.91] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.47084e+01 | |||
Coefficient B | -3.38746e+03 | |||
Coefficient C | -6.14290e+01 | |||
Temperature range, min. | 285.75 | |||
Temperature range, max. | 421.91 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 0.68 | kPa | 285.75 | Calculated Property |
Pvap | 1.75 | kPa | 300.88 | Calculated Property |
Pvap | 4.06 | kPa | 316.01 | Calculated Property |
Pvap | 8.57 | kPa | 331.14 | Calculated Property |
Pvap | 16.71 | kPa | 346.27 | Calculated Property |
Pvap | 30.44 | kPa | 361.39 | Calculated Property |
Pvap | 52.34 | kPa | 376.52 | Calculated Property |
Pvap | 85.66 | kPa | 391.65 | Calculated Property |
Pvap | 134.25 | kPa | 406.78 | Calculated Property |
Pvap | 202.63 | kPa | 421.91 | Calculated Property |
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