Chemical Properties of Decanoic acid, methyl ester (CAS 110-42-9)

InChI

InChI=1S/C11H22O2/c1-3-4-5-6-7-8-9-10-11(12)13-2/h3-10H2,1-2H3

InChI Key

YRHYCMZPEVDGFQ-UHFFFAOYSA-N

Formula

C11H22O2

SMILES

CCCCCCCCCC(=O)OC

Molecular Weight¹

186.29

CAS

110-42-9

Other Names

• Capric acid methyl ester
• Metholene 2095
• Methyl caprate
• Methyl caprinate
• Methyl decanoate
• Methyl n-decanoate
• Methyl tridecanoate
• Methyl-n-caprate
• Uniphat A30
• capric acid, methyl ester
• n-Capric acid methyl ester

• 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_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• 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
ΔcH°liquid	[-6831.90; -6799.00]	kJ/mol
ΔcH°liquid	-6799.00 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-6831.90 ± 1.70	kJ/mol	NIST
ΔfG°	-192.18	kJ/mol	Joback Calculated Property
ΔfH°gas	-515.17	kJ/mol	Joback Calculated Property
ΔfusH°	35.92	kJ/mol	Heat Ca...
ΔvapH°	[66.10; 66.90]	kJ/mol
ΔvapH°	66.10 ± 0.20	kJ/mol	NIST
ΔvapH°	66.90	kJ/mol	NIST
ΔvapH°	66.30 ± 0.50	kJ/mol	NIST
ΔvapH°	66.75 ± 0.57	kJ/mol	NIST
ΔvapH°	66.80 ± 0.60	kJ/mol	NIST
log10WS	[-4.69; -4.63]
log10WS	-4.63		Aq. Sol...
log10WS	-4.69		Estimat...
logPoct/wat	3.300		Crippen Calculated Property
McVol	173.290	ml/mol	McGowan Calculated Property
Pc	2014.51	kPa	Joback Calculated Property
Inp	[224.56; 1333.00]
Inp	1323.80		NIST
Inp	1319.30		NIST
Inp	1313.00		NIST
Inp	1321.00		NIST
Inp	1312.00		NIST
Inp	1306.00		NIST
Inp	1310.00		NIST
Inp	1307.00		NIST
Inp	1308.00		NIST
Inp	1328.00		NIST
Inp	1324.00		NIST
Inp	1307.00		NIST
Inp	1305.00		NIST
Inp	1324.00		NIST
Inp	1327.00		NIST
Inp	1325.00		NIST
Inp	1325.10		NIST
Inp	1328.00		NIST
Inp	1326.00		NIST
Inp	1326.00		NIST
Inp	1325.00		NIST
Inp	1325.00		NIST
Inp	1309.00		NIST
Inp	1324.00		NIST
Inp	1326.00		NIST
Inp	1306.00		NIST
Inp	1312.00		NIST
Inp	1310.00		NIST
Inp	1311.40		NIST
Inp	1307.00		NIST
Inp	1306.20		NIST
Inp	1306.60		NIST
Inp	1309.00		NIST
Inp	1303.76		NIST
Inp	1309.67		NIST
Inp	1309.08		NIST
Inp	1320.62		NIST
Inp	1311.06		NIST
Inp	1313.09		NIST
Inp	1306.48		NIST
Inp	1324.00		NIST
Inp	1310.00		NIST
Inp	1322.60		NIST
Inp	1328.60		NIST
Inp	1326.00		NIST
Inp	1306.00		NIST
Inp	1307.00		NIST
Inp	1309.00		NIST
Inp	1321.00		NIST
Inp	1305.00		NIST
Inp	1316.00		NIST
Inp	1325.00		NIST
Inp	1325.00		NIST
Inp	1326.00		NIST
Inp	1325.00		NIST
Inp	1326.00		NIST
Inp	1333.00		NIST
Inp	1327.00		NIST
Inp	1326.00		NIST
Inp	1311.00		NIST
Inp	1327.00		NIST
Inp	1326.00		NIST
Inp	1306.00		NIST
Inp	1326.00		NIST
Inp	1305.00		NIST
Inp	1306.00		NIST
Inp	1308.00		NIST
Inp	1313.00		NIST
Inp	1307.00		NIST
Inp	1307.00		NIST
Inp	1308.00		NIST
Inp	1307.00		NIST
Inp	1306.00		NIST
Inp	1323.00		NIST
Inp	1326.00		NIST
Inp	1325.00		NIST
Inp	1328.00		NIST
Inp	1325.00		NIST
Inp	1326.00		NIST
Inp	1322.00		NIST
Inp	1326.00		NIST
Inp	1302.00		NIST
Inp	1324.00		NIST
Inp	1324.00		NIST
Inp	1325.00		NIST
Inp	1307.00		NIST
Inp	1329.00		NIST
Inp	1307.00		NIST
Inp	1328.00		NIST
Inp	1328.00		NIST
Inp	1314.00		NIST
Inp	1309.00		NIST
Inp	1306.00		NIST
Inp	1307.00		NIST
Inp	1308.00		NIST
Inp	1305.00		NIST
Inp	Outlier 224.56		NIST
Inp	Outlier 226.16		NIST
Inp	Outlier 230.80		NIST
Inp	Outlier 226.04		NIST
Inp	Outlier 226.04		NIST
I	[1550.00; 1636.00]
I	1597.00		NIST
I	Outlier 1636.00		NIST
I	1624.00		NIST
I	1570.00		NIST
I	1598.30		NIST
I	1603.00		NIST
I	1605.20		NIST
I	1616.30		NIST
I	1592.50		NIST
I	1600.70		NIST
I	1606.90		NIST
I	1613.20		NIST
I	1581.00		NIST
I	1581.00		NIST
I	1592.00		NIST
I	1593.00		NIST
I	1615.00		NIST
I	1586.00		NIST
I	1583.00		NIST
I	1614.00		NIST
I	1597.00		NIST
I	1603.00		NIST
I	1586.00		NIST
I	1590.00		NIST
I	1613.00		NIST
I	1585.00		NIST
I	1594.00		NIST
I	1604.00		NIST
I	1599.00		NIST
I	Outlier 1550.00		NIST
I	Outlier 1552.00		NIST
I	1590.00		NIST
I	1586.00		NIST
I	1596.00		NIST
I	1581.00		NIST
I	1602.00		NIST
I	1583.00		NIST
I	1584.00		NIST
I	1595.00		NIST
I	1593.00		NIST
I	1600.00		NIST
I	1585.00		NIST
I	1628.00		NIST
I	1628.00		NIST
I	1593.00		NIST
I	1628.00		NIST
I	1585.00		NIST
I	1581.00		NIST
I	1573.00		NIST
I	1600.00		NIST
I	1586.00		NIST
Tboil	[497.05; 497.20]	K
Tboil	497.20	K	NIST
Tboil	497.05 ± 1.00	K	NIST
Tc	698.36	K	Joback Calculated Property
Tfus	260.40 ± 0.05	K	NIST
Vc	0.675	m3/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[415.24; 496.57]	J/mol×K	[527.37; 698.36]
Cp,gas	415.24	J/mol×K	527.37	Joback Calculated Property
Cp,gas	430.19	J/mol×K	555.87	Joback Calculated Property
Cp,gas	444.58	J/mol×K	584.37	Joback Calculated Property
Cp,gas	458.41	J/mol×K	612.87	Joback Calculated Property
Cp,gas	471.67	J/mol×K	641.36	Joback Calculated Property
Cp,gas	484.39	J/mol×K	669.86	Joback Calculated Property
Cp,gas	496.57	J/mol×K	698.36	Joback Calculated Property
Cp,liquid	[382.80; 417.20]	J/mol×K	[298.15; 373.15]
Cp,liquid	382.80	J/mol×K	298.15	NIST
Cp,liquid	384.70	J/mol×K	303.15	Heat ca...
Cp,liquid	387.60	J/mol×K	313.15	Heat ca...
Cp,liquid	391.80	J/mol×K	323.15	Heat ca...
Cp,liquid	396.70	J/mol×K	333.15	Heat ca...
Cp,liquid	401.90	J/mol×K	343.15	Heat ca...
Cp,liquid	407.30	J/mol×K	353.15	Heat ca...
Cp,liquid	412.40	J/mol×K	363.15	Heat ca...
Cp,liquid	417.20	J/mol×K	373.15	Heat ca...
η	[0.0007421; 0.0029888]	Pa×s	[278.15; 363.15]
η	0.0029888	Pa×s	278.15	Densiti...
η	0.0026543	Pa×s	283.15	Densiti...
η	0.0023733	Pa×s	288.15	Densiti...
η	0.0021360	Pa×s	293.15	Densiti...
η	0.0019335	Pa×s	298.15	Densiti...
η	0.0017601	Pa×s	303.15	Densiti...
η	0.0016091	Pa×s	308.15	Densiti...
η	0.0014773	Pa×s	313.15	Densiti...
η	0.0013613	Pa×s	318.15	Densiti...
η	0.0012589	Pa×s	323.15	Densiti...
η	0.0011675	Pa×s	328.15	Densiti...
η	0.0010864	Pa×s	333.15	Densiti...
η	0.0010133	Pa×s	338.15	Densiti...
η	0.0009477	Pa×s	343.15	Densiti...
η	0.0008886	Pa×s	348.15	Densiti...
η	0.0008342	Pa×s	353.15	Densiti...
η	0.0007859	Pa×s	358.15	Densiti...
η	0.0007421	Pa×s	363.15	Densiti...
ΔvapH	[49.90; 63.05]	kJ/mol	[293.00; 498.00]
ΔvapH	63.05	kJ/mol	293.00	NIST
ΔvapH	62.90 ± 0.10	kJ/mol	337.00	NIST
ΔvapH	63.00	kJ/mol	347.00	NIST
ΔvapH	62.00	kJ/mol	350.00	NIST
ΔvapH	57.10	kJ/mol	439.50	NIST
ΔvapH	49.90	kJ/mol	498.00	NIST
Pvap	[4.73e-04; 12.80]	kPa	[273.35; 432.65]
Pvap	4.73e-04	kPa	273.35	Fatty a...
Pvap	4.98e-04	kPa	273.84	Fatty a...
Pvap	5.25e-04	kPa	274.32	Fatty a...
Pvap	5.54e-04	kPa	274.80	Fatty a...
Pvap	5.88e-04	kPa	275.29	Fatty a...
Pvap	6.15e-04	kPa	275.77	Fatty a...
Pvap	6.49e-04	kPa	276.26	Fatty a...
Pvap	6.85e-04	kPa	276.74	Fatty a...
Pvap	7.23e-04	kPa	277.23	Fatty a...
Pvap	7.60e-04	kPa	277.71	Fatty a...
Pvap	8.03e-04	kPa	278.20	Fatty a...
Pvap	8.44e-04	kPa	278.69	Fatty a...
Pvap	8.87e-04	kPa	279.18	Fatty a...
Pvap	9.34e-04	kPa	279.66	Fatty a...
Pvap	9.82e-04	kPa	280.15	Fatty a...
Pvap	1.03e-03	kPa	280.64	Fatty a...
Pvap	1.09e-03	kPa	281.12	Fatty a...
Pvap	1.13e-03	kPa	281.47	Fatty a...
Pvap	1.31e-03	kPa	282.96	Fatty a...
Pvap	1.39e-03	kPa	283.48	Fatty a...
Pvap	1.53e-03	kPa	284.46	Fatty a...
Pvap	1.61e-03	kPa	284.96	Fatty a...
Pvap	1.69e-03	kPa	285.43	Fatty a...
Pvap	1.73e-03	kPa	285.64	Fatty a...
Pvap	1.74e-03	kPa	285.74	Fatty a...
Pvap	1.78e-03	kPa	285.95	Fatty a...
Pvap	1.87e-03	kPa	286.44	Fatty a...
Pvap	1.97e-03	kPa	286.95	Fatty a...
Pvap	2.06e-03	kPa	287.44	Fatty a...
Pvap	2.17e-03	kPa	287.94	Fatty a...
Pvap	2.17e-03	kPa	287.94	Fatty a...
Pvap	2.39e-03	kPa	288.93	Fatty a...
Pvap	2.49e-03	kPa	289.31	Fatty a...
Pvap	2.51e-03	kPa	289.43	Fatty a...
Pvap	2.76e-03	kPa	290.42	Fatty a...
Pvap	2.79e-03	kPa	290.53	Fatty a...
Pvap	2.89e-03	kPa	290.92	Fatty a...
Pvap	3.15e-03	kPa	291.81	Fatty a...
Pvap	3.18e-03	kPa	291.92	Fatty a...
Pvap	3.34e-03	kPa	292.42	Fatty a...
Pvap	3.49e-03	kPa	292.87	Experim...
Pvap	3.50e-03	kPa	292.90	Fatty a...
Pvap	3.67e-03	kPa	293.41	Fatty a...
Pvap	3.84e-03	kPa	293.91	Fatty a...
Pvap	3.99e-03	kPa	294.30	Fatty a...
Pvap	4.22e-03	kPa	294.90	Fatty a...
Pvap	4.41e-03	kPa	295.40	Fatty a...
Pvap	4.44e-03	kPa	295.51	Fatty a...
Pvap	4.62e-03	kPa	295.90	Fatty a...
Pvap	4.84e-03	kPa	296.39	Fatty a...
Pvap	4.99e-03	kPa	296.77	Fatty a...
Pvap	5.30e-03	kPa	297.39	Fatty a...
Pvap	5.53e-03	kPa	297.89	Fatty a...
Pvap	5.57e-03	kPa	297.98	Fatty a...
Pvap	6.06e-03	kPa	298.88	Fatty a...
Pvap	6.34e-03	kPa	299.38	Fatty a...
Pvap	6.92e-03	kPa	300.37	Fatty a...
Pvap	6.95e-03	kPa	300.46	Fatty a...
Pvap	7.24e-03	kPa	300.87	Fatty a...
Pvap	7.89e-03	kPa	301.87	Fatty a...
Pvap	8.24e-03	kPa	302.37	Fatty a...
Pvap	8.52e-03	kPa	302.84	Fatty a...
Pvap	8.63e-03	kPa	302.94	Fatty a...
Pvap	8.40e-03	kPa	302.97	Experim...
Pvap	8.98e-03	kPa	303.36	Fatty a...
Pvap	9.24e-03	kPa	303.76	Fatty a...
Pvap	9.30e-03	kPa	303.81	Fatty a...
Pvap	9.29e-03	kPa	303.82	Fatty a...
Pvap	9.29e-03	kPa	303.82	Fatty a...
Pvap	9.37e-03	kPa	303.86	Fatty a...
Pvap	0.01	kPa	304.85	Fatty a...
Pvap	0.01	kPa	304.85	Fatty a...
Pvap	0.01	kPa	305.24	Fatty a...
Pvap	0.01	kPa	305.26	Fatty a...
Pvap	0.01	kPa	305.29	Fatty a...
Pvap	0.01	kPa	305.35	Fatty a...
Pvap	0.01	kPa	305.42	Fatty a...
Pvap	0.02	kPa	313.01	Experim...
Pvap	0.04	kPa	323.04	Experim...
Pvap	0.09	kPa	333.13	Experim...
Pvap	0.17	kPa	343.30	Experim...
Pvap	0.31	kPa	352.40	Experim...
Pvap	0.56	kPa	362.72	Experim...
Pvap	0.93	kPa	372.54	Experim...
Pvap	1.56	kPa	382.62	Experim...
Pvap	2.00	kPa	389.10	Isobari...
Pvap	2.00	kPa	389.10	Isobari...
Pvap	2.52	kPa	392.75	Experim...
Pvap	3.92	kPa	402.71	Experim...
Pvap	4.00	kPa	404.15	Isobari...
Pvap	6.01	kPa	412.79	Experim...
Pvap	6.00	kPa	412.93	Isobari...
Pvap	6.00	kPa	413.57	Isobari...
Pvap	8.89	kPa	422.71	Experim...
Pvap	10.00	kPa	424.43	Isobari...
Pvap	12.80	kPa	432.65	Experim...
n0	[1.39819; 1.43209]		[278.15; 358.15]
n0	1.43209		278.15	Thermop...
n0	1.42995		283.15	Thermop...
n0	1.42783		288.15	Thermop...
n0	1.42571		293.15	Thermop...
n0	1.42359		298.15	Thermop...
n0	1.42350		298.15	Measure...
n0	1.42148		303.15	Thermop...
n0	1.41938		308.15	Thermop...
n0	1.41726		313.15	Thermop...
n0	1.41510		318.15	Thermop...
n0	1.41295		323.15	Thermop...
n0	1.41083		328.15	Thermop...
n0	1.40871		333.15	Thermop...
n0	1.40659		338.15	Thermop...
n0	1.40448		343.15	Thermop...
n0	1.40237		348.15	Thermop...
n0	1.40028		353.15	Thermop...
n0	1.39819		358.15	Thermop...
ρl	[847.62; 872.25]	kg/m3	[293.15; 323.15]
ρl	872.25	kg/m3	293.15	Measure...
ρl	868.16	kg/m3	298.15	Measure...
ρl	864.06	kg/m3	303.15	Measure...
ρl	859.96	kg/m3	308.15	Measure...
ρl	855.85	kg/m3	313.15	Measure...
ρl	851.74	kg/m3	318.15	Measure...
ρl	847.62	kg/m3	323.15	Measure...
λ	[0.12; 0.15]	W/m×K	[267.10; 399.95]
λ	0.15	W/m×K	267.10	Experim...
λ	0.15	W/m×K	267.11	Experim...
λ	0.15	W/m×K	277.00	Experim...
λ	0.15	W/m×K	277.07	Experim...
λ	0.14	W/m×K	288.82	Experim...
λ	0.14	W/m×K	288.84	Experim...
λ	0.14	W/m×K	300.83	Experim...
λ	0.14	W/m×K	300.86	Experim...
λ	0.14	W/m×K	311.66	Experim...
λ	0.14	W/m×K	311.87	Experim...
λ	0.14	W/m×K	324.72	Experim...
λ	0.14	W/m×K	324.92	Experim...
λ	0.13	W/m×K	336.71	Experim...
λ	0.13	W/m×K	336.71	Experim...
λ	0.13	W/m×K	348.66	Experim...
λ	0.13	W/m×K	348.81	Experim...
λ	0.13	W/m×K	354.58	Experim...
λ	0.13	W/m×K	354.59	Experim...
λ	0.13	W/m×K	360.11	Experim...
λ	0.13	W/m×K	360.61	Experim...
λ	0.13	W/m×K	368.98	Experim...
λ	0.13	W/m×K	369.47	Experim...
λ	0.12	W/m×K	379.50	Experim...
λ	0.12	W/m×K	379.65	Experim...
λ	0.12	W/m×K	389.35	Experim...
λ	0.12	W/m×K	389.39	Experim...
λ	0.12	W/m×K	399.87	Experim...
λ	0.12	W/m×K	399.95	Experim...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	[381.20; 387.20]	K	[1.30; 2.00]
Tboilr	381.20	K	1.30	NIST
Tboilr	387.20	K	2.00	NIST

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (1)
3. Mass density, kg/m3 (1)
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	313.71	383.90
4070.00	313.82	382.10
8030.00	313.83	380.50
12010.00	313.99	378.50
16140.00	314.01	376.60
100.00	324.79	387.60
4070.00	324.79	386.00
8030.00	325.01	384.40
12010.00	325.06	382.50
16140.00	325.20	379.30
100.00	334.12	393.20
4070.00	334.53	390.30
8030.00	334.33	388.30
12010.00	334.60	386.20
16140.00	334.84	384.20
Reference

Viscosity, Pa*s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.30	293.15	0.0022
20000.00	293.15	0.0027
40000.00	293.15	0.0032
60000.00	293.15	0.0039
80000.00	293.15	0.0047
100000.00	293.15	0.0055
120000.00	293.15	0.0065
140000.00	293.15	0.0077
160000.00	293.15	0.0090
101.30	313.15	0.0015
20000.00	313.15	0.0018
40000.00	313.15	0.0022
60000.00	313.15	0.0027
80000.00	313.15	0.0031
100000.00	313.15	0.0036
120000.00	313.15	0.0042
140000.00	313.15	0.0049
160000.00	313.15	0.0056
180000.00	313.15	0.0063
200000.00	313.15	0.0072
101.30	333.15	0.0011
20000.00	333.15	0.0013
40000.00	333.15	0.0016
60000.00	333.15	0.0019
80000.00	333.15	0.0022
100000.00	333.15	0.0025
120000.00	333.15	0.0029
140000.00	333.15	0.0033
160000.00	333.15	0.0037
180000.00	333.15	0.0042
200000.00	333.15	0.0047
101.30	353.15	0.0008
20000.00	353.15	0.0010
40000.00	353.15	0.0012
60000.00	353.15	0.0014
80000.00	353.15	0.0016
100000.00	353.15	0.0019
120000.00	353.15	0.0021
140000.00	353.15	0.0024
160000.00	353.15	0.0027
180000.00	353.15	0.0030
200000.00	353.15	0.0034
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	868.0
298.15	3000.00	870.0
298.15	6000.00	872.0
298.15	9000.00	874.0
298.15	12000.00	877.0
298.15	15000.00	878.0
308.15	100.00	860.0
308.15	3010.00	862.0
308.15	6000.00	864.0
308.15	9000.00	866.0
308.15	12000.00	869.0
308.15	15000.00	871.0
318.15	100.00	853.0
318.15	3000.00	854.0
318.15	6000.00	856.0
318.15	9000.00	859.0
318.15	12000.00	861.0
318.15	15000.00	863.0
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
283.15	101.30	1362.6
283.15	10000.00	1408.9
283.15	20000.00	1452.2
283.15	30000.00	1493.2
283.15	40000.00	1531.7
283.15	50000.00	1568.0
283.15	60000.00	1602.6
283.15	70000.00	1634.5
283.15	80000.00	1666.4
283.15	90000.00	1696.9
283.15	100000.00	1726.9
283.15	110000.00	1755.2
283.15	120000.00	1783.4
283.15	130000.00	1809.5
283.15	140000.00	1835.9
303.15	101.30	1287.7
303.15	10000.00	1339.2
303.15	20000.00	1385.8
303.15	30000.00	1429.6
303.15	40000.00	1470.3
303.15	50000.00	1508.7
303.15	60000.00	1544.9
303.15	70000.00	1580.2
303.15	80000.00	1614.1
303.15	90000.00	1646.1
303.15	100000.00	1676.9
303.15	110000.00	1706.8
303.15	120000.00	1735.1
303.15	130000.00	1762.8
303.15	140000.00	1789.2
303.15	150000.00	1815.2
303.15	170000.00	1864.9
303.15	190000.00	1912.7
303.15	210000.00	1957.6
323.15	101.30	1214.8
323.15	10000.00	1269.1
323.15	20000.00	1319.3
323.15	30000.00	1365.7
323.15	40000.00	1409.0
323.15	50000.00	1449.5
323.15	60000.00	1487.8
323.15	70000.00	1524.0
323.15	80000.00	1558.3
323.15	90000.00	1591.2
323.15	100000.00	1623.3
323.15	110000.00	1653.9
323.15	120000.00	1684.6
323.15	130000.00	1711.9
323.15	140000.00	1739.6
323.15	150000.00	1765.9
323.15	170000.00	1817.0
323.15	190000.00	1864.8
323.15	210000.00	1910.9
343.15	101.30	1142.8
343.15	10000.00	1202.4
343.15	20000.00	1255.9
343.15	30000.00	1304.9
343.15	40000.00	1350.5
343.15	50000.00	1393.5
343.15	60000.00	1433.7
343.15	70000.00	1471.7
343.15	80000.00	1508.2
343.15	90000.00	1541.7
343.15	100000.00	1574.1
343.15	110000.00	1606.0
343.15	120000.00	1636.2
343.15	130000.00	1665.9
343.15	140000.00	1694.0
343.15	150000.00	1721.2
343.15	170000.00	1773.2
343.15	190000.00	1822.0
343.15	210000.00	1868.7
363.15	10000.00	1138.5
363.15	20000.00	1195.9
363.15	30000.00	1247.9
363.15	40000.00	1296.3
363.15	50000.00	1341.1
363.15	60000.00	1382.7
363.15	70000.00	1421.6
363.15	80000.00	1458.4
363.15	90000.00	1493.8
363.15	100000.00	1527.4
363.15	110000.00	1559.7
363.15	120000.00	1590.9
363.15	130000.00	1620.7
363.15	140000.00	1649.4
363.15	150000.00	1677.2
363.15	170000.00	1730.6
363.15	190000.00	1780.4
363.15	210000.00	1827.2
383.15	10000.00	1077.4
383.15	20000.00	1138.6
383.15	30000.00	1193.5
383.15	40000.00	1244.5
383.15	50000.00	1291.3
383.15	60000.00	1334.9
383.15	70000.00	1375.4
383.15	80000.00	1414.2
383.15	90000.00	1450.6
383.15	100000.00	1485.3
383.15	110000.00	1518.9
383.15	120000.00	1550.9
383.15	130000.00	1581.2
383.15	140000.00	1610.8
383.15	150000.00	1641.0
383.15	170000.00	1692.7
383.15	190000.00	1743.0
383.15	210000.00	1791.1
403.15	10000.00	1017.7
403.15	20000.00	1083.2
403.15	30000.00	1141.7
403.15	40000.00	1194.7
403.15	50000.00	1242.9
403.15	60000.00	1288.1
403.15	70000.00	1330.6
403.15	80000.00	1370.3
403.15	90000.00	1407.7
403.15	100000.00	1442.8
403.15	110000.00	1476.6
403.15	120000.00	1509.7
403.15	130000.00	1541.7
403.15	140000.00	1571.6
403.15	150000.00	1600.1
403.15	170000.00	1655.5
403.15	190000.00	1706.6
403.15	210000.00	1754.5
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[381.00; 520.45]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.61003e+01
Coefficient B			-4.73527e+03
Coefficient C			-8.15400e+01
Temperature range, min.			381.00
Temperature range, max.			520.45
Pvap	1.33	kPa	381.00	Calculated Property
Pvap	2.90	kPa	396.49	Calculated Property
Pvap	5.87	kPa	411.99	Calculated Property
Pvap	11.16	kPa	427.48	Calculated Property
Pvap	20.07	kPa	442.98	Calculated Property
Pvap	34.39	kPa	458.47	Calculated Property
Pvap	56.47	kPa	473.97	Calculated Property
Pvap	89.30	kPa	489.46	Calculated Property
Pvap	136.56	kPa	504.96	Calculated Property
Pvap	202.67	kPa	520.45	Calculated Property

Similar Compounds

Find more compounds similar to Decanoic acid, methyl ester.

Mixtures

• 1-Propanol + Decanoic acid, methyl ester
• 1-Butanol + Decanoic acid, methyl ester
• 1-Pentanol + Decanoic acid, methyl ester
• Octanoic acid, methyl ester + Decanoic acid, methyl ester
• Dodecanoic acid, methyl ester + Decanoic acid, methyl ester
• Decanoic acid, methyl ester + Cyclohexane, methyl-
• Heptane + Decanoic acid, methyl ester
• Dodecane + Decanoic acid, methyl ester
• Decanoic acid, methyl ester + Tetradecane
• Hexadecane + Decanoic acid, methyl ester
• n-Hexane + Decanoic acid, methyl ester
• Octane + Decanoic acid, methyl ester
• Decane + Decanoic acid, methyl ester
• Butanoic acid, methyl ester + Dodecane + Decanoic acid, methyl ester
• Ethane + Decanoic acid, methyl ester

Sources

• Crippen Method
• Phase behaviour of high molecular mass methyl esters in supercritical ethane
• Measurement of the thermal conductivity of biofuel mixtures: Methyl caprate components of biodiesel and alcohols
• 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
• Isobaric vapor-liquid equilibrium for binary system of methyl caprylate + methyl caprate at 2, 6 and 10 kPa
• Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
• 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
• Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
• Isobaric molar heat capacities of binary mixtures containing methyl caprate and methyl laurate at pressures up to 16.2 MPa
• Temperature and pressure dependence of densities and viscosities for binary mixtures of methyl decanoate plus n-heptane
• Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
• Experimental Investigation of the Thermophysical Properties of the Bio-Aviation Fuel Surrogates: Binary and Ternary Mixtures of n-Dodecane, Methyl Butyrate, and Methyl Decanoate
• 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
• Speed of Sound, Density, and Derivative Properties of Fatty Acid Methyl and Ethyl Esters under High Pressure: Methyl Caprate and Ethyl Caprate
• Viscosities of Fatty Acid Methyl and Ethyl Esters under High Pressure: Methyl Caprate and Ethyl Caprate
• Joback Method
• Aqueous Solubility Prediction Method
• Estimated Solubility 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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