Chemical Properties of Decanoic acid, ethyl ester (CAS 110-38-3)

InChI

InChI=1S/C12H24O2/c1-3-5-6-7-8-9-10-11-12(13)14-4-2/h3-11H2,1-2H3

InChI Key

RGXWDWUGBIJHDO-UHFFFAOYSA-N

Formula

C12H24O2

SMILES

CCCCCCCCCC(=O)OCC

Molecular Weight¹

200.32

CAS

110-38-3

Other Names

• Ethyl caprinate
• Ethyl decylate
• Ethyl ester of decanoic acid
• Ethyl n-decanoate
• NSC 8909
• capric acid, ethyl ester
• ethyl caprate
• ethyl decanoate
• n-Capric 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_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : 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 : 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	0.6799		Relay (1.0) Calculated Property
ΔcH°liquid	-7448.00 ± 1.00	kJ/mol	NIST
ΔfG°	-260.21	kJ/mol	Joback Calculated Property
ΔfH°gas	-612.00 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-679.60 ± 1.10	kJ/mol	NIST
ΔfusH°	32.29	kJ/mol	Thermodynamics of Ethyl Decanoate
ΔvapH°	[67.00; 70.50]	kJ/mol
ΔvapH°	70.50	kJ/mol	NIST
ΔvapH°	67.00 ± 1.00	kJ/mol	NIST
ΔvapH°	67.60	kJ/mol	NIST
ΔvapH°	67.40 ± 1.30	kJ/mol	NIST
IE	9.54	eV	Relay (1.0) Calculated Property
log10WS	[-4.10; -4.10]
log10WS	-4.10		Aq. Solubility Prediction
log10WS	-4.10		Estimated Solubility
logPoct/wat	3.690		Crippen Calculated Property
McVol	187.380	ml/mol	McGowan Calculated Property
Pc	1787.88	kPa	Joback Calculated Property
Inp	[235.80; 1407.00]
Inp	1376.00		NIST
Inp	1378.00		NIST
Inp	1380.00		NIST
Inp	1385.00		NIST
Inp	1400.00		NIST
Inp	1376.00		NIST
Inp	1406.00		NIST
Inp	1380.00		NIST
Inp	1379.00		NIST
Inp	1382.00		NIST
Inp	1380.00		NIST
Inp	1379.00		NIST
Inp	1381.00		NIST
Inp	1378.00		NIST
Inp	1378.00		NIST
Inp	1381.00		NIST
Inp	1391.00		NIST
Inp	1386.00		NIST
Inp	1387.00		NIST
Inp	1395.00		NIST
Inp	1393.00		NIST
Inp	1392.00		NIST
Inp	1396.00		NIST
Inp	1367.00		NIST
Inp	1373.00		NIST
Inp	1399.10		NIST
Inp	1380.00		NIST
Inp	1397.00		NIST
Inp	1382.00		NIST
Inp	1394.00		NIST
Inp	1383.00		NIST
Inp	1382.00		NIST
Inp	1395.00		NIST
Inp	1397.00		NIST
Inp	1395.00		NIST
Inp	1397.00		NIST
Inp	1377.00		NIST
Inp	1395.00		NIST
Inp	1397.00		NIST
Inp	1381.00		NIST
Inp	1386.00		NIST
Inp	1379.00		NIST
Inp	1392.20		NIST
Inp	1397.00		NIST
Inp	1405.00		NIST
Inp	1392.00		NIST
Inp	1392.00		NIST
Inp	1399.00		NIST
Inp	1390.00		NIST
Inp	1374.00		NIST
Inp	1374.00		NIST
Inp	1397.00		NIST
Inp	1405.00		NIST
Inp	1407.00		NIST
Inp	1394.00		NIST
Inp	1390.00		NIST
Inp	1394.00		NIST
Inp	1395.00		NIST
Inp	1397.00		NIST
Inp	1394.00		NIST
Inp	1394.00		NIST
Inp	1397.00		NIST
Inp	1390.00		NIST
Inp	1375.00		NIST
Inp	1396.00		NIST
Inp	1380.00		NIST
Inp	1399.00		NIST
Inp	1399.00		NIST
Inp	1395.00		NIST
Inp	1397.00		NIST
Inp	1391.00		NIST
Inp	1378.00		NIST
Inp	1379.00		NIST
Inp	1375.00		NIST
Inp	1380.00		NIST
Inp	1383.00		NIST
Inp	1379.00		NIST
Inp	1379.00		NIST
Inp	1380.00		NIST
Inp	1379.00		NIST
Inp	1381.00		NIST
Inp	1393.00		NIST
Inp	1378.00		NIST
Inp	1398.00		NIST
Inp	1398.00		NIST
Inp	1397.00		NIST
Inp	1403.00		NIST
Inp	1396.00		NIST
Inp	1398.00		NIST
Inp	1397.00		NIST
Inp	1373.00		NIST
Inp	1396.00		NIST
Inp	1392.00		NIST
Inp	1394.00		NIST
Inp	1380.00		NIST
Inp	1376.00		NIST
Inp	1396.00		NIST
Inp	1381.00		NIST
Inp	1398.00		NIST
Inp	1386.00		NIST
Inp	1379.00		NIST
Inp	1397.00		NIST
Inp	1398.00		NIST
Inp	1379.00		NIST
Inp	1397.00		NIST
Inp	1398.00		NIST
Inp	1398.00		NIST
Inp	1383.00		NIST
Inp	1394.00		NIST
Inp	1398.00		NIST
Inp	1378.00		NIST
Inp	1377.00		NIST
Inp	1379.00		NIST
Inp	1379.00		NIST
Inp	1379.00		NIST
Inp	1379.00		NIST
Inp	1378.00		NIST
Inp	1387.00		NIST
Inp	Outlier 235.80		NIST
Inp	Outlier 235.80		NIST
Inp	1395.00		NIST
Inp	1373.00		NIST
Inp	1394.00		NIST
Inp	1381.00		NIST
Inp	1398.00		NIST
Inp	1379.00		NIST
Ip	[1595.00; 1684.00]
Ip	1647.00		NIST
Ip	Outlier 1668.00		NIST
Ip	1639.00		NIST
Ip	Outlier 1678.00		NIST
Ip	1636.00		NIST
Ip	1624.00		NIST
Ip	1624.00		NIST
Ip	1664.00		NIST
Ip	1643.00		NIST
Ip	1634.00		NIST
Ip	1633.00		NIST
Ip	1643.00		NIST
Ip	1647.00		NIST
Ip	1638.00		NIST
Ip	1648.00		NIST
Ip	1633.00		NIST
Ip	1630.00		NIST
Ip	1622.00		NIST
Ip	Outlier 1606.00		NIST
Ip	1644.00		NIST
Ip	Outlier 1595.00		NIST
Ip	1660.00		NIST
Ip	1625.00		NIST
Ip	1635.00		NIST
Ip	1634.00		NIST
Ip	1622.00		NIST
Ip	1624.00		NIST
Ip	1655.00		NIST
Ip	1625.00		NIST
Ip	1625.00		NIST
Ip	1643.00		NIST
Ip	1637.00		NIST
Ip	1637.00		NIST
Ip	1629.00		NIST
Ip	1665.00		NIST
Ip	1631.00		NIST
Ip	1647.00		NIST
Ip	1642.00		NIST
Ip	1638.00		NIST
Ip	1635.00		NIST
Ip	1635.00		NIST
Ip	1639.00		NIST
Ip	1645.00		NIST
Ip	1629.00		NIST
Ip	1635.00		NIST
Ip	1639.00		NIST
Ip	Outlier 1684.00		NIST
Ip	1644.00		NIST
Ip	1635.00		NIST
Ip	1645.00		NIST
Ip	1639.00		NIST
Ip	1638.00		NIST
Ip	1640.00		NIST
Ip	Outlier 1610.00		NIST
Ip	Outlier 1610.00		NIST
Ip	1634.00		NIST
Ip	1644.00		NIST
Ip	1659.00		NIST
Ip	1625.00		NIST
Ip	1647.00		NIST
Ip	1648.00		NIST
Ip	1630.00		NIST
Ip	1615.00		NIST
Ip	1665.00		NIST
Ip	1632.00		NIST
Ip	1642.00		NIST
Ip	1645.00		NIST
Ip	1634.00		NIST
Ip	Outlier 1678.00		NIST
Ip	1634.00		NIST
Ip	1634.00		NIST
Ip	1634.00		NIST
Ip	1637.00		NIST
Ip	1624.00		NIST
Ip	1644.00		NIST
Ip	1626.00		NIST
Ip	1626.00		NIST
Ip	1626.00		NIST
Ip	1626.00		NIST
Ip	1624.00		NIST
Ip	1643.00		NIST
Ip	1635.00		NIST
Ip	1645.00		NIST
Ip	1652.00		NIST
Ip	1647.00		NIST
Ip	1638.00		NIST
Ip	1643.00		NIST
Ip	1662.00		NIST
Ip	1647.00		NIST
Ip	1652.00		NIST
Ip	1652.00		NIST
Ip	1629.00		NIST
Ip	1651.00		NIST
Ip	1623.00		NIST
Ip	1651.00		NIST
Ip	1639.00		NIST
Ip	1651.00		NIST
Ip	1644.00		NIST
Ip	1625.00		NIST
Ip	1665.00		NIST
Ip	1634.00		NIST
Ip	1648.00		NIST
Ip	1624.00		NIST
Ip	1647.00		NIST
Ip	1624.00		NIST
Ip	1633.00		NIST
Ip	1647.00		NIST
Ip	1635.00		NIST
Ip	Outlier 1610.00		NIST
Ip	1655.00		NIST
Ip	1631.00		NIST
Ip	1622.00		NIST
Ip	1639.00		NIST
Ip	1623.00		NIST
Ip	1646.00		NIST
Ip	1651.00		NIST
Ip	1639.00		NIST
Ip	1645.00		NIST
Ip	1624.00		NIST
Ip	1631.00		NIST
Ip	1645.00		NIST
Ip	1647.00		NIST
Ip	1633.00		NIST
Ip	1647.00		NIST
Ip	1639.00		NIST
Ip	Outlier 1684.00		NIST
Ip	1643.00		NIST
Ip	1638.00		NIST
Ip	1652.00		NIST
Ip	1634.00		NIST
Ip	1631.00		NIST
Ip	1651.00		NIST
Ip	1645.00		NIST
Tboil	[514.70; 518.20]	K
Tboil	518.20	K	NIST
Tboil	514.70 ± 1.00	K	NIST
Tboil	518.05 ± 1.00	K	NIST
Tc	688.19	K	Relay (1.0) Calculated Property
Tfus	253.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Ttriple	252.00	K	Heat capacities of potential organic phase change materials
Vc	0.735	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	[0.0008929; 0.0028960]	Pa×s	[283.15; 353.15]
η	0.0028960	Pa×s	283.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0025882	Pa×s	288.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0023263	Pa×s	293.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0021029	Pa×s	298.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0019111	Pa×s	303.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0017453	Pa×s	308.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0016000	Pa×s	313.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0014729	Pa×s	318.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0013599	Pa×s	323.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0012594	Pa×s	328.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0011695	Pa×s	333.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0010892	Pa×s	338.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0010171	Pa×s	343.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0009516	Pa×s	348.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
η	0.0008929	Pa×s	353.15	Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
ΔfusH	32.29	kJ/mol	187.50	NIST
ΔvapH	[58.40; 69.90]	kJ/mol	[305.00; 437.00]
ΔvapH	69.90 ± 0.70	kJ/mol	305.00	NIST
ΔvapH	58.40 ± 0.10	kJ/mol	422.00	NIST
ΔvapH	59.60	kJ/mol	437.00	NIST
Pvap	[4.46e-03; 22.35]	kPa	[303.10; 462.37]
Pvap	4.46e-03	kPa	303.10	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.01	kPa	313.16	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.05	kPa	333.23	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.10	kPa	343.20	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.18	kPa	353.16	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.33	kPa	363.12	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	0.58	kPa	373.15	Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap	0.98	kPa	383.15	Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap	1.59	kPa	393.15	Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap	2.50	kPa	403.15	Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap	3.65	kPa	412.15	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	3.83	kPa	413.15	Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap	5.47	kPa	422.13	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	5.73	kPa	423.15	Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap	8.07	kPa	432.24	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	8.37	kPa	433.15	Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap	11.55	kPa	442.23	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	11.99	kPa	443.15	Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap	16.28	kPa	452.28	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
Pvap	16.84	kPa	453.15	Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
Pvap	22.35	kPa	462.37	Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
n0	[1.39826; 1.43213]		[278.15; 358.15]
n0	1.43213		278.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.43000		283.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42789		288.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42577		293.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42366		298.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.42155		303.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41944		308.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41729		313.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41512		318.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41297		323.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.41084		328.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40873		333.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40661		338.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40451		343.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40241		348.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.40034		353.15	Thermophysical properties of fatty acid methyl and ethyl esters
n0	1.39826		358.15	Thermophysical properties of fatty acid methyl and ethyl esters
ρl	[839.64; 864.06]	kg/m3	[293.15; 323.15]
ρl	864.06	kg/m3	293.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	860.05	kg/m3	298.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	860.01	kg/m3	298.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	855.99	kg/m3	303.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	855.94	kg/m3	303.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	851.87	kg/m3	308.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	851.92	kg/m3	308.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	847.85	kg/m3	313.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	847.80	kg/m3	313.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	843.77	kg/m3	318.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	843.72	kg/m3	318.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	839.69	kg/m3	323.15	Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
ρl	839.64	kg/m3	323.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
λliquid	[0.12; 0.15]	W/m×K	[270.00; 400.44]
λliquid	0.15	W/m×K	270.00	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.15	W/m×K	279.98	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.14	W/m×K	289.85	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.14	W/m×K	299.64	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.14	W/m×K	309.60	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.14	W/m×K	319.72	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.14	W/m×K	329.53	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.13	W/m×K	339.49	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.13	W/m×K	349.51	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.13	W/m×K	359.46	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.13	W/m×K	369.30	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.12	W/m×K	374.44	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.12	W/m×K	379.49	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.12	W/m×K	389.25	Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
λliquid	0.12	W/m×K	400.44	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. Viscosity, Pa*s (1)
3. Speed of sound, m/s (3)

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
294.00	100.00	400.39
294.00	3080.00	399.98
294.00	6090.00	399.53
294.00	8970.00	399.07
294.00	12120.00	398.72
294.10	14870.00	398.28
294.10	17910.00	397.82
294.10	21090.00	397.38
294.10	24040.00	396.93
304.00	130.00	406.09
304.00	3030.00	405.62
304.00	6160.00	405.12
304.00	9030.00	404.66
304.00	11950.00	404.19
304.00	15090.00	403.69
304.00	17870.00	403.23
304.10	21100.00	402.75
304.10	24050.00	402.24
313.90	110.00	411.45
313.90	2920.00	410.92
313.90	5990.00	410.45
313.90	9080.00	409.95
314.00	11910.00	409.43
314.00	15030.00	408.93
314.00	18090.00	408.41
314.00	21080.00	407.89
314.00	24110.00	407.34
323.80	150.00	416.54
323.90	3040.00	416.03
323.90	5930.00	415.53
323.90	9070.00	415.03
323.90	11980.00	414.54
323.90	15050.00	414.03
324.00	18050.00	413.54
324.00	21210.00	413.06
324.00	24030.00	412.57
333.80	120.00	423.19
333.80	2960.00	422.70
333.80	5990.00	422.28
333.80	9040.00	421.77
333.90	12030.00	421.17
333.90	14940.00	420.66
333.90	18050.00	420.15
333.90	21100.00	419.65
334.00	24050.00	419.11
343.70	150.00	429.52
343.70	3000.00	429.02
343.70	6190.00	428.50
343.80	8990.00	427.96
343.80	12100.00	427.46
343.80	14910.00	426.93
343.80	17990.00	426.40
343.80	21010.00	426.07
343.90	23970.00	425.54
353.70	110.00	435.96
353.70	2980.00	435.41
353.70	6020.00	434.91
353.70	8990.00	434.40
353.80	11920.00	433.87
353.80	14940.00	433.36
353.80	17960.00	432.85
353.80	21070.00	432.33
353.90	23980.00	431.81
Reference

Viscosity, Pa*s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.30	293.15	0.0023
20000.00	293.15	0.0029
40000.00	293.15	0.0036
60000.00	293.15	0.0044
80000.00	293.15	0.0053
100000.00	293.15	0.0063
120000.00	293.15	0.0075
140000.00	293.15	0.0088
160000.00	293.15	0.0103
180000.00	293.15	0.0121
200000.00	293.15	0.0141
101.30	313.15	0.0016
20000.00	313.15	0.0020
40000.00	313.15	0.0024
60000.00	313.15	0.0029
80000.00	313.15	0.0034
100000.00	313.15	0.0040
120000.00	313.15	0.0046
140000.00	313.15	0.0053
160000.00	313.15	0.0062
180000.00	313.15	0.0071
200000.00	313.15	0.0082
101.30	333.15	0.0012
20000.00	333.15	0.0014
40000.00	333.15	0.0017
60000.00	333.15	0.0021
80000.00	333.15	0.0024
100000.00	333.15	0.0028
120000.00	333.15	0.0032
140000.00	333.15	0.0037
160000.00	333.15	0.0042
180000.00	333.15	0.0048
200000.00	333.15	0.0054
101.30	353.15	0.0009
20000.00	353.15	0.0011
40000.00	353.15	0.0013
60000.00	353.15	0.0016
80000.00	353.15	0.0018
100000.00	353.15	0.0021
120000.00	353.15	0.0024
140000.00	353.15	0.0027
160000.00	353.15	0.0031
180000.00	353.15	0.0035
200000.00	353.15	0.0039
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
300.78	100.00	1283.2
310.85	100.00	1248.4
320.90	100.00	1213.6
330.81	100.00	1178.4
340.24	100.00	1144.5
350.99	100.00	1106.3
360.32	100.00	1073.2
371.22	100.00	1035.6
379.78	100.00	1005.8
389.06	100.00	973.3
400.76	100.00	933.3
410.85	100.00	900.2
419.60	100.00	871.4
429.56	100.00	839.8
439.28	100.00	809.5
451.03	100.00	773.3
460.11	100.00	746.8
469.45	100.00	719.5
479.25	100.00	691.6
340.79	3000.00	1157.6
350.77	3000.00	1124.1
360.75	3000.00	1090.9
371.46	3000.00	1054.6
379.78	3000.00	1026.4
311.01	3000.00	1258.4
389.32	3000.00	996.7
400.79	3000.00	958.4
408.81	3000.00	933.4
320.94	3000.00	1226.4
419.67	3000.00	899.1
429.56	3000.00	868.5
439.85	3000.00	836.6
450.25	3000.00	805.8
330.76	3000.00	1192.9
459.85	3000.00	778.6
469.25	3000.00	752.4
300.79	3000.00	1290.7
479.29	3000.00	724.5
490.81	3000.00	693.8
500.76	3000.00	667.8
510.65	3000.00	642.8
520.19	3000.00	619.7
530.36	3000.00	595.4
540.66	3000.00	570.8
548.94	3000.00	551.9
558.46	3000.00	529.8
389.19	5000.00	1010.9
400.90	5000.00	973.6
409.55	5000.00	946.8
320.91	5000.00	1233.3
350.97	5000.00	1133.3
419.68	5000.00	915.0
429.60	5000.00	884.8
310.85	5000.00	1265.0
440.02	5000.00	854.6
360.51	5000.00	1102.5
450.25	5000.00	825.6
458.86	5000.00	801.3
300.81	5000.00	1295.7
469.28	5000.00	771.9
479.90	5000.00	743.2
490.41	5000.00	715.7
371.31	5000.00	1068.1
500.41	5000.00	690.3
510.27	5000.00	666.3
379.62	5000.00	1040.4
520.25	5000.00	642.5
529.91	5000.00	619.5
540.12	5000.00	595.3
340.76	5000.00	1166.4
549.74	5000.00	574.5
330.87	5000.00	1199.5
559.93	5000.00	551.9
440.37	7000.00	871.6
449.52	7000.00	845.4
350.89	7000.00	1145.9
360.55	7000.00	1115.4
410.30	7000.00	960.7
330.77	7000.00	1210.4
460.20	7000.00	816.0
469.32	7000.00	792.0
300.71	7000.00	1302.7
371.22	7000.00	1081.7
479.47	7000.00	764.5
488.69	7000.00	740.9
339.12	7000.00	1183.0
419.73	7000.00	932.2
500.55	7000.00	711.6
510.41	7000.00	686.9
379.56	7000.00	1055.4
320.98	7000.00	1241.3
520.27	7000.00	664.6
400.81	7000.00	989.3
530.11	7000.00	641.3
310.93	7000.00	1271.5
540.06	7000.00	618.1
430.45	7000.00	901.1
549.99	7000.00	596.7
389.22	7000.00	1025.0
562.07	7000.00	570.2
411.61	10000.00	983.4
448.51	10000.00	878.1
340.56	10000.00	1209.4
509.33	10000.00	722.7
423.29	10000.00	949.4
330.79	10000.00	1239.7
470.42	10000.00	819.1
520.04	10000.00	696.8
392.15	10000.00	1042.5
360.27	10000.00	1145.7
350.12	10000.00	1179.1
529.04	10000.00	678.0
401.26	10000.00	1015.0
300.78	10000.00	1329.5
481.50	10000.00	791.1
463.71	10000.00	837.3
540.09	10000.00	651.8
310.58	10000.00	1301.3
432.01	10000.00	925.0
383.22	10000.00	1069.6
439.20	10000.00	903.9
549.87	10000.00	630.6
369.47	10000.00	1115.6
321.00	10000.00	1269.6
492.02	10000.00	764.5
561.00	10000.00	607.0
499.48	10000.00	745.9
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
283.15	101.30	1352.7
283.15	10000.00	1398.5
283.15	20000.00	1442.3
283.15	30000.00	1483.7
283.15	40000.00	1522.5
283.15	50000.00	1558.3
283.15	60000.00	1593.9
283.15	70000.00	1627.0
283.15	80000.00	1658.8
283.15	90000.00	1689.9
283.15	100000.00	1720.7
283.15	110000.00	1753.7
283.15	120000.00	1781.4
283.15	130000.00	1808.5
283.15	140000.00	1834.6
283.15	150000.00	1860.3
283.15	170000.00	1908.7
283.15	190000.00	1951.8
283.15	210000.00	1998.0
303.15	101.30	1275.0
303.15	10000.00	1325.7
303.15	20000.00	1373.2
303.15	30000.00	1416.8
303.15	40000.00	1458.3
303.15	50000.00	1498.0
303.15	60000.00	1535.5
303.15	70000.00	1569.9
303.15	80000.00	1603.2
303.15	90000.00	1635.3
303.15	100000.00	1666.2
303.15	110000.00	1696.2
303.15	120000.00	1724.8
303.15	130000.00	1752.9
303.15	140000.00	1779.2
303.15	150000.00	1805.4
303.15	170000.00	1854.6
303.15	190000.00	1902.4
303.15	210000.00	1947.7
323.15	101.30	1203.1
323.15	10000.00	1258.2
323.15	20000.00	1309.5
323.15	30000.00	1355.9
323.15	40000.00	1399.1
323.15	50000.00	1439.4
323.15	60000.00	1478.4
323.15	70000.00	1515.1
323.15	80000.00	1550.3
323.15	90000.00	1583.7
323.15	100000.00	1615.7
323.15	110000.00	1645.8
323.15	120000.00	1676.7
323.15	130000.00	1705.7
323.15	140000.00	1733.7
323.15	150000.00	1760.3
323.15	170000.00	1811.6
323.15	190000.00	1861.2
323.15	210000.00	1909.8
343.15	101.30	1133.3
343.15	10000.00	1192.8
343.15	20000.00	1247.0
343.15	30000.00	1297.2
343.15	40000.00	1343.0
343.15	50000.00	1385.7
343.15	60000.00	1425.7
343.15	70000.00	1463.9
343.15	80000.00	1500.3
343.15	90000.00	1535.3
343.15	100000.00	1568.4
343.15	110000.00	1600.4
343.15	120000.00	1631.5
343.15	130000.00	1661.5
343.15	140000.00	1690.0
343.15	150000.00	1717.3
343.15	170000.00	1769.7
343.15	190000.00	1818.5
343.15	210000.00	1865.0
363.15	101.30	1065.9
363.15	10000.00	1130.1
363.15	20000.00	1188.5
363.15	30000.00	1241.2
363.15	40000.00	1289.6
363.15	50000.00	1334.7
363.15	60000.00	1376.5
363.15	70000.00	1415.4
363.15	80000.00	1452.8
363.15	90000.00	1488.9
363.15	100000.00	1522.8
363.15	110000.00	1556.0
363.15	120000.00	1586.9
363.15	130000.00	1617.1
363.15	140000.00	1646.6
363.15	150000.00	1675.1
363.15	170000.00	1727.6
363.15	190000.00	1777.0
363.15	210000.00	1824.5
383.15	101.30	1001.3
383.15	10000.00	1071.1
383.15	20000.00	1132.9
383.15	30000.00	1188.3
383.15	40000.00	1239.3
383.15	50000.00	1286.4
383.15	60000.00	1329.7
383.15	70000.00	1370.2
383.15	80000.00	1408.3
383.15	90000.00	1445.0
383.15	100000.00	1480.0
383.15	110000.00	1513.4
383.15	120000.00	1545.8
383.15	130000.00	1576.6
383.15	140000.00	1606.2
383.15	150000.00	1634.6
383.15	170000.00	1687.7
383.15	190000.00	1740.7
383.15	210000.00	1786.8
403.15	101.30	937.8
403.15	10000.00	1013.4
403.15	20000.00	1080.3
403.15	30000.00	1138.6
403.15	40000.00	1191.3
403.15	50000.00	1240.5
403.15	60000.00	1285.9
403.15	70000.00	1328.1
403.15	80000.00	1367.6
403.15	90000.00	1404.6
403.15	100000.00	1439.8
403.15	110000.00	1473.4
403.15	120000.00	1506.4
403.15	130000.00	1537.5
403.15	140000.00	1567.3
403.15	150000.00	1596.2
403.15	170000.00	1650.9
403.15	190000.00	1702.8
403.15	210000.00	1751.8
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
292.92	100.00	1313.79
292.91	15200.00	1389.41
292.90	30390.00	1453.47
292.90	45590.00	1511.65
292.90	60790.00	1565.94
292.90	75990.00	1616.66
292.91	91180.00	1664.29
292.90	101320.00	1693.93
298.18	100.00	1293.91
298.18	15200.00	1370.56
298.17	30390.00	1436.06
298.17	45590.00	1494.88
298.17	60790.00	1549.43
298.17	75990.00	1601.26
298.17	91180.00	1648.56
298.17	101320.00	1678.78
303.16	100.00	1275.23
303.17	15200.00	1353.08
303.16	30390.00	1419.13
303.16	45590.00	1479.56
303.16	60790.00	1534.66
303.16	75990.00	1586.89
303.16	91180.00	1634.96
303.16	101320.00	1665.86
308.14	100.00	1256.76
308.14	15200.00	1335.4
308.14	30390.00	1403.03
308.13	45590.00	1464.56
308.14	60790.00	1520.06
308.13	75990.00	1572.07
308.14	91180.00	1621.75
308.13	101320.00	1652.91
313.11	100.00	1238.5
313.11	15200.00	1318.7
313.10	30390.00	1387.45
313.09	45590.00	1449.78
313.10	60790.00	1506.18
313.09	75990.00	1559.16
313.09	91180.00	1608.6
313.09	101320.00	1638.96
318.28	100.00	1219.66
318.27	15200.00	1301.59
318.27	30390.00	1371.72
318.27	45590.00	1434.89
318.27	60790.00	1491.63
318.26	75990.00	1544.9
318.26	91180.00	1594.65
318.26	101320.00	1626.53
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[276.38; 646.53]	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			1.73890e+01
Coefficient B			1.08904e+00
Coefficient C			-5.34400e-04
Coefficient D			7.45000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	276.38	J/mol×K	273.00	Calculated Property
Cp,gas	339.08	J/mol×K	353.78	Calculated Property
Cp,gas	395.84	J/mol×K	434.56	Calculated Property
Cp,gas	446.88	J/mol×K	515.33	Calculated Property
Cp,gas	492.46	J/mol×K	596.11	Calculated Property
Cp,gas	532.80	J/mol×K	676.89	Calculated Property
Cp,gas	568.14	J/mol×K	757.67	Calculated Property
Cp,gas	598.72	J/mol×K	838.44	Calculated Property
Cp,gas	624.77	J/mol×K	919.22	Calculated Property
Cp,gas	646.53	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[388.72; 549.89]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.48029e+01
Coefficient B			-4.41987e+03
Coefficient C			-8.42230e+01
Temperature range, min.			388.72
Temperature range, max.			549.89
Pvap	1.33	kPa	388.72	Calculated Property
Pvap	2.99	kPa	406.63	Calculated Property
Pvap	6.14	kPa	424.54	Calculated Property
Pvap	11.76	kPa	442.44	Calculated Property
Pvap	21.16	kPa	460.35	Calculated Property
Pvap	36.09	kPa	478.26	Calculated Property
Pvap	58.77	kPa	496.17	Calculated Property
Pvap	91.89	kPa	514.07	Calculated Property
Pvap	138.63	kPa	531.98	Calculated Property
Pvap	202.64	kPa	549.89	Calculated Property

Similar Compounds

Find more compounds similar to Decanoic acid, ethyl ester.

Mixtures

• Decanoic acid, ethyl ester + Hexadecane
• Decanoic acid, ethyl ester + Tetradecane
• Decanoic acid, ethyl ester + Carbon dioxide
• Decanoic acid, ethyl ester + Cyclohexane, ethyl-

Sources

• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Cheméo Relay (1.0)
• Crippen Method
• Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
• Experimental investigation and modeling of thermophysical properties of ethyl decanoate at high temperatures
• Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
• Heat capacities of potential organic phase change materials
• Thermophysical properties of fatty acid methyl and ethyl esters
• High Pressure Phase Equilibria of the CO2/Saturated Ethyl Esters Homologous Series
• Isobaric Molar Heat Capacity of Ethyl Octanoate and Ethyl Decanoate at Pressures up to 24 MPa
• 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
• Speed of Sound, Density, and Derivative Properties of Fatty Acid Methyl and Ethyl Esters under High Pressure: Methyl Caprate and Ethyl Caprate
• Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
• High-Pressure Physicochemical Properties of Ethyl Caprylate and Ethyl Caprate
• Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
• Viscosities of Fatty Acid Methyl and Ethyl Esters under High Pressure: Methyl Caprate and Ethyl Caprate
• Thermodynamics of Ethyl Decanoate
• Joback Method
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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