Property | Value | Unit | Source |
---|---|---|---|
PAff | 666.70 | kJ/mol | NIST |
BasG | 637.00 | kJ/mol | NIST |
ΔfG° | -561.00 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-640.60; -639.90] | kJ/mol |
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ΔfH°gas | -640.60 ± 5.90 | kJ/mol | NIST |
ΔfH°gas | -639.90 ± 1.00 | kJ/mol | NIST |
ΔfH°(+) ion | 649.00 | kJ/mol | NIST |
ΔfH(+) ion,0K | 653.00 | kJ/mol | NIST |
ΔfusH° | 6.10 | kJ/mol | Joback Calculated Property |
ΔvapH° | 22.93 | kJ/mol | Joback Calculated Property |
IE | [13.02; 14.60] | eV |
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IE | 13.04 ± 0.03 | eV | NIST |
IE | 13.04 ± 0.03 | eV | NIST |
IE | 13.04 | eV | NIST |
IE | 13.02 | eV | NIST |
IE | 13.20 ± 0.10 | eV | NIST |
IE | Outlier 14.60 ± 0.10 | eV | NIST |
IE | 13.60 | eV | NIST |
log10WS | -0.70 | Crippen Calculated Property | |
logPoct/wat | 1.045 | Crippen Calculated Property | |
McVol | 30.060 | ml/mol | McGowan Calculated Property |
Pc | 5560.87 | kPa | Joback Calculated Property |
Tboil | 190.00 | K | NIST |
Tc | 430.23 | K | Joback Calculated Property |
Tfus | 152.14 | K | Joback Calculated Property |
Vc | 0.134 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [44.14; 54.09] | J/mol×K | [274.69; 430.23] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 44 46 48 50 52 54 300 350 400 | ||||
Cp,gas | 44.14 | J/mol×K | 274.69 | Joback Calculated Property |
Cp,gas | 45.94 | J/mol×K | 300.61 | Joback Calculated Property |
Cp,gas | 47.68 | J/mol×K | 326.54 | Joback Calculated Property |
Cp,gas | 49.36 | J/mol×K | 352.46 | Joback Calculated Property |
Cp,gas | 50.99 | J/mol×K | 378.38 | Joback Calculated Property |
Cp,gas | 52.57 | J/mol×K | 404.31 | Joback Calculated Property |
Cp,gas | 54.09 | J/mol×K | 430.23 | Joback Calculated Property |
ΔfusH | 6.70 | kJ/mol | 161.90 | NIST |
ΔsubH | 23.20 | kJ/mol | 144.50 | NIST |
ΔvapH | 20.00 | kJ/mol | 174.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.68] | kPa | [142.83; 201.85] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41385e+01 | |||
Coefficient B | -1.43630e+03 | |||
Coefficient C | -3.91300e+01 | |||
Temperature range, min. | 142.83 | |||
Temperature range, max. | 201.85 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 160 180 200 | ||||
Pvap | 1.33 | kPa | 142.83 | Calculated Property |
Pvap | 3.04 | kPa | 149.39 | Calculated Property |
Pvap | 6.32 | kPa | 155.95 | Calculated Property |
Pvap | 12.14 | kPa | 162.50 | Calculated Property |
Pvap | 21.85 | kPa | 169.06 | Calculated Property |
Pvap | 37.16 | kPa | 175.62 | Calculated Property |
Pvap | 60.20 | kPa | 182.18 | Calculated Property |
Pvap | 93.48 | kPa | 188.73 | Calculated Property |
Pvap | 139.90 | kPa | 195.29 | Calculated Property |
Pvap | 202.68 | kPa | 201.85 | Calculated Property |
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