Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -5094.00 ± 4.80 | kJ/mol | NIST |
ΔfG° | -257.16 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -487.30 ± 4.90 | kJ/mol | NIST |
ΔfH°solid | -626.60 ± 4.80 | kJ/mol | NIST |
ΔfusH° | 24.65 | kJ/mol | Joback Calculated Property |
ΔsubH° | [139.30; 139.30] | kJ/mol |
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ΔsubH° | 139.30 ± 0.90 | kJ/mol | NIST |
ΔsubH° | 139.30 | kJ/mol | NIST |
ΔsubH° | 139.30 ± 0.90 | kJ/mol | NIST |
ΔvapH° | [105.40; 107.00] | kJ/mol |
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ΔvapH° | 107.00 ± 2.20 | kJ/mol | NIST |
ΔvapH° | 105.40 ± 1.80 | kJ/mol | NIST |
log10WS | -1.70 | Crippen Calculated Property | |
logPoct/wat | 1.312 | Crippen Calculated Property | |
McVol | 135.320 | ml/mol | McGowan Calculated Property |
Pc | 3079.57 | kPa | Joback Calculated Property |
Inp | 1313.00 | NIST | |
I | [2366.00; 2366.00] |
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|
I | 2366.00 | NIST | |
I | 2366.00 | NIST | |
Tboil | 566.80 | K | Joback Calculated Property |
Tc | 752.00 | K | Critica... |
Tfus | 331.60 | K | Thermod... |
Ttriple | 332.70 ± 0.10 | K | NIST |
Vc | 0.521 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [344.83; 400.10] | J/mol×K | [566.80; 723.62] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 340 350 360 370 380 390 400 600 650 700 | ||||
Cp,gas | 344.83 | J/mol×K | 566.80 | Joback Calculated Property |
Cp,gas | 354.99 | J/mol×K | 592.94 | Joback Calculated Property |
Cp,gas | 364.75 | J/mol×K | 619.07 | Joback Calculated Property |
Cp,gas | 374.14 | J/mol×K | 645.21 | Joback Calculated Property |
Cp,gas | 383.15 | J/mol×K | 671.35 | Joback Calculated Property |
Cp,gas | 391.80 | J/mol×K | 697.49 | Joback Calculated Property |
Cp,gas | 400.10 | J/mol×K | 723.62 | Joback Calculated Property |
Cp,liquid | [371.35; 396.17] | J/mol×K | [333.65; 353.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 370 375 380 385 390 395 335 340 345 350 | ||||
Cp,liquid | 371.35 | J/mol×K | 333.65 | Heat Ca... |
Cp,liquid | 373.24 | J/mol×K | 335.15 | Heat Ca... |
Cp,liquid | 375.13 | J/mol×K | 336.65 | Heat Ca... |
Cp,liquid | 377.03 | J/mol×K | 338.15 | Heat Ca... |
Cp,liquid | 378.93 | J/mol×K | 339.65 | Heat Ca... |
Cp,liquid | 380.83 | J/mol×K | 341.15 | Heat Ca... |
Cp,liquid | 382.74 | J/mol×K | 342.65 | Heat Ca... |
Cp,liquid | 384.65 | J/mol×K | 344.15 | Heat Ca... |
Cp,liquid | 386.56 | J/mol×K | 345.65 | Heat Ca... |
Cp,liquid | 388.48 | J/mol×K | 347.15 | Heat Ca... |
Cp,liquid | 390.40 | J/mol×K | 348.65 | Heat Ca... |
Cp,liquid | 392.32 | J/mol×K | 350.15 | Heat Ca... |
Cp,liquid | 394.24 | J/mol×K | 351.65 | Heat Ca... |
Cp,liquid | 396.17 | J/mol×K | 353.15 | Heat Ca... |
η | [0.0000464; 0.0502473] | Pa×s | [301.56; 566.80] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 0.01 0.02 0.03 0.04 0.05 300 400 500 | ||||
η | 0.0502473 | Pa×s | 301.56 | Joback Calculated Property |
η | 0.0074475 | Pa×s | 345.77 | Joback Calculated Property |
η | 0.0017017 | Pa×s | 389.97 | Joback Calculated Property |
η | 0.0005252 | Pa×s | 434.18 | Joback Calculated Property |
η | 0.0002014 | Pa×s | 478.39 | Joback Calculated Property |
η | 0.0000908 | Pa×s | 522.59 | Joback Calculated Property |
η | 0.0000464 | Pa×s | 566.80 | Joback Calculated Property |
ΔfusH | [36.10; 36.10] | kJ/mol | [332.80; 332.80] | ![]() |
ΔfusH | 36.10 | kJ/mol | 332.80 | NIST |
ΔfusH | 36.10 | kJ/mol | 332.80 | NIST |
ΔvapH | [101.00; 104.90] | kJ/mol | [298.15; 356.00] | ![]() |
ΔvapH | 104.90 | kJ/mol | 298.15 | Vaporiz... |
ΔvapH | 101.00 | kJ/mol | 356.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 445.20 | K | 2.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [422.32; 537.37] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.97169e+01 | |||
Coefficient B | -6.40965e+03 | |||
Coefficient C | -9.24240e+01 | |||
Temperature range, min. | 422.32 | |||
Temperature range, max. | 537.37 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 | ||||
Pvap | 1.33 | kPa | 422.32 | Calculated Property |
Pvap | 2.75 | kPa | 435.10 | Calculated Property |
Pvap | 5.39 | kPa | 447.89 | Calculated Property |
Pvap | 10.08 | kPa | 460.67 | Calculated Property |
Pvap | 18.08 | kPa | 473.45 | Calculated Property |
Pvap | 31.22 | kPa | 486.24 | Calculated Property |
Pvap | 52.08 | kPa | 499.02 | Calculated Property |
Pvap | 84.20 | kPa | 511.80 | Calculated Property |
Pvap | 132.33 | kPa | 524.59 | Calculated Property |
Pvap | 202.64 | kPa | 537.37 | Calculated Property |
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