Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 60.63 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 34.42 | kJ/mol | Joback Calculated Property |
ΔfusH° | 10.59 | kJ/mol | Joback Calculated Property |
ΔvapH° | 38.81 | kJ/mol | Joback Calculated Property |
IE | [10.45; 10.51] | eV |
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IE | 10.50 | eV | NIST |
IE | 10.51 | eV | NIST |
IE | 10.50 | eV | NIST |
IE | 10.45 | eV | NIST |
log10WS | -0.14 | Crippen Calculated Property | |
logPoct/wat | -0.388 | Crippen Calculated Property | |
McVol | 50.400 | ml/mol | McGowan Calculated Property |
Pc | 6239.25 | kPa | Joback Calculated Property |
Inp | [546.00; 576.00] |
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|
Inp | 576.00 | NIST | |
Inp | 559.00 | NIST | |
Inp | 552.00 | NIST | |
Inp | 576.00 | NIST | |
Inp | 559.00 | NIST | |
Inp | 569.00 | NIST | |
Inp | 552.00 | NIST | |
Inp | 546.00 | NIST | |
Inp | 559.00 | NIST | |
Inp | 566.00 | NIST | |
Inp | 546.00 | NIST | |
I | [1320.00; 1357.00] |
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|
I | 1343.00 | NIST | |
I | 1334.00 | NIST | |
I | 1352.00 | NIST | |
I | 1343.00 | NIST | |
I | 1334.00 | NIST | |
I | 1352.00 | NIST | |
I | 1320.00 | NIST | |
I | 1357.00 | NIST | |
Tboil | [385.00; 387.50] | K |
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Tboil | 387.50 ± 0.50 | K | NIST |
Tboil | 386.80 | K | NIST |
Tboil | 386.75 ± 0.50 | K | NIST |
Tboil | 385.00 ± 3.00 | K | NIST |
Tc | 523.88 | K | Joback Calculated Property |
Tfus | 221.35 ± 0.30 | K | NIST |
Vc | 0.184 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [81.35; 101.24] | J/mol×K | [350.34; 523.88] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 80 85 90 95 100 350 400 450 500 | ||||
Cp,gas | 81.35 | J/mol×K | 350.34 | Joback Calculated Property |
Cp,gas | 85.08 | J/mol×K | 379.26 | Joback Calculated Property |
Cp,gas | 88.64 | J/mol×K | 408.19 | Joback Calculated Property |
Cp,gas | 92.02 | J/mol×K | 437.11 | Joback Calculated Property |
Cp,gas | 95.25 | J/mol×K | 466.04 | Joback Calculated Property |
Cp,gas | 98.32 | J/mol×K | 494.96 | Joback Calculated Property |
Cp,gas | 101.24 | J/mol×K | 523.88 | Joback Calculated Property |
ΔvapH | 42.00 | kJ/mol | 340.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [3.63e-03; 6558.50] | kPa | [221.35; 580.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.46079e+01 | |||
Coefficient B | -7.44693e+03 | |||
Coefficient C | -8.68936e+00 | |||
Coefficient D | 6.86908e-06 | |||
Temperature range, min. | 221.35 | |||
Temperature range, max. | 580.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 300 400 500 | ||||
Pvap | 3.63e-03 | kPa | 221.35 | Calculated Property |
Pvap | 0.17 | kPa | 261.20 | Calculated Property |
Pvap | 2.46 | kPa | 301.05 | Calculated Property |
Pvap | 17.97 | kPa | 340.90 | Calculated Property |
Pvap | 82.41 | kPa | 380.75 | Calculated Property |
Pvap | 275.69 | kPa | 420.60 | Calculated Property |
Pvap | 739.66 | kPa | 460.45 | Calculated Property |
Pvap | 1696.22 | kPa | 500.30 | Calculated Property |
Pvap | 3474.37 | kPa | 540.15 | Calculated Property |
Pvap | 6558.50 | kPa | 580.00 | Calculated Property |
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