Chemical Properties of Ethyl Oleate (CAS 111-62-6)

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

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.8812		Relay (1.0) Calculated Property
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°	-112.63	kJ/mol	Joback Calculated Property
ΔfH°gas	-715.10	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	47.73	kJ/mol	Solid liquid equilibrium in ternary mixtures of ethyl oleate, ethyl laurate and ethyl palmitate
ΔvapH°	102.62	kJ/mol	Relay (1.0) Calculated Property
IE	8.88	eV	Relay (1.0) Calculated Property
log10WS	-6.49		Relay (1.0) Calculated Property
logPoct/wat	6.587		Crippen Calculated Property
McVol	295.800	ml/mol	McGowan Calculated Property
Pc	1053.46	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	Outlier 2142.00		NIST
Inp	2175.00		NIST
Inp	2185.00		NIST
Ip	[2442.00; 2493.00]
Ip	2446.00		NIST
Ip	2446.00		NIST
Ip	2455.00		NIST
Ip	2470.00		NIST
Ip	2445.00		NIST
Ip	2461.00		NIST
Ip	2484.00		NIST
Ip	2468.00		NIST
Ip	2480.00		NIST
Ip	2480.00		NIST
Ip	2472.00		NIST
Ip	2470.00		NIST
Ip	2476.00		NIST
Ip	2487.00		NIST
Ip	2489.00		NIST
Ip	2493.00		NIST
Ip	2442.00		NIST
Ip	2489.00		NIST
Tboil	479.70	K	NIST
Tc	777.53	K	Relay (1.0) Calculated Property
Tfus	[241.15; 293.15]	K
Tfus	254.00	K	Influence of Additives (Isoamyl Laurate or Isoamyl Nonanoate) in the Solid-Liquid Equilibrium of Fatty Acid Ethyl Esters
Tfus	241.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	293.15 ± 4.00	K	NIST
Vc	1.127	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	[0.0017018; 0.0103900]	Pa×s	[278.15; 363.15]
η	0.0103900	Pa×s	278.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0088392	Pa×s	283.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0075953	Pa×s	288.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0065909	Pa×s	293.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0057694	Pa×s	298.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0050921	Pa×s	303.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0045248	Pa×s	308.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0040480	Pa×s	313.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0036409	Pa×s	318.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0032922	Pa×s	323.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0029905	Pa×s	328.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0027294	Pa×s	333.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0025016	Pa×s	338.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0023014	Pa×s	343.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0021243	Pa×s	348.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0019671	Pa×s	353.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0018272	Pa×s	358.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0017018	Pa×s	363.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
ΔvapH	92.40	kJ/mol	432.50	NIST
Pvap	[1.33; 9.33]	kPa	[486.64; 536.83]
Pvap	1.33	kPa	486.64	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	2.67	kPa	500.98	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	4.00	kPa	508.03	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	5.33	kPa	514.61	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	5.33	kPa	514.61	Vapor liquid equilibrium of fatty acid ethyl esters determined using DSC
Pvap	6.67	kPa	523.69	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	8.00	kPa	528.56	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	9.33	kPa	536.83	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	9.33	kPa	536.83	Vapor liquid equilibrium of fatty acid ethyl esters determined using DSC
ρl	[857.97; 865.23]	kg/m3	[298.15; 308.15]
ρl	865.23	kg/m3	298.15	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
ρl	861.60	kg/m3	303.15	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
ρl	857.97	kg/m3	308.15	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

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[432.09; 1028.67]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-4.06500e+00
Coefficient B			1.86904e+00
Coefficient C			-1.05340e-03
Coefficient D			2.17100e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	432.09	J/mol×K	273.00	Calculated Property
Cp,gas	534.93	J/mol×K	353.78	Calculated Property
Cp,gas	627.03	J/mol×K	434.56	Calculated Property
Cp,gas	709.08	J/mol×K	515.33	Calculated Property
Cp,gas	781.75	J/mol×K	596.11	Calculated Property
Cp,gas	845.75	J/mol×K	676.89	Calculated Property
Cp,gas	901.76	J/mol×K	757.67	Calculated Property
Cp,gas	950.45	J/mol×K	838.44	Calculated Property
Cp,gas	992.53	J/mol×K	919.22	Calculated Property
Cp,gas	1028.67	J/mol×K	1000.00	Calculated Property

Similar Compounds

Find more compounds similar to Ethyl Oleate.

Mixtures

• Hexadecanoic acid, ethyl ester + Ethyl Oleate
• Dodecanoic 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

• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Cheméo Relay (1.0)
• 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

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.