| Property | Value | Unit | Source |
|---|---|---|---|
| IE | [8.40; 13.75] | eV |
|
| IE | 8.80 | eV | NIST |
| IE | 8.90 | eV | NIST |
| IE | 8.40 | eV | NIST |
| IE | Outlier 13.75 | eV | NIST |
| IE | 10.21 | eV | NIST |
| IE | 8.80 | eV | NIST |
| IE | 9.27 | eV | NIST |
| Tfus | [832.00; 832.00] | K |
|
| Tfus | 832.00 | K | Ultrasonic velocity for an equimolar mixture of molten AgI and NaCl in the biphasic region |
| Tfus | 832.00 | K | Densities of a dissolving mixture of molten (AgI + NaCl) |
| Tfus | 832.00 | K | An anion effect on the separation of AgI-containing melts using sound waves |
| Ttriple | 832.00 | K | Phase-boundary potential in the two-liquid-phase (AgI + NaCl) system |
Cheméo can also estimate Normal Boiling Point Temperature, Critical Temperature, Critical Pressure, Critical Volume, Enthalpy of formation at standard conditions, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, 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 | [0.13; 101.32] | kPa | [1093.15; 1779.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39563e+01 | |||
| Coefficient B | -1.54173e+04 | |||
| Coefficient C | -1.28120e+02 | |||
| Temperature range, min. | 1093.15 | |||
| Temperature range, max. | 1779.15 | |||
| Pvap | 0.13 | kPa | 1093.15 | Calculated Property |
| Pvap | 0.43 | kPa | 1169.37 | Calculated Property |
| Pvap | 1.17 | kPa | 1245.59 | Calculated Property |
| Pvap | 2.83 | kPa | 1321.82 | Calculated Property |
| Pvap | 6.15 | kPa | 1398.04 | Calculated Property |
| Pvap | 12.22 | kPa | 1474.26 | Calculated Property |
| Pvap | 22.58 | kPa | 1550.48 | Calculated Property |
| Pvap | 39.19 | kPa | 1626.71 | Calculated Property |
| Pvap | 64.48 | kPa | 1702.93 | Calculated Property |
| Pvap | 101.32 | kPa | 1779.15 | Calculated Property |
| Pvap | [0.13; 101.59] | kPa | [1093.00; 1779.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39616e+01 | |||
| Coefficient B | -1.54216e+04 | |||
| Coefficient C | -1.27973e+02 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 1093.00 | |||
| Temperature range, max. | 1779.00 | |||
| Pvap | 0.13 | kPa | 1093.00 | Calculated Property |
| Pvap | 0.43 | kPa | 1169.22 | Calculated Property |
| Pvap | 1.17 | kPa | 1245.44 | Calculated Property |
| Pvap | 2.84 | kPa | 1321.67 | Calculated Property |
| Pvap | 6.16 | kPa | 1397.89 | Calculated Property |
| Pvap | 12.25 | kPa | 1474.11 | Calculated Property |
| Pvap | 22.63 | kPa | 1550.33 | Calculated Property |
| Pvap | 39.28 | kPa | 1626.56 | Calculated Property |
| Pvap | 64.64 | kPa | 1702.78 | Calculated Property |
| Pvap | 101.59 | kPa | 1779.00 | 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.
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