- InChI
- InChI=1S/C20H38O2/c1-3-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19-20(21)22-4-2/h11-12H,3-10,13-19H2,1-2H3/b12-11-
- InChI Key
- LVGKNOAMLMIIKO-QXMHVHEDSA-N
- Formula
- C20H38O2
- SMILES
- CCCCCCCCC=CCCCCCCCC(=O)OCC
- Molecular Weight1
- 310.51
- CAS
- 111-62-6
- Other Names
-
- (Z)-9-Octadecenoic acid ethyl ester
- (Z)-9-octadecenoic acid, ethyl ester
- 9-Octadecenoic acid (Z)-, ethyl ester
- Ethyl Z-9-octadecenoate
- Ethyl cis-9-octadecenoate
- ethyl (Z)-9-octadeceneoate
- oleic acid, ethyl ester
- 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).
- 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).
- 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 | [-12525.00; -12481.50] | kJ/mol |
|
| ΔcH°liquid | -12525.00 ± 12.00 | kJ/mol | NIST |
| ΔcH°liquid | -12481.50 | kJ/mol | NIST |
| ΔfG° | -36.18 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -583.71 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 47.73 | kJ/mol | Solid l... |
| ΔvapH° | 69.23 | kJ/mol | Joback Calculated Property |
| log10WS | -6.91 | Crippen Calculated Property | |
| logPoct/wat | 6.587 | Crippen Calculated Property | |
| McVol | 295.800 | ml/mol | McGowan Calculated Property |
| Pc | 1082.06 | kPa | Joback Calculated Property |
| Inp | [2142.00; 2185.00] |
|
|
| Inp | Outlier 2142.00 | NIST | |
| Inp | 2149.00 | NIST | |
| Inp | 2175.00 | NIST | |
| Inp | 2179.00 | NIST | |
| Inp | 2179.00 | NIST | |
| Inp | 2171.00 | NIST | |
| Inp | 2171.00 | NIST | |
| Inp | 2160.00 | NIST | |
| Inp | 2168.80 | NIST | |
| Inp | 2185.00 | NIST | |
| Inp | 2180.00 | NIST | |
| Inp | 2180.00 | NIST | |
| Inp | 2150.00 | NIST | |
| Inp | 2173.00 | NIST | |
| Inp | 2171.00 | NIST | |
| Inp | 2172.00 | NIST | |
| Inp | 2155.00 | NIST | |
| Inp | 2168.00 | NIST | |
| Inp | 2173.00 | NIST | |
| Inp | 2149.00 | NIST | |
| Inp | 2175.00 | NIST | |
| Inp | 2175.00 | NIST | |
| Inp | 2185.00 | NIST | |
| Inp | 2175.00 | NIST | |
| Inp | Outlier 2142.00 | NIST | |
| I | [2442.00; 2493.00] |
|
|
| I | 2446.00 | NIST | |
| I | 2455.00 | NIST | |
| I | 2470.00 | NIST | |
| I | 2445.00 | NIST | |
| I | 2461.00 | NIST | |
| I | 2484.00 | NIST | |
| I | 2468.00 | NIST | |
| I | 2480.00 | NIST | |
| I | 2480.00 | NIST | |
| I | 2472.00 | NIST | |
| I | 2470.00 | NIST | |
| I | 2476.00 | NIST | |
| I | 2487.00 | NIST | |
| I | 2489.00 | NIST | |
| I | 2493.00 | NIST | |
| I | 2442.00 | NIST | |
| I | 2489.00 | NIST | |
| I | 2446.00 | NIST | |
| Tboil | 479.70 | K | NIST |
| Tc | 911.93 | K | Joback Calculated Property |
| Tfus | [254.00; 293.15] | K |
|
| Tfus | 254.00 | K | Influen... |
| Tfus | 293.15 ± 4.00 | K | NIST |
| Vc | 1.159 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [885.45; 987.32] | J/mol×K | [737.45; 911.93] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 880 900 920 940 960 980 750 800 850 900 | ||||
| Cp,gas | 885.45 | J/mol×K | 737.45 | Joback Calculated Property |
| Cp,gas | 904.58 | J/mol×K | 766.53 | Joback Calculated Property |
| Cp,gas | 922.81 | J/mol×K | 795.61 | Joback Calculated Property |
| Cp,gas | 940.17 | J/mol×K | 824.69 | Joback Calculated Property |
| Cp,gas | 956.69 | J/mol×K | 853.77 | Joback Calculated Property |
| Cp,gas | 972.40 | J/mol×K | 882.85 | Joback Calculated Property |
| Cp,gas | 987.32 | J/mol×K | 911.93 | Joback Calculated Property |
| η | [0.0017018; 0.0103900] | Pa×s | [278.15; 363.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 300 350 | ||||
| η | 0.0103900 | Pa×s | 278.15 | Densiti... |
| η | 0.0088392 | Pa×s | 283.15 | Densiti... |
| η | 0.0075953 | Pa×s | 288.15 | Densiti... |
| η | 0.0065909 | Pa×s | 293.15 | Densiti... |
| η | 0.0057694 | Pa×s | 298.15 | Densiti... |
| η | 0.0050921 | Pa×s | 303.15 | Densiti... |
| η | 0.0045248 | Pa×s | 308.15 | Densiti... |
| η | 0.0040480 | Pa×s | 313.15 | Densiti... |
| η | 0.0036409 | Pa×s | 318.15 | Densiti... |
| η | 0.0032922 | Pa×s | 323.15 | Densiti... |
| η | 0.0029905 | Pa×s | 328.15 | Densiti... |
| η | 0.0027294 | Pa×s | 333.15 | Densiti... |
| η | 0.0025016 | Pa×s | 338.15 | Densiti... |
| η | 0.0023014 | Pa×s | 343.15 | Densiti... |
| η | 0.0021243 | Pa×s | 348.15 | Densiti... |
| η | 0.0019671 | Pa×s | 353.15 | Densiti... |
| η | 0.0018272 | Pa×s | 358.15 | Densiti... |
| η | 0.0017018 | Pa×s | 363.15 | Densiti... |
| ΔvapH | 92.40 | kJ/mol | 432.50 | NIST |
| Pvap | [1.33; 9.33] | kPa | [486.64; 536.83] |
|
|
T(K) Vapor pressure (kPa) 2 4 6 8 10 500 520 | ||||
| Pvap | 1.33 | kPa | 486.64 | Determi... |
| Pvap | 2.67 | kPa | 500.98 | Determi... |
| Pvap | 4.00 | kPa | 508.03 | Determi... |
| Pvap | 5.33 | kPa | 514.61 | Determi... |
| Pvap | 5.33 | kPa | 514.61 | Vapor l... |
| Pvap | 6.67 | kPa | 523.69 | Determi... |
| Pvap | 8.00 | kPa | 528.56 | Determi... |
| Pvap | 9.33 | kPa | 536.83 | Determi... |
| Pvap | 9.33 | kPa | 536.83 | Vapor l... |
| ρl | [857.97; 865.23] | kg/m3 | [298.15; 308.15] |
|
| ρl | 865.23 | kg/m3 | 298.15 | A syste... |
| ρl | 861.60 | kg/m3 | 303.15 | A syste... |
| ρl | 857.97 | kg/m3 | 308.15 | A syste... |
Similar Compounds
Find more compounds similar to Ethyl Oleate.
Mixtures
- Dodecanoic acid, ethyl ester + Ethyl Oleate
- Hexadecanoic acid, ethyl ester + Ethyl Oleate
- Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Ethyl Oleate
- 1-Propanol + Ethyl Oleate
- Ethyl Oleate + Nonanoic acid, 3-methylbutyl ester
- Isoamyl laurate + Ethyl Oleate
Sources
- Crippen Method
- Crippen Method
- Solid liquid equilibrium in ternary mixtures of ethyl oleate, ethyl laurate and ethyl palmitate
- A systematic study on volumetric and transport properties of binary systems 1-propanol + n-hexadecane, 1-butanol + n-hexadecane and 1-propanol + ethyl oleate at different temperatures: Experimental and modeling
- Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
- Vapor liquid equilibrium of fatty acid ethyl esters determined using DSC
- Influence of Additives (Isoamyl Laurate or Isoamyl Nonanoate) in the Solid-Liquid Equilibrium of Fatty Acid Ethyl Esters
- Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
- Joback Method
- McGowan Method
- NIST Webbook
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