| Property | Value | Unit | Source |
|---|---|---|---|
| ω | -0.1670 | KDB | |
| ΔfG° | 31.86 | kJ/mol | KDB |
| ΔfH°gas | [61.34; 61.38] | kJ/mol |
|
| ΔfH°gas | 61.34 | kJ/mol | KDB |
| ΔfH°gas | 61.38 ± 0.04 | kJ/mol | NIST |
| IE | [10.40; 14.84] | eV |
|
| IE | 10.44 | eV | NIST |
| IE | 10.44 | eV | NIST |
| IE | 10.43 ± 0.08 | eV | NIST |
| IE | 10.47 ± 0.05 | eV | NIST |
| IE | 10.40 | eV | NIST |
| IE | 10.44 | eV | NIST |
| IE | 10.49 ± 0.01 | eV | NIST |
| IE | 10.44 ± 0.01 | eV | NIST |
| IE | Outlier 14.84 ± 0.00 | eV | NIST |
| Pc | 172000.00 | kPa | KDB |
| S°gas,1 bar | 174.97 ± 0.01 | J/mol×K | NIST |
| S°liquid | 75.90 ± 0.12 | J/mol×K | NIST |
| Tboil | [629.70; 629.88] | K |
|
| Tboil | 629.88 | K | KDB |
| Tboil | 629.81 ± 0.01 | K | NIST |
| Tboil | 629.70 ± 0.50 | K | NIST |
| Tc | [0.00; 1750.00] | K |
|
| Tc | 1750.00 | K | KDB |
| Tc | 0.00 | K | NIST |
| Tfus | [234.29; 234.50] | K |
|
| Tfus | 234.29 | K | Determination of melting temperatures in hydrocarbon mixtures by differential scanning calorimetry |
| Tfus | 234.32 | K | KDB |
| Tfus | 234.30 ± 0.01 | K | NIST |
| Tfus | 234.31 ± 0.01 | K | NIST |
| Tfus | 234.50 ± 0.20 | K | NIST |
| Ttriple | [234.29; 234.31] | K |
|
| Ttriple | 234.31 | K | KDB |
| Ttriple | 234.30 ± 0.00 | K | NIST |
| Ttriple | 234.29 ± 0.20 | K | NIST |
| Vc | 0.043 | m3/kmol | KDB |
| Zc | 0.5083020 | KDB |
Cheméo can also estimate Enthalpy of vaporization at standard conditions, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.93e-07; 159643.00] | kPa | [234.31; 1735.00] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.61630e+01 | |||
| Coefficient B | -7.24765e+03 | |||
| Coefficient C | -2.05000e+00 | |||
| Temperature range, min. | 234.31 | |||
| Temperature range, max. | 1735.00 | |||
| Pvap | 2.93e-07 | kPa | 234.31 | Calculated Property |
| Pvap | 0.14 | kPa | 401.05 | Calculated Property |
| Pvap | 28.57 | kPa | 567.80 | Calculated Property |
| Pvap | 527.64 | kPa | 734.54 | Calculated Property |
| Pvap | 3304.85 | kPa | 901.28 | Calculated Property |
| Pvap | 11659.62 | kPa | 1068.03 | Calculated Property |
| Pvap | 29247.81 | kPa | 1234.77 | Calculated Property |
| Pvap | 58928.42 | kPa | 1401.51 | Calculated Property |
| Pvap | 102276.84 | kPa | 1568.26 | Calculated Property |
| Pvap | 159643.00 | kPa | 1735.00 | Calculated Property |
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.