| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5311 | Relay (1.0) Calculated Property | |
| ΔfG° | -368.32 | kJ/mol | Relay (1.0-beta) Calculated Property |
| ΔfH°gas | -952.54 | kJ/mol | Relay (1.0) Calculated Property |
| ΔvapH° | [48.50; 53.90] | kJ/mol |
|
| ΔvapH° | 53.90 | kJ/mol | NIST |
| ΔvapH° | 52.30 | kJ/mol | NIST |
| ΔvapH° | 48.50 ± 0.30 | kJ/mol | NIST |
| IE | 9.77 | eV | NIST |
| log10WS | -1.46 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.568 | Crippen Calculated Property | |
| Pc | 2040.00 | kPa | Vapor-Liquid Critical Properties of Some Tetraalkoxysilanes |
| Inp | [847.00; 869.00] |
|
|
| Inp | Outlier 869.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 851.20 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 847.00 | NIST | |
| S°liquid | 533.10 | J/mol×K | NIST |
| Tboil | [439.70; 442.00] | K |
|
| Tboil | 439.70 ± 1.00 | K | NIST |
| Tboil | 442.00 | K | NIST |
| Tboil | 441.95 ± 0.50 | K | NIST |
| Tc | 583.88 | K | Relay (1.0) Calculated Property |
| Tfus | 191.00 ± 0.10 | K | NIST |
| Vc | 0.663 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [352.10; 364.40] | J/mol×K | [298.15; 298.15] | |
| Cp,liquid | 364.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 352.10 | J/mol×K | 298.15 | NIST |
| ΔfusH | [11.14; 13.20] | kJ/mol | [187.70; 191.00] | |
| ΔfusH | 13.20 | kJ/mol | 187.70 | NIST |
| ΔfusH | 11.14 | kJ/mol | 191.00 | NIST |
| ΔfusH | 11.14 | kJ/mol | 191.00 | NIST |
| ΔvapH | [40.90; 50.00] | kJ/mol | [365.00; 420.50] | |
| ΔvapH | 49.50 | kJ/mol | 365.00 | NIST |
| ΔvapH | 50.00 | kJ/mol | 376.50 | NIST |
| ΔvapH | 40.90 | kJ/mol | 420.50 | NIST |
| Pvap | [24.00; 53.32] | kPa | [393.40; 419.20] | |
| Pvap | 24.00 | kPa | 393.40 | Vapor-Liquid Equilibrium Measurements for Tetraethyl Orthosilicate + Ethanol at 24.00 kPa and 53.32 kPa |
| Pvap | 53.32 | kPa | 419.20 | Vapor-Liquid Equilibrium Measurements for Tetraethyl Orthosilicate + Ethanol at 24.00 kPa and 53.32 kPa |
| n0 | [1.38250; 1.38350] | [293.15; 298.15] | ||
| n0 | 1.38350 | 293.15 | Isobaric Vapor Liquid Equilibrium Data for the Binary Mixtures 2-Methyl Propan-2-ol with Tetraethoxysilane and 1-Phenyl Ethanone at 95.5 kPa | |
| n0 | 1.38250 | 298.15 | (Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa | |
| ρl | 1032.00 | kg/m3 | 293.15 | Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa |
| ΔfusS | [58.33; 70.32] | J/mol×K | [187.70; 191.00] | |
| ΔfusS | 70.32 | J/mol×K | 187.70 | NIST |
| ΔfusS | 58.33 | J/mol×K | 191.00 | NIST |
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