Chemical Properties of Methyl tetradecanoate (CAS 124-10-7)

InChI

InChI=1S/C15H30O2/c1-3-4-5-6-7-8-9-10-11-12-13-14-15(16)17-2/h3-14H2,1-2H3

InChI Key

ZAZKJZBWRNNLDS-UHFFFAOYSA-N

Formula

C15H30O2

SMILES

CCCCCCCCCCCCCC(=O)OC

Molecular Weight¹

242.40

CAS

124-10-7

Other Names

• Acide myristique methyl ester
• Emery 2214
• Metholeneat 2495
• Methyl myristylate
• Methyl n-tetradecanoate
• Uniphat A50
• methyl myristate
• myristic acid, methyl ester
• tetradecanoic acid, methyl ester

• 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_fusH : Enthalpy of fusion at a given temperature (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. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.7872		Relay (1.0) Calculated Property
ΔcH°liquid	[-9445.60; -9430.70]	kJ/mol
ΔcH°liquid	-9430.70 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-9445.60 ± 2.10	kJ/mol	NIST
ΔfG°	-158.50	kJ/mol	Joback Calculated Property
ΔfH°gas	-666.28	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	52.01	kJ/mol	Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K
ΔvapH°	[85.90; 87.00]	kJ/mol
ΔvapH°	86.98	kJ/mol	NIST
ΔvapH°	85.90 ± 0.80	kJ/mol	NIST
ΔvapH°	86.60	kJ/mol	NIST
ΔvapH°	86.20 ± 1.00	kJ/mol	NIST
ΔvapH°	86.98 ± 0.94	kJ/mol	NIST
ΔvapH°	87.00 ± 0.90	kJ/mol	NIST
IE	9.72	eV	Relay (1.0) Calculated Property
log10WS	-5.48		Relay (1.0) Calculated Property
logPoct/wat	4.861		Crippen Calculated Property
McVol	229.650	ml/mol	McGowan Calculated Property
Pc	1465.73	kPa	Joback Calculated Property
Inp	[286.80; 1738.00]
Inp	1710.60		NIST
Inp	1710.00		NIST
Inp	1718.00		NIST
Inp	1712.00		NIST
Inp	1713.00		NIST
Inp	1713.00		NIST
Inp	1707.00		NIST
Inp	1726.00		NIST
Inp	1706.00		NIST
Inp	1726.00		NIST
Inp	1726.00		NIST
Inp	1727.00		NIST
Inp	1713.00		NIST
Inp	1725.00		NIST
Inp	1714.00		NIST
Inp	1727.00		NIST
Inp	1738.00		NIST
Inp	1719.00		NIST
Inp	1706.00		NIST
Inp	1706.00		NIST
Inp	1707.00		NIST
Inp	1707.44		NIST
Inp	1708.00		NIST
Inp	1707.00		NIST
Inp	1715.00		NIST
Inp	1725.00		NIST
Inp	1714.00		NIST
Inp	1722.20		NIST
Inp	1728.00		NIST
Inp	1726.00		NIST
Inp	1728.00		NIST
Inp	1699.00		NIST
Inp	1699.00		NIST
Inp	1708.00		NIST
Inp	1727.00		NIST
Inp	1724.00		NIST
Inp	1725.00		NIST
Inp	1723.00		NIST
Inp	1738.00		NIST
Inp	1723.00		NIST
Inp	1726.00		NIST
Inp	1723.00		NIST
Inp	1727.40		NIST
Inp	1725.00		NIST
Inp	1723.00		NIST
Inp	1727.00		NIST
Inp	1706.00		NIST
Inp	1722.00		NIST
Inp	1710.00		NIST
Inp	1724.00		NIST
Inp	1725.00		NIST
Inp	1709.00		NIST
Inp	1729.00		NIST
Inp	1707.00		NIST
Inp	1727.00		NIST
Inp	1707.00		NIST
Inp	1705.00		NIST
Inp	1708.00		NIST
Inp	1708.00		NIST
Inp	1707.00		NIST
Inp	1712.00		NIST
Inp	1722.00		NIST
Inp	1726.00		NIST
Inp	1735.00		NIST
Inp	1684.00		NIST
Inp	1735.00		NIST
Inp	1708.00		NIST
Inp	1727.00		NIST
Inp	1727.00		NIST
Inp	1707.00		NIST
Inp	1707.00		NIST
Inp	1723.00		NIST
Inp	1707.00		NIST
Inp	1725.00		NIST
Inp	1717.00		NIST
Inp	1706.00		NIST
Inp	1725.00		NIST
Inp	1707.00		NIST
Inp	1708.00		NIST
Inp	1714.00		NIST
Inp	1715.00		NIST
Inp	Outlier 288.78		NIST
Inp	Outlier 291.18		NIST
Inp	Outlier 297.60		NIST
Inp	Outlier 297.60		NIST
Inp	Outlier 297.70		NIST
Inp	Outlier 286.80		NIST
Inp	Outlier 290.52		NIST
Inp	Outlier 290.32		NIST
Inp	Outlier 290.32		NIST
Inp	Outlier 290.32		NIST
Inp	1722.20		NIST
I	[1978.00; 2037.00]
I	2005.00		NIST
I	2037.00		NIST
I	1990.00		NIST
I	1990.00		NIST
I	1990.00		NIST
I	1998.00		NIST
I	1990.00		NIST
I	2006.00		NIST
I	2034.00		NIST
I	1988.00		NIST
I	2028.00		NIST
I	2008.00		NIST
I	2008.00		NIST
I	2000.00		NIST
I	1998.00		NIST
I	2032.00		NIST
I	2036.00		NIST
I	2014.00		NIST
I	2006.00		NIST
I	1987.00		NIST
I	2021.00		NIST
I	2034.00		NIST
I	2014.00		NIST
I	2009.00		NIST
I	1999.00		NIST
I	1990.00		NIST
I	1990.00		NIST
I	2020.00		NIST
I	1978.00		NIST
I	2000.00		NIST
I	1998.00		NIST
I	2028.00		NIST
Tboil	596.20	K	NIST
Tc	730.00	K	Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
Tfus	[290.00; 292.00]	K
Tfus	290.00 ± 1.00	K	NIST
Tfus	291.85 ± 0.30	K	NIST
Tfus	292.00 ± 2.00	K	NIST
Vc	0.897	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[620.74; 714.65]	J/mol×K	[618.89; 786.41]
Cp,gas	620.74	J/mol×K	618.89	Joback Calculated Property
Cp,gas	638.14	J/mol×K	646.81	Joback Calculated Property
Cp,gas	654.83	J/mol×K	674.73	Joback Calculated Property
Cp,gas	670.81	J/mol×K	702.65	Joback Calculated Property
Cp,gas	686.10	J/mol×K	730.57	Joback Calculated Property
Cp,gas	700.70	J/mol×K	758.49	Joback Calculated Property
Cp,gas	714.65	J/mol×K	786.41	Joback Calculated Property
Cp,liquid	505.40	J/mol×K	298.15	NIST
η	[0.0014233; 0.0044420]	Pa×s	[293.15; 353.15]
η	0.0044420	Pa×s	293.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0039821	Pa×s	298.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0035430	Pa×s	303.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0034960	Pa×s	303.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0031651	Pa×s	308.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0028447	Pa×s	313.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0028410	Pa×s	313.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0025709	Pa×s	318.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0023343	Pa×s	323.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0022520	Pa×s	323.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0021295	Pa×s	328.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0019498	Pa×s	333.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0018190	Pa×s	333.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0017932	Pa×s	338.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0016549	Pa×s	343.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0015210	Pa×s	343.15	Group Contribution Model for Predicting Viscosity of Fatty Compounds
η	0.0015321	Pa×s	348.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0014233	Pa×s	353.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
ΔfusH	[50.21; 50.21]	kJ/mol	[291.60; 291.60]
ΔfusH	50.21	kJ/mol	291.60	NIST
ΔfusH	50.21	kJ/mol	291.60	NIST
ΔsubH	137.70 ± 2.10	kJ/mol	281.00	NIST
ΔvapH	[65.30; 87.00]	kJ/mol	[293.00; 498.00]
ΔvapH	75.06	kJ/mol	293.00	NIST
ΔvapH	86.10	kJ/mol	298.15	the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
ΔvapH	87.00	kJ/mol	313.00	NIST
ΔvapH	79.80	kJ/mol	350.00	NIST
ΔvapH	76.00 ± 0.20	kJ/mol	382.00	NIST
ΔvapH	77.40	kJ/mol	390.50	NIST
ΔvapH	75.60	kJ/mol	454.00	NIST
ΔvapH	65.30	kJ/mol	498.00	NIST
Pvap	[1.13e-04; 4.00]	kPa	[302.71; 459.62]
Pvap	1.13e-04	kPa	302.71	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.50e-04	kPa	305.30	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.66e-04	kPa	306.14	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.95e-04	kPa	307.76	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	2.14e-04	kPa	308.58	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	2.54e-04	kPa	310.23	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	2.81e-04	kPa	311.21	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	3.26e-04	kPa	312.71	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	3.62e-04	kPa	313.70	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	4.20e-04	kPa	315.17	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	4.65e-04	kPa	316.16	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	5.36e-04	kPa	317.65	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	5.91e-04	kPa	318.63	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	6.86e-04	kPa	320.12	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	7.62e-04	kPa	321.26	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	8.69e-04	kPa	322.58	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	9.62e-04	kPa	323.72	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.11e-03	kPa	325.20	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.22e-03	kPa	326.19	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.39e-03	kPa	327.67	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.52e-03	kPa	328.66	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.74e-03	kPa	330.13	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	1.91e-03	kPa	331.13	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	2.76e-03	kPa	332.40	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	2.17e-03	kPa	332.60	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	2.38e-03	kPa	333.60	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	2.75e-03	kPa	335.34	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	2.94e-03	kPa	336.07	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	3.41e-03	kPa	337.83	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	3.63e-03	kPa	338.55	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	4.21e-03	kPa	340.31	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	4.47e-03	kPa	341.01	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	5.98e-03	kPa	342.28	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	5.88e-03	kPa	342.28	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	5.17e-03	kPa	342.80	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	5.47e-03	kPa	343.48	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	6.33e-03	kPa	345.28	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	6.70e-03	kPa	345.96	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	7.72e-03	kPa	347.76	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	8.13e-03	kPa	348.43	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	9.38e-03	kPa	350.25	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	9.87e-03	kPa	350.91	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.01	kPa	352.35	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	352.35	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	352.73	Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
Pvap	0.01	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	0.03	kPa	362.59	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	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	0.05	kPa	372.73	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	0.05	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	0.09	kPa	382.82	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	0.10	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	0.17	kPa	392.86	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	0.17	kPa	392.87	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	0.17	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	0.30	kPa	402.76	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	0.30	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	0.51	kPa	412.80	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	0.51	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	0.83	kPa	422.64	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	0.84	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	1.31	kPa	432.57	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	1.31	kPa	432.57	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	1.31	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	1.35	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	1.72	kPa	437.72	Vapor-Liquid Equilibria of Binary Systems with Long-Chain Organic Compounds (Fatty Alcohol, Fatty Ester, Acylglycerol, and n-Paraffin) at Subatmospheric Pressures
Pvap	2.06	kPa	442.36	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	2.05	kPa	442.37	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	2.05	kPa	442.38	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	2.12	kPa	443.15	Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
Pvap	3.12	kPa	452.24	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	3.13	kPa	452.25	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	3.13	kPa	452.26	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	3.27	kPa	453.15	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	459.62	Vapor liquid equilibrium of fatty acid ethyl esters determined using DSC
n0	[1.41083; 1.43704]		[293.15; 358.15]
n0	1.43704		293.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43490		298.15	Liquid-Liquid Equilibria for Ternary Mixtures of gamma-Valerolactone + n-Tetradecane + (Butanoic Acid or Hexanoic Acid or Methyl Myristate) at 298.15 K
n0	1.43499		298.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43296		303.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43093		308.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42890		313.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42681		318.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42472		323.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42254		328.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42020		333.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41783		338.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41630		343.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41474		348.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41282		353.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41083		358.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	[844.34; 867.17]	kg/m3	[293.15; 323.15]
ρl	867.17	kg/m3	293.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	863.35	kg/m3	298.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	859.54	kg/m3	303.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	855.74	kg/m3	308.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	851.94	kg/m3	313.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	848.14	kg/m3	318.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
ρl	844.34	kg/m3	323.15	Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
λ	[0.13; 0.15]	W/m×K	[304.02; 402.41]
λ	0.15	W/m×K	304.02	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.15	W/m×K	304.33	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	320.10	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	320.81	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	327.18	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	327.53	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	338.31	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	338.55	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	342.21	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	342.28	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	354.31	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	354.58	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	359.14	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.14	W/m×K	359.27	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	377.12	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	377.13	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	386.13	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	386.27	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	394.31	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	394.48	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	402.41	Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
λ	0.13	W/m×K	402.41	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	429.20	K	0.90	NIST

Datasets

1. Viscosity, Pa*s (1)
2. Speed of sound, m/s (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
303.15	101.30	0.0035
303.15	20000.00	0.0044
303.15	40000.00	0.0055
313.15	101.30	0.0028
313.15	20000.00	0.0035
313.15	40000.00	0.0043
313.15	60000.00	0.0052
313.15	80000.00	0.0063
313.15	100000.00	0.0075
333.15	101.30	0.0019
333.15	20000.00	0.0024
333.15	40000.00	0.0029
333.15	60000.00	0.0035
333.15	80000.00	0.0041
333.15	100000.00	0.0048
353.15	101.30	0.0014
353.15	20000.00	0.0017
353.15	40000.00	0.0021
353.15	60000.00	0.0025
353.15	80000.00	0.0029
353.15	100000.00	0.0034
Reference

Speed of sound, m/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
100.00	303.15	1335.8
10000.00	303.15	1382.9
20000.00	303.15	1426.9
30000.00	303.15	1468.1
40000.00	303.15	1507.6
50000.00	303.15	1544.9
60000.00	303.15	1580.2
70000.00	303.15	1614.2
100.00	323.15	1264.0
10000.00	323.15	1316.4
20000.00	323.15	1364.8
30000.00	323.15	1409.6
40000.00	323.15	1451.9
50000.00	323.15	1492.5
60000.00	323.15	1530.5
70000.00	323.15	1566.8
80000.00	323.15	1601.2
100.00	343.15	1195.7
10000.00	343.15	1251.2
20000.00	343.15	1302.9
30000.00	343.15	1350.8
40000.00	343.15	1396.0
50000.00	343.15	1437.4
60000.00	343.15	1477.5
70000.00	343.15	1515.0
80000.00	343.15	1550.8
100.00	363.15	1130.9
10000.00	363.15	1190.4
20000.00	363.15	1245.2
30000.00	363.15	1295.9
40000.00	363.15	1342.5
50000.00	363.15	1385.7
60000.00	363.15	1426.7
70000.00	363.15	1465.5
80000.00	363.15	1502.6
100.00	383.15	1066.7
10000.00	383.15	1131.3
20000.00	383.15	1189.6
30000.00	383.15	1242.9
40000.00	383.15	1291.7
50000.00	383.15	1338.0
60000.00	383.15	1380.3
70000.00	383.15	1420.4
80000.00	383.15	1457.6
100.00	393.15	1036.2
10000.00	393.15	1103.6
20000.00	393.15	1163.5
30000.00	393.15	1217.8
40000.00	393.15	1267.7
50000.00	393.15	1314.4
60000.00	393.15	1357.8
70000.00	393.15	1397.8
80000.00	393.15	1436.8
Reference

Similar Compounds

Find more compounds similar to Methyl tetradecanoate.

Mixtures

• Cyclohexane, methyl- + Methyl tetradecanoate
• Hexadecanoic acid, methyl ester + Methyl tetradecanoate
• Tetradecane + Methyl tetradecanoate
• 1-Hexadecanol + Methyl tetradecanoate
• Methyl tetradecanoate + Methyl Alcohol
• Ethane + Methyl tetradecanoate
• Pentadecane + Methyl tetradecanoate
• Hexadecane + Methyl tetradecanoate
• Glycerin + Methyl tetradecanoate + Methyl Alcohol
• 9-Octadecenoic acid (Z)-, methyl ester + Hexadecanoic acid, methyl ester + Methyl tetradecanoate
• Ethanol + Glycerin + Methyl tetradecanoate
• Glycerin + Methyl tetradecanoate + Water

Sources

• Cheméo Relay (1.0)
• Crippen Method
• 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
• Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
• Isobaric vapor liquid equilibrium for binary system of methyl myristate + methyl palmitate at 0.5, 1.0 and 1.4 kPa
• Isobaric vapor-liquid equilibrium for the three binary systems of C14 - C16 n-alkane + methyl myristate at 5.00 kPa
• 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
• Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
• Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
• Thermophysical properties of fatty acid methyl and ethyl esters
• Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
• the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
• Vapor liquid equilibrium of fatty acid ethyl esters determined using DSC
• Viscosities of Fatty Acid Methyl and Ethyl Esters under High Pressure: Methyl Myristate and Ethyl Myristate
• 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
• Vapor-Liquid Equilibria of Binary Systems with Long-Chain Organic Compounds (Fatty Alcohol, Fatty Ester, Acylglycerol, and n-Paraffin) at Subatmospheric Pressures
• Liquid-Liquid Equilibria for Ternary Mixtures of gamma-Valerolactone + n-Tetradecane + (Butanoic Acid or Hexanoic Acid or Methyl Myristate) at 298.15 K
• 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
• Isobaric Vapor Liquid Equilibrium of the Mixture of Methyl Palmitate and Methyl Stearate at 0.1 kPa, 1 kPa, 5 kPa, and 10 kPa
• Article Ternary Liquid Liquid Equilibrium of Biodiesel Compounds for Systems Consisting of a Methyl Ester + Glycerin + Water
• Speed of Sound, Density, and Derivative Properties of Ethyl Myristate, Methyl Myristate, and Methyl Palmitate under High Pressure
• Group Contribution Model for Predicting Viscosity of Fatty Compounds
• Viscosities of Fatty Mixtures: Experimental Data and Prediction
• Joback Method
• McGowan Method
• NIST Webbook

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