- InChI
- InChI=1S/C11H20O2/c1-4-7-8-10(5-2)9-13-11(12)6-3/h6,10H,3-5,7-9H2,1-2H3
- InChI Key
- GOXQRTZXKQZDDN-UHFFFAOYSA-N
- Formula
- C11H20O2
- SMILES
- C=CC(=O)OCC(CC)CCCC
- Molecular Weight1
- 184.28
- CAS
- 103-11-7
- Other Names
-
- 1-Hexanol, 2-ethyl-, acrylate
- 2-Ethyl-1-hexyl acrylate
- 2-Ethylhexanol acrylate
- 2-Ethylhexyl 2-propenoate
- 2-Ethylhexyl ester of acrylic acid
- 2-Ethylhexylester kyseliny akrylove
- 2-Propenoic acid, 2-ethylhexyl ester
- 2-ethylhexyl propenoate
- 2EHA
- Acrylic acid, 2-ethylhexyl ester
- NSC 4803
- ethylhexyl acrylate
- propenoic acid, 2-ethylhexyl ester
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (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).
- 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 |
|---|---|---|---|
| ΔfG° | -106.78 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -395.02 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 22.23 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 48.18 | kJ/mol | Joback Calculated Property |
| log10WS | -2.90 | Crippen Calculated Property | |
| logPoct/wat | 2.932 | Crippen Calculated Property | |
| McVol | 168.990 | ml/mol | McGowan Calculated Property |
| Pc | 2108.07 | kPa | Joback Calculated Property |
| Inp | [1192.00; 1224.00] |
|
|
| Inp | 1215.00 | NIST | |
| Inp | Outlier 1192.00 | NIST | |
| Inp | 1220.00 | NIST | |
| Inp | 1215.00 | NIST | |
| Inp | 1224.00 | NIST | |
| Inp | 1224.00 | NIST | |
| I | [1494.00; 1500.00] |
|
|
| I | 1495.00 | NIST | |
| I | 1500.00 | NIST | |
| I | 1494.00 | NIST | |
| Tboil | 490.20 | K | NIST |
| Tc | 701.05 | K | Joback Calculated Property |
| Tfus | 269.13 | K | Joback Calculated Property |
| Vc | 0.650 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [396.43; 476.13] | J/mol×K | [523.61; 701.05] |
|
| Cp,gas | 396.43 | J/mol×K | 523.61 | Joback Calculated Property |
| Cp,gas | 411.21 | J/mol×K | 553.18 | Joback Calculated Property |
| Cp,gas | 425.37 | J/mol×K | 582.76 | Joback Calculated Property |
| Cp,gas | 438.94 | J/mol×K | 612.33 | Joback Calculated Property |
| Cp,gas | 451.91 | J/mol×K | 641.90 | Joback Calculated Property |
| Cp,gas | 464.30 | J/mol×K | 671.47 | Joback Calculated Property |
| Cp,gas | 476.13 | J/mol×K | 701.05 | Joback Calculated Property |
| η | [0.0001982; 0.0041707] | Pa×s | [269.13; 523.61] |
|
| η | 0.0041707 | Pa×s | 269.13 | Joback Calculated Property |
| η | 0.0017765 | Pa×s | 311.54 | Joback Calculated Property |
| η | 0.0009284 | Pa×s | 353.96 | Joback Calculated Property |
| η | 0.0005575 | Pa×s | 396.37 | Joback Calculated Property |
| η | 0.0003694 | Pa×s | 438.78 | Joback Calculated Property |
| η | 0.0002632 | Pa×s | 481.20 | Joback Calculated Property |
| η | 0.0001982 | Pa×s | 523.61 | Joback Calculated Property |
| ΔvapH | 55.30 | kJ/mol | 406.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [7.61e-09; 2083.68] | kPa | [183.15; 655.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.19057e+01 | |||
| Coefficient B | -8.53516e+03 | |||
| Coefficient C | -6.54285e+00 | |||
| Coefficient D | 2.78538e-06 | |||
| Temperature range, min. | 183.15 | |||
| Temperature range, max. | 655.00 | |||
| Pvap | 7.61e-09 | kPa | 183.15 | Calculated Property |
| Pvap | 4.98e-05 | kPa | 235.58 | Calculated Property |
| Pvap | 0.01 | kPa | 288.01 | Calculated Property |
| Pvap | 0.37 | kPa | 340.43 | Calculated Property |
| Pvap | 4.60 | kPa | 392.86 | Calculated Property |
| Pvap | 29.58 | kPa | 445.29 | Calculated Property |
| Pvap | 123.44 | kPa | 497.72 | Calculated Property |
| Pvap | 382.88 | kPa | 550.14 | Calculated Property |
| Pvap | 963.27 | kPa | 602.57 | Calculated Property |
| Pvap | 2083.68 | kPa | 655.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Ethylhexyl acrylate.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Ultrasonic velocities, densities, and excess molar volumes of binary mixtures of N,N-dimethyl formamide with methyl acrylate, or ethyl acrylate, or butyl acrylate, or 2-ethyl hexyl acrylate at T = 308.15 K
- Joback Method
- McGowan Method
- NIST Webbook
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that the value is more than 2 standard deviations away from the
property mean.