Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | [-6463.20; -6463.00] | kJ/mol |
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ΔcH°solid | -6463.20 ± 2.60 | kJ/mol | NIST |
ΔcH°solid | -6463.00 ± 1.00 | kJ/mol | NIST |
ΔfG° | 249.96 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [108.60; 108.80] | kJ/mol |
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ΔfH°gas | 108.80 ± 3.00 | kJ/mol | NIST |
ΔfH°gas | 108.60 | kJ/mol | NIST |
ΔfH°solid | [25.90; 26.10] | kJ/mol |
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ΔfH°solid | 26.10 ± 3.00 | kJ/mol | NIST |
ΔfH°solid | 25.90 ± 1.20 | kJ/mol | NIST |
ΔfusH° | 18.53 | kJ/mol | Solid-L... |
ΔsubH° | [82.70; 82.70] | kJ/mol |
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ΔsubH° | 82.70 ± 0.30 | kJ/mol | NIST |
ΔsubH° | 82.70 ± 0.30 | kJ/mol | NIST |
ΔsubH° | 82.70 | kJ/mol | NIST |
ΔvapH° | 47.55 | kJ/mol | Joback Calculated Property |
IE | [7.50; 8.30] | eV |
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IE | 7.50 | eV | NIST |
IE | 8.30 ± 0.05 | eV | NIST |
IE | 7.71 | eV | NIST |
IE | 7.64 ± 0.03 | eV | NIST |
log10WS | -4.23 | Crippen Calculated Property | |
logPoct/wat | 3.457 | Crippen Calculated Property | |
McVol | 136.720 | ml/mol | McGowan Calculated Property |
Pc | 3005.73 | kPa | Joback Calculated Property |
Inp | [249.39; 1480.00] |
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|
Inp | 1440.80 | NIST | |
Inp | 1456.80 | NIST | |
Inp | 1472.40 | NIST | |
Inp | 1449.00 | NIST | |
Inp | 1471.00 | NIST | |
Inp | 1472.70 | NIST | |
Inp | 1472.10 | NIST | |
Inp | 1459.70 | NIST | |
Inp | 1472.70 | NIST | |
Inp | 1480.00 | NIST | |
Inp | 1459.70 | NIST | |
Inp | 1472.70 | NIST | |
Inp | 1480.00 | NIST | |
Inp | 1472.70 | NIST | |
Inp | 1472.10 | NIST | |
Inp | 1450.00 | NIST | |
Inp | 1457.00 | NIST | |
Inp | 1448.00 | NIST | |
Inp | 1449.00 | NIST | |
Inp | 1457.00 | NIST | |
Inp | 1449.00 | NIST | |
Inp | Outlier 249.39 | NIST | |
Inp | Outlier 252.00 | NIST | |
Inp | Outlier 249.52 | NIST | |
Inp | Outlier 250.70 | NIST | |
Inp | Outlier 249.52 | NIST | |
Inp | 1457.00 | NIST | |
Inp | 1472.70 | NIST | |
Inp | 1459.70 | NIST | |
Inp | 1450.00 | NIST | |
Inp | 1440.80 | NIST | |
Inp | Outlier 250.70 | NIST | |
I | [1989.00; 1989.00] |
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|
I | 1989.00 | NIST | |
I | 1989.00 | NIST | |
S°solid,1 bar | 224.72 | J/mol×K | NIST |
Tboil | 529.58 | K | Joback Calculated Property |
Tc | 761.14 | K | Joback Calculated Property |
Tfus | 335.00 ± 2.00 | K | NIST |
Ttriple | [336.32; 336.32] | K |
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Ttriple | 336.32 ± 0.02 | K | NIST |
Ttriple | 336.32 ± 0.02 | K | NIST |
Vc | 0.521 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [296.31; 371.48] | J/mol×K | [529.58; 761.14] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 300 320 340 360 600 700 | ||||
Cp,gas | 296.31 | J/mol×K | 529.58 | Joback Calculated Property |
Cp,gas | 311.16 | J/mol×K | 568.17 | Joback Calculated Property |
Cp,gas | 325.00 | J/mol×K | 606.77 | Joback Calculated Property |
Cp,gas | 337.89 | J/mol×K | 645.36 | Joback Calculated Property |
Cp,gas | 349.89 | J/mol×K | 683.95 | Joback Calculated Property |
Cp,gas | 361.06 | J/mol×K | 722.55 | Joback Calculated Property |
Cp,gas | 371.48 | J/mol×K | 761.14 | Joback Calculated Property |
Cp,solid | [241.80; 242.80] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,solid | 242.80 | J/mol×K | 298.15 | NIST |
Cp,solid | 241.80 | J/mol×K | 298.15 | NIST |
η | [0.0002960; 0.0012561] | Pa×s | [309.16; 529.58] | ![]() |
T(K) Dynamic viscosity (Pa×s) 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 350 400 450 500 | ||||
η | 0.0012561 | Pa×s | 309.16 | Joback Calculated Property |
η | 0.0008686 | Pa×s | 345.90 | Joback Calculated Property |
η | 0.0006448 | Pa×s | 382.63 | Joback Calculated Property |
η | 0.0005043 | Pa×s | 419.37 | Joback Calculated Property |
η | 0.0004103 | Pa×s | 456.11 | Joback Calculated Property |
η | 0.0003443 | Pa×s | 492.84 | Joback Calculated Property |
η | 0.0002960 | Pa×s | 529.58 | Joback Calculated Property |
ΔfusH | [0.05; 18.53] | kJ/mol | [336.30; 338.20] | ![]() |
ΔfusH | 15.77 | kJ/mol | 336.30 | NIST |
ΔfusH | 15.77 | kJ/mol | 336.30 | NIST |
ΔfusH | 0.05 | kJ/mol | 336.33 | NIST |
ΔfusH | 18.53 | kJ/mol | 338.20 | NIST |
ΔsubH | [77.90; 79.60] | kJ/mol | [332.00; 336.00] | ![]() |
ΔsubH | 77.90 | kJ/mol | 332.00 | NIST |
ΔsubH | 79.60 | kJ/mol | 336.00 | NIST |
ΔvapH | [59.70; 64.80] | kJ/mol | [375.50; 375.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 60 61 62 63 64 65 | ||||
ΔvapH | 62.80 | kJ/mol | 375.50 | NIST |
ΔvapH | 64.80 | kJ/mol | 375.50 | NIST |
ΔvapH | 62.20 | kJ/mol | 375.50 | NIST |
ΔvapH | 60.70 | kJ/mol | 375.50 | NIST |
ΔvapH | 59.70 | kJ/mol | 375.50 | NIST |
ΔfusS | 46.86 | J/mol×K | 336.33 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 413.20 | K | 2.40 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [402.00; 552.34] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.58900e+01 | |||
Coefficient B | -4.93899e+03 | |||
Coefficient C | -8.54500e+01 | |||
Temperature range, min. | 402.00 | |||
Temperature range, max. | 552.34 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 550 | ||||
Pvap | 1.33 | kPa | 402.00 | Calculated Property |
Pvap | 2.91 | kPa | 418.70 | Calculated Property |
Pvap | 5.91 | kPa | 435.41 | Calculated Property |
Pvap | 11.24 | kPa | 452.11 | Calculated Property |
Pvap | 20.22 | kPa | 468.82 | Calculated Property |
Pvap | 34.63 | kPa | 485.52 | Calculated Property |
Pvap | 56.80 | kPa | 502.23 | Calculated Property |
Pvap | 89.68 | kPa | 518.93 | Calculated Property |
Pvap | 136.87 | kPa | 535.64 | Calculated Property |
Pvap | 202.66 | kPa | 552.34 | Calculated Property |
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