Chemical Properties of Acetic acid, pentyl ester (CAS 628-63-7)

InChI

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

InChI Key

PGMYKACGEOXYJE-UHFFFAOYSA-N

Formula

C7H14O2

SMILES

CCCCCOC(C)=O

Molecular Weight¹

130.18

CAS

628-63-7

Other Names

• 1-Acetoxypentane
• 1-PENTYL ACETATE
• 1-Pentanol acetate
• AMYL ACETIC ESTER
• Acetate d'amyle
• Acetic acid n-amyl ester
• Acetic acid, amyl ester
• Acetic acid, n-pentyl ester
• Amyl acetate
• Amyl acetic ether
• Amylazetat
• Amylester kyseliny octove
• Banana oil
• Birnenoel
• N-AMYL ACETATE
• N-PENTYL ACETATE
• NSC 7923
• Octan amylu
• Pear oil
• Pent-acetate
• Pent-acetate 28
• Pentyl acetate
• Pentyl ester of acetic acid
• Primary amyl acetate
• acetic acid, n-amyl ester
• ethanoic acid, pentyl ester
• n-Pentyl ethanoate
• pentyl ethanoate

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_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).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (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	0.4837		Relay (1.0) Calculated Property
ΔcH°liquid	-4372.13	kJ/mol	NIST
ΔfG°	-225.86	kJ/mol	Joback Calculated Property
ΔfH°gas	-516.82	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	16.67	kJ/mol	Joback Calculated Property
ΔvapH°	48.60 ± 0.40	kJ/mol	NIST
IE	9.83	eV	Relay (1.0) Calculated Property
log10WS	[-1.89; -1.89]
log10WS	-1.89		Aq. Solubility Prediction
log10WS	-1.89		Estimated Solubility
logPoct/wat	1.740		Crippen Calculated Property
McVol	116.930	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
Pc	[2685.00; 2770.00]	kPa
Pc	2685.00 ± 150.00	kPa	NIST
Pc	2770.00 ± 20.00	kPa	NIST
ρc	277.42 ± 11.98	kg/m3	NIST
Inp	[848.00; 928.00]
Inp	896.40		NIST
Inp	887.63		NIST
Inp	908.68		NIST
Inp	867.00		NIST
Inp	910.30		NIST
Inp	909.30		NIST
Inp	907.60		NIST
Inp	885.00		NIST
Inp	867.00		NIST
Inp	879.00		NIST
Inp	912.00		NIST
Inp	912.00		NIST
Inp	896.50		NIST
Inp	Outlier 856.00		NIST
Inp	868.00		NIST
Inp	Outlier 855.00		NIST
Inp	891.00		NIST
Inp	891.00		NIST
Inp	893.00		NIST
Inp	Outlier 848.00		NIST
Inp	899.00		NIST
Inp	898.00		NIST
Inp	Outlier 855.00		NIST
Inp	Outlier 856.00		NIST
Inp	866.00		NIST
Inp	893.00		NIST
Inp	899.00		NIST
Inp	895.00		NIST
Inp	898.00		NIST
Inp	898.00		NIST
Inp	895.00		NIST
Inp	898.00		NIST
Inp	903.00		NIST
Inp	905.00		NIST
Inp	919.00		NIST
Inp	891.00		NIST
Inp	Outlier 859.00		NIST
Inp	916.00		NIST
Inp	904.00		NIST
Inp	916.00		NIST
Inp	914.00		NIST
Inp	893.00		NIST
Inp	926.00		NIST
Inp	928.00		NIST
Inp	893.00		NIST
Inp	917.00		NIST
Inp	892.00		NIST
Inp	918.00		NIST
Inp	896.00		NIST
Inp	912.00		NIST
Inp	916.00		NIST
Inp	906.00		NIST
Inp	913.00		NIST
Inp	893.00		NIST
Inp	895.00		NIST
Inp	905.00		NIST
Inp	880.00		NIST
Inp	893.00		NIST
Inp	893.00		NIST
Inp	915.00		NIST
Inp	910.00		NIST
Inp	Outlier 859.00		NIST
Inp	897.00		NIST
Inp	911.00		NIST
Inp	890.00		NIST
Inp	894.00		NIST
Inp	895.00		NIST
Inp	897.00		NIST
Inp	896.00		NIST
Inp	896.00		NIST
Inp	895.00		NIST
Inp	916.00		NIST
Inp	916.00		NIST
Inp	914.00		NIST
Inp	891.00		NIST
Inp	906.00		NIST
Inp	891.00		NIST
Inp	891.00		NIST
Inp	919.00		NIST
Inp	895.00		NIST
Inp	904.00		NIST
Inp	891.00		NIST
Inp	912.00		NIST
Inp	916.00		NIST
Inp	918.00		NIST
Inp	895.00		NIST
Inp	891.00		NIST
Inp	896.00		NIST
Inp	897.00		NIST
Inp	892.00		NIST
Inp	892.00		NIST
Inp	895.00		NIST
Inp	895.00		NIST
Inp	895.00		NIST
Inp	898.00		NIST
Inp	Outlier 859.00		NIST
Inp	893.00		NIST
Inp	892.00		NIST
I	[1150.00; 1222.00]
I	1195.00		NIST
I	1182.00		NIST
I	Outlier 1212.00		NIST
I	1168.00		NIST
I	1182.00		NIST
I	1177.00		NIST
I	1175.00		NIST
I	1177.00		NIST
I	1196.00		NIST
I	1170.00		NIST
I	1160.00		NIST
I	1183.00		NIST
I	1152.00		NIST
I	1176.00		NIST
I	1193.00		NIST
I	1175.00		NIST
I	1169.00		NIST
I	1161.00		NIST
I	1167.00		NIST
I	1176.00		NIST
I	1179.00		NIST
I	1181.00		NIST
I	1167.00		NIST
I	1152.00		NIST
I	1169.00		NIST
I	1180.00		NIST
I	1176.00		NIST
I	Outlier 1204.00		NIST
I	1162.00		NIST
I	1192.00		NIST
I	1169.00		NIST
I	1150.00		NIST
I	1161.00		NIST
I	1185.00		NIST
I	1176.00		NIST
I	1161.00		NIST
I	1173.00		NIST
I	1172.00		NIST
I	1167.00		NIST
I	1177.00		NIST
I	1180.00		NIST
I	1161.00		NIST
I	1174.00		NIST
I	1174.00		NIST
I	Outlier 1222.00		NIST
I	1161.00		NIST
I	1159.00		NIST
I	1159.00		NIST
I	1183.00		NIST
I	1183.00		NIST
I	1183.00		NIST
I	1174.00		NIST
I	1185.00		NIST
I	1183.00		NIST
I	1180.00		NIST
I	1161.00		NIST
I	1183.00		NIST
I	1183.00		NIST
I	1177.00		NIST
I	1194.00		NIST
I	1194.00		NIST
I	1194.00		NIST
I	1161.00		NIST
I	1169.00		NIST
I	1182.00		NIST
Tboil	422.25	K	Quaternary phase equilibrium of water-carboxylic acid mixture (formic-propionic acid or acetic-propionic acid)-solvent liquid systems at 298.15 K
Tc	[599.90; 600.00]	K
Tc	600.00 ± 2.00	K	NIST
Tc	599.90 ± 0.60	K	NIST
Tfus	[182.88; 202.35]	K
Tfus	182.88	K	Aq. Solubility Prediction
Tfus	202.35 ± 0.30	K	NIST
Vc	0.447	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
Cp,liquid	276.10	J/mol×K	304.00	NIST
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	43.20	kJ/mol	376.00	NIST
Pvap	[0.09; 79.99]	kPa	[274.20; 414.20]
Pvap	0.09	kPa	274.20	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.09	kPa	274.30	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.10	kPa	275.60	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.10	kPa	275.60	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.11	kPa	278.20	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.14	kPa	280.80	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.17	kPa	283.20	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.24	kPa	288.20	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.34	kPa	293.30	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.48	kPa	298.40	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.66	kPa	303.30	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.81	kPa	306.70	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	0.90	kPa	308.20	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	1.03	kPa	310.60	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	1.22	kPa	313.40	Vapour pressures and enthalpies of vaporization of aliphatic esters
Pvap	26.66	kPa	380.05	Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
Pvap	53.33	kPa	400.72	Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
Pvap	79.99	kPa	414.20	Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
n0	[1.39100; 1.40270]		[293.13; 318.15]
n0	1.40270		293.13	Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
n0	1.40260		293.15	Phase equilibria of water + 1-propanol + solvent (n-amyl acetate, cyclohexanol, and cyclohexyl acetate) at T = 298.2K
n0	1.40210		293.15	Isobaric Vapor-Liquid Equilibria for Water + Acetic Acid + (n-Pentyl Acetate or Isopropyl Acetate)
n0	1.39990		298.15	Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
n0	1.40050		298.15	Isobaric Vapor-Liquid Equilibrium for Binary Mixtures of 3-Methyl-1-butanol + 3-Methyl-1-butyl Ethanoate and 1-Pentanol + Pentyl Ethanoate at 101.3 kPa
n0	1.39910		298.20	Experimental and correlated liquid-liquid equilibrium data for water-phosphoric acid-ester
n0	1.39610		303.15	Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
n0	1.39100		318.15	Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
ρl	[855.36; 876.25]	kg/m3	[293.15; 313.15]
ρl	876.25	kg/m3	293.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl	870.17	kg/m3	298.15	Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
ρl	871.32	kg/m3	298.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl	870.17	kg/m3	298.15	Surface Tension and Surface Properties of Binary Mixtures of 1,4-Dioxane or N,N-Dimethyl Formamide with n-Alkyl Acetates
ρl	865.78	kg/m3	303.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl	860.58	kg/m3	308.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
ρl	855.36	kg/m3	313.15	Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	871.4
298.15	1000.00	871.9
298.15	2000.00	872.7
298.15	2700.00	873.3
298.15	3000.00	873.5
298.15	5000.00	875.3
298.15	10000.00	879.1
298.15	15000.00	882.7
298.15	20000.00	886.2
298.15	25000.00	889.6
298.15	30000.00	893.6
298.15	35000.00	897.9
303.15	100.00	866.5
303.15	1000.00	867.1
303.15	2000.00	867.9
303.15	2700.00	868.5
303.15	3000.00	868.7
303.15	5000.00	870.5
303.15	10000.00	874.4
303.15	15000.00	878.1
303.15	20000.00	881.6
303.15	25000.00	885.1
303.15	30000.00	889.4
303.15	35000.00	893.8
308.15	100.00	861.6
308.15	1000.00	862.2
308.15	2000.00	863.1
308.15	2700.00	863.7
308.15	3000.00	863.9
308.15	5000.00	865.8
308.15	10000.00	869.8
308.15	15000.00	873.6
308.15	20000.00	877.3
308.15	25000.00	880.8
308.15	30000.00	885.2
308.15	35000.00	889.7
313.15	100.00	856.7
313.15	1000.00	857.4
313.15	2000.00	858.3
313.15	2700.00	858.9
313.15	3000.00	859.2
313.15	5000.00	861.0
313.15	10000.00	865.2
313.15	15000.00	869.0
313.15	20000.00	872.8
313.15	25000.00	876.4
313.15	30000.00	880.9
313.15	35000.00	885.5
318.15	100.00	851.9
318.15	1000.00	852.6
318.15	2000.00	853.5
318.15	2700.00	854.2
318.15	3000.00	854.4
318.15	5000.00	856.4
318.15	10000.00	860.7
318.15	15000.00	864.7
318.15	20000.00	868.5
318.15	25000.00	872.3
318.15	30000.00	876.9
318.15	35000.00	881.7
323.15	100.00	847.1
323.15	1000.00	847.7
323.15	2000.00	848.7
323.15	2700.00	849.3
323.15	3000.00	849.6
323.15	5000.00	851.7
323.15	10000.00	856.1
323.15	15000.00	860.2
323.15	20000.00	864.2
323.15	25000.00	868.1
323.15	30000.00	872.8
323.15	35000.00	877.6
328.15	100.00	842.3
328.15	1000.00	843.2
328.15	2000.00	844.4
328.15	2700.00	845.2
328.15	3000.00	845.5
328.15	5000.00	847.1
328.15	10000.00	851.6
328.15	15000.00	855.9
328.15	20000.00	860.0
328.15	25000.00	864.1
328.15	30000.00	869.0
328.15	35000.00	874.0
333.15	100.00	837.8
333.15	1000.00	838.7
333.15	2000.00	839.8
333.15	2700.00	840.5
333.15	3000.00	840.8
333.15	5000.00	842.7
333.15	10000.00	847.4
333.15	15000.00	851.8
333.15	20000.00	856.0
333.15	25000.00	860.1
333.15	30000.00	865.1
333.15	35000.00	870.2
338.15	100.00	832.9
338.15	1000.00	834.0
338.15	2000.00	835.1
338.15	2700.00	835.8
338.15	3000.00	836.1
338.15	5000.00	838.1
338.15	10000.00	842.9
338.15	15000.00	847.5
338.15	20000.00	851.9
338.15	25000.00	856.2
338.15	30000.00	861.3
338.15	35000.00	866.5
343.15	100.00	828.3
343.15	1000.00	829.3
343.15	2000.00	830.4
343.15	2700.00	831.2
343.15	3000.00	831.5
343.15	5000.00	833.5
343.15	10000.00	838.5
343.15	15000.00	843.2
343.15	20000.00	847.7
343.15	25000.00	852.1
343.15	30000.00	857.3
343.15	35000.00	862.7
348.15	100.00	823.2
348.15	1000.00	824.6
348.15	2000.00	825.7
348.15	2700.00	826.5
348.15	3000.00	826.9
348.15	5000.00	828.8
348.15	10000.00	834.0
348.15	15000.00	838.9
348.15	20000.00	843.5
348.15	25000.00	847.9
348.15	30000.00	853.3
348.15	35000.00	858.8
353.15	100.00	818.7
353.15	1000.00	819.9
353.15	2000.00	821.1
353.15	2700.00	821.9
353.15	3000.00	822.3
353.15	5000.00	824.4
353.15	10000.00	829.8
353.15	15000.00	835.0
353.15	20000.00	839.7
353.15	25000.00	844.3
353.15	30000.00	849.8
353.15	35000.00	855.4
358.15	100.00	811.3
358.15	1000.00	812.2
358.15	2000.00	813.4
358.15	2700.00	814.1
358.15	3000.00	814.5
358.15	5000.00	816.9
358.15	10000.00	822.5
358.15	15000.00	827.7
358.15	20000.00	832.5
358.15	25000.00	838.0
358.15	30000.00	843.9
358.15	35000.00	849.7
363.15	100.00	806.3
363.15	1000.00	807.4
363.15	2000.00	808.7
363.15	2700.00	809.6
363.15	3000.00	809.9
363.15	5000.00	812.4
363.15	10000.00	818.1
363.15	15000.00	823.4
363.15	20000.00	828.3
363.15	25000.00	833.9
363.15	30000.00	839.9
363.15	35000.00	845.6
368.15	100.00	801.2
368.15	1000.00	802.3
368.15	2000.00	803.7
368.15	2700.00	804.6
368.15	3000.00	805.0
368.15	5000.00	807.5
368.15	10000.00	813.4
368.15	15000.00	818.8
368.15	20000.00	824.0
368.15	25000.00	829.8
368.15	30000.00	835.9
368.15	35000.00	841.4
373.15	100.00	795.5
373.15	1000.00	796.4
373.15	2000.00	797.7
373.15	2700.00	799.5
373.15	3000.00	799.0
373.15	5000.00	802.5
373.15	10000.00	808.2
373.15	15000.00	813.9
373.15	20000.00	819.8
373.15	25000.00	826.3
373.15	30000.00	831.3
378.15	100.00	790.4
378.15	1000.00	791.6
378.15	2000.00	793.1
378.15	2700.00	794.0
378.15	3000.00	794.4
378.15	5000.00	797.1
378.15	10000.00	803.5
383.15	100.00	786.8
383.15	1000.00	788.1
383.15	2000.00	789.6
383.15	2700.00	790.7
383.15	3000.00	791.1
383.15	5000.00	793.9
383.15	10000.00	800.5
383.15	15000.00	806.6
383.15	20000.00	811.7
383.15	25000.00	816.5
383.15	30000.00	824.0
383.15	35000.00	830.0
388.15	100.00	781.9
388.15	1000.00	783.4
388.15	2000.00	785.0
388.15	2700.00	786.0
388.15	3000.00	786.5
388.15	5000.00	789.4
388.15	10000.00	796.3
388.15	15000.00	802.5
388.15	20000.00	808.1
388.15	25000.00	813.7
388.15	30000.00	819.7
388.15	35000.00	826.2
393.15	100.00	777.2
393.15	1000.00	778.7
393.15	2000.00	780.3
393.15	2700.00	781.4
393.15	3000.00	781.9
393.15	5000.00	784.9
393.15	10000.00	791.9
393.15	15000.00	798.4
393.15	20000.00	803.9
393.15	25000.00	809.7
393.15	30000.00	815.7
393.15	35000.00	822.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[316.02; 444.97]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.53552e+01
Coefficient B			-3.88429e+03
Coefficient C			-5.82300e+01
Temperature range, min.			316.02
Temperature range, max.			444.97
Pvap	1.33	kPa	316.02	Calculated Property
Pvap	2.95	kPa	330.35	Calculated Property
Pvap	6.02	kPa	344.68	Calculated Property
Pvap	11.48	kPa	359.00	Calculated Property
Pvap	20.66	kPa	373.33	Calculated Property
Pvap	35.31	kPa	387.66	Calculated Property
Pvap	57.72	kPa	401.99	Calculated Property
Pvap	90.72	kPa	416.31	Calculated Property
Pvap	137.71	kPa	430.64	Calculated Property
Pvap	202.66	kPa	444.97	Calculated Property
Pvap	[2.28e-05; 2719.53]	kPa	[202.35; 598.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			8.62684e+01
Coefficient B			-8.63027e+03
Coefficient C			-1.02643e+01
Coefficient D			4.74624e-06
Temperature range, min.			202.35
Temperature range, max.			598.00
Pvap	2.28e-05	kPa	202.35	Calculated Property
Pvap	6.72e-03	kPa	246.31	Calculated Property
Pvap	0.28	kPa	290.27	Calculated Property
Pvap	3.76	kPa	334.23	Calculated Property
Pvap	24.65	kPa	378.19	Calculated Property
Pvap	101.45	kPa	422.16	Calculated Property
Pvap	303.74	kPa	466.12	Calculated Property
Pvap	728.14	kPa	510.08	Calculated Property
Pvap	1489.89	kPa	554.04	Calculated Property
Pvap	2719.53	kPa	598.00	Calculated Property

Similar Compounds

Find more compounds similar to Acetic acid, pentyl ester.

Mixtures

• Acetic acid, pentyl ester + Water
• 1-Propanol + Acetic acid, pentyl ester + Water
• Acetic acid, pentyl ester + Heptane
• Acetic acid, pentyl ester + Nonane
• Undecane + Acetic acid, pentyl ester
• Acetic acid, pentyl ester + Tridecane
• Acetic acid, pentyl ester + Pentadecane
• Heptadecane + Acetic acid, pentyl ester
• Benzene + Acetic acid, pentyl ester
• Toluene + Acetic acid, pentyl ester
• n-Hexane + Acetic acid, pentyl ester
• Acetic acid, pentyl ester + Octane
• Acetic acid, pentyl ester + Decane
• Acetic acid, pentyl ester + Cyclohexane
• 1-Hexene + Acetic acid, pentyl ester
• Acetic acid, pentyl ester + 1-Heptene
• Acetic acid, pentyl ester + Cyclohexene
• Acetic acid, pentyl ester + 1-Octyne
• 1,7-Octadiene + Acetic acid, pentyl ester
• Acetic acid, pentyl ester + Ethylbenzene

Find more mixtures with Acetic acid, pentyl ester.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Phase equilibria of water + 1-propanol + solvent (n-amyl acetate, cyclohexanol, and cyclohexyl acetate) at T = 298.2K
• Quaternary phase equilibrium of water-carboxylic acid mixture (formic-propionic acid or acetic-propionic acid)-solvent liquid systems at 298.15 K
• Vapour pressures and enthalpies of vaporization of aliphatic esters
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• Solubility, liquid-liquid equilibrium and critical states for quaternary system acetic acid - n-amyl alcohol - n-amyl acetate - water at 303.15 K and atmospheric pressure
• Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
• Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
• Experimental and correlated liquid-liquid equilibrium data for water-phosphoric acid-ester
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
• Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
• Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
• Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
• Isobaric Vapor-Liquid Equilibria for Water + Acetic Acid + (n-Pentyl Acetate or Isopropyl Acetate)
• PVT Property Measurements for Some Aliphatic Esters from (298 to 393) K and up to 35 MPa
• Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
• Liquid-Liquid Equilibria for the Acetic Acid + Water + Amyl Acetate and Acetic Acid + Water + 2-Methyl Ethyl Acetate Ternary Systems
• Surface Tension and Surface Properties of Binary Mixtures of 1,4-Dioxane or N,N-Dimethyl Formamide with n-Alkyl Acetates
• Isobaric Vapor-Liquid Equilibrium for Binary Mixtures of 3-Methyl-1-butanol + 3-Methyl-1-butyl Ethanoate and 1-Pentanol + Pentyl Ethanoate at 101.3 kPa
• 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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