Chemical Properties of Oleic Acid (CAS 112-80-1)

InChI

InChI=1S/C18H34O2/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18(19)20/h9-10H,2-8,11-17H2,1H3,(H,19,20)/b10-9-

InChI Key

ZQPPMHVWECSIRJ-KTKRTIGZSA-N

Formula

C18H34O2

SMILES

CCCCCCCCC=CCCCCCCCC(=O)O

Molecular Weight¹

282.46

CAS

112-80-1

Other Names

• (Z)-9-Octadecanoic acid
• (Z)-9-octadecenoic acid
• (Z)-Octadec-9-enoic acid
• .DELTA.9-cis-octadecenoic acid
• .DELTA.9-cis-oleic acid
• 9-(Z)-octadecenoic acid
• 9-Octadecenoic acid (9Z)-
• 9-Octadecenoic acid (Z)-
• 9-Octadecenoic acid, cis-
• 9-cis-octadecenoic acid
• 9-octadecenoic acid, (Z)-
• Century cd fatty acid
• D 100
• Elaic acid
• Elaidoic acid
• Emersol 210
• Emersol 211
• Emersol 213
• Emersol 220 White Oleic Acid
• Emersol 221 Low Titer White Oleic Acid
• Emersol 6313 NF
• Emersol 6321
• Glycon RO
• Glycon WO
• Groco 2
• Groco 4
• Groco 5l
• Groco 6
• Hy-phi 1055
• Hy-phi 1088
• Hy-phi 2066
• Hy-phi 2088
• Hy-phi 2102
• Industrene 205
• Industrene 206
• K 52
• L'Acide oleique
• Metaupon
• Oelsauere
• Oleinic acid
• Pamolyn
• Priolene 6906
• Tego-oleic 130
• Wochem no. 320
• Z-9-Octadecenoic acid
• cis-.DELTA.9-octadecenoic acid
• cis-9-octadecenoic acid
• cis-Octadec-9-enoic acid
• cis-oleic acid
• cis-«DELTA»9-Octadecenoate
• cis-«DELTA»9-octadecenoic acid
• emersol 205
• extraolein 90
• industrene 105
• lunac O-CA
• neo-Fat 90-04
• neo-Fat 92-04
• oleine 7503
• pamolyn 100
• priolene 6907
• vopcolene 27
• wecoline OO
• «DELTA»9-cis-Oleic acid

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• 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_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (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_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ : Gas thermal conductivity (W/m×K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	1.1822		ChemSep v8.3 pure component data
ΔcH°liquid	-11160.70	kJ/mol	NIST
μ	1.44	debye	ChemSep v8.3 pure component data
ΔfG°	-227.80	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	-649.70	kJ/mol	ChemSep v8.3 pure component data
ΔfH°liquid	-764.80	kJ/mol	NIST
ΔfusH°	52.72	kJ/mol	Joback Calculated Property
ΔvapH°	124.37	kJ/mol	Relay (1.0) Calculated Property
IE	9.17	eV	Relay (1.0) Calculated Property
log10WS	-5.79		Relay (1.0) Calculated Property
logPoct/wat	6.109		Crippen Calculated Property
McVol	267.620	ml/mol	McGowan Calculated Property
Pc	1390.00	kPa	ChemSep v8.3 pure component data
Ptriple	1.40e-08	kPa	ChemSep v8.3 pure component data
Inp	[2090.00; 2180.00]
Inp	2140.00		NIST
Inp	2171.00		NIST
Inp	2115.00		NIST
Inp	2097.00		NIST
Inp	2102.00		NIST
Inp	2175.00		NIST
Inp	2141.00		NIST
Inp	2137.00		NIST
Inp	2152.00		NIST
Inp	2141.00		NIST
Inp	2147.00		NIST
Inp	2152.00		NIST
Inp	2113.00		NIST
Inp	2146.10		NIST
Inp	2130.00		NIST
Inp	2175.00		NIST
Inp	2175.00		NIST
Inp	2131.00		NIST
Inp	2141.00		NIST
Inp	2147.00		NIST
Inp	2147.00		NIST
Inp	2116.00		NIST
Inp	2146.00		NIST
Inp	Outlier 2090.00		NIST
Inp	2180.00		NIST
Inp	2180.00		NIST
Inp	2115.00		NIST
Inp	2115.00		NIST
Inp	2110.00		NIST
Inp	2161.00		NIST
Inp	2112.00		NIST
Inp	2115.00		NIST
Inp	2131.00		NIST
Inp	2152.00		NIST
Inp	2175.00		NIST
Inp	2120.00		NIST
Inp	2173.00		NIST
Inp	2161.00		NIST
Inp	2098.00		NIST
Inp	2112.00		NIST
Inp	2146.00		NIST
Inp	2141.00		NIST
Inp	2155.00		NIST
Inp	2131.00		NIST
Inp	2161.00		NIST
Inp	2155.00		NIST
Inp	2140.00		NIST
I	[3142.00; 3200.00]
I	3184.00		NIST
I	3173.00		NIST
I	3172.00		NIST
I	3142.00		NIST
I	3150.00		NIST
I	3157.00		NIST
I	3157.00		NIST
I	3184.00		NIST
I	3200.00		NIST
I	3172.00		NIST
I	3157.00		NIST
Tboil	633.00	K	ChemSep v8.3 pure component data
Tc	781.00	K	ChemSep v8.3 pure component data
Tfus	[286.70; 289.45]	K
Tfus	286.70	K	Solid-Liquid Equilibria in Fatty Acid/Triglycerol Systems
Tfus	287.15	K	ChemSep v8.3 pure component data
Tfus	289.45 ± 0.30	K	NIST
Tfus	289.45 ± 0.50	K	NIST
Ttriple	286.53	K	ChemSep v8.3 pure component data
UQi	10.50		ChemSep v8.3 pure component data
URi	12.76		ChemSep v8.3 pure component data
Vc	1.000	m3/kmol	ChemSep v8.3 pure component data
Zc	0.2140000		ChemSep v8.3 pure component data

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔfusH	[39.60; 39.60]	kJ/mol	[286.50; 286.50]
ΔfusH	39.60	kJ/mol	286.50	NIST
ΔfusH	39.60	kJ/mol	286.50	NIST
ΔvapH	[83.80; 132.60]	kJ/mol	[298.15; 537.00]
ΔvapH	132.60	kJ/mol	298.15	Vaporization, Sublimation and Fusion Enthalpies of Some Saturated and Unsaturated Long Chain Fatty Acids by Correlation Gas Chromatography
ΔvapH	83.80	kJ/mol	537.00	NIST
Pvap	[1.33; 9.33]	kPa	[496.70; 547.40]
Pvap	1.33	kPa	496.70	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	2.67	kPa	513.10	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	4.00	kPa	524.70	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	5.33	kPa	532.10	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	6.67	kPa	538.80	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	8.00	kPa	543.80	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
Pvap	9.33	kPa	547.40	Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	467.70	K	0.10	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[417.80; 1069.78]	J/mol×K	[298.15; 1500.10]	ChemSep v8.3 pure component data
Equation			Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is Cp,gas in J/mol×K, T in K
Coefficient A			3.20000e+02
Coefficient B			9.36200e+02
Coefficient C			1.74310e+03
Coefficient D			6.75400e+02
Coefficient E			7.82500e+02
Comment			ChemSep eq 107, IdealGasHeatCapacityCp
Temperature range, min.			298.15
Temperature range, max.			1500.10
Cp,gas	417.80	J/mol×K	298.15	Calculated Property
Cp,gas	563.38	J/mol×K	431.70	Calculated Property
Cp,gas	682.59	J/mol×K	565.25	Calculated Property
Cp,gas	775.63	J/mol×K	698.80	Calculated Property
Cp,gas	851.10	J/mol×K	832.35	Calculated Property
Cp,gas	913.27	J/mol×K	965.90	Calculated Property
Cp,gas	964.49	J/mol×K	1099.45	Calculated Property
Cp,gas	1006.59	J/mol×K	1233.00	Calculated Property
Cp,gas	1041.22	J/mol×K	1366.55	Calculated Property
Cp,gas	1069.78	J/mol×K	1500.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[517.92; 1114.05]	J/mol×K	[286.53; 550.00]	ChemSep v8.3 pure component data
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			4.59000e+02
Coefficient B			-8.66000e-01
Coefficient C			3.74000e-03
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidHeatCapacityCp
Temperature range, min.			286.53
Temperature range, max.			550.00
Cp,liquid	517.92	J/mol×K	286.53	Calculated Property
Cp,liquid	558.51	J/mol×K	315.80	Calculated Property
Cp,liquid	605.52	J/mol×K	345.08	Calculated Property
Cp,liquid	658.94	J/mol×K	374.35	Calculated Property
Cp,liquid	718.76	J/mol×K	403.63	Calculated Property
Cp,liquid	785.00	J/mol×K	432.90	Calculated Property
Cp,liquid	857.65	J/mol×K	462.18	Calculated Property
Cp,liquid	936.70	J/mol×K	491.45	Calculated Property
Cp,liquid	1022.17	J/mol×K	520.73	Calculated Property
Cp,liquid	1114.05	J/mol×K	550.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0450386; 0.0003617]	Pa×s	[286.53; 633.00]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-4.47740e+01
Coefficient B			4.44430e+03
Coefficient C			4.62420e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			286.53
Temperature range, max.			633.00
η	0.0450386	Pa×s	286.53	Calculated Property
η	0.0128500	Pa×s	325.03	Calculated Property
η	0.0050680	Pa×s	363.52	Calculated Property
η	0.0025035	Pa×s	402.02	Calculated Property
η	0.0014542	Pa×s	440.52	Calculated Property
η	0.0009523	Pa×s	479.01	Calculated Property
η	0.0006827	Pa×s	517.51	Calculated Property
η	0.0005250	Pa×s	556.01	Calculated Property
η	0.0004264	Pa×s	594.50	Calculated Property
η	0.0003617	Pa×s	633.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[111.74; 0.00]	kJ/mol	[286.53; 781.00]	ChemSep v8.3 pure component data
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			1.33880e+02
Coefficient B			3.95530e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.81000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			286.53
Temperature range, max.			781.00
ΔvapH	111.74	kJ/mol	286.53	Calculated Property
ΔvapH	106.65	kJ/mol	341.47	Calculated Property
ΔvapH	101.16	kJ/mol	396.41	Calculated Property
ΔvapH	95.18	kJ/mol	451.35	Calculated Property
ΔvapH	88.56	kJ/mol	506.29	Calculated Property
ΔvapH	81.08	kJ/mol	561.24	Calculated Property
ΔvapH	72.36	kJ/mol	616.18	Calculated Property
ΔvapH	61.64	kJ/mol	671.12	Calculated Property
ΔvapH	46.86	kJ/mol	726.06	Calculated Property
ΔvapH	0.00	kJ/mol	781.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.36; 203.46]	kPa	[514.15; 709.15]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.52924e+01
Coefficient B			-5.81882e+03
Coefficient C			-1.25923e+02
Temperature range, min.			514.15
Temperature range, max.			709.15
Pvap	1.36	kPa	514.15	Calculated Property
Pvap	2.99	kPa	535.82	Calculated Property
Pvap	6.11	kPa	557.48	Calculated Property
Pvap	11.63	kPa	579.15	Calculated Property
Pvap	20.90	kPa	600.82	Calculated Property
Pvap	35.66	kPa	622.48	Calculated Property
Pvap	58.21	kPa	644.15	Calculated Property
Pvap	91.35	kPa	665.82	Calculated Property
Pvap	138.45	kPa	687.48	Calculated Property
Pvap	203.46	kPa	709.15	Calculated Property
Pvap	[1.40e-08; 1366.66]	kPa	[286.53; 781.00]	ChemSep v8.3 pure component data
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.55542e+02
Coefficient B			-1.90530e+04
Coefficient C			-1.89970e+01
Coefficient D			4.26990e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			286.53
Temperature range, max.			781.00
Pvap	1.40e-08	kPa	286.53	Calculated Property
Pvap	2.56e-05	kPa	341.47	Calculated Property
Pvap	4.09e-03	kPa	396.41	Calculated Property
Pvap	0.15	kPa	451.35	Calculated Property
Pvap	2.03	kPa	506.29	Calculated Property
Pvap	14.66	kPa	561.24	Calculated Property
Pvap	67.64	kPa	616.18	Calculated Property
Pvap	227.02	kPa	671.12	Calculated Property
Pvap	605.63	kPa	726.06	Calculated Property
Pvap	1366.66	kPa	781.00	Calculated Property
Pvap	[0.13; 98.91]	kPa	[449.70; 633.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.62296e+01
Coefficient B			-5.88450e+03
Coefficient C			-1.27258e+02
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			449.70
Temperature range, max.			633.00
Pvap	0.13	kPa	449.70	Calculated Property
Pvap	0.39	kPa	470.07	Calculated Property
Pvap	1.03	kPa	490.43	Calculated Property
Pvap	2.43	kPa	510.80	Calculated Property
Pvap	5.26	kPa	531.17	Calculated Property
Pvap	10.59	kPa	551.53	Calculated Property
Pvap	19.99	kPa	571.90	Calculated Property
Pvap	35.69	kPa	592.27	Calculated Property
Pvap	60.70	kPa	612.63	Calculated Property
Pvap	98.91	kPa	633.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[891.00; 282.47]	kg/m3	[286.53; 781.00]	ChemSep v8.3 pure component data
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.53267e+01
Coefficient B			2.66670e-01
Coefficient C			7.81000e+02
Coefficient D			3.06870e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			286.53
Temperature range, max.			781.00
ρl	891.00	kg/m3	286.53	Calculated Property
ρl	855.39	kg/m3	341.47	Calculated Property
ρl	818.18	kg/m3	396.41	Calculated Property
ρl	778.94	kg/m3	451.35	Calculated Property
ρl	737.12	kg/m3	506.29	Calculated Property
ρl	691.78	kg/m3	561.24	Calculated Property
ρl	641.35	kg/m3	616.18	Calculated Property
ρl	582.68	kg/m3	671.12	Calculated Property
ρl	507.20	kg/m3	726.06	Calculated Property
ρl	282.47	kg/m3	781.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[286.53; 781.00]	ChemSep v8.3 pure component data
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K
Coefficient A			5.31940e-02
Coefficient B			1.03550e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.81000e+02
Comment			ChemSep eq 106, SurfaceTension
Temperature range, min.			286.53
Temperature range, max.			781.00
γ	0.03	N/m	286.53	Calculated Property
γ	0.03	N/m	341.47	Calculated Property
γ	0.03	N/m	396.41	Calculated Property
γ	0.02	N/m	451.35	Calculated Property
γ	0.02	N/m	506.29	Calculated Property
γ	0.01	N/m	561.24	Calculated Property
γ	0.01	N/m	616.18	Calculated Property
γ	0.01	N/m	671.12	Calculated Property
γ	0.00	N/m	726.06	Calculated Property
γ	0.00	N/m	781.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.03; 0.05]	W/m×K	[633.00; 1000.00]	ChemSep v8.3 pure component data
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			1.42000e-04
Coefficient B			9.37900e-01
Coefficient C			8.04000e+02
Coefficient D			0.00000e+00
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			633.00
Temperature range, max.			1000.00
λ	0.03	W/m×K	633.00	Calculated Property
λ	0.03	W/m×K	673.78	Calculated Property
λ	0.03	W/m×K	714.56	Calculated Property
λ	0.03	W/m×K	755.33	Calculated Property
λ	0.04	W/m×K	796.11	Calculated Property
λ	0.04	W/m×K	836.89	Calculated Property
λ	0.04	W/m×K	877.67	Calculated Property
λ	0.05	W/m×K	918.44	Calculated Property
λ	0.05	W/m×K	959.22	Calculated Property
λ	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.15; 0.09]	W/m×K	[286.53; 625.00]	ChemSep v8.3 pure component data
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K
Coefficient A			2.08330e-01
Coefficient B			-1.92770e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidThermalConductivity
Temperature range, min.			286.53
Temperature range, max.			625.00
λ	0.15	W/m×K	286.53	Calculated Property
λ	0.15	W/m×K	324.14	Calculated Property
λ	0.14	W/m×K	361.75	Calculated Property
λ	0.13	W/m×K	399.35	Calculated Property
λ	0.12	W/m×K	436.96	Calculated Property
λ	0.12	W/m×K	474.57	Calculated Property
λ	0.11	W/m×K	512.18	Calculated Property
λ	0.10	W/m×K	549.78	Calculated Property
λ	0.10	W/m×K	587.39	Calculated Property
λ	0.09	W/m×K	625.00	Calculated Property

Similar Compounds

Find more compounds similar to Oleic Acid.

Mixtures

• Oleic Acid + n-Hexane + Tetradecanoic acid, 1,2,3-propanetriyl ester
• Oleic Acid + Tetradecanoic acid, 1,2,3-propanetriyl ester + 1-Hexanol
• Oleic Acid + Tetradecanoic acid, 1,2,3-propanetriyl ester + 1-Butanol
• Oleic Acid + 1-Propanol + Tetradecanoic acid, 1,2,3-propanetriyl ester
• Oleic Acid + 2-Propanol + Tetradecanoic acid, 1,2,3-propanetriyl ester
• Oleic Acid + Triolein + Ethanol
• Oleic Acid + Heptane + Water
• Oleic Acid + 1-Butanol + Water
• Propane + Oleic Acid
• Oleic Acid + n-Hexane
• Oleic Acid + Heptane
• Oleic Acid + Pentane, 2,2,4-trimethyl-
• Oleic Acid + 1-Hexene
• Oleic Acid + Toluene
• Oleic Acid + Cyclohexane
• Oleic Acid + Benzene, ethyl-
• Oleic Acid + Methyl Alcohol
• Oleic Acid + Ethanol
• Oleic Acid + 1-Propanol
• Oleic Acid + 2-Propanol

Find more mixtures with Oleic Acid.

Sources

• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Binary, ternary and quaternary liquid liquid equilibria in 1-butanol, oleic acid, water and n-heptane mixtures
• Hydrogen solubility in triolein, and propane solubility in oleic acid for second generation BDF synthesis by use of hydrodeoxygenation reaction
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
• Vapor Liquid Equilibrium of Carbon Dioxide + Ethyl Acetate + Oleic Acid Mixtures at High Pressures
• Solubility of Squalene and Fatty Acids in Carbon Dioxide at Supercritical Conditions: Binary and Ternary Systems
• High-Pressure Phase Equilibria of the Ternary System Oleic Acid + Squalene + Carbon Dioxide
• Solid-Liquid Equilibria in Fatty Acid/Triglycerol Systems
• Vapor Liquid Equilibrium Data for Carbon Dioxide + (R,S)-1,2-Isopropylidene Glycerol (Solketal) + Oleic Acid Systems at High Pressure
• Vaporization, Sublimation and Fusion Enthalpies of Some Saturated and Unsaturated Long Chain Fatty Acids by Correlation Gas Chromatography
• Liquid Liquid Equilibrium for Ternary Systems Containing Water, Oleic Acid, and Alcohols at 313.15 K. Effect of Alcohol Chain Length
• Viscosities of Fatty Mixtures: Experimental Data and Prediction
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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