| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6666 | Relay (1.0) Calculated Property | |
| ΔfH°gas | -261.29 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 15.79 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 68.98 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.60 | eV | Relay (1.0) Calculated Property |
| log10WS | [-0.70; -0.70] |
|
|
| log10WS | -0.70 | Aq. Solubility Prediction | |
| log10WS | -0.70 | Estimated Solubility | |
| logPoct/wat | 1.058 | Crippen Calculated Property | |
| McVol | 111.560 | ml/mol | McGowan Calculated Property |
| Pc | 4005.77 | kPa | Joback Calculated Property |
| Inp | [1185.00; 1245.30] |
|
|
| Inp | 1210.00 | NIST | |
| Inp | 1214.00 | NIST | |
| Inp | 1191.60 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1221.00 | NIST | |
| Inp | 1223.00 | NIST | |
| Inp | 1226.00 | NIST | |
| Inp | 1245.30 | NIST | |
| Inp | 1229.00 | NIST | |
| Inp | 1221.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1220.00 | NIST | |
| Inp | 1213.00 | NIST | |
| Inp | 1226.00 | NIST | |
| Inp | 1226.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1221.00 | NIST | |
| Inp | 1220.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1191.60 | NIST | |
| I | [2080.00; 2144.00] |
|
|
| I | 2103.00 | NIST | |
| I | 2087.00 | NIST | |
| I | 2144.00 | NIST | |
| I | 2126.00 | NIST | |
| I | 2142.00 | NIST | |
| I | 2107.00 | NIST | |
| I | 2080.00 | NIST | |
| I | 2115.00 | NIST | |
| I | 2100.00 | NIST | |
| I | 2139.00 | NIST | |
| I | 2103.00 | NIST | |
| I | 2115.00 | NIST | |
| Tboil | [510.20; 518.20] | K |
|
| Tboil | 510.20 | K | NIST |
| Tboil | 518.20 | K | NIST |
| Tc | 749.40 | K | DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development |
| Tfus | 285.90 | K | Aq. Solubility Prediction |
Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation 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,gas | [245.88; 300.95] | J/mol×K | [523.72; 719.69] | |
| Cp,gas | 245.88 | J/mol×K | 523.72 | Joback Calculated Property |
| Cp,gas | 256.37 | J/mol×K | 556.38 | Joback Calculated Property |
| Cp,gas | 266.32 | J/mol×K | 589.04 | Joback Calculated Property |
| Cp,gas | 275.73 | J/mol×K | 621.70 | Joback Calculated Property |
| Cp,gas | 284.64 | J/mol×K | 654.37 | Joback Calculated Property |
| Cp,gas | 293.04 | J/mol×K | 687.03 | Joback Calculated Property |
| Cp,gas | 300.95 | J/mol×K | 719.69 | Joback Calculated Property |
| Cp,liquid | 294.63 | J/mol×K | 298.15 | NIST |
| η | [0.0001115; 0.0104901] | Pa×s | [289.39; 523.72] | |
| η | 0.0104901 | Pa×s | 289.39 | Joback Calculated Property |
| η | 0.0031358 | Pa×s | 328.44 | Joback Calculated Property |
| η | 0.0012117 | Pa×s | 367.50 | Joback Calculated Property |
| η | 0.0005620 | Pa×s | 406.56 | Joback Calculated Property |
| η | 0.0002983 | Pa×s | 445.61 | Joback Calculated Property |
| η | 0.0001753 | Pa×s | 484.67 | Joback Calculated Property |
| η | 0.0001115 | Pa×s | 523.72 | Joback Calculated Property |
| ΔvapH | 66.00 | kJ/mol | 435.00 | NIST |
| ρl | [1081.00; 1107.00] | kg/m3 | [293.15; 323.15] | |
| ρl | 1107.00 | kg/m3 | 293.15 | Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures |
| ρl | 1103.00 | kg/m3 | 298.15 | Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures |
| ρl | 1103.41 | kg/m3 | 298.15 | THERMODYNAMICS OF MIXTURES CONTAINING ALKOXYETHANOLS. XXVIII. LIQUID-LIQUID EQUILIBRIA FOR 2-PHENOXYETHANOL + SELECTED ALKANES |
| ρl | 1099.00 | kg/m3 | 303.15 | Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures |
| ρl | 1090.00 | kg/m3 | 313.15 | Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures |
| ρl | 1081.00 | kg/m3 | 323.15 | Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [394.33; 547.68] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.55600e+01 | |||
| Coefficient B | -4.77760e+03 | |||
| Coefficient C | -8.15080e+01 | |||
| Temperature range, min. | 394.33 | |||
| Temperature range, max. | 547.68 | |||
| Pvap | 1.33 | kPa | 394.33 | Calculated Property |
| Pvap | 2.93 | kPa | 411.37 | Calculated Property |
| Pvap | 5.98 | kPa | 428.41 | Calculated Property |
| Pvap | 11.39 | kPa | 445.45 | Calculated Property |
| Pvap | 20.48 | kPa | 462.49 | Calculated Property |
| Pvap | 35.04 | kPa | 479.52 | Calculated Property |
| Pvap | 57.36 | kPa | 496.56 | Calculated Property |
| Pvap | 90.30 | kPa | 513.60 | Calculated Property |
| Pvap | 137.37 | kPa | 530.64 | Calculated Property |
| Pvap | 202.65 | kPa | 547.68 | Calculated Property |
Find more compounds similar to Ethanol, 2-phenoxy-.
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