Chemical Properties of Pentanoic acid, ethyl ester (CAS 539-82-2)

InChI

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

InChI Key

ICMAFTSLXCXHRK-UHFFFAOYSA-N

Formula

C7H14O2

SMILES

CCCCC(=O)OCC

Molecular Weight¹

130.18

CAS

539-82-2

Other Names

• ETHYL ESTER VALERIC ACID
• ETHYL N-VALERATE
• ETHYL PENTANOATE
• Ethyl valerate
• Pentyl propanoate
• Valeric acid, ethyl ester
• n-Valeric 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).
• 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).
• 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.
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given 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.

Physical Properties

Property	Value	Unit	Source
ω	0.4805		Relay (1.0) Calculated Property
ΔcH°liquid	[-4202.40; -4201.60]	kJ/mol
ΔcH°liquid	-4201.60 ± 2.50	kJ/mol	NIST
ΔcH°liquid	-4202.40 ± 2.50	kJ/mol	NIST
ΔfG°	-225.86	kJ/mol	Joback Calculated Property
ΔfH°gas	[-507.70; -507.00]	kJ/mol
ΔfH°gas	-507.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-507.70	kJ/mol	NIST
ΔfH°gas	-507.00 ± 3.00	kJ/mol	NIST
ΔfH°liquid	[-554.10; -553.10]	kJ/mol
ΔfH°liquid	-554.10 ± 0.80	kJ/mol	NIST
ΔfH°liquid	-553.80 ± 2.50	kJ/mol	NIST
ΔfH°liquid	-553.10 ± 8.40	kJ/mol	NIST
ΔfusH°	16.67	kJ/mol	Joback Calculated Property
ΔvapH°	[46.00; 47.10]	kJ/mol
ΔvapH°	47.00 ± 1.00	kJ/mol	NIST
ΔvapH°	47.10	kJ/mol	NIST
ΔvapH°	47.01 ± 0.10	kJ/mol	NIST
ΔvapH°	46.00 ± 1.00	kJ/mol	NIST
ΔvapH°	46.10	kJ/mol	NIST
IE	9.86	eV	Relay (1.0) Calculated Property
log10WS	[-2.25; -1.75]
log10WS	-1.75		Aq. Solubility Prediction
log10WS	-2.25		Estimated Solubility
logPoct/wat	1.740		Crippen Calculated Property
McVol	116.930	ml/mol	McGowan Calculated Property
Pc	2730.40	kPa	Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
Inp	[871.00; 929.00]
Inp	883.00		NIST
Inp	896.00		NIST
Inp	913.00		NIST
Inp	882.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	878.00		NIST
Inp	879.00		NIST
Inp	871.00		NIST
Inp	888.00		NIST
Inp	881.00		NIST
Inp	888.00		NIST
Inp	887.00		NIST
Inp	887.00		NIST
Inp	888.00		NIST
Inp	882.00		NIST
Inp	900.00		NIST
Inp	876.00		NIST
Inp	902.00		NIST
Inp	898.00		NIST
Inp	902.00		NIST
Inp	904.00		NIST
Inp	Outlier 929.00		NIST
Inp	901.00		NIST
Inp	898.00		NIST
Inp	901.00		NIST
Inp	881.00		NIST
Inp	881.00		NIST
Inp	893.00		NIST
Inp	884.00		NIST
Inp	871.00		NIST
Inp	871.00		NIST
Inp	871.00		NIST
Inp	904.00		NIST
Inp	907.00		NIST
Inp	903.00		NIST
Inp	900.00		NIST
Inp	898.00		NIST
Inp	900.00		NIST
Inp	901.00		NIST
Inp	893.00		NIST
Inp	900.00		NIST
Inp	875.00		NIST
Inp	905.00		NIST
Inp	900.00		NIST
Inp	900.00		NIST
Inp	904.00		NIST
Inp	898.00		NIST
Inp	915.00		NIST
Inp	900.00		NIST
Inp	898.00		NIST
Inp	905.00		NIST
Inp	884.00		NIST
Inp	908.00		NIST
Inp	900.00		NIST
Inp	882.00		NIST
Inp	884.00		NIST
Inp	884.00		NIST
Inp	888.00		NIST
Inp	888.00		NIST
Inp	898.00		NIST
Inp	902.00		NIST
Inp	Outlier 919.00		NIST
Inp	904.00		NIST
Inp	901.00		NIST
Inp	900.00		NIST
Inp	900.00		NIST
Inp	876.00		NIST
Inp	900.00		NIST
Inp	887.00		NIST
Inp	900.00		NIST
Inp	876.00		NIST
Inp	884.00		NIST
Inp	902.00		NIST
Inp	885.00		NIST
Inp	880.00		NIST
Inp	901.00		NIST
Inp	902.00		NIST
Inp	884.00		NIST
Inp	893.00		NIST
Inp	900.00		NIST
Inp	904.00		NIST
Inp	905.00		NIST
Inp	884.00		NIST
Inp	898.00		NIST
Inp	880.00		NIST
I	[1113.00; 1170.00]
I	1125.00		NIST
I	Outlier 1159.00		NIST
I	1113.00		NIST
I	1131.00		NIST
I	Outlier 1162.00		NIST
I	1130.00		NIST
I	1140.00		NIST
I	1142.00		NIST
I	1140.00		NIST
I	1134.00		NIST
I	1139.00		NIST
I	1138.00		NIST
I	1125.00		NIST
I	1146.00		NIST
I	1134.00		NIST
I	1137.00		NIST
I	1127.00		NIST
I	1125.00		NIST
I	1131.00		NIST
I	1124.00		NIST
I	1125.00		NIST
I	1139.00		NIST
I	1139.00		NIST
I	1131.00		NIST
I	Outlier 1160.00		NIST
I	1120.00		NIST
I	1129.00		NIST
I	1138.00		NIST
I	1133.00		NIST
I	1139.00		NIST
I	Outlier 1161.00		NIST
I	1122.00		NIST
I	1133.00		NIST
I	1140.00		NIST
I	1142.00		NIST
I	1136.00		NIST
I	1128.00		NIST
I	1128.00		NIST
I	1133.00		NIST
I	1148.00		NIST
I	1116.00		NIST
I	1145.00		NIST
I	Outlier 1170.00		NIST
I	1135.00		NIST
I	1158.00		NIST
I	1147.00		NIST
I	1141.00		NIST
I	1141.00		NIST
I	1124.00		NIST
I	1138.00		NIST
I	1131.00		NIST
I	1132.00		NIST
I	1127.00		NIST
I	1122.00		NIST
I	1145.00		NIST
I	1118.00		NIST
I	1136.00		NIST
I	1124.00		NIST
I	1140.00		NIST
I	1142.00		NIST
I	1120.00		NIST
I	1127.00		NIST
I	1149.00		NIST
I	1124.00		NIST
I	1127.00		NIST
I	1124.00		NIST
I	1149.00		NIST
I	1134.00		NIST
I	Outlier 1160.00		NIST
I	1138.00		NIST
I	1133.00		NIST
I	1125.00		NIST
I	1130.00		NIST
Tboil	[407.00; 419.30]	K
Tboil	419.20	K	KDB
Tboil	419.30	K	Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
Tboil	417.70	K	NIST
Tboil	417.20 ± 0.40	K	NIST
Tboil	418.60 ± 0.25	K	NIST
Tboil	408.15 ± 1.50	K	NIST
Tboil	417.70 ± 1.00	K	NIST
Tboil	417.00 ± 5.00	K	NIST
Tboil	417.90 ± 2.00	K	NIST
Tboil	Outlier 407.00 ± 2.00	K	NIST
Tc	[570.00; 593.30]	K
Tc	570.00	K	KDB
Tc	593.30 ± 1.00	K	NIST
Tc	570.20 ± 20.00	K	NIST
Tfus	[181.90; 182.05]	K
Tfus	181.90	K	KDB
Tfus	182.05	K	Aq. Solubility Prediction
Vc	0.449	m3/kmol	Relay (1.0) 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
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	38.00	kJ/mol	293.00	NIST
n0	[1.39800; 1.39810]		[298.15; 298.15]
n0	1.39800		298.15	Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
n0	1.39810		298.15	Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester + alkane and ester + ester binary systems and the ternary dodecane + ethyl pentanoate + ethyl ethanoate
ρl	[872.36; 877.15]	kg/m3	[293.20; 298.20]
ρl	877.15	kg/m3	293.20	Modeling extraction equilibria of butyric acid distributed between water and tri-n-butyl amine/diluent or tri-n-butyl phosphate/diluent system: Extension of the LSER approach
ρl	872.36	kg/m3	298.20	Modeling phase equilibria of ternary systems (water + formic acid + ester or alcohol) through UNIFAC-original, SERLAS, NRTL, NRTL-modified, and three-suffix Margules: Parameter estimation using genetic algorithm
λ	[0.12; 0.15]	W/m×K	[249.21; 363.57]
λ	0.15	W/m×K	249.21	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.15	W/m×K	263.90	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	273.50	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	283.80	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	288.74	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	289.42	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	293.69	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	298.79	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	303.69	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	308.61	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	313.74	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	318.49	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	323.74	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	328.62	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	333.51	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	338.47	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	343.55	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	348.55	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	353.49	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	358.46	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	363.57	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[345.40; 414.90]	K	[7.10; 91.70]
Tboil	345.40	K	7.10	Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
Tboil	350.70	K	8.90	Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
Tboil	361.10	K	13.90	Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
Tboil	374.90	K	24.10	Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
Tboil	388.30	K	39.10	Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
Tboil	395.70	K	52.70	Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
Tboil	403.90	K	69.30	Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
Tboil	414.90	K	91.70	Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state

Datasets

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	870.7
100.00	303.15	865.5
100.00	308.15	860.3
100.00	313.15	855.0
100.00	318.15	849.8
100.00	323.15	844.4
100.00	328.15	839.1
100.00	333.15	833.7
100.00	338.15	828.4
100.00	343.15	823.0
100.00	348.15	817.7
100.00	353.15	812.2
100.00	363.15	801.2
100.00	373.15	790.7
100.00	383.15	779.9
100.00	393.15	769.0
1000.00	298.15	871.5
1000.00	303.15	866.4
1000.00	308.15	861.2
1000.00	313.15	855.9
1000.00	318.15	850.6
1000.00	323.15	845.3
1000.00	328.15	840.0
1000.00	333.15	834.7
1000.00	338.15	829.5
1000.00	343.15	824.1
1000.00	348.15	818.7
1000.00	353.15	813.3
1000.00	363.15	802.5
1000.00	373.15	792.0
1000.00	383.15	781.3
1000.00	393.15	770.5
2000.00	298.15	872.4
2000.00	303.15	867.4
2000.00	308.15	862.1
2000.00	313.15	856.9
2000.00	318.15	851.7
2000.00	323.15	846.4
2000.00	328.15	841.1
2000.00	333.15	836.0
2000.00	338.15	830.7
2000.00	343.15	825.3
2000.00	348.15	820.0
2000.00	353.15	814.6
2000.00	363.15	803.9
2000.00	373.15	793.5
2000.00	383.15	783.0
2000.00	393.15	772.3
2780.00	298.15	873.0
2780.00	303.15	868.1
2780.00	308.15	862.9
2780.00	313.15	857.7
2780.00	318.15	852.4
2780.00	323.15	847.2
2780.00	328.15	842.0
2780.00	333.15	836.9
2780.00	338.15	831.5
2780.00	343.15	826.2
2780.00	348.15	821.0
2780.00	353.15	815.6
2780.00	363.15	805.0
2780.00	373.15	794.7
2780.00	383.15	784.2
2780.00	393.15	773.6
3000.00	298.15	873.2
3000.00	303.15	868.3
3000.00	308.15	863.1
3000.00	313.15	857.9
3000.00	318.15	852.7
3000.00	323.15	847.4
3000.00	328.15	842.3
3000.00	333.15	837.1
3000.00	338.15	831.8
3000.00	343.15	826.5
3000.00	348.15	821.3
3000.00	353.15	815.9
3000.00	363.15	805.5
3000.00	373.15	795.0
3000.00	383.15	784.5
3000.00	393.15	774.1
5000.00	298.15	875.1
5000.00	303.15	870.1
5000.00	308.15	865.0
5000.00	313.15	859.9
5000.00	318.15	854.6
5000.00	323.15	849.4
5000.00	328.15	844.4
5000.00	333.15	839.3
5000.00	338.15	834.0
5000.00	343.15	828.8
5000.00	348.15	823.7
5000.00	353.15	818.4
5000.00	363.15	808.1
5000.00	373.15	797.9
5000.00	383.15	787.6
5000.00	393.15	777.4
10000.00	298.15	879.4
10000.00	303.15	874.5
10000.00	308.15	869.5
10000.00	313.15	864.5
10000.00	318.15	859.4
10000.00	323.15	854.3
10000.00	328.15	849.4
10000.00	333.15	844.5
10000.00	338.15	839.4
10000.00	343.15	834.4
10000.00	348.15	829.4
10000.00	353.15	824.3
10000.00	363.15	814.6
10000.00	373.15	804.8
10000.00	383.15	795.0
10000.00	393.15	785.1
15000.00	298.15	883.4
15000.00	303.15	878.7
15000.00	308.15	873.8
15000.00	313.15	868.9
15000.00	318.15	863.9
15000.00	323.15	859.0
15000.00	328.15	854.2
15000.00	333.15	849.5
15000.00	338.15	844.5
15000.00	343.15	839.6
15000.00	348.15	834.8
15000.00	353.15	829.9
15000.00	363.15	820.5
15000.00	373.15	810.9
15000.00	383.15	801.5
15000.00	393.15	791.6
20000.00	298.15	887.3
20000.00	303.15	882.6
20000.00	308.15	877.8
20000.00	313.15	873.0
20000.00	318.15	868.2
20000.00	323.15	863.4
20000.00	328.15	858.7
20000.00	333.15	854.1
20000.00	338.15	849.3
20000.00	343.15	844.5
20000.00	348.15	839.9
20000.00	353.15	835.1
20000.00	363.15	826.0
20000.00	373.15	816.7
20000.00	383.15	807.6
20000.00	393.15	797.7
25000.00	298.15	891.0
25000.00	303.15	886.5
25000.00	308.15	881.8
25000.00	313.15	877.0
25000.00	318.15	872.3
25000.00	323.15	867.6
25000.00	328.15	863.0
25000.00	333.15	858.6
25000.00	338.15	853.9
25000.00	343.15	849.2
25000.00	348.15	844.7
25000.00	353.15	840.0
25000.00	363.15	831.2
25000.00	373.15	822.2
25000.00	383.15	813.4
25000.00	393.15	803.5
30000.00	298.15	894.6
30000.00	303.15	890.2
30000.00	308.15	885.6
30000.00	313.15	880.9
30000.00	318.15	876.3
30000.00	323.15	871.7
30000.00	328.15	867.1
30000.00	333.15	862.9
30000.00	338.15	858.2
30000.00	343.15	853.7
30000.00	348.15	849.3
30000.00	353.15	844.7
30000.00	363.15	836.0
30000.00	373.15	827.3
30000.00	383.15	818.9
30000.00	393.15	809.0
35000.00	298.15	898.1
35000.00	303.15	893.8
35000.00	308.15	889.2
35000.00	313.15	884.6
35000.00	318.15	880.1
35000.00	323.15	875.5
35000.00	328.15	871.1
35000.00	333.15	867.0
35000.00	338.15	862.4
35000.00	343.15	858.0
35000.00	348.15	853.6
35000.00	353.15	849.1
35000.00	363.15	840.8
35000.00	373.15	832.3
35000.00	383.15	824.0
35000.00	393.15	814.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[312.40; 439.62]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.53691e+01
Coefficient B			-3.84124e+03
Coefficient C			-5.77010e+01
Temperature range, min.			312.40
Temperature range, max.			439.62
Pvap	1.33	kPa	312.40	Calculated Property
Pvap	2.95	kPa	326.54	Calculated Property
Pvap	6.02	kPa	340.67	Calculated Property
Pvap	11.48	kPa	354.81	Calculated Property
Pvap	20.64	kPa	368.94	Calculated Property
Pvap	35.29	kPa	383.08	Calculated Property
Pvap	57.69	kPa	397.21	Calculated Property
Pvap	90.68	kPa	411.35	Calculated Property
Pvap	137.66	kPa	425.48	Calculated Property
Pvap	202.63	kPa	439.62	Calculated Property
Pvap	[4.54; 179.54]	kPa	[328.15; 430.15]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			4.34447e+02
Coefficient B			-2.34143e+04
Coefficient C			-6.33502e+01
Coefficient D			5.04777e-05
Temperature range, min.			328.15
Temperature range, max.			430.15
Pvap	4.54	kPa	328.15	Calculated Property
Pvap	8.38	kPa	339.48	Calculated Property
Pvap	14.42	kPa	350.82	Calculated Property
Pvap	23.36	kPa	362.15	Calculated Property
Pvap	35.94	kPa	373.48	Calculated Property
Pvap	52.89	kPa	384.82	Calculated Property
Pvap	74.95	kPa	396.15	Calculated Property
Pvap	102.88	kPa	407.48	Calculated Property
Pvap	137.45	kPa	418.82	Calculated Property
Pvap	179.54	kPa	430.15	Calculated Property

Similar Compounds

Find more compounds similar to Pentanoic acid, ethyl ester.

Mixtures

• Pentanoic acid, ethyl ester + Butanoic acid + Water
• Pentanoic acid, ethyl ester + Formic acid + Water
• Pentanoic acid, ethyl ester + Ethanol
• Pentanoic acid, ethyl ester + Ethane, 1,2-dichloro-
• Pentanoic acid, ethyl ester + Propane, 1,3-dichloro-
• Pentanoic acid, ethyl ester + Butane, 1,4-dichloro-
• Pentanoic acid, ethyl ester + Pentane, 1,5-dichloro-
• Pentanoic acid, ethyl ester + Hexane, 1,6-dichloro-
• Pentanoic acid, ethyl ester + Ethane, 1,2-dibromo-
• Pentanoic acid, ethyl ester + Propane, 1,3-dibromo-
• Pentanoic acid, ethyl ester + Butane, 1,4-dibromo-
• Pentanoic acid, ethyl ester + Pentane, 1,5-dibromo-
• Pentanoic acid, ethyl ester + Hexane, 1,6-dibromo-
• Pentanoic acid, ethyl ester + Dodecane
• Pentanoic acid, ethyl ester + Ethyl Acetate
• Pentanoic acid, ethyl ester + Dodecane + Ethyl Acetate
• Pentanoic acid, ethyl ester + Carbon dioxide
• Pentanoic acid, ethyl ester + Carbon dioxide + Ethanol
• Pentanoic acid, ethyl ester + Ethanol + Water
• Pentanoic acid, ethyl ester + Pentanoic acid + Water

Find more mixtures with Pentanoic acid, ethyl ester.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
• Modeling extraction equilibria of butyric acid distributed between water and tri-n-butyl amine/diluent or tri-n-butyl phosphate/diluent system: Extension of the LSER approach
• Modeling phase equilibria of ternary systems (water + formic acid + ester or alcohol) through UNIFAC-original, SERLAS, NRTL, NRTL-modified, and three-suffix Margules: Parameter estimation using genetic algorithm
• Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester + alkane and ester + ester binary systems and the ternary dodecane + ethyl pentanoate + ethyl ethanoate
• Liquid-liquid equilibrium of ternary systems comprising ethyl valerate(1), water(2), ethanol(3) and valeric acid(4)
• Phase equilibrium measurements and thermodynamic modelling for the systems involving valeric acid, ethanol, ethyl valerate and water plus CO2
• Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
• Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
• PVT Property Measurements for Ethyl Propionate, Ethyl Butyrate, and Ethyl Pentanoate Esters from (298 to 393) K and up to 35 MPa
• Joback Method
• KDB
• 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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