| Property | Value | Unit | Source |
|---|---|---|---|
| ΔvapH° | 26.00 ± 0.60 | kJ/mol | NIST |
| IE | [9.40; 10.57] | eV |
|
| IE | 9.80 ± 0.04 | eV | NIST |
| IE | 9.80 ± 0.03 | eV | NIST |
| IE | 9.60 | eV | NIST |
| IE | 9.99 ± 0.03 | eV | NIST |
| IE | 9.79 ± 0.04 | eV | NIST |
| IE | 9.40 ± 0.10 | eV | NIST |
| IE | 9.85 ± 0.16 | eV | NIST |
| IE | 9.74 ± 0.05 | eV | NIST |
| IE | 9.86 ± 0.02 | eV | NIST |
| IE | 9.85 ± 0.16 | eV | NIST |
| IE | 9.90 ± 0.10 | eV | NIST |
| IE | 9.98 ± 0.03 | eV | NIST |
| IE | 10.29 | eV | NIST |
| IE | 10.40 | eV | NIST |
| IE | Outlier 10.57 | eV | NIST |
| logPoct/wat | 1.954 | Crippen Calculated Property | |
| Pc | 2821.00 ± 1.00 | kPa | NIST |
| Inp | [419.00; 430.00] |
|
|
| Inp | 428.10 | NIST | |
| Inp | 425.90 | NIST | |
| Inp | 429.80 | NIST | |
| Inp | 428.10 | NIST | |
| Inp | 428.00 | NIST | |
| Inp | 428.40 | NIST | |
| Inp | 427.60 | NIST | |
| Inp | 426.80 | NIST | |
| Inp | 425.90 | NIST | |
| Inp | 424.80 | NIST | |
| Inp | 423.60 | NIST | |
| Inp | 422.40 | NIST | |
| Inp | 430.00 | NIST | |
| Inp | 429.80 | NIST | |
| Inp | 429.40 | NIST | |
| Inp | 429.00 | NIST | |
| Inp | 420.00 | NIST | |
| Inp | 420.00 | NIST | |
| Inp | Outlier 419.00 | NIST | |
| S°liquid | [272.04; 277.27] | J/mol×K |
|
| S°liquid | 272.04 | J/mol×K | NIST |
| S°liquid | 277.27 | J/mol×K | NIST |
| Tboil | [299.00; 299.70] | K |
|
| Tboil | 299.70 | K | NIST |
| Tboil | 299.00 ± 3.00 | K | NIST |
| Tc | 448.64 ± 0.03 | K | NIST |
| Tfus | 229.50 | K | Relay (1.0) Calculated Property |
| Ttriple | [165.92; 174.12] | K |
|
| Ttriple | Outlier 165.92 ± 0.01 | K | NIST |
| Ttriple | 171.01 ± 0.01 | K | NIST |
| Ttriple | 174.07 ± 0.01 | K | NIST |
| Ttriple | 170.98 ± 0.01 | K | NIST |
| Ttriple | 174.04 ± 0.01 | K | NIST |
| Ttriple | 171.04 ± 0.02 | K | NIST |
| Ttriple | 174.12 ± 0.02 | K | NIST |
| Vc | 0.362 ± 0.008 | m3/kmol | NIST |
Cheméo can also estimate Enthalpy of formation 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 |
|---|---|---|---|---|
| Cp,liquid | [164.56; 197.90] | J/mol×K | [177.45; 290.00] | |
| Cp,liquid | 164.56 | J/mol×K | 177.45 | NIST |
| Cp,liquid | 189.84 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 197.90 | J/mol×K | 290.00 | NIST |
| ΔfusH | [6.74; 6.74] | kJ/mol | [174.00; 174.00] | |
| ΔfusH | 6.74 | kJ/mol | 174.00 | NIST |
| ΔfusH | 6.74 | kJ/mol | 174.00 | NIST |
| ΔvapH | [24.20; 24.20] | kJ/mol | [299.00; 299.80] | |
| ΔvapH | 24.20 ± 0.10 | kJ/mol | 299.00 | NIST |
| ΔvapH | 24.20 | kJ/mol | 299.80 | NIST |
| ΔvapS | 80.73 | J/mol×K | 299.80 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [214.68; 321.34] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.38189e+01 | |||
| Coefficient B | -2.44422e+03 | |||
| Coefficient C | -3.40420e+01 | |||
| Temperature range, min. | 214.68 | |||
| Temperature range, max. | 321.34 | |||
| Pvap | 1.33 | kPa | 214.68 | Calculated Property |
| Pvap | 3.07 | kPa | 226.53 | Calculated Property |
| Pvap | 6.41 | kPa | 238.38 | Calculated Property |
| Pvap | 12.34 | kPa | 250.23 | Calculated Property |
| Pvap | 22.21 | kPa | 262.08 | Calculated Property |
| Pvap | 37.72 | kPa | 273.94 | Calculated Property |
| Pvap | 60.94 | kPa | 285.79 | Calculated Property |
| Pvap | 94.29 | kPa | 297.64 | Calculated Property |
| Pvap | 140.51 | kPa | 309.49 | Calculated Property |
| Pvap | 202.62 | kPa | 321.34 | Calculated Property |
Find more compounds similar to Silane, tetramethyl-.
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