Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 272.56 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 117.83 | kJ/mol | Joback Calculated Property |
ΔfusH° | 19.32 | kJ/mol | Joback Calculated Property |
ΔvapH° | 52.63 | kJ/mol | Joback Calculated Property |
IE | [8.05; 8.80] | eV |
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IE | 8.80 ± 0.05 | eV | NIST |
IE | 8.05 ± 0.02 | eV | NIST |
log10WS | -5.03 | Crippen Calculated Property | |
logPoct/wat | 3.970 | Crippen Calculated Property | |
McVol | 160.600 | ml/mol | McGowan Calculated Property |
Pc | 2684.64 | kPa | Joback Calculated Property |
Inp | [241.94; 1546.00] |
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|
Inp | 1546.00 | NIST | |
Inp | 261.78 | NIST | |
Inp | 243.90 | NIST | |
Inp | 241.94 | NIST | |
I | [1916.00; 1950.00] |
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|
I | 1950.00 | NIST | |
I | 1916.00 | NIST | |
S°liquid | 332.60 | J/mol×K | NIST |
Tboil | [530.00; 531.00] | K |
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Tboil | 531.00 ± 4.00 | K | NIST |
Tboil | 531.00 ± 4.00 | K | NIST |
Tboil | 531.00 ± 3.00 | K | NIST |
Tboil | 531.00 ± 4.00 | K | NIST |
Tboil | 530.00 ± 4.00 | K | NIST |
Tc | 824.77 | K | Joback Calculated Property |
Tfus | 325.42 | K | Joback Calculated Property |
Ttriple | 293.09 ± 0.01 | K | NIST |
Vc | 0.604 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [371.85; 457.50] | J/mol×K | [583.04; 824.77] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 380 400 420 440 460 600 700 800 | ||||
Cp,gas | 371.85 | J/mol×K | 583.04 | Joback Calculated Property |
Cp,gas | 388.95 | J/mol×K | 623.33 | Joback Calculated Property |
Cp,gas | 404.83 | J/mol×K | 663.62 | Joback Calculated Property |
Cp,gas | 419.57 | J/mol×K | 703.90 | Joback Calculated Property |
Cp,gas | 433.22 | J/mol×K | 744.19 | Joback Calculated Property |
Cp,gas | 445.84 | J/mol×K | 784.48 | Joback Calculated Property |
Cp,gas | 457.50 | J/mol×K | 824.77 | Joback Calculated Property |
Cp,liquid | 298.06 | J/mol×K | 298.15 | NIST |
η | [0.0001716; 0.0014925] | Pa×s | [325.42; 583.04] | ![]() |
T(K) Dynamic viscosity (Pa×s) 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 400 500 | ||||
η | 0.0014925 | Pa×s | 325.42 | Joback Calculated Property |
η | 0.0008435 | Pa×s | 368.36 | Joback Calculated Property |
η | 0.0005371 | Pa×s | 411.29 | Joback Calculated Property |
η | 0.0003724 | Pa×s | 454.23 | Joback Calculated Property |
η | 0.0002751 | Pa×s | 497.17 | Joback Calculated Property |
η | 0.0002132 | Pa×s | 540.10 | Joback Calculated Property |
η | 0.0001716 | Pa×s | 583.04 | Joback Calculated Property |
ΔfusH | [2.28; 2.28] | kJ/mol | [293.09; 293.10] | ![]() |
ΔfusH | 2.28 | kJ/mol | 293.09 | NIST |
ΔfusH | 2.28 | kJ/mol | 293.10 | NIST |
ΔfusH | 2.28 | kJ/mol | 293.10 | NIST |
ΔsubH | 65.70 | kJ/mol | 285.50 | NIST |
ΔfusS | 7.78 | J/mol×K | 293.09 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [394.92; 564.87] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43603e+01 | |||
Coefficient B | -4.30779e+03 | |||
Coefficient C | -8.88100e+01 | |||
Temperature range, min. | 394.92 | |||
Temperature range, max. | 564.87 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 550 | ||||
Pvap | 1.33 | kPa | 394.92 | Calculated Property |
Pvap | 3.02 | kPa | 413.80 | Calculated Property |
Pvap | 6.25 | kPa | 432.69 | Calculated Property |
Pvap | 12.00 | kPa | 451.57 | Calculated Property |
Pvap | 21.60 | kPa | 470.45 | Calculated Property |
Pvap | 36.78 | kPa | 489.34 | Calculated Property |
Pvap | 59.69 | kPa | 508.22 | Calculated Property |
Pvap | 92.92 | kPa | 527.10 | Calculated Property |
Pvap | 139.45 | kPa | 545.99 | Calculated Property |
Pvap | 202.64 | kPa | 564.87 | Calculated Property |
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