Chemical Properties of Hexanoic acid, methyl ester (CAS 106-70-7)

InChI

InChI=1S/C7H14O2/c1-3-4-5-6-7(8)9-2/h3-6H2,1-2H3

InChI Key

NUKZAGXMHTUAFE-UHFFFAOYSA-N

Formula

C7H14O2

SMILES

CCCCCC(=O)OC

Molecular Weight¹

130.18

CAS

106-70-7

Other Names

• Caproic acid, methyl ester
• Methyl caproate
• Methyl capronate
• Methyl ester of hexanoic acid
• Methyl hexanoate
• Methyl hexoate
• Methyl hexylate
• Methyl n-hexanoate
• Methyl n-hexoate
• NSC 5023
• n-Caproic 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_fH°_liquid : Liquid phase 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	[-4215.00; -4184.00]	kJ/mol
ΔcH°liquid	-4184.00 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-4215.00 ± 0.60	kJ/mol	NIST
ΔfG°	-225.86	kJ/mol	Joback Calculated Property
ΔfH°gas	-494.00 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-540.20 ± 1.00	kJ/mol	NIST
ΔfusH°	16.67	kJ/mol	Joback Calculated Property
ΔvapH°	[46.00; 48.70]	kJ/mol
ΔvapH°	48.40 ± 0.20	kJ/mol	NIST
ΔvapH°	47.70 ± 0.10	kJ/mol	NIST
ΔvapH°	47.90	kJ/mol	NIST
ΔvapH°	48.20	kJ/mol	NIST
ΔvapH°	47.80 ± 0.50	kJ/mol	NIST
ΔvapH°	48.70 ± 0.30	kJ/mol	NIST
ΔvapH°	48.04 ± 0.12	kJ/mol	NIST
ΔvapH°	48.00 ± 0.10	kJ/mol	NIST
ΔvapH°	Outlier 46.00 ± 1.00	kJ/mol	NIST
ΔvapH°	46.20	kJ/mol	NIST
log10WS	[-2.00; -1.87]
log10WS	-2.00		Aq. Sol...
log10WS	-1.87		Estimat...
logPoct/wat	1.740		Crippen Calculated Property
McVol	116.930	ml/mol	McGowan Calculated Property
Pc	2940.89	kPa	Joback Calculated Property
Inp	[142.00; 938.00]
Inp	907.00		NIST
Inp	907.00		NIST
Inp	908.30		NIST
Inp	923.40		NIST
Inp	922.60		NIST
Inp	921.80		NIST
Inp	908.00		NIST
Inp	904.00		NIST
Inp	905.00		NIST
Inp	913.00		NIST
Inp	902.00		NIST
Inp	902.00		NIST
Inp	913.00		NIST
Inp	910.00		NIST
Inp	906.00		NIST
Inp	911.00		NIST
Inp	909.00		NIST
Inp	909.00		NIST
Inp	910.00		NIST
Inp	905.00		NIST
Inp	913.00		NIST
Inp	905.00		NIST
Inp	907.00		NIST
Inp	931.00		NIST
Inp	910.00		NIST
Inp	915.00		NIST
Inp	902.00		NIST
Inp	925.00		NIST
Inp	915.00		NIST
Inp	936.00		NIST
Inp	924.00		NIST
Inp	938.00		NIST
Inp	911.00		NIST
Inp	925.00		NIST
Inp	903.00		NIST
Inp	923.00		NIST
Inp	926.00		NIST
Inp	933.00		NIST
Inp	904.00		NIST
Inp	934.00		NIST
Inp	905.00		NIST
Inp	904.00		NIST
Inp	904.00		NIST
Inp	904.00		NIST
Inp	908.50		NIST
Inp	907.40		NIST
Inp	908.00		NIST
Inp	908.00		NIST
Inp	906.00		NIST
Inp	909.00		NIST
Inp	927.00		NIST
Inp	910.00		NIST
Inp	907.00		NIST
Inp	922.50		NIST
Inp	931.40		NIST
Inp	914.00		NIST
Inp	932.00		NIST
Inp	924.00		NIST
Inp	931.00		NIST
Inp	925.00		NIST
Inp	918.00		NIST
Inp	916.00		NIST
Inp	922.00		NIST
Inp	905.00		NIST
Inp	905.00		NIST
Inp	907.00		NIST
Inp	925.00		NIST
Inp	907.00		NIST
Inp	916.00		NIST
Inp	919.00		NIST
Inp	927.00		NIST
Inp	930.00		NIST
Inp	929.00		NIST
Inp	924.00		NIST
Inp	924.00		NIST
Inp	928.00		NIST
Inp	925.00		NIST
Inp	924.00		NIST
Inp	923.20		NIST
Inp	927.00		NIST
Inp	915.00		NIST
Inp	936.00		NIST
Inp	936.00		NIST
Inp	909.00		NIST
Inp	927.00		NIST
Inp	927.00		NIST
Inp	906.00		NIST
Inp	905.00		NIST
Inp	910.00		NIST
Inp	906.00		NIST
Inp	906.00		NIST
Inp	907.00		NIST
Inp	907.00		NIST
Inp	906.00		NIST
Inp	910.00		NIST
Inp	914.00		NIST
Inp	906.00		NIST
Inp	907.00		NIST
Inp	907.00		NIST
Inp	905.00		NIST
Inp	906.00		NIST
Inp	921.00		NIST
Inp	906.00		NIST
Inp	923.00		NIST
Inp	927.00		NIST
Inp	911.00		NIST
Inp	924.00		NIST
Inp	929.00		NIST
Inp	911.00		NIST
Inp	927.00		NIST
Inp	936.00		NIST
Inp	925.00		NIST
Inp	924.00		NIST
Inp	922.00		NIST
Inp	906.00		NIST
Inp	931.00		NIST
Inp	906.00		NIST
Inp	902.00		NIST
Inp	922.00		NIST
Inp	926.00		NIST
Inp	926.00		NIST
Inp	906.00		NIST
Inp	911.00		NIST
Inp	934.00		NIST
Inp	934.00		NIST
Inp	934.00		NIST
Inp	934.00		NIST
Inp	906.00		NIST
Inp	907.00		NIST
Inp	902.00		NIST
Inp	914.00		NIST
Inp	904.00		NIST
Inp	906.00		NIST
Inp	905.00		NIST
Inp	906.00		NIST
Inp	906.00		NIST
Inp	Outlier 142.00		NIST
Inp	Outlier 148.05		NIST
Inp	919.00		NIST
Inp	924.00		NIST
Inp	927.00		NIST
Inp	906.00		NIST
Inp	910.00		NIST
Inp	905.00		NIST
I	[1142.00; 1208.00]
I	1183.00		NIST
I	1177.00		NIST
I	1184.00		NIST
I	1177.00		NIST
I	1188.00		NIST
I	1184.00		NIST
I	1190.00		NIST
I	1182.00		NIST
I	1180.00		NIST
I	1180.00		NIST
I	1176.00		NIST
I	1186.00		NIST
I	1176.00		NIST
I	1173.00		NIST
I	1175.00		NIST
I	1173.00		NIST
I	1175.00		NIST
I	1189.00		NIST
I	1197.00		NIST
I	1181.00		NIST
I	1187.00		NIST
I	1183.00		NIST
I	1172.00		NIST
I	1177.00		NIST
I	1184.00		NIST
I	1183.00		NIST
I	1190.00		NIST
I	1171.00		NIST
I	1189.00		NIST
I	Outlier 1208.00		NIST
I	1204.00		NIST
I	1202.00		NIST
I	1194.00		NIST
I	1197.00		NIST
I	1185.00		NIST
I	1172.00		NIST
I	1197.00		NIST
I	1184.00		NIST
I	1191.00		NIST
I	1178.00		NIST
I	1178.00		NIST
I	1191.00		NIST
I	Outlier 1142.00		NIST
I	Outlier 1154.00		NIST
I	1193.00		NIST
I	1182.00		NIST
I	1184.00		NIST
I	1186.00		NIST
I	1185.00		NIST
I	1184.00		NIST
I	1202.00		NIST
I	1192.00		NIST
I	1174.00		NIST
I	1188.00		NIST
I	1185.00		NIST
I	1177.00		NIST
I	1200.00		NIST
I	1180.00		NIST
I	1187.00		NIST
I	Outlier 1208.00		NIST
I	1172.00		NIST
I	1192.00		NIST
I	1197.00		NIST
I	1177.00		NIST
I	1188.00		NIST
I	1197.00		NIST
I	1177.00		NIST
I	1183.00		NIST
I	1183.00		NIST
I	1200.00		NIST
Tboil	435.85	K	Joback Calculated Property
Tc	612.24	K	Joback Calculated Property
Tfus	[202.20; 203.60]	K
Tfus	203.60 ± 0.05	K	NIST
Tfus	202.20 ± 0.50	K	NIST
Vc	0.452	m3/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[238.65; 299.73]	J/mol×K	[435.85; 612.24]
Cp,gas	238.65	J/mol×K	435.85	Joback Calculated Property
Cp,gas	249.76	J/mol×K	465.25	Joback Calculated Property
Cp,gas	260.50	J/mol×K	494.65	Joback Calculated Property
Cp,gas	270.86	J/mol×K	524.04	Joback Calculated Property
Cp,gas	280.85	J/mol×K	553.44	Joback Calculated Property
Cp,gas	290.48	J/mol×K	582.84	Joback Calculated Property
Cp,gas	299.73	J/mol×K	612.24	Joback Calculated Property
Cp,liquid	[246.40; 269.60]	J/mol×K	[303.15; 373.15]
Cp,liquid	246.40	J/mol×K	303.15	Heat ca...
Cp,liquid	248.80	J/mol×K	313.15	Heat ca...
Cp,liquid	251.50	J/mol×K	323.15	Heat ca...
Cp,liquid	254.60	J/mol×K	333.15	Heat ca...
Cp,liquid	257.90	J/mol×K	343.15	Heat ca...
Cp,liquid	261.50	J/mol×K	353.15	Heat ca...
Cp,liquid	265.50	J/mol×K	363.15	Heat ca...
Cp,liquid	269.60	J/mol×K	373.15	Heat ca...
η	[0.0002656; 0.0031909]	Pa×s	[240.81; 435.85]
η	0.0031909	Pa×s	240.81	Joback Calculated Property
η	0.0016480	Pa×s	273.32	Joback Calculated Property
η	0.0009795	Pa×s	305.82	Joback Calculated Property
η	0.0006434	Pa×s	338.33	Joback Calculated Property
η	0.0004549	Pa×s	370.84	Joback Calculated Property
η	0.0003401	Pa×s	403.34	Joback Calculated Property
η	0.0002656	Pa×s	435.85	Joback Calculated Property
ΔvapH	[45.20; 46.40]	kJ/mol	[325.00; 350.00]
ΔvapH	46.40 ± 0.10	kJ/mol	325.00	NIST
ΔvapH	45.30	kJ/mol	349.00	NIST
ΔvapH	45.20	kJ/mol	350.00	NIST
Pvap	[0.03; 96.03]	kPa	[262.64; 422.29]
Pvap	0.03	kPa	262.64	Experim...
Pvap	0.08	kPa	272.74	Experim...
Pvap	0.14	kPa	280.70	Transpi...
Pvap	0.16	kPa	282.84	Experim...
Pvap	0.17	kPa	283.60	Transpi...
Pvap	0.18	kPa	284.60	Transpi...
Pvap	0.21	kPa	286.60	Transpi...
Pvap	0.22	kPa	287.60	Transpi...
Pvap	0.26	kPa	289.50	Transpi...
Pvap	0.28	kPa	290.50	Transpi...
Pvap	0.27	kPa	290.50	Transpi...
Pvap	0.31	kPa	292.50	Transpi...
Pvap	0.34	kPa	292.87	Experim...
Pvap	0.34	kPa	293.30	Transpi...
Pvap	0.35	kPa	293.40	Transpi...
Pvap	0.34	kPa	293.50	Transpi...
Pvap	0.39	kPa	295.40	Transpi...
Pvap	0.42	kPa	296.40	Transpi...
Pvap	0.46	kPa	298.30	Transpi...
Pvap	0.47	kPa	298.40	Transpi...
Pvap	0.54	kPa	300.30	Transpi...
Pvap	0.65	kPa	303.30	Transpi...
Pvap	0.73	kPa	304.30	Transpi...
Pvap	0.89	kPa	307.63	Experim...
Pvap	0.90	kPa	307.90	Experim...
Pvap	0.89	kPa	308.30	Transpi...
Pvap	0.92	kPa	309.30	Transpi...
Pvap	1.05	kPa	312.30	Transpi...
Pvap	1.15	kPa	312.30	Transpi...
Pvap	1.46	kPa	316.30	Transpi...
Pvap	1.60	kPa	317.65	Experim...
Pvap	1.76	kPa	320.40	Transpi...
Pvap	2.22	kPa	324.40	Transpi...
Pvap	2.68	kPa	328.40	Transpi...
Pvap	3.18	kPa	331.40	Transpi...
Pvap	3.53	kPa	332.72	Experim...
Pvap	7.13	kPa	347.57	Experim...
Pvap	13.06	kPa	362.19	Experim...
Pvap	23.11	kPa	377.31	Experim...
Pvap	38.94	kPa	392.48	Experim...
Pvap	62.31	kPa	407.40	Experim...
Pvap	96.03	kPa	422.29	Experim...
n0	[1.37490; 1.41212]		[278.15; 358.15]
n0	1.41212		278.15	Thermop...
n0	1.40984		283.15	Thermop...
n0	1.40757		288.15	Thermop...
n0	1.40529		293.15	Thermop...
n0	1.40300		298.15	Thermop...
n0	1.40480		298.15	Vapor-L...
n0	1.40480		298.15	Vapor-L...
n0	1.40070		303.15	Thermop...
n0	1.39841		308.15	Thermop...
n0	1.39610		313.15	Thermop...
n0	1.39373		318.15	Thermop...
n0	1.39136		323.15	Thermop...
n0	1.38902		328.15	Thermop...
n0	1.38667		333.15	Thermop...
n0	1.38432		338.15	Thermop...
n0	1.38169		343.15	Thermop...
n0	1.37961		348.15	Thermop...
n0	1.37725		353.15	Thermop...
n0	1.37490		358.15	Thermop...
ρl	879.76	kg/m3	298.15	Densiti...
λ	[0.12; 0.15]	W/m×K	[263.83; 368.50]
λ	0.15	W/m×K	263.83	Experim...
λ	0.15	W/m×K	268.65	Experim...
λ	0.14	W/m×K	273.70	Experim...
λ	0.14	W/m×K	278.59	Experim...
λ	0.14	W/m×K	283.75	Experim...
λ	0.14	W/m×K	288.67	Experim...
λ	0.14	W/m×K	293.64	Experim...
λ	0.14	W/m×K	298.72	Experim...
λ	0.14	W/m×K	303.63	Experim...
λ	0.13	W/m×K	308.61	Experim...
λ	0.13	W/m×K	313.60	Experim...
λ	0.13	W/m×K	321.08	Experim...
λ	0.13	W/m×K	328.54	Experim...
λ	0.13	W/m×K	333.52	Experim...
λ	0.13	W/m×K	338.55	Experim...
λ	0.13	W/m×K	343.49	Experim...
λ	0.12	W/m×K	348.48	Experim...
λ	0.12	W/m×K	353.70	Experim...
λ	0.12	W/m×K	358.38	Experim...
λ	0.12	W/m×K	363.41	Experim...
λ	0.12	W/m×K	368.50	Experim...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	325.20	K	2.00	NIST

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (1)
3. Speed of sound, m/s (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
294.86	105.00	0.0009
294.75	5079.00	0.0009
294.63	9980.00	0.0010
294.34	15024.00	0.0010
293.98	19999.00	0.0011
293.48	25055.00	0.0011
292.99	29973.00	0.0012
303.12	107.00	0.0008
303.09	5026.00	0.0008
303.05	10031.00	0.0009
303.01	15014.00	0.0009
302.98	19967.00	0.0009
302.89	24988.00	0.0010
302.79	29963.00	0.0010
312.74	103.00	0.0007
312.70	4988.00	0.0007
312.71	10033.00	0.0008
312.69	15010.00	0.0008
312.69	20046.00	0.0008
312.62	24986.00	0.0008
312.57	29951.00	0.0009
322.29	98.00	0.0006
322.29	5048.00	0.0006
322.08	9972.00	0.0007
322.32	15008.00	0.0007
322.12	19979.00	0.0007
322.14	24972.00	0.0008
321.96	29975.00	0.0008
331.89	9984.00	0.0006
331.83	14994.00	0.0006
331.93	20001.00	0.0007
331.80	25008.00	0.0007
331.74	30010.00	0.0007
341.39	20015.00	0.0006
341.41	25042.00	0.0006
341.38	29965.00	0.0006
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	884.48
293.15	1000.00	884.65
293.15	3000.00	886.42
293.15	5000.00	887.67
293.15	10000.00	891.64
293.15	15000.00	895.33
293.15	20000.00	898.81
293.15	25000.00	902.28
293.15	30000.00	905.55
293.15	35000.00	908.69
293.15	40000.00	911.73
293.15	50000.00	917.83
293.15	60000.00	923.06
303.15	100.00	874.56
303.15	1000.00	875.42
303.15	3000.00	877.13
303.15	5000.00	878.76
303.15	10000.00	882.75
303.15	15000.00	886.63
303.15	20000.00	890.21
303.15	25000.00	893.78
303.15	30000.00	897.24
303.15	35000.00	900.52
303.15	40000.00	903.67
303.15	50000.00	909.79
303.15	60000.00	915.57
313.15	100.00	865.26
313.15	1000.00	865.64
313.15	3000.00	867.5
313.15	5000.00	869.26
313.15	10000.00	873.55
313.15	15000.00	877.59
313.15	20000.00	881.48
313.15	25000.00	885.29
313.15	30000.00	888.86
313.15	35000.00	892.33
313.15	40000.00	895.54
313.15	50000.00	901.99
313.15	60000.00	907.83
323.15	100.00	855.18
323.15	1000.00	856.16
323.15	3000.00	858.01
323.15	5000.00	859.89
323.15	10000.00	864.44
323.15	15000.00	868.76
323.15	20000.00	872.98
323.15	25000.00	876.76
323.15	30000.00	880.55
323.15	35000.00	884.15
323.15	40000.00	887.68
323.15	50000.00	894.33
323.15	60000.00	900.65
333.15	100.00	845.43
333.15	1000.00	846.26
333.15	3000.00	848.43
333.15	5000.00	850.38
333.15	10000.00	855.15
333.15	15000.00	859.63
333.15	20000.00	864.0
333.15	25000.00	868.18
333.15	30000.00	871.99
333.15	35000.00	875.8
333.15	40000.00	879.63
333.15	50000.00	886.48
333.15	60000.00	892.97
343.15	100.00	835.2
343.15	1000.00	836.39
343.15	3000.00	838.54
343.15	5000.00	840.78
343.15	10000.00	845.7
343.15	15000.00	850.49
343.15	20000.00	855.28
343.15	25000.00	859.46
343.15	30000.00	863.7
343.15	35000.00	867.75
343.15	40000.00	871.46
343.15	50000.00	878.77
343.15	60000.00	885.3
353.15	100.00	825.57
353.15	1000.00	826.5
353.15	3000.00	828.96
353.15	5000.00	831.13
353.15	10000.00	836.55
353.15	15000.00	841.75
353.15	20000.00	846.44
353.15	25000.00	851.08
353.15	30000.00	855.46
353.15	35000.00	859.68
353.15	40000.00	863.59
353.15	50000.00	871.08
353.15	60000.00	878.16
363.15	100.00	815.64
363.15	1000.00	816.87
363.15	3000.00	819.47
363.15	5000.00	821.87
363.15	10000.00	827.32
363.15	15000.00	833.11
363.15	20000.00	837.93
363.15	25000.00	842.64
363.15	30000.00	847.27
363.15	35000.00	851.7
363.15	40000.00	856.02
363.15	50000.00	863.88
363.15	60000.00	871.24
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
297.83	110.00	1225.1
306.48	110.00	1182.9
317.92	100.00	1137.0
327.21	110.00	1090.2
336.91	100.00	1055.2
346.90	100.00	1021.1
357.28	100.00	970.4
367.48	100.00	938.2
377.88	110.00	903.5
387.73	100.00	866.5
398.60	90.00	827.8
407.93	100.00	799.0
417.52	110.00	764.3
298.76	1010.00	1231.7
308.59	1010.00	1186.9
318.30	1000.00	1142.6
327.58	1010.00	1097.9
337.95	1000.00	1065.3
346.56	1010.00	1029.7
357.85	1010.00	989.8
367.24	1010.00	947.2
377.91	1010.00	910.8
387.01	1010.00	874.2
397.64	1010.00	842.1
406.65	1010.00	810.8
417.08	1010.00	775.9
427.06	1000.00	746.0
436.99	1010.00	714.9
447.88	1000.00	672.6
457.84	990.00	642.8
466.46	1010.00	613.5
478.01	1010.00	570.1
417.21	5010.00	808.2
427.25	5000.00	786.5
437.07	5000.00	751.6
447.00	4990.00	723.0
456.84	5000.00	695.3
466.28	5000.00	663.1
478.34	5010.00	623.4
487.67	5000.00	595.0
497.36	5000.00	568.5
507.11	5010.00	535.1
517.60	5010.00	504.9
528.29	5000.00	472.6
538.26	5010.00	439.9
547.96	5000.00	406.1
558.34	5000.00	378.3
567.58	5000.00	346.5
575.39	5000.00	317.9
586.99	5010.00	275.0
298.35	7010.00	1261.9
308.90	7000.00	1221.1
317.60	7010.00	1175.8
327.38	7010.00	1130.2
337.21	7010.00	1102.7
347.43	7000.00	1067.3
357.33	7010.00	1033.1
367.18	7000.00	989.6
377.97	7000.00	961.0
387.07	7000.00	922.0
397.54	7020.00	891.4
406.79	7020.00	857.7
416.99	7010.00	835.1
427.33	7000.00	805.5
487.58	1000.00	535.4
497.17	1010.00	499.6
506.88	1000.00	464.6
516.99	1010.00	426.2
298.85	3000.00	1240.3
309.19	3010.00	1197.6
319.17	3010.00	1152.2
327.90	3000.00	1107.9
337.97	3000.00	1078.0
347.71	3010.00	1040.3
356.24	3010.00	1011.9
366.38	3010.00	970.6
377.25	3000.00	927.9
386.63	3000.00	894.6
396.70	3000.00	862.0
406.78	3010.00	828.8
417.12	3000.00	796.9
427.25	3000.00	770.6
439.30	3000.00	727.5
446.68	3010.00	706.2
456.61	3000.00	673.8
466.22	3010.00	642.9
478.43	3010.00	596.3
487.67	3010.00	565.4
497.43	3010.00	534.1
506.49	3000.00	503.9
517.56	3000.00	468.7
529.52	3000.00	426.0
538.04	3000.00	396.8
547.56	3000.00	362.7
557.68	3000.00	321.9
566.56	3010.00	285.3
576.45	3010.00	241.0
437.97	6990.00	771.5
447.38	7000.00	744.5
457.10	7010.00	715.1
466.30	7000.00	689.7
478.28	7000.00	646.3
487.69	7000.00	617.0
497.38	7000.00	591.6
506.97	7010.00	563.3
517.52	7010.00	531.6
528.46	7000.00	504.0
538.26	7000.00	472.1
548.26	7000.00	446.0
557.89	7010.00	423.0
567.72	7010.00	390.1
576.35	7000.00	365.2
587.76	7000.00	334.6
298.17	10000.00	1274.4
308.58	10010.00	1227.8
317.52	10010.00	1181.0
327.40	10010.00	1143.2
337.71	10010.00	1111.9
346.92	10020.00	1081.3
356.68	10010.00	1048.7
366.89	10000.00	1005.5
377.70	10000.00	974.3
386.85	10000.00	945.8
397.25	10010.00	909.9
406.89	10000.00	885.7
417.21	10020.00	864.4
427.38	10010.00	833.5
438.10	9980.00	802.1
447.21	10010.00	776.0
456.81	9990.00	747.0
586.48	3000.00	197.5
298.56	5000.00	1252.4
309.13	5010.00	1210.5
318.41	5010.00	1160.9
327.64	5010.00	1120.6
337.21	5000.00	1091.3
347.75	5010.00	1054.8
357.35	5000.00	1022.1
366.68	5000.00	980.4
377.72	5000.00	939.5
387.29	5000.00	908.4
397.83	5000.00	875.5
406.99	5010.00	841.7
466.30	10010.00	720.4
478.28	10000.00	677.8
487.71	10000.00	653.5
497.44	10000.00	629.4
507.02	10020.00	599.2
517.63	10010.00	571.0
528.65	10010.00	547.3
538.35	10000.00	516.1
548.18	9980.00	498.8
558.07	10000.00	472.6
565.69	10010.00	446.4
577.04	10010.00	420.8
588.07	10030.00	393.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[315.12; 449.30]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.49142e+01
Coefficient B			-3.75133e+03
Coefficient C			-5.86470e+01
Temperature range, min.			315.12
Temperature range, max.			449.30
Pvap	1.33	kPa	315.12	Calculated Property
Pvap	2.98	kPa	330.03	Calculated Property
Pvap	6.12	kPa	344.94	Calculated Property
Pvap	11.70	kPa	359.85	Calculated Property
Pvap	21.05	kPa	374.76	Calculated Property
Pvap	35.93	kPa	389.66	Calculated Property
Pvap	58.55	kPa	404.57	Calculated Property
Pvap	91.65	kPa	419.48	Calculated Property
Pvap	138.44	kPa	434.39	Calculated Property
Pvap	202.65	kPa	449.30	Calculated Property

Similar Compounds

Find more compounds similar to Hexanoic acid, methyl ester.

Mixtures

• Hexanoic acid, methyl ester + Water
• Acetonitrile + Hexanoic acid, methyl ester
• Propanenitrile + Hexanoic acid, methyl ester

Sources

• Crippen Method
• Transpiration method: Vapor pressures and enthalpies of vaporization of some low-boiling esters
• High-pressure liquid densities of fatty acid methyl esters: Measurement and prediction with the PC-SAFT equation of state
• 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
• Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions
• Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
• Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
• Thermophysical properties of fatty acid methyl and ethyl esters
• Liquid viscosities for methyl hexanoate, methyl heptanoate, methyl caprylate, and methyl nonanoate at high pressures
• Measurement of Speed of Sound in Methyl Hexanoate from 297.83 to 588.07 K and up to 10 MPa
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Acetonitrile (2) Systems at 93.32 kPa
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Propanenitrile (2) Systems at 93.32 kPa
• Joback Method
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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