Chemical Properties of 9,12-Octadecadienoic acid (Z,Z)- (CAS 60-33-3)

InChI

InChI=1S/C18H32O2/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18(19)20/h6-7,9-10H,2-5,8,11-17H2,1H3,(H,19,20)/b7-6-,10-9-

InChI Key

OYHQOLUKZRVURQ-HZJYTTRNSA-N

Formula

C18H32O2

SMILES

CCCCCC=CCC=CCCCCCCCC(=O)O

Molecular Weight¹

280.45

CAS

60-33-3

Other Names

• (Z,Z)-9,12-octadecadienoic acid
• (Z,Z)-Octadeca-9, 12-dienoic acid
• 9,12-Linoleic acid
• 9,12-OCTADECADIENOIC ACID
• 9,12-Octadecadienoic acid (9Z,12Z)-
• 9,12-Octadecadienoic acid, cis,cis-
• 9-(Z), 12-(Z)-Octadecadienoic acid
• 9-cis,12-cis-Linoleic acid
• 9Z,12Z-Linoleic acid
• Acide linoleique
• Emersol 310
• Emersol 315
• Extra Linoleic 90
• Grape seed oil
• Leinoleic acid
• Linoleic
• Linolic acid
• Octadeca-9,12-dienoic acid, (cis,cis)-
• Polylin 515
• Polylin No. 515
• Telfairic acid
• Unifac 6550
• Vespula pensylvanica b708568k063
• all-cis-9,12-Octadecadienoic acid
• cis,cis-9,12-Octadecadienoic acid
• cis,cis-Linoleic acid
• cis-9,cis-12-octadecadienoic acid
• cis-«DELTA»9,12-Octadecadienoic acid
• linoleic acid

• ω : Acentric Factor.
• 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	1.1801		ChemSep v8.3 pure component data
μ	1.22	debye	ChemSep v8.3 pure component data
ΔfG°	-117.20	kJ/mol	ChemSep v8.3 pure component data
ΔfH°gas	-539.90	kJ/mol	ChemSep v8.3 pure component data
ΔfH°liquid	-634.70	kJ/mol	NIST
ΔfusH°	52.92	kJ/mol	Joback Calculated Property
ΔvapH°	124.00	kJ/mol	Relay (1.0) Calculated Property
IE	8.88	eV	Relay (1.0) Calculated Property
log10WS	-5.36		Relay (1.0) Calculated Property
logPoct/wat	5.885		Crippen Calculated Property
McVol	263.320	ml/mol	McGowan Calculated Property
Pc	1410.00	kPa	ChemSep v8.3 pure component data
Ptriple	6.46e-10	kPa	ChemSep v8.3 pure component data
Inp	[2095.00; 2179.00]
Inp	2134.00		NIST
Inp	2140.00		NIST
Inp	2130.00		NIST
Inp	2131.00		NIST
Inp	2095.20		NIST
Inp	2104.00		NIST
Inp	2144.00		NIST
Inp	2170.00		NIST
Inp	2095.00		NIST
Inp	2095.00		NIST
Inp	Outlier 2173.00		NIST
Inp	2156.00		NIST
Inp	2126.00		NIST
Inp	2159.00		NIST
Inp	2114.00		NIST
Inp	2130.00		NIST
Inp	2152.00		NIST
Inp	2113.00		NIST
Inp	2113.00		NIST
Inp	2106.00		NIST
Inp	2112.00		NIST
Inp	2145.80		NIST
Inp	Outlier 2179.00		NIST
Inp	2113.00		NIST
Inp	2147.00		NIST
Inp	2128.00		NIST
Inp	2136.00		NIST
Inp	2133.00		NIST
Inp	2109.00		NIST
Inp	2135.00		NIST
Inp	2136.00		NIST
Inp	2113.00		NIST
Inp	2154.00		NIST
Inp	2111.00		NIST
Inp	2130.00		NIST
Inp	2146.00		NIST
Inp	2144.00		NIST
Inp	2156.00		NIST
Inp	2136.00		NIST
Inp	2122.00		NIST
Inp	2156.00		NIST
Inp	2132.00		NIST
Inp	2150.00		NIST
Inp	2107.00		NIST
Inp	2128.00		NIST
Inp	2130.00		NIST
Inp	2131.00		NIST
Inp	2140.00		NIST
Inp	2123.00		NIST
Inp	2123.00		NIST
Inp	2119.00		NIST
Inp	2107.00		NIST
Inp	2125.00		NIST
Inp	2125.00		NIST
Inp	2130.00		NIST
Inp	2104.00		NIST
Inp	2097.00		NIST
Inp	2125.00		NIST
Inp	2130.00		NIST
Inp	2152.00		NIST
Inp	2118.00		NIST
Inp	2115.00		NIST
Inp	2105.00		NIST
Inp	2140.00		NIST
Inp	2144.00		NIST
Inp	2156.00		NIST
Inp	2152.00		NIST
Inp	Outlier 2179.00		NIST
Inp	2133.00		NIST
Inp	2154.00		NIST
Inp	2150.00		NIST
Inp	2125.00		NIST
Inp	2130.00		NIST
I	[3157.00; 3215.00]
I	Outlier 3215.00		NIST
I	3168.00		NIST
I	3157.00		NIST
I	3157.00		NIST
I	3160.00		NIST
I	3176.00		NIST
I	3157.00		NIST
Tboil	628.00	K	ChemSep v8.3 pure component data
Tc	775.00	K	ChemSep v8.3 pure component data
Tfus	[266.20; 268.20]	K
Tfus	268.20	K	Solid-Liquid Equilibria in Fatty Acid/Triglycerol Systems
Tfus	267.83	K	Solid Liquid Equilibrium of Binary Mixtures Containing Fatty Acids and Triacylglycerols
Tfus	268.15	K	ChemSep v8.3 pure component data
Tfus	266.40 ± 0.80	K	NIST
Tfus	266.20 ± 1.00	K	NIST
Ttriple	268.15	K	ChemSep v8.3 pure component data
UQi	10.29		ChemSep v8.3 pure component data
URi	12.53		ChemSep v8.3 pure component data
Vc	0.990	m3/kmol	ChemSep v8.3 pure component data
Zc	0.2170000		ChemSep v8.3 pure component data

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔfusH	47.70	kJ/mol	303.00	NIST
ΔvapH	134.10	kJ/mol	298.00	Vapor Pressures and Vaporization, Sublimation, and Fusion Enthalpies of Some Fatty Acids

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	502.70	K	2.10	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[394.30; 1049.31]	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			3.32000e+02
Coefficient B			1.04200e+03
Coefficient C			2.28840e+03
Coefficient D			7.98400e+02
Coefficient E			9.23500e+02
Comment			ChemSep eq 107, IdealGasHeatCapacityCp
Temperature range, min.			298.15
Temperature range, max.			1500.10
Cp,gas	394.30	J/mol×K	298.15	Calculated Property
Cp,gas	532.03	J/mol×K	431.70	Calculated Property
Cp,gas	654.18	J/mol×K	565.25	Calculated Property
Cp,gas	741.97	J/mol×K	698.80	Calculated Property
Cp,gas	809.68	J/mol×K	832.35	Calculated Property
Cp,gas	867.85	J/mol×K	965.90	Calculated Property
Cp,gas	920.37	J/mol×K	1099.45	Calculated Property
Cp,gas	968.08	J/mol×K	1233.00	Calculated Property
Cp,gas	1011.05	J/mol×K	1366.55	Calculated Property
Cp,gas	1049.31	J/mol×K	1500.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[593.32; 828.63]	J/mol×K	[387.50; 581.25]	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			1.22700e+02
Coefficient B			1.21450e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidHeatCapacityCp
Temperature range, min.			387.50
Temperature range, max.			581.25
Cp,liquid	593.32	J/mol×K	387.50	Calculated Property
Cp,liquid	619.46	J/mol×K	409.03	Calculated Property
Cp,liquid	645.61	J/mol×K	430.56	Calculated Property
Cp,liquid	671.76	J/mol×K	452.08	Calculated Property
Cp,liquid	697.90	J/mol×K	473.61	Calculated Property
Cp,liquid	724.05	J/mol×K	495.14	Calculated Property
Cp,liquid	750.19	J/mol×K	516.67	Calculated Property
Cp,liquid	776.34	J/mol×K	538.19	Calculated Property
Cp,liquid	802.48	J/mol×K	559.72	Calculated Property
Cp,liquid	828.63	J/mol×K	581.25	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0488306; 0.0002297]	Pa×s	[268.15; 628.00]	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			-1.23720e+01
Coefficient B			2.50790e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			268.15
Temperature range, max.			628.00
η	0.0488306	Pa×s	268.15	Calculated Property
η	0.0145089	Pa×s	308.13	Calculated Property
η	0.0056971	Pa×s	348.12	Calculated Property
η	0.0027122	Pa×s	388.10	Calculated Property
η	0.0014832	Pa×s	428.08	Calculated Property
η	0.0008992	Pa×s	468.07	Calculated Property
η	0.0005898	Pa×s	508.05	Calculated Property
η	0.0004115	Pa×s	548.03	Calculated Property
η	0.0003014	Pa×s	588.02	Calculated Property
η	0.0002297	Pa×s	628.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[113.72; 0.00]	kJ/mol	[268.15; 775.00]	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			1.35220e+02
Coefficient B			4.07850e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.75000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			268.15
Temperature range, max.			775.00
ΔvapH	113.72	kJ/mol	268.15	Calculated Property
ΔvapH	108.38	kJ/mol	324.47	Calculated Property
ΔvapH	102.64	kJ/mol	380.78	Calculated Property
ΔvapH	96.38	kJ/mol	437.10	Calculated Property
ΔvapH	89.48	kJ/mol	493.42	Calculated Property
ΔvapH	81.69	kJ/mol	549.73	Calculated Property
ΔvapH	72.65	kJ/mol	606.05	Calculated Property
ΔvapH	61.58	kJ/mol	662.37	Calculated Property
ΔvapH	46.41	kJ/mol	718.68	Calculated Property
ΔvapH	0.00	kJ/mol	775.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.36; 203.20]	kPa	[489.15; 671.15]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.60422e+01
Coefficient B			-6.13615e+03
Coefficient C			-9.91760e+01
Temperature range, min.			489.15
Temperature range, max.			671.15
Pvap	1.36	kPa	489.15	Calculated Property
Pvap	2.95	kPa	509.37	Calculated Property
Pvap	5.97	kPa	529.59	Calculated Property
Pvap	11.31	kPa	549.82	Calculated Property
Pvap	20.30	kPa	570.04	Calculated Property
Pvap	34.71	kPa	590.26	Calculated Property
Pvap	56.90	kPa	610.48	Calculated Property
Pvap	89.83	kPa	630.71	Calculated Property
Pvap	137.14	kPa	650.93	Calculated Property
Pvap	203.20	kPa	671.15	Calculated Property
Pvap	[6.46e-10; 1403.25]	kPa	[268.15; 775.00]	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			1.34562e+02
Coefficient B			-1.82290e+04
Coefficient C			-1.56920e+01
Coefficient D			2.77980e-18
Coefficient E			6.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			268.15
Temperature range, max.			775.00
Pvap	6.46e-10	kPa	268.15	Calculated Property
Pvap	4.33e-06	kPa	324.47	Calculated Property
Pvap	1.43e-03	kPa	380.78	Calculated Property
Pvap	0.08	kPa	437.10	Calculated Property
Pvap	1.41	kPa	493.42	Calculated Property
Pvap	11.84	kPa	549.73	Calculated Property
Pvap	59.36	kPa	606.05	Calculated Property
Pvap	209.26	kPa	662.37	Calculated Property
Pvap	582.86	kPa	718.68	Calculated Property
Pvap	1403.25	kPa	775.00	Calculated Property
Pvap	[6.42e-10; 99.96]	kPa	[268.15; 628.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.48236e+02
Coefficient B			-1.87631e+04
Coefficient C			-1.78156e+01
Coefficient D			2.59652e-06
Coefficient E			0.00000e+00
Temperature range, min.			268.15
Temperature range, max.			628.00
Pvap	6.42e-10	kPa	268.15	Calculated Property
Pvap	5.03e-07	kPa	308.13	Calculated Property
Pvap	6.67e-05	kPa	348.12	Calculated Property
Pvap	2.68e-03	kPa	388.10	Calculated Property
Pvap	0.05	kPa	428.08	Calculated Property
Pvap	0.44	kPa	468.07	Calculated Property
Pvap	2.65	kPa	508.05	Calculated Property
Pvap	11.33	kPa	548.03	Calculated Property
Pvap	37.30	kPa	588.02	Calculated Property
Pvap	99.96	kPa	628.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[917.06; 283.27]	kg/m3	[268.15; 775.00]	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			7.56052e+01
Coefficient B			2.66900e-01
Coefficient C			7.75000e+02
Coefficient D			2.76070e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			268.15
Temperature range, max.			775.00
ρl	917.06	kg/m3	268.15	Calculated Property
ρl	883.23	kg/m3	324.47	Calculated Property
ρl	847.62	kg/m3	380.78	Calculated Property
ρl	809.78	kg/m3	437.10	Calculated Property
ρl	769.09	kg/m3	493.42	Calculated Property
ρl	724.54	kg/m3	549.73	Calculated Property
ρl	674.40	kg/m3	606.05	Calculated Property
ρl	615.21	kg/m3	662.37	Calculated Property
ρl	537.48	kg/m3	718.68	Calculated Property
ρl	283.27	kg/m3	775.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[268.15; 775.00]	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			5.61700e-02
Coefficient B			1.14890e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.75000e+02
Comment			ChemSep eq 106, SurfaceTension
Temperature range, min.			268.15
Temperature range, max.			775.00
γ	0.03	N/m	268.15	Calculated Property
γ	0.03	N/m	324.47	Calculated Property
γ	0.03	N/m	380.78	Calculated Property
γ	0.02	N/m	437.10	Calculated Property
γ	0.02	N/m	493.42	Calculated Property
γ	0.01	N/m	549.73	Calculated Property
γ	0.01	N/m	606.05	Calculated Property
γ	0.01	N/m	662.37	Calculated Property
γ	0.00	N/m	718.68	Calculated Property
γ	0.00	N/m	775.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.03; 0.05]	W/m×K	[628.00; 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			1.57710e-04
Coefficient B			9.22800e-01
Coefficient C			7.78350e+02
Coefficient D			0.00000e+00
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			628.00
Temperature range, max.			1000.00
λ	0.03	W/m×K	628.00	Calculated Property
λ	0.03	W/m×K	669.33	Calculated Property
λ	0.03	W/m×K	710.67	Calculated Property
λ	0.03	W/m×K	752.00	Calculated Property
λ	0.04	W/m×K	793.33	Calculated Property
λ	0.04	W/m×K	834.67	Calculated Property
λ	0.04	W/m×K	876.00	Calculated Property
λ	0.05	W/m×K	917.33	Calculated Property
λ	0.05	W/m×K	958.67	Calculated Property
λ	0.05	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.15; 0.08]	W/m×K	[268.15; 628.00]	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			1.94200e-01
Coefficient B			-1.81690e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidThermalConductivity
Temperature range, min.			268.15
Temperature range, max.			628.00
λ	0.15	W/m×K	268.15	Calculated Property
λ	0.14	W/m×K	308.13	Calculated Property
λ	0.13	W/m×K	348.12	Calculated Property
λ	0.12	W/m×K	388.10	Calculated Property
λ	0.12	W/m×K	428.08	Calculated Property
λ	0.11	W/m×K	468.07	Calculated Property
λ	0.10	W/m×K	508.05	Calculated Property
λ	0.09	W/m×K	548.03	Calculated Property
λ	0.09	W/m×K	588.02	Calculated Property
λ	0.08	W/m×K	628.00	Calculated Property

Similar Compounds

Find more compounds similar to 9,12-Octadecadienoic acid (Z,Z)-.

Mixtures

• 9,12-Octadecadienoic acid (Z,Z)- + Ethanol + GLYCEROL TRICAPRYLATE
• n-Hexane + 9,12-Octadecadienoic acid (Z,Z)-
• 9,12-Octadecadienoic acid (Z,Z)- + Heptane
• 9,12-Octadecadienoic acid (Z,Z)- + Pentane, 2,2,4-trimethyl-
• 1-Hexene + 9,12-Octadecadienoic acid (Z,Z)-
• Toluene + 9,12-Octadecadienoic acid (Z,Z)-
• 9,12-Octadecadienoic acid (Z,Z)- + Cyclohexane
• 9,12-Octadecadienoic acid (Z,Z)- + Benzene, ethyl-
• 9,12-Octadecadienoic acid (Z,Z)- + Methyl Alcohol
• 9,12-Octadecadienoic acid (Z,Z)- + Ethanol
• 1-Propanol + 9,12-Octadecadienoic acid (Z,Z)-
• 9,12-Octadecadienoic acid (Z,Z)- + 1-Butanol
• 2-Propanol + 9,12-Octadecadienoic acid (Z,Z)-
• Trichloromethane + 9,12-Octadecadienoic acid (Z,Z)-
• 9,12-Octadecadienoic acid (Z,Z)- + Benzene, chloro-
• 9,12-Octadecadienoic acid (Z,Z)- + Ethane, 1,2-dichloro-
• 9,12-Octadecadienoic acid (Z,Z)- + Benzene, (chloromethyl)-
• 9,12-Octadecadienoic acid (Z,Z)- + Ethyl Acetate
• 9,12-Octadecadienoic acid (Z,Z)- + Acetone
• 9,12-Octadecadienoic acid (Z,Z)- + Anisole

Find more mixtures with 9,12-Octadecadienoic acid (Z,Z)-.

Sources

• KDB Vapor Pressure Data
• 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
• Phase equilibrium measurements of ternary systems formed by linoleic and linolenic acids in carbon dioxide/ethanol mixtures
• 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)
• Measurements of Binary Diffusion Coefficient and Partition Ratio at Infinite Dilution for Linoleic Acid and Arachidonic Acid in Supercritical Carbon Dioxide
• Solid-Liquid Equilibria in Fatty Acid/Triglycerol Systems
• Solid Liquid Equilibrium of Binary Mixtures Containing Fatty Acids and Triacylglycerols
• Vapor Pressures and Vaporization, Sublimation, and Fusion Enthalpies of Some Fatty Acids
• Viscosities of Fatty Mixtures: Experimental Data and Prediction
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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.
These property values are available through the Cheméo API. A free account gives you an access key.