Chemical Properties of Dodecanoic acid, ethyl ester (CAS 106-33-2)

InChI

InChI=1S/C14H28O2/c1-3-5-6-7-8-9-10-11-12-13-14(15)16-4-2/h3-13H2,1-2H3

InChI Key

MMXKVMNBHPAILY-UHFFFAOYSA-N

Formula

C14H28O2

SMILES

CCCCCCCCCCCC(=O)OCC

Molecular Weight¹

228.37

CAS

106-33-2

Other Names

• Ethyl dodecanoate
• Ethyl dodecylate
• Ethyl ester dodecanoic acid
• Ethyl ester of dodecanoic acid
• Ethyl laurate
• Ethyl laurinate
• Ethyl n-dodecanoate
• Ethyl n-dodecanote
• Lauric acid, ethyl ester

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• 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_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_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (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. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.7511		Relay (1.0) Calculated Property
ΔcH°liquid	-8778.00 ± 1.00	kJ/mol	NIST
ΔfG°	-166.92	kJ/mol	Joback Calculated Property
ΔfH°gas	-658.93	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	39.83	kJ/mol	Solid liquid equilibrium in ternary mixtures of ethyl oleate, ethyl laurate and ethyl palmitate
ΔvapH°	80.00	kJ/mol	NIST
IE	9.58	eV	Relay (1.0) Calculated Property
log10WS	-4.95		Relay (1.0) Calculated Property
logPoct/wat	4.470		Crippen Calculated Property
McVol	215.560	ml/mol	McGowan Calculated Property
Pc	1579.71	kPa	Joback Calculated Property
Inp	[267.60; 1603.00]
Inp	1576.00		NIST
Inp	1578.00		NIST
Inp	1578.00		NIST
Inp	1577.00		NIST
Inp	1588.00		NIST
Inp	1577.00		NIST
Inp	1578.00		NIST
Inp	1579.00		NIST
Inp	1578.00		NIST
Inp	1579.00		NIST
Inp	1558.00		NIST
Inp	1582.00		NIST
Inp	1581.00		NIST
Inp	1593.00		NIST
Inp	1597.00		NIST
Inp	1596.00		NIST
Inp	1566.00		NIST
Inp	1597.00		NIST
Inp	1596.00		NIST
Inp	1581.00		NIST
Inp	1595.00		NIST
Inp	1591.00		NIST
Inp	1577.00		NIST
Inp	1581.00		NIST
Inp	1590.00		NIST
Inp	1591.00		NIST
Inp	1590.00		NIST
Inp	1591.00		NIST
Inp	1591.00		NIST
Inp	1577.00		NIST
Inp	1581.00		NIST
Inp	1579.00		NIST
Inp	1593.00		NIST
Inp	1592.00		NIST
Inp	1595.00		NIST
Inp	1596.00		NIST
Inp	1597.00		NIST
Inp	1588.00		NIST
Inp	1563.00		NIST
Inp	1593.00		NIST
Inp	1593.00		NIST
Inp	1576.00		NIST
Inp	1577.00		NIST
Inp	1596.00		NIST
Inp	1594.00		NIST
Inp	1598.00		NIST
Inp	1595.00		NIST
Inp	1590.00		NIST
Inp	1578.00		NIST
Inp	1591.00		NIST
Inp	1578.00		NIST
Inp	1579.00		NIST
Inp	1578.00		NIST
Inp	1581.00		NIST
Inp	1578.00		NIST
Inp	1579.00		NIST
Inp	1597.00		NIST
Inp	1578.00		NIST
Inp	1579.00		NIST
Inp	1570.00		NIST
Inp	1577.00		NIST
Inp	1592.00		NIST
Inp	1603.00		NIST
Inp	1603.00		NIST
Inp	1595.00		NIST
Inp	1595.00		NIST
Inp	1595.00		NIST
Inp	1590.00		NIST
Inp	1591.00		NIST
Inp	1582.00		NIST
Inp	1576.00		NIST
Inp	1577.00		NIST
Inp	1594.00		NIST
Inp	1597.00		NIST
Inp	1596.00		NIST
Inp	1598.00		NIST
Inp	1579.00		NIST
Inp	1597.00		NIST
Inp	1597.00		NIST
Inp	1597.00		NIST
Inp	1597.00		NIST
Inp	1597.00		NIST
Inp	1583.00		NIST
Inp	1595.00		NIST
Inp	1597.00		NIST
Inp	1579.00		NIST
Inp	1579.00		NIST
Inp	1576.00		NIST
Inp	1577.00		NIST
Inp	Outlier 267.60		NIST
Inp	1593.00		NIST
Inp	1596.00		NIST
Inp	1581.00		NIST
Inp	1591.00		NIST
Inp	1577.00		NIST
Inp	1576.00		NIST
Inp	1558.00		NIST
Inp	1597.00		NIST
Inp	1595.00		NIST
Inp	1579.00		NIST
I	[1811.00; 1874.00]
I	1842.00		NIST
I	1860.00		NIST
I	1840.00		NIST
I	Outlier 1874.00		NIST
I	1846.00		NIST
I	Outlier 1873.00		NIST
I	1844.00		NIST
I	1844.00		NIST
I	1850.00		NIST
I	1847.00		NIST
I	1833.00		NIST
I	1856.00		NIST
I	1825.00		NIST
I	Outlier 1811.00		NIST
I	1848.00		NIST
I	1840.00		NIST
I	1825.00		NIST
I	1825.00		NIST
I	1824.00		NIST
I	1824.00		NIST
I	1848.00		NIST
I	1849.00		NIST
I	1848.00		NIST
I	1849.00		NIST
I	1850.00		NIST
I	1840.00		NIST
I	1851.00		NIST
I	1835.00		NIST
I	1851.00		NIST
I	1849.00		NIST
I	1850.00		NIST
I	1839.00		NIST
I	1850.00		NIST
I	1828.00		NIST
I	1836.00		NIST
I	1865.00		NIST
I	1866.00		NIST
I	1843.00		NIST
I	1830.00		NIST
I	1820.00		NIST
I	1829.00		NIST
I	1826.00		NIST
I	1850.00		NIST
I	1822.00		NIST
I	1820.00		NIST
I	1822.00		NIST
I	1820.00		NIST
I	1822.00		NIST
I	1826.00		NIST
I	1848.00		NIST
I	1850.00		NIST
I	1849.00		NIST
I	1850.00		NIST
I	1835.00		NIST
I	1856.00		NIST
I	1850.00		NIST
I	1850.00		NIST
I	1835.00		NIST
I	1849.00		NIST
I	1818.00		NIST
I	1827.00		NIST
I	1849.00		NIST
I	1839.00		NIST
I	1837.00		NIST
I	1836.00		NIST
I	1818.00		NIST
I	1837.00		NIST
I	1835.00		NIST
I	1833.00		NIST
I	1853.00		NIST
I	1823.00		NIST
I	1851.00		NIST
I	1824.00		NIST
I	1826.00		NIST
I	1850.00		NIST
I	1860.00		NIST
I	1848.00		NIST
I	1826.00		NIST
I	1844.00		NIST
I	1842.00		NIST
I	Outlier 1873.00		NIST
Tboil	[448.00; 463.00]	K
Tboil	448.00 ± 2.00	K	NIST
Tboil	463.00 ± 1.50	K	NIST
Tc	712.20	K	Relay (1.0) Calculated Property
Tfus	[262.50; 273.20]	K
Tfus	273.20	K	Solid-liquid equilibrium in ternary mixtures of ethyl laurate, ethyl palmitate and ethyl stearate
Tfus	272.20	K	High pressure solid-liquid equilibrium of fatty acid ethyl esters binary systems
Tfus	262.50 ± 0.20	K	NIST
Ttriple	273.00	K	Influence of Additives (Isoamyl Laurate or Isoamyl Nonanoate) in the Solid-Liquid Equilibrium of Fatty Acid Ethyl Esters
Vc	0.844	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[567.02; 658.29]	J/mol×K	[596.01; 764.02]
Cp,gas	567.02	J/mol×K	596.01	Joback Calculated Property
Cp,gas	583.90	J/mol×K	624.01	Joback Calculated Property
Cp,gas	600.10	J/mol×K	652.01	Joback Calculated Property
Cp,gas	615.63	J/mol×K	680.02	Joback Calculated Property
Cp,gas	630.49	J/mol×K	708.02	Joback Calculated Property
Cp,gas	644.71	J/mol×K	736.02	Joback Calculated Property
Cp,gas	658.29	J/mol×K	764.02	Joback Calculated Property
η	[0.0011708; 0.0043353]	Pa×s	[283.15; 353.15]
η	0.0043353	Pa×s	283.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0038135	Pa×s	288.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0033797	Pa×s	293.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0030152	Pa×s	298.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0027073	Pa×s	303.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0024455	Pa×s	308.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0022198	Pa×s	313.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0020240	Pa×s	318.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0018531	Pa×s	323.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0017037	Pa×s	328.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0015703	Pa×s	333.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0014529	Pa×s	338.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0013486	Pa×s	343.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0012543	Pa×s	348.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0011708	Pa×s	353.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
ΔfusH	[9.31; 9.31]	kJ/mol	[271.45; 271.50]
ΔfusH	9.31	kJ/mol	271.45	NIST
ΔfusH	9.31	kJ/mol	271.50	NIST
ΔfusH	9.31	kJ/mol	271.50	NIST
ΔvapH	67.20	kJ/mol	410.50	NIST
Pvap	[1.83e-03; 9.33]	kPa	[313.10; 464.35]
Pvap	1.83e-03	kPa	313.10	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.03	kPa	351.88	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.07	kPa	362.10	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.12	kPa	372.12	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.23	kPa	382.17	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.40	kPa	392.24	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.67	kPa	402.20	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	1.33	kPa	420.05	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	1.70	kPa	422.15	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	2.67	kPa	432.13	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	2.65	kPa	432.26	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	3.99	kPa	442.27	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	4.00	kPa	443.41	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	5.33	kPa	451.05	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	5.80	kPa	452.31	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	6.67	kPa	456.47	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	8.49	kPa	462.43	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	8.00	kPa	462.44	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
Pvap	9.33	kPa	464.35	Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
n0	[1.40479; 1.43791]		[278.15; 358.15]
n0	1.43791		278.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43583		283.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43375		288.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43169		293.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42961		298.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42755		303.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42547		308.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42335		313.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42125		318.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41915		323.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41707		328.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41501		333.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41295		338.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41090		343.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40886		348.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40684		353.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40479		358.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	[838.70; 862.16]	kg/m3	[293.15; 323.15]
ρl	862.16	kg/m3	293.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	858.19	kg/m3	298.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	858.25	kg/m3	298.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	854.30	kg/m3	303.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	854.36	kg/m3	303.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	850.46	kg/m3	308.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	850.40	kg/m3	308.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	846.50	kg/m3	313.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	846.56	kg/m3	313.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	842.60	kg/m3	318.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	842.66	kg/m3	318.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	838.70	kg/m3	323.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	838.75	kg/m3	323.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
λ	[0.12; 0.15]	W/m×K	[274.73; 400.08]
λ	0.15	W/m×K	274.73	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.15	W/m×K	284.69	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.15	W/m×K	294.56	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.14	W/m×K	304.59	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.14	W/m×K	314.47	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.14	W/m×K	324.41	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.14	W/m×K	334.28	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.14	W/m×K	344.09	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	349.21	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	354.09	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	359.09	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	369.13	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	379.10	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.13	W/m×K	389.10	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λ	0.12	W/m×K	400.08	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel

Datasets

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

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

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
313.27	140.00	474.00
313.26	5030.00	472.00
313.26	9990.00	471.00
313.27	14970.00	470.00
313.29	20040.00	470.00
313.28	25150.00	469.00
323.22	160.00	480.00
323.23	4980.00	478.00
323.23	10110.00	477.00
323.23	14920.00	476.00
323.22	20140.00	475.00
323.22	25150.00	474.00
333.20	140.00	487.00
333.20	4920.00	485.00
333.20	10150.00	483.00
333.20	15060.00	482.00
333.20	19970.00	481.00
333.21	25020.00	480.00
343.15	140.00	493.00
343.16	5160.00	491.00
343.16	10270.00	489.00
343.19	15130.00	488.00
343.19	20220.00	487.00
343.21	25180.00	486.00
353.14	180.00	501.00
353.14	4970.00	498.00
353.17	9950.00	496.00
353.17	14920.00	494.00
353.17	20020.00	492.00
353.18	24950.00	491.00
363.17	110.00	508.00
363.18	5010.00	507.00
363.29	10190.00	505.00
363.29	15070.00	503.00
363.29	20150.00	501.00
363.29	25100.00	500.00
373.19	110.00	516.00
373.20	4900.00	514.00
373.21	10170.00	512.00
373.21	15020.00	511.00
373.22	19850.00	509.00
373.25	24930.00	508.00
383.23	100.00	523.00
383.23	5000.00	521.00
383.23	10040.00	520.00
383.24	15080.00	518.00
383.25	19940.00	517.00
383.28	25150.00	515.00
393.22	110.00	532.00
393.20	4910.00	530.00
393.22	10100.00	530.00
393.27	15020.00	529.00
393.23	19780.00	528.00
393.27	24830.00	527.00
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	869.69
1000.00	283.15	870.36
3000.00	283.15	871.92
5000.00	283.15	872.91
10000.00	283.15	876.08
15000.00	283.15	878.96
20000.00	283.15	881.89
25000.00	283.15	884.58
30000.00	283.15	887.29
35000.00	283.15	890.05
40000.00	283.15	892.47
50000.00	283.15	897.22
60000.00	283.15	901.93
100.00	293.15	862.5
1000.00	293.15	863.0
3000.00	293.15	864.24
5000.00	293.15	865.2
10000.00	293.15	868.58
15000.00	293.15	871.64
20000.00	293.15	874.58
25000.00	293.15	877.55
30000.00	293.15	880.26
35000.00	293.15	882.89
40000.00	293.15	885.52
50000.00	293.15	890.85
60000.00	293.15	895.29
100.00	303.15	854.28
1000.00	303.15	855.02
3000.00	303.15	856.39
5000.00	303.15	857.69
10000.00	303.15	860.98
15000.00	303.15	864.33
20000.00	303.15	867.23
25000.00	303.15	870.25
30000.00	303.15	873.21
35000.00	303.15	876.08
40000.00	303.15	878.71
50000.00	303.15	883.88
60000.00	303.15	888.85
100.00	313.15	846.91
1000.00	313.15	847.32
3000.00	313.15	848.68
5000.00	313.15	850.07
10000.00	313.15	853.51
15000.00	313.15	856.86
20000.00	313.15	860.1
25000.00	313.15	863.29
30000.00	313.15	866.24
35000.00	313.15	869.1
40000.00	313.15	871.83
50000.00	313.15	877.43
60000.00	313.15	882.35
100.00	323.15	838.9
1000.00	323.15	839.64
3000.00	323.15	841.1
5000.00	323.15	842.59
10000.00	323.15	846.29
15000.00	323.15	849.77
20000.00	323.15	853.3
25000.00	323.15	856.35
30000.00	323.15	859.5
35000.00	323.15	862.45
40000.00	323.15	865.48
50000.00	323.15	871.16
60000.00	323.15	876.11
100.00	333.15	831.05
1000.00	333.15	831.72
3000.00	333.15	833.53
5000.00	333.15	835.15
10000.00	333.15	838.84
15000.00	333.15	842.47
20000.00	333.15	846.07
25000.00	333.15	849.47
30000.00	333.15	852.73
35000.00	333.15	855.75
40000.00	333.15	859.06
50000.00	333.15	864.9
60000.00	333.15	870.44
100.00	343.15	823.11
1000.00	343.15	824.13
3000.00	343.15	825.84
5000.00	343.15	827.55
10000.00	343.15	831.53
15000.00	343.15	835.33
20000.00	343.15	839.18
25000.00	343.15	842.57
30000.00	343.15	846.08
35000.00	343.15	849.44
40000.00	343.15	852.46
50000.00	343.15	858.61
60000.00	343.15	864.08
100.00	353.15	815.47
1000.00	353.15	816.33
3000.00	353.15	818.26
5000.00	353.15	819.99
10000.00	353.15	824.24
15000.00	353.15	828.35
20000.00	353.15	832.01
25000.00	353.15	835.81
30000.00	353.15	839.36
35000.00	353.15	842.72
40000.00	353.15	846.01
50000.00	353.15	852.29
60000.00	353.15	858.27
100.00	363.15	807.52
1000.00	363.15	808.53
3000.00	363.15	810.45
5000.00	363.15	812.32
10000.00	363.15	816.46
15000.00	363.15	821.01
20000.00	363.15	824.82
25000.00	363.15	828.56
30000.00	363.15	832.36
35000.00	363.15	835.98
40000.00	363.15	839.55
50000.00	363.15	845.99
60000.00	363.15	852.14
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.06	100.00	853.9
303.07	3050.00	856.6
303.26	5990.00	858.4
303.22	9020.00	860.5
303.23	11990.00	862.5
303.24	15030.00	864.5
313.08	100.00	846.3
313.08	3010.00	848.3
313.10	5980.00	850.4
313.15	9030.00	852.6
313.17	12010.00	854.4
313.26	15030.00	857.5
323.14	100.00	838.3
323.09	3050.00	840.8
323.17	5980.00	842.9
323.17	8980.00	845.0
323.17	11990.00	847.0
323.18	15020.00	849.0
333.17	100.00	830.8
333.17	3010.00	833.0
333.07	6000.00	835.8
333.20	9040.00	838.1
333.17	12040.00	840.3
333.15	15040.00	842.5
342.95	100.00	823.2
343.00	3000.00	825.3
343.19	5980.00	828.3
343.28	9020.00	830.8
343.19	11980.00	832.8
343.19	15020.00	834.9
353.15	100.00	815.3
353.15	3050.00	818.4
353.20	6030.00	820.9
353.19	9020.00	823.2
353.18	12010.00	825.6
353.19	15020.00	827.9
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	1339.9
293.15	10000.00	1390.8
293.15	20000.00	1436.7
293.15	30000.00	1479.3
293.15	40000.00	1519.0
293.15	50000.00	1555.9
293.15	60000.00	1591.9
293.15	70000.00	1626.2
293.15	80000.00	1659.7
293.15	90000.00	1690.9
293.15	100000.00	1720.9
293.15	120000.00	1778.5
313.15	100.00	1266.1
313.15	10000.00	1317.6
313.15	20000.00	1365.0
313.15	30000.00	1409.3
313.15	40000.00	1452.1
313.15	50000.00	1491.4
313.15	60000.00	1529.2
313.15	70000.00	1564.8
313.15	80000.00	1600.2
313.15	90000.00	1632.3
313.15	100000.00	1663.0
313.15	120000.00	1721.9
313.15	140000.00	1777.9
313.15	160000.00	1830.9
333.15	100.00	1194.0
333.15	10000.00	1250.3
333.15	20000.00	1300.9
333.15	30000.00	1348.0
333.15	40000.00	1393.4
333.15	50000.00	1434.3
333.15	60000.00	1473.3
333.15	70000.00	1509.8
333.15	80000.00	1545.4
333.15	90000.00	1578.6
333.15	100000.00	1610.9
333.15	120000.00	1674.1
333.15	140000.00	1730.4
333.15	160000.00	1782.7
333.15	180000.00	1835.3
333.15	200000.00	1883.8
353.15	100.00	1125.7
353.15	10000.00	1186.0
353.15	20000.00	1240.6
353.15	30000.00	1290.3
353.15	40000.00	1337.1
353.15	50000.00	1379.7
353.15	60000.00	1419.8
353.15	70000.00	1458.8
353.15	80000.00	1496.2
353.15	90000.00	1530.6
353.15	100000.00	1564.4
353.15	120000.00	1627.0
353.15	140000.00	1685.1
353.15	160000.00	1740.7
353.15	180000.00	1793.6
353.15	200000.00	1843.5
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[412.32; 573.39]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.52891e+01
Coefficient B			-4.79892e+03
Coefficient C			-9.24240e+01
Temperature range, min.			412.32
Temperature range, max.			573.39
Pvap	1.33	kPa	412.32	Calculated Property
Pvap	2.95	kPa	430.22	Calculated Property
Pvap	6.03	kPa	448.11	Calculated Property
Pvap	11.51	kPa	466.01	Calculated Property
Pvap	20.71	kPa	483.91	Calculated Property
Pvap	35.40	kPa	501.80	Calculated Property
Pvap	57.84	kPa	519.70	Calculated Property
Pvap	90.85	kPa	537.60	Calculated Property
Pvap	137.80	kPa	555.49	Calculated Property
Pvap	202.64	kPa	573.39	Calculated Property

Similar Compounds

Find more compounds similar to Dodecanoic acid, ethyl ester.

Mixtures

• Dodecanoic acid, ethyl ester + Ethyl Oleate
• Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester
• Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Ethyl Oleate
• Dodecanoic acid, ethyl ester + Octadecanoic acid, ethyl ester
• Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Octadecanoic acid, ethyl ester
• Dodecanoic acid, ethyl ester + Tetradecanoic acid, ethyl ester
• Hexadecane + Dodecanoic acid, ethyl ester
• Dodecanoic acid, ethyl ester + Nonanoic acid, 3-methylbutyl ester
• Isoamyl laurate + Dodecanoic acid, ethyl ester
• Cyclohexane, ethyl- + Dodecanoic acid, ethyl ester
• Dodecanoic acid, ethyl ester + Ethanol
• Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Tetradecanoic acid, ethyl ester
• Dodecanoic acid, ethyl ester + Dodecane
• Carbon dioxide + Dodecanoic acid, ethyl ester

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Measurement and correlation of vapor liquid equilibria for ethanol + ethyl laurate and ethanol + ethyl myristate systems near critical temperature of ethanol
• Solid liquid equilibrium in ternary mixtures of ethyl oleate, ethyl laurate and ethyl palmitate
• Solid-liquid equilibrium in ternary mixtures of ethyl laurate, ethyl palmitate and ethyl stearate
• Solid-liquid equilibrium in ternary mixtures of ethyl laurate, ethyl palmitate and ethyl myristate
• High pressure solid-liquid equilibrium of fatty acid ethyl esters binary systems
• Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
• Experimental and correlational study of isobaric molar heat capacities of fatty acid esters: Ethyl nonanoate and ethyl dodecanoate
• Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
• Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
• High-pressure liquid densities and derived thermodynamic properties for methyl laurate and ethyl laurate
• Phase equilibrium measurements and thermodynamic modeling of binary mixtures containing a diesel compound n-dodecane + biodiesel compounds: Ethyl dodecanoate and ethyl octanoate
• 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
• Thermophysical properties of fatty acid methyl and ethyl esters
• Measurement and correlation of viscosities and densities of methyl dodecanoate and ethyl dodecanoate at elevated pressures
• High Pressure Phase Equilibria of the CO2/Saturated Ethyl Esters Homologous Series
• Influence of Additives (Isoamyl Laurate or Isoamyl Nonanoate) in the Solid-Liquid Equilibrium of Fatty Acid Ethyl Esters
• Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
• Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
• Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
• Joback Method
• 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.
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