Property | Value | Unit | Source |
---|---|---|---|
EA | [0.73; 1.28] | eV |
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EA | 0.73 ± 0.01 | eV | NIST |
EA | 0.77 | eV | NIST |
EA | 1.28 | eV | NIST |
IE | [8.90; 10.00] | eV |
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IE | 9.20 | eV | NIST |
IE | 10.00 | eV | NIST |
IE | 8.90 ± 0.10 | eV | NIST |
IE | 8.92 ± 0.06 | eV | NIST |
IE | 9.80 ± 0.04 | eV | NIST |
IE | 9.00 | eV | NIST |
Tfus | [1074.00; 1074.00] | K |
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Tfus | 1074.00 | K | Ultraso... |
Tfus | 1074.00 | K | Densiti... |
Ttriple | 1074.00 | K | Phase-b... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
ρs | [1882.00; 1931.20] | kg/m3 | [1013.00; 1073.00] | ![]() |
T(K) Solid Density (kg/m3) 1880 1890 1900 1910 1920 1930 1020 1040 1060 | ||||
ρs | 1931.20 | kg/m3 | 1013.00 | Density... |
ρs | 1905.80 | kg/m3 | 1023.00 | Density... |
ρs | 1890.40 | kg/m3 | 1033.00 | Density... |
ρs | 1888.30 | kg/m3 | 1043.00 | Density... |
ρs | 1882.00 | kg/m3 | 1053.00 | Density... |
ρs | 1884.90 | kg/m3 | 1063.00 | Density... |
ρs | 1889.80 | kg/m3 | 1073.00 | Density... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.04; 101.33] | kPa | [1073.90; 1738.20] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.63209e+01 | |||
Coefficient B | -1.94159e+04 | |||
Coefficient C | -7.90800e+01 | |||
Temperature range, min. | 1073.90 | |||
Temperature range, max. | 1738.20 | |||
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 1200 1400 1600 | ||||
Pvap | 0.04 | kPa | 1073.90 | Calculated Property |
Pvap | 0.16 | kPa | 1147.71 | Calculated Property |
Pvap | 0.51 | kPa | 1221.52 | Calculated Property |
Pvap | 1.43 | kPa | 1295.33 | Calculated Property |
Pvap | 3.56 | kPa | 1369.14 | Calculated Property |
Pvap | 8.05 | kPa | 1442.96 | Calculated Property |
Pvap | 16.71 | kPa | 1516.77 | Calculated Property |
Pvap | 32.31 | kPa | 1590.58 | Calculated Property |
Pvap | 58.76 | kPa | 1664.39 | Calculated Property |
Pvap | 101.33 | kPa | 1738.20 | Calculated Property |
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