| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.0316 | Relay (1.0) Calculated Property | |
| EA | [1.30; 1.30] | eV |
|
| EA | 1.30 ± 0.03 | eV | NIST |
| EA | 1.30 ± 0.00 | eV | NIST |
| EA | 1.30 ± 0.01 | eV | NIST |
| EA | 1.30 ± 0.20 | eV | NIST |
| ΔfH°gas | 284.90 ± 0.80 | kJ/mol | NIST |
| IE | [7.50; 7.80] | eV |
|
| IE | 7.58 | eV | NIST |
| IE | 7.58 | eV | NIST |
| IE | 7.57 | eV | NIST |
| IE | 7.50 | eV | NIST |
| IE | 7.62 ± 0.07 | eV | NIST |
| IE | 7.57 | eV | NIST |
| IE | 7.50 ± 0.30 | eV | NIST |
| IE | 7.58 | eV | NIST |
| IE | Outlier 7.80 ± 0.20 | eV | NIST |
| IE | 7.60 | eV | NIST |
| IE | 7.51 ± 0.07 | eV | NIST |
| IE | 7.58 | eV | NIST |
| IE | 7.53 | eV | NIST |
| Pc | 2752.34 | kPa | Relay (1.0-beta) Calculated Property |
| S°gas,1 bar | 173.00 ± 0.00 | J/mol×K | NIST |
| S°solid,1 bar | 42.55 ± 0.20 | J/mol×K | NIST |
| Tboil | 542.51 | K | Relay (1.0) Calculated Property |
| Tc | 811.99 | K | Relay (1.0) Calculated Property |
| Tfus | 724.19 | K | Relay (1.0) Calculated Property |
| Vc | 0.134 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, 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.
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Crystal | Pressure, kPa - Crystal | Isobaric coefficient of expansion, 1/K - Crystal |
| 300.00 | 101.33 | 0.0000 |
| Reference | ||
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.00e-03; 110.75] | kPa | [1283.00; 2453.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.66364e+01 | |||
| Coefficient B | -2.82950e+04 | |||
| Coefficient C | -8.12200e+01 | |||
| Temperature range, min. | 1283.00 | |||
| Temperature range, max. | 2453.15 | |||
| Pvap | 1.00e-03 | kPa | 1283.00 | Calculated Property |
| Pvap | 9.96e-03 | kPa | 1413.02 | Calculated Property |
| Pvap | 0.07 | kPa | 1543.03 | Calculated Property |
| Pvap | 0.32 | kPa | 1673.05 | Calculated Property |
| Pvap | 1.23 | kPa | 1803.07 | Calculated Property |
| Pvap | 3.89 | kPa | 1933.08 | Calculated Property |
| Pvap | 10.59 | kPa | 2063.10 | Calculated Property |
| Pvap | 25.50 | kPa | 2193.12 | Calculated Property |
| Pvap | 55.45 | kPa | 2323.13 | Calculated Property |
| Pvap | 110.75 | kPa | 2453.15 | Calculated Property |
| Pvap | [0.92; 82.43] | kPa | [1823.00; 2425.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 9.10219e+00 | |||
| Coefficient B | -5.76920e+03 | |||
| Coefficient C | -1.19495e+03 | |||
| Reference | Hartmann and Schneider, 1929 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 1823.00 | |||
| Temperature range, max. | 2425.00 | |||
| Pvap | 0.92 | kPa | 1823.00 | Calculated Property |
| Pvap | 2.23 | kPa | 1889.89 | Calculated Property |
| Pvap | 4.62 | kPa | 1956.78 | Calculated Property |
| Pvap | 8.50 | kPa | 2023.67 | Calculated Property |
| Pvap | 14.30 | kPa | 2090.56 | Calculated Property |
| Pvap | 22.38 | kPa | 2157.44 | Calculated Property |
| Pvap | 33.04 | kPa | 2224.33 | Calculated Property |
| Pvap | 46.51 | kPa | 2291.22 | Calculated Property |
| Pvap | 62.95 | kPa | 2358.11 | Calculated Property |
| Pvap | 82.43 | kPa | 2425.00 | 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.
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