- InChI
- InChI=1S/C8H10O/c1-2-7-5-3-4-6-8(7)9/h3-6,9H,2H2,1H3
- InChI Key
- IXQGCWUGDFDQMF-UHFFFAOYSA-N
- Formula
- C8H10O
- SMILES
- CCc1ccccc1O
- Molecular Weight1
- 122.16
- CAS
- 90-00-6
- Other Names
-
- 1-ETHYL-2-HYDROXYBENZENE
- 1-Hydroxy-2-ethylbenzene
- 2-ETHYLPHENOL
- Ethylphenol
- Florol
- NSC 10112
- PHLOROL
- Phenol, o-ethyl-
- o-Ethylphenol
- o-Hydroxyethylbenzene
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -4368.39 | kJ/mol | NIST |
| ΔfG° | -25.73 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-145.80; -145.20] | kJ/mol |
|
| ΔfH°gas | -145.80 | kJ/mol | KDB |
| ΔfH°gas | -145.20 | kJ/mol | NIST |
| ΔfH°liquid | -208.80 | kJ/mol | NIST |
| ΔfusH° | 16.30 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [63.60; 64.50] | kJ/mol |
|
| ΔvapH° | 64.50 | kJ/mol | NIST |
| ΔvapH° | 63.60 | kJ/mol | NIST |
| ΔvapH° | 63.60 | kJ/mol | NIST |
| log10WS | -1.36 | Aq. Sol... | |
| logPoct/wat | 1.955 | Crippen Calculated Property | |
| McVol | 105.690 | ml/mol | McGowan Calculated Property |
| Pc | 4409.10 | kPa | Joback Calculated Property |
| Inp | [188.30; 1177.00] |
|
|
| Inp | 1110.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1112.80 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1138.00 | NIST | |
| Inp | 1148.70 | NIST | |
| Inp | 1136.20 | NIST | |
| Inp | 1136.50 | NIST | |
| Inp | 1137.90 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1140.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1145.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1148.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | Outlier 190.00 | NIST | |
| Inp | Outlier 189.73 | NIST | |
| Inp | Outlier 188.30 | NIST | |
| Inp | Outlier 190.21 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1148.70 | NIST | |
| I | [2028.00; 2084.00] |
|
|
| I | 2079.00 | NIST | |
| I | 2069.00 | NIST | |
| I | 2068.00 | NIST | |
| I | 2054.00 | NIST | |
| I | 2059.00 | NIST | |
| I | 2050.00 | NIST | |
| I | 2071.00 | NIST | |
| I | Outlier 2028.00 | NIST | |
| I | 2084.00 | NIST | |
| I | 2063.00 | NIST | |
| I | 2068.00 | NIST | |
| I | 2044.00 | NIST | |
| I | 2044.00 | NIST | |
| I | 2079.00 | NIST | |
| I | 2063.00 | NIST | |
| Tboil | [469.20; 482.65] | K |
|
| Tboil | 477.67 | K | KDB |
| Tboil | Outlier 469.20 | K | NIST |
| Tboil | 480.20 | K | NIST |
| Tboil | 480.65 ± 3.00 | K | NIST |
| Tboil | 480.15 ± 3.00 | K | NIST |
| Tboil | 480.15 ± 2.00 | K | NIST |
| Tboil | 474.65 ± 3.00 | K | NIST |
| Tboil | 478.05 ± 2.00 | K | NIST |
| Tboil | 481.15 ± 3.00 | K | NIST |
| Tboil | 474.65 ± 4.00 | K | NIST |
| Tboil | 479.15 ± 4.00 | K | NIST |
| Tboil | 477.65 ± 3.00 | K | NIST |
| Tboil | 480.65 ± 3.00 | K | NIST |
| Tboil | 478.05 ± 3.00 | K | NIST |
| Tboil | 482.65 ± 3.00 | K | NIST |
| Tc | [702.95; 703.00] | K |
|
| Tc | 703.00 | K | KDB |
| Tc | 702.95 ± 0.30 | K | NIST |
| Tfus | [250.15; 414.65] | K |
|
| Tfus | 291.00 | K | KDB |
| Tfus | 261.65 | K | Aq. Sol... |
| Tfus | 269.84 ± 0.10 | K | NIST |
| Tfus | 255.15 ± 10.00 | K | NIST |
| Tfus | 250.15 ± 10.00 | K | NIST |
| Tfus | 250.15 ± 10.00 | K | NIST |
| Tfus | 255.15 ± 5.00 | K | NIST |
| Tfus | Outlier 414.65 | K | NIST |
| Vc | 0.342 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [224.79; 284.56] | J/mol×K | [489.74; 715.75] |
|
| Cp,gas | 224.79 | J/mol×K | 489.74 | Joback Calculated Property |
| Cp,gas | 236.73 | J/mol×K | 527.41 | Joback Calculated Property |
| Cp,gas | 247.77 | J/mol×K | 565.08 | Joback Calculated Property |
| Cp,gas | 258.00 | J/mol×K | 602.74 | Joback Calculated Property |
| Cp,gas | 267.49 | J/mol×K | 640.41 | Joback Calculated Property |
| Cp,gas | 276.31 | J/mol×K | 678.08 | Joback Calculated Property |
| Cp,gas | 284.56 | J/mol×K | 715.75 | Joback Calculated Property |
| η | [0.0000969; 0.0051808] | Pa×s | [318.06; 489.74] |
|
| η | 0.0051808 | Pa×s | 318.06 | Joback Calculated Property |
| η | 0.0020303 | Pa×s | 346.67 | Joback Calculated Property |
| η | 0.0009178 | Pa×s | 375.29 | Joback Calculated Property |
| η | 0.0004643 | Pa×s | 403.90 | Joback Calculated Property |
| η | 0.0002571 | Pa×s | 432.51 | Joback Calculated Property |
| η | 0.0001531 | Pa×s | 461.13 | Joback Calculated Property |
| η | 0.0000969 | Pa×s | 489.74 | Joback Calculated Property |
| ΔsubH | 80.30 ± 0.50 | kJ/mol | 297.50 | NIST |
| ΔvapH | [43.10; 63.50] | kJ/mol | [297.50; 457.00] |
|
| ΔvapH | 63.50 | kJ/mol | 297.50 | NIST |
| ΔvapH | 47.00 | kJ/mol | 406.50 | NIST |
| ΔvapH | 51.40 | kJ/mol | 406.50 | NIST |
| ΔvapH | 49.50 | kJ/mol | 406.50 | NIST |
| ΔvapH | 48.60 | kJ/mol | 406.50 | NIST |
| ΔvapH | 43.10 | kJ/mol | 406.50 | NIST |
| ΔvapH | 51.60 | kJ/mol | 419.50 | NIST |
| ΔvapH | 50.50 | kJ/mol | 457.00 | NIST |
| ρl | 1037.00 | kg/m3 | 273.00 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [362.14; 505.79] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53904e+01 | |||
| Coefficient B | -4.35252e+03 | |||
| Coefficient C | -7.39420e+01 | |||
| Temperature range, min. | 362.14 | |||
| Temperature range, max. | 505.79 | |||
| Pvap | 1.33 | kPa | 362.14 | Calculated Property |
| Pvap | 2.95 | kPa | 378.10 | Calculated Property |
| Pvap | 6.01 | kPa | 394.06 | Calculated Property |
| Pvap | 11.47 | kPa | 410.02 | Calculated Property |
| Pvap | 20.63 | kPa | 425.98 | Calculated Property |
| Pvap | 35.27 | kPa | 441.95 | Calculated Property |
| Pvap | 57.66 | kPa | 457.91 | Calculated Property |
| Pvap | 90.65 | kPa | 473.87 | Calculated Property |
| Pvap | 137.65 | kPa | 489.83 | Calculated Property |
| Pvap | 202.66 | kPa | 505.79 | Calculated Property |
| Pvap | [0.79; 162.92] | kPa | [350.00; 500.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | -2.29537e+02 | |||
| Coefficient B | 3.61538e+03 | |||
| Coefficient C | 3.82332e+01 | |||
| Coefficient D | -4.08192e-05 | |||
| Temperature range, min. | 350.00 | |||
| Temperature range, max. | 500.00 | |||
| Pvap | 0.79 | kPa | 350.00 | Calculated Property |
| Pvap | 1.79 | kPa | 366.67 | Calculated Property |
| Pvap | 3.83 | kPa | 383.33 | Calculated Property |
| Pvap | 7.72 | kPa | 400.00 | Calculated Property |
| Pvap | 14.68 | kPa | 416.67 | Calculated Property |
| Pvap | 26.43 | kPa | 433.33 | Calculated Property |
| Pvap | 45.03 | kPa | 450.00 | Calculated Property |
| Pvap | 72.76 | kPa | 466.67 | Calculated Property |
| Pvap | 111.66 | kPa | 483.33 | Calculated Property |
| Pvap | 162.92 | kPa | 500.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Phenol, 2-ethyl-.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Liquid-Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass
- Effect of Isomers on Partition Coefficients for Phenolic Compounds in the 1-Butyl-3-methylimidazolium Hexafluorophosphate + Water Two-Phase System
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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