Chemical Properties of Dodecanoic acid, methyl ester (CAS 111-82-0)

InChI

InChI=1S/C13H26O2/c1-3-4-5-6-7-8-9-10-11-12-13(14)15-2/h3-12H2,1-2H3

InChI Key

UQDUPQYQJKYHQI-UHFFFAOYSA-N

Formula

C13H26O2

SMILES

CCCCCCCCCCCC(=O)OC

Molecular Weight¹

214.34

CAS

111-82-0

Other Names

• Metholene 2296
• Methyl dodecylate
• Methyl laurinate
• Methyl n-dodecanoate
• NSC 5027
• Uniphat A40
• lauric acid, methyl ester
• methyl dodecanoate
• methyl laurate

• 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).
• 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_subH : Enthalpy of sublimation 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_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.7164		Relay (1.0) Calculated Property
ΔcH°liquid	[-8137.80; -8117.00]	kJ/mol
ΔcH°liquid	-8117.00 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-8137.80 ± 1.60	kJ/mol	NIST
ΔfG°	-251.79	kJ/mol	Joback Calculated Property
ΔfH°gas	-625.09	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	43.15	kJ/mol	Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K
ΔvapH°	[76.50; 77.20]	kJ/mol
ΔvapH°	77.17	kJ/mol	NIST
ΔvapH°	76.60 ± 0.40	kJ/mol	NIST
ΔvapH°	76.80	kJ/mol	NIST
ΔvapH°	76.50 ± 0.70	kJ/mol	NIST
ΔvapH°	77.17 ± 0.56	kJ/mol	NIST
ΔvapH°	77.20 ± 0.60	kJ/mol	NIST
IE	9.68	eV	Relay (1.0) Calculated Property
log10WS	[-4.69; -4.69]
log10WS	-4.69		Aq. Solubility Prediction
log10WS	-4.69		Estimated Solubility
logPoct/wat	4.080		Crippen Calculated Property
McVol	201.470	ml/mol	McGowan Calculated Property
Pc	1651.11	kPa	Joback Calculated Property
Inp	[256.90; 1533.00]
Inp	1514.90		NIST
Inp	1510.00		NIST
Inp	1518.00		NIST
Inp	1508.00		NIST
Inp	1513.00		NIST
Inp	1513.00		NIST
Inp	1527.00		NIST
Inp	1525.00		NIST
Inp	1526.00		NIST
Inp	1527.00		NIST
Inp	1526.00		NIST
Inp	1509.00		NIST
Inp	1507.00		NIST
Inp	1527.00		NIST
Inp	1509.00		NIST
Inp	1505.00		NIST
Inp	1506.00		NIST
Inp	1506.00		NIST
Inp	1506.00		NIST
Inp	1509.00		NIST
Inp	1507.00		NIST
Inp	1524.00		NIST
Inp	1526.00		NIST
Inp	1527.00		NIST
Inp	1513.00		NIST
Inp	1521.30		NIST
Inp	1521.70		NIST
Inp	1526.00		NIST
Inp	1527.00		NIST
Inp	1514.00		NIST
Inp	1506.00		NIST
Inp	1503.00		NIST
Inp	1501.00		NIST
Inp	1523.00		NIST
Inp	1526.00		NIST
Inp	1526.80		NIST
Inp	1525.00		NIST
Inp	1521.00		NIST
Inp	1510.00		NIST
Inp	1533.00		NIST
Inp	1509.00		NIST
Inp	1525.00		NIST
Inp	1508.00		NIST
Inp	1508.00		NIST
Inp	1507.00		NIST
Inp	1505.00		NIST
Inp	1506.00		NIST
Inp	1509.00		NIST
Inp	1507.00		NIST
Inp	1510.00		NIST
Inp	1525.00		NIST
Inp	1526.00		NIST
Inp	1532.00		NIST
Inp	1532.00		NIST
Inp	1508.00		NIST
Inp	1526.00		NIST
Inp	1521.00		NIST
Inp	1528.00		NIST
Inp	1507.00		NIST
Inp	1525.00		NIST
Inp	1528.00		NIST
Inp	1531.00		NIST
Inp	1517.00		NIST
Inp	1510.00		NIST
Inp	1507.00		NIST
Inp	Outlier 258.35		NIST
Inp	Outlier 260.37		NIST
Inp	Outlier 265.90		NIST
Inp	Outlier 265.80		NIST
Inp	Outlier 265.90		NIST
Inp	Outlier 256.90		NIST
Inp	Outlier 260.05		NIST
Inp	1501.00		NIST
Inp	1521.00		NIST
Inp	1508.00		NIST
Inp	1509.00		NIST
Inp	1525.00		NIST
Inp	1526.00		NIST
Inp	1528.00		NIST
Inp	1514.90		NIST
Inp	1513.00		NIST
Inp	1521.30		NIST
Inp	1506.00		NIST
I	[1770.00; 1834.00]
I	1802.00		NIST
I	Outlier 1834.00		NIST
I	Outlier 1770.00		NIST
I	1798.00		NIST
I	1805.90		NIST
I	1807.10		NIST
I	1813.00		NIST
I	1784.90		NIST
I	1801.50		NIST
I	1806.70		NIST
I	1819.70		NIST
I	1785.00		NIST
I	1801.00		NIST
I	1800.00		NIST
I	1813.00		NIST
I	1785.00		NIST
I	1812.00		NIST
I	1805.00		NIST
I	1810.00		NIST
I	1804.00		NIST
I	1800.00		NIST
I	1804.00		NIST
I	1793.00		NIST
I	1808.00		NIST
I	1806.00		NIST
I	Outlier 1770.00		NIST
I	1814.00		NIST
I	1814.00		NIST
I	1791.00		NIST
I	1808.00		NIST
I	1811.00		NIST
I	1804.00		NIST
I	1793.00		NIST
I	1809.00		NIST
I	1793.00		NIST
I	1785.00		NIST
I	1815.00		NIST
I	1800.00		NIST
I	1800.00		NIST
I	1804.00		NIST
I	1815.00		NIST
I	1802.00		NIST
I	1807.10		NIST
I	1819.70		NIST
I	1808.00		NIST
I	1791.00		NIST
I	1785.00		NIST
Tboil	540.00	K	KDB
Tc	[712.00; 712.15]	K
Tc	712.00	K	KDB
Tc	712.15 ± 3.00	K	NIST
Tfus	[278.00; 278.45]	K
Tfus	278.30	K	KDB
Tfus	278.25	K	Aq. Solubility Prediction
Tfus	278.45 ± 0.35	K	NIST
Tfus	278.00 ± 0.05	K	NIST
Vc	0.787	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[449.00; 486.80]	J/mol×K	[303.15; 373.15]
Cp,liquid	449.00	J/mol×K	303.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
Cp,liquid	452.80	J/mol×K	313.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
Cp,liquid	457.40	J/mol×K	323.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
Cp,liquid	462.60	J/mol×K	333.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
Cp,liquid	468.40	J/mol×K	343.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
Cp,liquid	474.50	J/mol×K	353.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
Cp,liquid	480.70	J/mol×K	363.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
Cp,liquid	486.80	J/mol×K	373.15	Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
η	[0.0011002; 0.0040678]	Pa×s	[283.15; 353.15]
η	0.0040678	Pa×s	283.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0035771	Pa×s	288.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0030960	Pa×s	293.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0031668	Pa×s	293.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0028237	Pa×s	298.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0025356	Pa×s	303.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0024750	Pa×s	303.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0022893	Pa×s	308.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0020776	Pa×s	313.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0020440	Pa×s	313.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0018944	Pa×s	318.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0017347	Pa×s	323.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0016430	Pa×s	323.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0015948	Pa×s	328.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0014714	Pa×s	333.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0013830	Pa×s	333.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0013621	Pa×s	338.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0012651	Pa×s	343.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0011730	Pa×s	343.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0011781	Pa×s	348.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0011002	Pa×s	353.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
ΔsubH	121.80 ± 2.10	kJ/mol	267.50	NIST
ΔvapH	[53.30; 83.60]	kJ/mol	[293.00; 498.00]
ΔvapH	80.80	kJ/mol	293.00	NIST
ΔvapH	69.33	kJ/mol	293.00	NIST
ΔvapH	75.80	kJ/mol	298.15	the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
ΔvapH	83.60	kJ/mol	310.00	NIST
ΔvapH	71.40	kJ/mol	350.00	NIST
ΔvapH	70.70 ± 0.20	kJ/mol	356.00	NIST
ΔvapH	71.40	kJ/mol	372.50	NIST
ΔvapH	74.90	kJ/mol	373.50	NIST
ΔvapH	62.30	kJ/mol	406.00	NIST
ΔvapH	63.60	kJ/mol	473.50	NIST
ΔvapH	53.30	kJ/mol	498.00	NIST
Pvap	[6.09e-03; 6.00]	kPa	[322.68; 443.30]
Pvap	6.72e-03	kPa	322.68	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	6.09e-03	kPa	323.80	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	7.01e-03	kPa	325.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	8.53e-03	kPa	327.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	9.82e-03	kPa	329.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.01	kPa	331.80	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.01	kPa	332.79	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	0.01	kPa	333.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.02	kPa	335.70	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.02	kPa	338.70	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.02	kPa	340.70	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.03	kPa	342.08	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	0.03	kPa	344.10	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.03	kPa	345.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.04	kPa	349.30	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.05	kPa	351.30	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.06	kPa	353.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	0.06	kPa	353.19	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	0.06	kPa	354.40	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.07	kPa	356.40	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.08	kPa	359.60	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.10	kPa	361.50	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.12	kPa	362.53	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	0.12	kPa	363.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	0.11	kPa	364.70	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.13	kPa	366.70	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.16	kPa	370.00	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.18	kPa	371.80	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.21	kPa	372.57	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	0.22	kPa	373.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	0.21	kPa	374.70	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.26	kPa	378.60	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.31	kPa	381.70	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.38	kPa	382.62	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	0.39	kPa	383.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	0.41	kPa	386.80	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.49	kPa	389.60	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.53	kPa	391.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.64	kPa	392.73	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	0.66	kPa	393.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	0.64	kPa	394.90	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.69	kPa	397.00	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.77	kPa	399.20	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.90	kPa	401.30	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.06	kPa	402.73	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	1.08	kPa	403.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	1.70	kPa	412.79	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	1.73	kPa	413.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	2.00	kPa	417.53	Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
Pvap	2.65	kPa	422.61	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	2.69	kPa	423.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	4.02	kPa	432.58	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	4.10	kPa	433.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	4.00	kPa	433.71	Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
Pvap	5.92	kPa	442.50	Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
Pvap	6.00	kPa	443.30	Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
n0	[1.40513; 1.43836]		[278.15; 358.15]
n0	1.43836		278.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43629		283.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43422		288.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43216		293.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43009		298.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42802		303.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42594		308.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42383		313.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42171		318.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41959		323.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41750		328.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41542		333.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41334		338.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41127		343.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40922		348.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40717		353.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40513		358.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	[829.90; 869.30]	kg/m3	[293.15; 343.15]
ρl	869.30	kg/m3	293.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	869.22	kg/m3	293.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	865.30	kg/m3	298.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	865.39	kg/m3	298.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	861.46	kg/m3	303.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	861.37	kg/m3	303.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	857.53	kg/m3	308.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	857.44	kg/m3	308.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	853.61	kg/m3	313.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	853.51	kg/m3	313.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	849.69	kg/m3	318.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	849.58	kg/m3	318.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	845.76	kg/m3	323.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	845.65	kg/m3	323.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	841.72	kg/m3	328.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	837.78	kg/m3	333.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	833.84	kg/m3	338.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
ρl	829.90	kg/m3	343.15	Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
λ	[0.12; 0.15]	W/m×K	[283.81; 402.69]
λ	0.15	W/m×K	283.81	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.15	W/m×K	284.03	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.15	W/m×K	295.89	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.15	W/m×K	295.90	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	306.72	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	306.79	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	307.82	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	307.84	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	317.62	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	317.69	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	327.44	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	327.69	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	337.37	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	337.57	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	349.53	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	349.67	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	359.29	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	359.31	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	369.45	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	369.47	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	379.17	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	379.47	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	390.25	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	390.33	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	402.63	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.12	W/m×K	402.69	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	[414.20; 535.20]	K	[2.00; 102.00]
Tboilr	414.20	K	2.00	NIST
Tboilr	535.20	K	102.00	NIST

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (1)
3. Mass density, kg/m3 (2)
4. Speed of sound, m/s (1)

Molar heat capacity at constant pressure, J/K/mol

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
100.00	313.97	442.60
4040.00	313.99	441.60
8070.00	314.06	439.50
12160.00	314.09	438.30
16180.00	314.14	436.90
100.00	323.88	449.50
4070.00	323.93	447.20
8060.00	324.01	445.80
12090.00	323.84	444.80
16080.00	323.94	443.30
100.00	333.88	456.40
4050.00	333.96	453.60
8050.00	334.00	452.10
12060.00	334.05	450.50
16170.00	334.11	448.00
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.04	110.00	0.0025
303.04	10512.00	0.0029
302.94	20178.00	0.0032
302.70	30290.00	0.0036
312.63	134.00	0.0021
312.61	10214.00	0.0023
312.50	20279.00	0.0026
312.33	30212.00	0.0029
331.66	132.00	0.0015
331.51	10354.00	0.0017
331.34	20420.00	0.0019
331.07	29762.00	0.0020
351.81	235.00	0.0011
351.74	10090.00	0.0013
351.57	20226.00	0.0014
351.24	29906.00	0.0015
362.23	2921.00	0.0010
361.75	10141.00	0.0011
361.60	19931.00	0.0013
361.57	30100.00	0.0014
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	876.58
1000.00	283.15	877.29
3000.00	283.15	879.12
5000.00	283.15	880.29
10000.00	283.15	883.41
15000.00	283.15	886.29
20000.00	283.15	889.1
25000.00	283.15	891.75
30000.00	283.15	894.31
35000.00	283.15	896.95
40000.00	283.15	899.33
50000.00	283.15	904.05
60000.00	283.15	909.85
100.00	293.15	869.3
1000.00	293.15	869.79
3000.00	293.15	871.19
5000.00	293.15	872.09
10000.00	293.15	875.46
15000.00	293.15	878.42
20000.00	293.15	881.47
25000.00	293.15	884.32
30000.00	293.15	887.1
35000.00	293.15	889.69
40000.00	293.15	892.27
50000.00	293.15	897.52
60000.00	293.15	901.95
100.00	303.15	860.98
1000.00	303.15	861.67
3000.00	303.15	863.19
5000.00	303.15	864.57
10000.00	303.15	867.78
15000.00	303.15	871.1
20000.00	303.15	874.06
25000.00	303.15	876.92
30000.00	303.15	879.85
35000.00	303.15	882.66
40000.00	303.15	885.34
50000.00	303.15	890.6
60000.00	303.15	895.49
100.00	313.15	853.31
1000.00	313.15	853.78
3000.00	313.15	855.32
5000.00	313.15	856.78
10000.00	313.15	860.3
15000.00	313.15	863.63
20000.00	313.15	866.74
25000.00	313.15	870.04
30000.00	313.15	872.94
35000.00	313.15	875.68
40000.00	313.15	878.33
50000.00	313.15	883.95
60000.00	313.15	888.91
100.00	323.15	845.42
1000.00	323.15	846.17
3000.00	323.15	847.65
5000.00	323.15	849.19
10000.00	323.15	852.91
15000.00	323.15	856.38
20000.00	323.15	859.88
25000.00	323.15	863.01
30000.00	323.15	866.2
35000.00	323.15	869.19
40000.00	323.15	872.15
50000.00	323.15	877.67
60000.00	323.15	883.06
100.00	333.15	837.89
1000.00	333.15	838.44
3000.00	333.15	840.13
5000.00	333.15	841.69
10000.00	333.15	845.49
15000.00	333.15	849.14
20000.00	333.15	852.7
25000.00	333.15	856.12
30000.00	333.15	859.27
35000.00	333.15	862.4
40000.00	333.15	865.66
50000.00	333.15	871.36
60000.00	333.15	876.77
100.00	343.15	829.64
1000.00	343.15	830.6
3000.00	343.15	832.28
5000.00	343.15	834.04
10000.00	343.15	837.93
15000.00	343.15	841.71
20000.00	343.15	845.7
25000.00	343.15	848.98
30000.00	343.15	852.48
35000.00	343.15	855.72
40000.00	343.15	858.94
50000.00	343.15	864.79
60000.00	343.15	870.31
100.00	353.15	821.96
1000.00	353.15	822.7
3000.00	353.15	824.65
5000.00	353.15	826.36
10000.00	353.15	830.59
15000.00	353.15	834.55
20000.00	353.15	838.32
25000.00	353.15	842.04
30000.00	353.15	845.62
35000.00	353.15	849.06
40000.00	353.15	853.14
50000.00	353.15	858.49
60000.00	353.15	864.35
100.00	363.15	813.95
1000.00	363.15	814.97
3000.00	363.15	816.88
5000.00	363.15	818.64
10000.00	363.15	822.93
15000.00	363.15	827.44
20000.00	363.15	831.22
25000.00	363.15	834.95
30000.00	363.15	838.64
35000.00	363.15	842.26
40000.00	363.15	845.87
50000.00	363.15	852.24
60000.00	363.15	858.43
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.10	100.00	861.8
303.11	3010.00	863.7
303.13	6030.00	865.7
303.16	9050.00	867.9
303.20	12030.00	869.8
303.20	15040.00	871.7
312.95	100.00	853.4
313.11	3030.00	855.3
313.08	6050.00	857.4
313.06	9040.00	859.2
313.12	12030.00	861.2
312.95	15050.00	863.4
323.05	100.00	845.5
323.17	3030.00	847.4
323.30	6050.00	849.3
323.33	9050.00	851.6
323.27	12040.00	853.8
323.40	15020.00	855.9
333.15	100.00	837.8
333.15	3040.00	840.3
333.15	6040.00	842.3
333.18	9050.00	844.7
333.16	12020.00	846.9
333.14	15030.00	849.0
343.18	100.00	829.4
343.22	3020.00	831.9
343.22	6020.00	833.9
343.21	9040.00	836.6
343.19	12060.00	838.5
343.19	15050.00	841.1
353.27	100.00	821.6
353.28	3040.00	824.4
353.23	6050.00	826.8
353.26	9030.00	829.5
353.18	12030.00	831.6
353.16	15040.00	834.1
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 2 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
293.15	100.00	1351.3
293.15	10000.00	1400.9
293.15	20000.00	1445.1
293.15	30000.00	1486.4
293.15	40000.00	1526.9
293.15	50000.00	1563.8
293.15	60000.00	1600.0
293.15	70000.00	1628.6
293.15	80000.00	1660.5
293.15	90000.00	1690.9
313.15	100.00	1276.4
313.15	10000.00	1328.0
313.15	20000.00	1375.3
313.15	30000.00	1420.0
313.15	40000.00	1461.6
313.15	50000.00	1500.9
313.15	60000.00	1537.0
313.15	70000.00	1573.3
313.15	80000.00	1607.4
313.15	90000.00	1637.8
313.15	100000.00	1671.1
313.15	120000.00	1728.6
313.15	140000.00	1784.4
333.15	100.00	1205.5
333.15	10000.00	1259.6
333.15	20000.00	1311.0
333.15	30000.00	1357.5
333.15	40000.00	1401.0
333.15	50000.00	1441.3
333.15	60000.00	1480.9
333.15	70000.00	1515.7
333.15	80000.00	1550.8
333.15	90000.00	1585.9
333.15	100000.00	1621.9
333.15	120000.00	1682.0
333.15	140000.00	1739.2
333.15	160000.00	1791.8
333.15	180000.00	1843.5
333.15	200000.00	1893.2
353.15	100.00	1133.5
353.15	10000.00	1192.2
353.15	20000.00	1247.2
353.15	30000.00	1295.9
353.15	40000.00	1342.5
353.15	50000.00	1386.1
353.15	60000.00	1426.2
353.15	70000.00	1463.8
353.15	80000.00	1500.1
353.15	90000.00	1534.8
353.15	100000.00	1568.3
353.15	120000.00	1632.8
353.15	140000.00	1690.8
353.15	160000.00	1744.4
353.15	180000.00	1802.7
353.15	200000.00	1851.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[297.60; 698.12]	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			1.64800e+01
Coefficient B			1.18404e+00
Coefficient C			-5.88800e-04
Coefficient D			8.64000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	297.60	J/mol×K	273.00	Calculated Property
Cp,gas	365.50	J/mol×K	353.78	Calculated Property
Cp,gas	426.91	J/mol×K	434.56	Calculated Property
Cp,gas	482.11	J/mol×K	515.33	Calculated Property
Cp,gas	531.37	J/mol×K	596.11	Calculated Property
Cp,gas	574.96	J/mol×K	676.89	Calculated Property
Cp,gas	613.16	J/mol×K	757.67	Calculated Property
Cp,gas	646.24	J/mol×K	838.44	Calculated Property
Cp,gas	674.47	J/mol×K	919.22	Calculated Property
Cp,gas	698.12	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[409.00; 565.34]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.55217e+01
Coefficient B			-4.84033e+03
Coefficient C			-9.12700e+01
Temperature range, min.			409.00
Temperature range, max.			565.34
Pvap	1.33	kPa	409.00	Calculated Property
Pvap	2.94	kPa	426.37	Calculated Property
Pvap	5.98	kPa	443.74	Calculated Property
Pvap	11.41	kPa	461.11	Calculated Property
Pvap	20.52	kPa	478.48	Calculated Property
Pvap	35.09	kPa	495.86	Calculated Property
Pvap	57.43	kPa	513.23	Calculated Property
Pvap	90.39	kPa	530.60	Calculated Property
Pvap	137.44	kPa	547.97	Calculated Property
Pvap	202.66	kPa	565.34	Calculated Property
Pvap	[5.30e-05; 1771.68]	kPa	[278.15; 712.00]	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			1.80226e+02
Coefficient B			-1.60241e+04
Coefficient C			-2.36787e+01
Coefficient D			1.04209e-05
Coefficient E			0.00000e+00
Temperature range, min.			278.15
Temperature range, max.			712.00
Pvap	5.30e-05	kPa	278.15	Calculated Property
Pvap	8.10e-03	kPa	326.36	Calculated Property
Pvap	0.24	kPa	374.56	Calculated Property
Pvap	2.73	kPa	422.77	Calculated Property
Pvap	16.06	kPa	470.97	Calculated Property
Pvap	61.91	kPa	519.18	Calculated Property
Pvap	179.71	kPa	567.38	Calculated Property
Pvap	431.09	kPa	615.59	Calculated Property
Pvap	910.66	kPa	663.79	Calculated Property
Pvap	1771.68	kPa	712.00	Calculated Property
Pvap	[0.26; 5.17]	kPa	[373.00; 439.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.56969e+01
Coefficient B			-5.30411e+03
Coefficient C			-6.15920e+01
Reference			Althouse and Triebold, 1944
Temperature range, min.			373.00
Temperature range, max.			439.00
Pvap	0.26	kPa	373.00	Calculated Property
Pvap	0.39	kPa	380.33	Calculated Property
Pvap	0.57	kPa	387.67	Calculated Property
Pvap	0.81	kPa	395.00	Calculated Property
Pvap	1.14	kPa	402.33	Calculated Property
Pvap	1.58	kPa	409.67	Calculated Property
Pvap	2.17	kPa	417.00	Calculated Property
Pvap	2.93	kPa	424.33	Calculated Property
Pvap	3.91	kPa	431.67	Calculated Property
Pvap	5.17	kPa	439.00	Calculated Property

Similar Compounds

Find more compounds similar to Dodecanoic acid, methyl ester.

Mixtures

• Dodecanoic acid, methyl ester + Glycerin + Methyl Alcohol
• Dodecanoic acid, methyl ester + Methyl Alcohol
• Dodecanoic acid, methyl ester + Decanoic acid, methyl ester
• 1-Propanol + Dodecanoic acid, methyl ester
• Dodecanoic acid, methyl ester + 1-Butanol
• Dodecanoic acid, methyl ester + 1-Pentanol
• Dodecanoic acid, methyl ester + Cyclohexane, methyl-
• Ethane + Dodecanoic acid, methyl ester
• Dodecanoic acid, methyl ester + Glycerin + Water
• Dodecanoic acid, methyl ester + Octanoic acid, ethyl ester
• Dodecanoic acid, methyl ester + 4,7-Methano-1H-indene, octahydro-
• Cyclohexane, (1-methylethyl)- + Dodecanoic acid, methyl ester
• Cyclohexane, (1-methylethyl)- + Dodecanoic acid, methyl ester + 4,7-Methano-1H-indene, octahydro-
• Dodecanoic acid, methyl ester + Tetradecane
• Ethanol + Dodecanoic acid, methyl ester + Glycerin

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Measurement and correlation of vapor liquid equilibria for methanol + methyl laurate and methanol + methyl myristate systems near critical temperature of methanol
• Phase behaviour of high molecular mass methyl esters in supercritical ethane
• Measurement and correlation of ternary vapor-liquid equilibria for methanol + glycerol + fatty acid methyl ester (methyl laurate, methyl myristate, methyl palmitate) systems at elevated temperatures and pressures
• Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
• High-pressure liquid densities and derived thermodynamic properties for methyl laurate and ethyl laurate
• Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
• Measurement of speed of sound, density compressibility and viscosity in liquid methyl laurate and ethyl laurate up to 200 MPa by using acoustic wave sensors
• Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
• Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
• Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
• Thermophysical properties of fatty acid methyl and ethyl esters
• Liquid viscosities for methyl hexanoate, methyl heptanoate, methyl caprylate, and methyl nonanoate at high pressures
• Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
• Experimental studies on the thermal conductivity of methyl laurate component of biodiesel with three alcohols
• the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
• Isobaric molar heat capacities of binary mixtures containing methyl caprate and methyl laurate at pressures up to 16.2 MPa
• Measurement and correlation of viscosities and densities of methyl dodecanoate and ethyl dodecanoate at elevated pressures
• Liquid Liquid Equilibrium for the Ternary System of Methyl Laurate/Methyl Myristate + Ethanol + Glycerol at 318.15 and 333.15 K
• Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
• Densities and Viscosities of Mixtures of Methyl Dodecanoate + Ethyl Octanoate at Pressures up to 15 MPa
• Densities and Viscosities for the Ternary Mixtures of exo-Tetrahydrodicyclopentadiene (1) + Isopropylcyclohexane (2) + Methyl Laurate (3) and Corresponding Binaries
• Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K
• Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
• Article Ternary Liquid Liquid Equilibrium of Biodiesel Compounds for Systems Consisting of a Methyl Ester + Glycerin + Water
• Group Contribution Model for Predicting Viscosity of Fatty Compounds
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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