Property | Value | Unit | Source |
---|---|---|---|
PAff | 803.60 | kJ/mol | NIST |
BasG | 772.80 | kJ/mol | NIST |
ΔcH°liquid | [-2562.30; -2560.60] | kJ/mol |
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ΔcH°liquid | -2560.60 ± 1.30 | kJ/mol | NIST |
ΔcH°liquid | -2562.30 ± 0.75 | kJ/mol | NIST |
EA | 0.01 ± 0.00 | eV | NIST |
ΔfG° | 113.54 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [22.80; 24.30] | kJ/mol |
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ΔfH°gas | 22.80 | kJ/mol | NIST |
ΔfH°gas | 24.30 ± 1.80 | kJ/mol | NIST |
ΔfH°liquid | [-13.80; -12.20] | kJ/mol |
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ΔfH°liquid | -13.80 | kJ/mol | NIST |
ΔfH°liquid | -12.20 ± 0.84 | kJ/mol | NIST |
ΔfusH° | 4.10 | kJ/mol | Joback Calculated Property |
ΔvapH° | [36.50; 37.22] | kJ/mol |
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ΔvapH° | 37.22 | kJ/mol | NIST |
ΔvapH° | 36.70 | kJ/mol | NIST |
ΔvapH° | 36.60 | kJ/mol | NIST |
ΔvapH° | 37.13 ± 0.02 | kJ/mol | NIST |
ΔvapH° | 36.50 | kJ/mol | NIST |
IE | [11.30; 11.74] | eV |
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IE | 11.30 | eV | NIST |
IE | 11.74 | eV | NIST |
IE | 11.74 | eV | NIST |
log10WS | -1.12 | Crippen Calculated Property | |
logPoct/wat | 1.166 | Crippen Calculated Property | |
McVol | 68.600 | ml/mol | McGowan Calculated Property |
Pc | 3815.10 | kPa | Joback Calculated Property |
Inp | [590.00; 643.00] |
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|
Inp | 638.00 | NIST | |
Inp | 643.00 | NIST | |
Inp | 594.40 | NIST | |
Inp | 592.00 | NIST | |
Inp | 590.00 | NIST | |
Inp | 626.00 | NIST | |
Inp | 600.00 | NIST | |
Inp | 623.00 | NIST | |
Inp | 623.00 | NIST | |
Inp | 637.20 | NIST | |
I | [993.00; 1010.00] |
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|
I | 993.00 | NIST | |
I | 1009.00 | NIST | |
I | 1010.00 | NIST | |
Tboil | [374.70; 382.00] | K |
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Tboil | 380.70 | K | NIST |
Tboil | 377.00 | K | NIST |
Tboil | 374.70 ± 1.50 | K | NIST |
Tboil | 374.70 ± 1.00 | K | NIST |
Tboil | 376.00 ± 3.00 | K | NIST |
Tboil | 376.70 ± 7.00 | K | NIST |
Tboil | 374.70 ± 3.00 | K | NIST |
Tboil | 375.00 ± 3.00 | K | NIST |
Tboil | 376.70 ± 2.00 | K | NIST |
Tboil | 376.00 ± 3.00 | K | NIST |
Tboil | 382.00 ± 5.00 | K | NIST |
Tboil | 376.50 ± 3.00 | K | NIST |
Tboil | 376.90 ± 0.50 | K | NIST |
Tboil | 380.00 ± 5.00 | K | NIST |
Tboil | 377.00 ± 0.30 | K | NIST |
Tboil | 381.00 ± 4.00 | K | NIST |
Tboil | 380.70 ± 6.00 | K | NIST |
Tboil | 376.40 ± 2.00 | K | NIST |
Tboil | 381.00 ± 5.00 | K | NIST |
Tc | 589.40 | K | Joback Calculated Property |
Tfus | [201.65; 201.65] | K |
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Tfus | 201.65 ± 0.50 | K | NIST |
Tfus | 201.65 ± 0.50 | K | NIST |
Vc | 0.280 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [118.18; 154.25] | J/mol×K | [392.56; 589.40] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 120 130 140 150 400 450 500 550 | ||||
Cp,gas | 118.18 | J/mol×K | 392.56 | Joback Calculated Property |
Cp,gas | 124.86 | J/mol×K | 425.37 | Joback Calculated Property |
Cp,gas | 131.27 | J/mol×K | 458.17 | Joback Calculated Property |
Cp,gas | 137.40 | J/mol×K | 490.98 | Joback Calculated Property |
Cp,gas | 143.27 | J/mol×K | 523.79 | Joback Calculated Property |
Cp,gas | 148.89 | J/mol×K | 556.60 | Joback Calculated Property |
Cp,gas | 154.25 | J/mol×K | 589.40 | Joback Calculated Property |
Cp,liquid | 156.20 | J/mol×K | 297.00 | NIST |
ΔvapH | [32.39; 37.50] | kJ/mol | [327.50; 377.00] | ![]() |
ΔvapH | 37.50 | kJ/mol | 327.50 | NIST |
ΔvapH | 35.90 | kJ/mol | 339.00 | NIST |
ΔvapH | 32.39 | kJ/mol | 377.00 | NIST |
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