Chemical Properties of Butanoic acid, ethyl ester (CAS 105-54-4)

InChI

InChI=1S/C6H12O2/c1-3-5-6(7)8-4-2/h3-5H2,1-2H3

InChI Key

OBNCKNCVKJNDBV-UHFFFAOYSA-N

Formula

C6H12O2

SMILES

CCCC(=O)OCC

Molecular Weight¹

116.16

CAS

105-54-4

Other Names

• BUTYRIC ESTER
• Ethyl ester of butanoic acid
• Ethyl n-butanoate
• Ethyl n-butyrate
• Methyl pentanoate
• NSC 8857
• UN 1180
• butyric acid, ethyl ester
• ethyl 1-butyrate
• ethyl butanoate
• ethyl butanoate (ethyl butyrate)
• ethyl butyrate
• n-Butyric 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).
• μ : Dipole Moment (debye).
• 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).
• 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_p : Polar retention indices.
• γ : Surface Tension (N/m).
• 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).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.4379; 0.4610]
ω	0.4379		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4610		KDB
ΔcH°liquid	[-3545.00; -3539.00]	kJ/mol
ΔcH°liquid	-3545.00	kJ/mol	NIST
ΔcH°liquid	-3539.00	kJ/mol	NIST
μ	1.80	debye	KDB
ΔfG°	-310.73	kJ/mol	Joback Calculated Property
ΔfH°gas	-485.00 ± 1.00	kJ/mol	NIST
ΔfH°liquid	-528.40 ± 0.79	kJ/mol	NIST
ΔfusH°	15.67	kJ/mol	Joback Calculated Property
ΔvapH°	[36.90; 44.00]	kJ/mol
ΔvapH°	42.71	kJ/mol	NIST
ΔvapH°	44.00 ± 1.00	kJ/mol	NIST
ΔvapH°	43.40	kJ/mol	NIST
ΔvapH°	43.70 ± 1.30	kJ/mol	NIST
ΔvapH°	42.68 ± 0.10	kJ/mol	NIST
ΔvapH°	42.00 ± 0.10	kJ/mol	NIST
ΔvapH°	42.00 ± 0.10	kJ/mol	NIST
ΔvapH°	Outlier 36.90 ± 0.04	kJ/mol	NIST
IE	9.82	eV	Relay (1.0) Calculated Property
log10WS	[-1.36; -1.28]
log10WS	-1.28		Aq. Solubility Prediction
log10WS	-1.36		Estimated Solubility
logPoct/wat	1.350		Crippen Calculated Property
McVol	102.840	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
Pc	[3060.00; 3141.08]	kPa
Pc	3100.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	3141.08	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3060.00	kPa	KDB
Pc	3064.00 ± 151.99	kPa	NIST
ρc	276.46 ± 9.99	kg/m3	NIST
Inp	[760.00; 818.00]
Inp	784.00		NIST
Inp	780.20		NIST
Inp	802.00		NIST
Inp	783.00		NIST
Inp	792.00		NIST
Inp	796.00		NIST
Inp	806.00		NIST
Inp	782.00		NIST
Inp	781.00		NIST
Inp	Outlier 760.00		NIST
Inp	782.00		NIST
Inp	778.00		NIST
Inp	782.00		NIST
Inp	788.00		NIST
Inp	784.00		NIST
Inp	788.00		NIST
Inp	775.00		NIST
Inp	785.00		NIST
Inp	793.00		NIST
Inp	789.00		NIST
Inp	791.00		NIST
Inp	792.00		NIST
Inp	789.00		NIST
Inp	789.00		NIST
Inp	790.00		NIST
Inp	793.00		NIST
Inp	790.00		NIST
Inp	Outlier 764.00		NIST
Inp	799.00		NIST
Inp	798.00		NIST
Inp	Outlier 764.00		NIST
Inp	790.00		NIST
Inp	791.00		NIST
Inp	778.00		NIST
Inp	779.00		NIST
Inp	803.00		NIST
Inp	801.00		NIST
Inp	803.00		NIST
Inp	788.00		NIST
Inp	778.00		NIST
Inp	776.00		NIST
Inp	804.00		NIST
Inp	802.00		NIST
Inp	798.00		NIST
Inp	802.00		NIST
Inp	802.00		NIST
Inp	808.00		NIST
Inp	808.00		NIST
Inp	800.00		NIST
Inp	805.00		NIST
Inp	802.00		NIST
Inp	794.00		NIST
Inp	805.00		NIST
Inp	801.00		NIST
Inp	800.00		NIST
Inp	797.00		NIST
Inp	781.00		NIST
Inp	800.00		NIST
Inp	781.00		NIST
Inp	781.00		NIST
Inp	800.00		NIST
Inp	805.00		NIST
Inp	785.00		NIST
Inp	781.00		NIST
Inp	781.00		NIST
Inp	806.00		NIST
Inp	802.20		NIST
Inp	790.00		NIST
Inp	802.00		NIST
Inp	802.00		NIST
Inp	803.00		NIST
Inp	800.00		NIST
Inp	802.00		NIST
Inp	802.00		NIST
Inp	802.00		NIST
Inp	802.00		NIST
Inp	804.00		NIST
Inp	804.00		NIST
Inp	774.00		NIST
Inp	791.00		NIST
Inp	782.00		NIST
Inp	779.00		NIST
Inp	800.00		NIST
Inp	785.00		NIST
Inp	787.00		NIST
Inp	804.00		NIST
Inp	802.00		NIST
Inp	778.00		NIST
Inp	778.00		NIST
Inp	778.00		NIST
Inp	778.00		NIST
Inp	Outlier 818.00		NIST
Inp	801.00		NIST
Inp	805.00		NIST
Inp	806.00		NIST
Inp	803.00		NIST
Inp	807.00		NIST
Inp	798.00		NIST
Inp	770.00		NIST
Inp	798.00		NIST
Inp	805.00		NIST
Inp	805.00		NIST
Inp	805.00		NIST
Inp	801.00		NIST
Inp	803.00		NIST
Inp	798.00		NIST
Inp	800.00		NIST
Inp	803.00		NIST
Inp	803.00		NIST
Inp	802.00		NIST
Inp	801.00		NIST
Inp	802.00		NIST
Inp	792.00		NIST
Inp	803.00		NIST
Inp	804.00		NIST
Inp	784.00		NIST
Inp	801.00		NIST
Inp	803.00		NIST
Inp	774.00		NIST
Inp	807.00		NIST
Inp	802.00		NIST
Inp	800.00		NIST
Inp	783.00		NIST
Inp	800.00		NIST
Inp	800.00		NIST
Inp	800.00		NIST
Inp	803.00		NIST
Inp	800.00		NIST
Inp	800.00		NIST
Inp	806.00		NIST
Inp	778.00		NIST
Inp	804.00		NIST
Inp	788.00		NIST
Inp	798.00		NIST
Inp	788.00		NIST
Inp	797.00		NIST
Inp	799.00		NIST
Inp	783.00		NIST
Inp	803.00		NIST
Inp	804.00		NIST
Inp	780.00		NIST
Inp	812.00		NIST
Inp	802.00		NIST
Inp	780.00		NIST
Inp	785.00		NIST
Inp	790.00		NIST
Inp	799.00		NIST
Inp	784.00		NIST
Inp	802.00		NIST
Inp	804.00		NIST
Inp	804.00		NIST
Inp	799.00		NIST
Inp	782.00		NIST
Inp	791.00		NIST
Inp	780.00		NIST
Inp	784.00		NIST
Inp	785.00		NIST
Inp	781.00		NIST
Inp	788.00		NIST
Inp	789.00		NIST
Inp	785.00		NIST
Inp	785.00		NIST
Inp	782.00		NIST
Inp	794.00		NIST
Inp	796.00		NIST
Inp	787.00		NIST
Inp	774.00		NIST
Inp	770.00		NIST
Inp	807.00		NIST
Inp	801.00		NIST
Inp	803.00		NIST
Inp	798.00		NIST
Inp	801.00		NIST
Inp	770.00		NIST
Inp	804.00		NIST
Inp	800.00		NIST
Inp	770.00		NIST
Inp	802.00		NIST
Inp	803.00		NIST
Inp	804.00		NIST
Inp	796.00		NIST
Inp	800.00		NIST
Inp	802.00		NIST
Inp	800.00		NIST
Inp	803.00		NIST
Inp	800.00		NIST
Inp	778.00		NIST
Inp	799.00		NIST
Inp	778.00		NIST
Inp	770.00		NIST
Inp	770.00		NIST
Inp	774.00		NIST
Inp	803.00		NIST
Inp	774.00		NIST
Inp	774.00		NIST
Inp	804.00		NIST
Inp	792.00		NIST
Inp	804.00		NIST
Inp	802.00		NIST
Inp	787.00		NIST
Inp	787.00		NIST
Inp	800.00		NIST
Inp	800.00		NIST
Inp	798.00		NIST
Inp	784.00		NIST
Inp	806.00		NIST
Inp	806.00		NIST
Inp	771.00		NIST
Inp	789.00		NIST
Inp	802.00		NIST
Inp	771.00		NIST
Inp	806.00		NIST
Inp	800.00		NIST
Inp	774.00		NIST
Inp	771.00		NIST
Inp	781.00		NIST
Inp	800.00		NIST
Inp	788.00		NIST
Inp	804.00		NIST
Inp	800.00		NIST
Inp	800.00		NIST
Inp	785.00		NIST
Inp	774.00		NIST
Inp	793.00		NIST
Inp	796.00		NIST
Inp	784.00		NIST
Inp	784.00		NIST
Inp	780.00		NIST
Inp	804.00		NIST
Inp	804.00		NIST
Inp	804.00		NIST
Inp	801.00		NIST
Inp	802.00		NIST
Inp	805.00		NIST
Inp	780.00		NIST
Inp	789.00		NIST
Inp	788.00		NIST
Inp	780.00		NIST
Inp	783.00		NIST
Inp	784.00		NIST
Inp	784.00		NIST
Inp	787.00		NIST
Inp	799.00		NIST
Inp	778.00		NIST
Inp	784.00		NIST
Inp	796.00		NIST
Inp	782.00		NIST
Inp	788.00		NIST
Inp	774.00		NIST
Inp	798.00		NIST
Inp	770.00		NIST
Inp	800.00		NIST
Inp	792.00		NIST
Inp	806.00		NIST
Inp	785.00		NIST
Inp	801.00		NIST
Inp	787.00		NIST
Inp	804.00		NIST
Inp	803.00		NIST
Inp	805.00		NIST
Inp	789.00		NIST
Inp	Outlier 764.00		NIST
Ip	[990.00; 1081.00]
Ip	1025.00		NIST
Ip	1051.00		NIST
Ip	1054.00		NIST
Ip	Outlier 1008.00		NIST
Ip	1032.00		NIST
Ip	1045.00		NIST
Ip	1032.00		NIST
Ip	1058.00		NIST
Ip	1057.00		NIST
Ip	1010.00		NIST
Ip	1044.00		NIST
Ip	1044.00		NIST
Ip	1040.00		NIST
Ip	1026.00		NIST
Ip	1042.00		NIST
Ip	1043.00		NIST
Ip	1045.00		NIST
Ip	Outlier 1005.00		NIST
Ip	1028.00		NIST
Ip	1036.00		NIST
Ip	1048.00		NIST
Ip	1035.00		NIST
Ip	1035.00		NIST
Ip	1041.00		NIST
Ip	1049.00		NIST
Ip	1061.00		NIST
Ip	1041.00		NIST
Ip	1033.00		NIST
Ip	1039.00		NIST
Ip	1027.00		NIST
Ip	1052.00		NIST
Ip	1048.00		NIST
Ip	1048.00		NIST
Ip	Outlier 1067.00		NIST
Ip	Outlier 1073.00		NIST
Ip	Outlier 1069.00		NIST
Ip	Outlier 1000.00		NIST
Ip	1037.00		NIST
Ip	1029.00		NIST
Ip	1052.00		NIST
Ip	1022.00		NIST
Ip	1022.00		NIST
Ip	Outlier 1001.00		NIST
Ip	1023.00		NIST
Ip	1041.00		NIST
Ip	1023.00		NIST
Ip	1030.00		NIST
Ip	1021.00		NIST
Ip	1036.00		NIST
Ip	1037.00		NIST
Ip	1021.00		NIST
Ip	1041.00		NIST
Ip	1057.00		NIST
Ip	1025.00		NIST
Ip	1020.00		NIST
Ip	1024.00		NIST
Ip	1025.00		NIST
Ip	1040.40		NIST
Ip	1039.00		NIST
Ip	1039.00		NIST
Ip	1021.00		NIST
Ip	1023.00		NIST
Ip	1044.00		NIST
Ip	1037.00		NIST
Ip	1040.00		NIST
Ip	1032.00		NIST
Ip	1025.00		NIST
Ip	1031.00		NIST
Ip	1057.00		NIST
Ip	1025.00		NIST
Ip	1032.00		NIST
Ip	1040.00		NIST
Ip	1040.00		NIST
Ip	1046.00		NIST
Ip	1040.00		NIST
Ip	1055.00		NIST
Ip	1034.00		NIST
Ip	1034.00		NIST
Ip	1032.00		NIST
Ip	1044.00		NIST
Ip	1028.00		NIST
Ip	1028.00		NIST
Ip	1056.00		NIST
Ip	1021.00		NIST
Ip	1034.00		NIST
Ip	1042.00		NIST
Ip	1056.00		NIST
Ip	1022.00		NIST
Ip	1047.00		NIST
Ip	1037.00		NIST
Ip	1038.00		NIST
Ip	1041.00		NIST
Ip	1041.00		NIST
Ip	1025.00		NIST
Ip	1043.00		NIST
Ip	1044.00		NIST
Ip	1041.00		NIST
Ip	1037.00		NIST
Ip	1035.00		NIST
Ip	1028.00		NIST
Ip	1048.00		NIST
Ip	1038.00		NIST
Ip	1021.00		NIST
Ip	1033.00		NIST
Ip	1038.00		NIST
Ip	1026.00		NIST
Ip	1040.00		NIST
Ip	1032.00		NIST
Ip	1028.00		NIST
Ip	1029.00		NIST
Ip	1037.00		NIST
Ip	1014.00		NIST
Ip	1042.00		NIST
Ip	1042.00		NIST
Ip	1036.00		NIST
Ip	1054.00		NIST
Ip	1015.00		NIST
Ip	1035.00		NIST
Ip	1046.00		NIST
Ip	1031.00		NIST
Ip	1031.00		NIST
Ip	1038.00		NIST
Ip	1050.00		NIST
Ip	1013.00		NIST
Ip	Outlier 1066.00		NIST
Ip	1030.00		NIST
Ip	1025.00		NIST
Ip	1047.00		NIST
Ip	1035.00		NIST
Ip	1057.00		NIST
Ip	1028.00		NIST
Ip	1044.00		NIST
Ip	1038.00		NIST
Ip	1032.00		NIST
Ip	1050.00		NIST
Ip	1036.00		NIST
Ip	1022.00		NIST
Ip	1036.00		NIST
Ip	1040.00		NIST
Ip	1036.00		NIST
Ip	1031.00		NIST
Ip	1025.00		NIST
Ip	1043.00		NIST
Ip	1048.00		NIST
Ip	1030.00		NIST
Ip	1023.00		NIST
Ip	1025.00		NIST
Ip	1031.00		NIST
Ip	1035.00		NIST
Ip	1043.00		NIST
Ip	1033.00		NIST
Ip	1025.00		NIST
Ip	1043.00		NIST
Ip	1033.00		NIST
Ip	1052.00		NIST
Ip	1043.00		NIST
Ip	1043.00		NIST
Ip	1029.00		NIST
Ip	1009.00		NIST
Ip	1025.00		NIST
Ip	1010.00		NIST
Ip	1018.00		NIST
Ip	1025.00		NIST
Ip	1030.90		NIST
Ip	1025.00		NIST
Ip	1060.00		NIST
Ip	1028.00		NIST
Ip	1035.00		NIST
Ip	1035.00		NIST
Ip	1035.00		NIST
Ip	1037.00		NIST
Ip	1035.00		NIST
Ip	1037.00		NIST
Ip	1035.00		NIST
Ip	1037.00		NIST
Ip	1035.00		NIST
Ip	1037.00		NIST
Ip	1028.00		NIST
Ip	1030.00		NIST
Ip	1039.00		NIST
Ip	1036.00		NIST
Ip	Outlier 1075.00		NIST
Ip	1060.00		NIST
Ip	1032.00		NIST
Ip	1039.00		NIST
Ip	1033.00		NIST
Ip	1033.00		NIST
Ip	Outlier 1002.00		NIST
Ip	1023.00		NIST
Ip	1023.00		NIST
Ip	1050.00		NIST
Ip	1026.00		NIST
Ip	Outlier 1076.00		NIST
Ip	Outlier 1078.00		NIST
Ip	Outlier 1079.00		NIST
Ip	1035.00		NIST
Ip	1040.00		NIST
Ip	1046.00		NIST
Ip	1031.00		NIST
Ip	1022.00		NIST
Ip	1043.00		NIST
Ip	1026.00		NIST
Ip	1043.00		NIST
Ip	1029.00		NIST
Ip	1022.00		NIST
Ip	1037.00		NIST
Ip	1037.00		NIST
Ip	1044.00		NIST
Ip	1028.00		NIST
Ip	Outlier 990.00		NIST
Ip	Outlier 1081.00		NIST
Ip	1043.00		NIST
Ip	1030.00		NIST
Ip	1040.00		NIST
Ip	1028.00		NIST
Ip	1045.00		NIST
Ip	1037.00		NIST
Ip	1042.00		NIST
Ip	1028.00		NIST
Ip	1043.00		NIST
Ip	1032.00		NIST
Ip	1046.00		NIST
Ip	1024.00		NIST
Ip	1043.00		NIST
Ip	1042.00		NIST
Ip	1033.00		NIST
Ip	1022.00		NIST
Ip	Outlier 1071.00		NIST
Ip	1056.00		NIST
Ip	1028.00		NIST
Ip	1025.00		NIST
Ip	1047.00		NIST
Ip	1025.00		NIST
Ip	1031.00		NIST
Ip	1047.00		NIST
Ip	1047.00		NIST
Ip	1023.00		NIST
Ip	1044.00		NIST
Ip	1023.00		NIST
Ip	1023.00		NIST
Ip	1046.00		NIST
Ip	1028.00		NIST
Ip	1025.00		NIST
Ip	1028.00		NIST
Ip	1041.00		NIST
Ip	1039.00		NIST
Ip	Outlier 1067.00		NIST
Ip	1029.00		NIST
Ip	1023.00		NIST
Ip	1036.00		NIST
Ip	1025.00		NIST
Ip	1037.00		NIST
Ip	1057.00		NIST
Tboil	[387.95; 394.90]	K
Tboil	394.55	K	Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
Tboil	393.78	K	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Tboil	394.17	K	Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
Tboil	394.13	K	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Tboil	394.60	K	KDB
Tboil	394.18 ± 0.40	K	NIST
Tboil	393.20	K	NIST
Tboil	393.00	K	NIST
Tboil	394.60	K	NIST
Tboil	393.95 ± 0.50	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	Outlier 388.65 ± 5.00	K	NIST
Tboil	393.15 ± 1.00	K	NIST
Tboil	394.55 ± 1.00	K	NIST
Tboil	393.15 ± 1.00	K	NIST
Tboil	393.00 ± 1.00	K	NIST
Tboil	394.70 ± 0.50	K	NIST
Tboil	394.15 ± 1.00	K	NIST
Tboil	394.50 ± 2.00	K	NIST
Tboil	393.10 ± 1.00	K	NIST
Tboil	394.70 ± 0.50	K	NIST
Tboil	394.35 ± 0.40	K	NIST
Tboil	393.40 ± 0.50	K	NIST
Tboil	393.30 ± 0.50	K	NIST
Tboil	393.20 ± 0.50	K	NIST
Tboil	393.35 ± 0.50	K	NIST
Tboil	393.45 ± 1.00	K	NIST
Tboil	391.65 ± 1.00	K	NIST
Tboil	392.15 ± 2.00	K	NIST
Tboil	394.90 ± 0.30	K	NIST
Tboil	393.15 ± 1.00	K	NIST
Tboil	393.40 ± 1.00	K	NIST
Tboil	394.65 ± 1.00	K	NIST
Tboil	394.40 ± 1.50	K	NIST
Tboil	391.90 ± 1.00	K	NIST
Tboil	393.15 ± 1.00	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	393.75 ± 1.00	K	NIST
Tboil	393.80 ± 0.50	K	NIST
Tboil	394.10 ± 1.50	K	NIST
Tboil	394.40 ± 1.00	K	NIST
Tboil	394.25 ± 1.00	K	NIST
Tboil	392.15 ± 1.00	K	NIST
Tboil	Outlier 387.95 ± 1.00	K	NIST
Tboil	Outlier 387.95 ± 1.00	K	NIST
Tc	[558.70; 577.50]	K
Tc	569.98	K	Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
Tc	568.80	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	568.80	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	566.00	K	KDB
Tc	568.80 ± 0.60	K	NIST
Tc	558.70 ± 10.00	K	NIST
Tc	566.00 ± 2.00	K	NIST
Tc	577.50 ± 6.00	K	NIST
Tfus	[170.65; 180.15]	K
Tfus	180.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	175.00	K	KDB
Tfus	178.90	K	Aq. Solubility Prediction
Tfus	175.30 ± 0.30	K	NIST
Tfus	170.65 ± 0.70	K	NIST
Vc	[0.395; 0.421]	m3/kmol
Vc	0.415	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc	0.395	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.421	m3/kmol	KDB
Zc	[0.2630000; 0.2737480]
Zc	0.2630000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc	0.2737480		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[220.10; 229.70]	J/mol×K	[290.00; 298.15]
Cp,liquid	229.70	J/mol×K	290.00	NIST
Cp,liquid	220.10	J/mol×K	297.20	NIST
Cp,liquid	220.10	J/mol×K	297.20	NIST
Cp,liquid	228.00	J/mol×K	298.15	NIST
η	[0.0003820; 0.0006620]	Pa×s	[293.15; 343.15]
η	0.0006620	Pa×s	293.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0006200	Pa×s	298.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0005830	Pa×s	303.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0005490	Pa×s	308.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0005190	Pa×s	313.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004910	Pa×s	318.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004650	Pa×s	323.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004420	Pa×s	328.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004200	Pa×s	333.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0004000	Pa×s	338.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
η	0.0003820	Pa×s	343.15	Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
ΔvapH	[35.47; 48.30]	kJ/mol	[323.00; 394.60]
ΔvapH	42.10 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	41.80	kJ/mol	324.00	NIST
ΔvapH	48.30	kJ/mol	333.50	NIST
ΔvapH	40.20	kJ/mol	362.50	NIST
ΔvapH	39.40	kJ/mol	382.50	NIST
ΔvapH	35.47	kJ/mol	394.60	NIST
Pvap	[22.50; 101.31]	kPa	[348.97; 394.13]
Pvap	22.50	kPa	348.97	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	25.00	kPa	351.83	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	27.50	kPa	354.39	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	30.03	kPa	356.76	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	32.51	kPa	359.00	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	35.02	kPa	361.08	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	35.41	kPa	361.56	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	37.52	kPa	363.04	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	40.04	kPa	364.86	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	40.41	kPa	365.24	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	42.51	kPa	366.66	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	45.03	kPa	368.24	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	47.51	kPa	369.87	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	50.00	kPa	371.33	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	50.01	kPa	371.44	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	52.51	kPa	372.86	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	54.40	kPa	373.83	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	55.03	kPa	374.31	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	57.52	kPa	375.67	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	58.98	kPa	376.28	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	376.95	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	60.00	kPa	377.21	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	60.00	kPa	377.23	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	65.03	kPa	379.48	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	65.75	kPa	379.65	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	67.53	kPa	380.68	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	70.00	kPa	381.82	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	72.52	kPa	382.96	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	75.01	kPa	384.07	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	77.20	kPa	384.82	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	77.51	kPa	385.13	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	79.99	kPa	386.19	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	82.52	kPa	387.22	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	84.14	kPa	387.65	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	85.02	kPa	388.21	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	87.54	kPa	389.17	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	89.98	kPa	390.12	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	90.84	kPa	390.23	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	92.53	kPa	391.06	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	94.92	kPa	391.95	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	97.45	kPa	392.83	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	100.40	kPa	393.63	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	100.01	kPa	393.71	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
Pvap	101.30	kPa	393.78	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
Pvap	101.31	kPa	394.13	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
n0	[1.38950; 1.38990]		[293.15; 298.15]
n0	1.38990		293.15	Vapor liquid equilibria of carbon dioxide with isopropyl acetate, diethyl carbonate and ethyl butyrate at elevated pressures
n0	1.38950		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	1.38980		298.15	Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
ρl	[847.00; 884.16]	kg/m3	[288.15; 323.15]
ρl	884.16	kg/m3	288.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	879.00	kg/m3	293.00	KDB
ρl	878.90	kg/m3	293.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	879.18	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	874.31	kg/m3	298.15	Acoustic and volumetric study of renewable oxygenated fuel additives at (298.15-323.15) K: Isomeric butanediols with ethylbutyrate
ρl	873.62	kg/m3	298.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	868.85	kg/m3	303.15	Acoustic and volumetric study of renewable oxygenated fuel additives at (298.15-323.15) K: Isomeric butanediols with ethylbutyrate
ρl	868.33	kg/m3	303.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	868.21	kg/m3	303.15	Densities, Viscosities, and Surface and Interfacial Tensions of the Ternary Mixture Water + Ethyl Butyrate + Methanol at 303.15 K.
ρl	863.02	kg/m3	308.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	863.40	kg/m3	308.15	Acoustic and volumetric study of renewable oxygenated fuel additives at (298.15-323.15) K: Isomeric butanediols with ethylbutyrate
ρl	857.94	kg/m3	313.15	Acoustic and volumetric study of renewable oxygenated fuel additives at (298.15-323.15) K: Isomeric butanediols with ethylbutyrate
ρl	857.70	kg/m3	313.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	852.49	kg/m3	318.15	Acoustic and volumetric study of renewable oxygenated fuel additives at (298.15-323.15) K: Isomeric butanediols with ethylbutyrate
ρl	852.36	kg/m3	318.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	847.03	kg/m3	323.15	Acoustic and volumetric study of renewable oxygenated fuel additives at (298.15-323.15) K: Isomeric butanediols with ethylbutyrate
ρl	847.00	kg/m3	323.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
λliquid	[0.12; 0.15]	W/m×K	[268.57; 363.52]
λliquid	0.15	W/m×K	268.57	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.14	W/m×K	273.61	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.14	W/m×K	278.63	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.14	W/m×K	283.58	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.14	W/m×K	288.65	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.14	W/m×K	293.58	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.14	W/m×K	298.53	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.13	W/m×K	303.56	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.13	W/m×K	308.67	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.13	W/m×K	313.49	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.13	W/m×K	318.61	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.13	W/m×K	323.42	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.13	W/m×K	328.48	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.12	W/m×K	333.46	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.12	W/m×K	338.50	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.12	W/m×K	343.51	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.12	W/m×K	348.54	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.12	W/m×K	353.36	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.12	W/m×K	358.57	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λliquid	0.12	W/m×K	363.52	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase

Datasets

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.15	873.3
100.00	303.15	868.1
100.00	308.15	862.6
100.00	313.15	857.3
100.00	318.15	851.9
100.00	323.15	846.7
100.00	328.15	841.4
100.00	333.15	835.8
100.00	338.15	830.3
100.00	343.15	824.8
100.00	348.15	819.1
100.00	353.15	813.5
100.00	363.15	799.9
100.00	373.15	788.5
100.00	383.15	776.9
100.00	393.15	765.1
1000.00	298.15	874.1
1000.00	303.15	868.9
1000.00	308.15	863.5
1000.00	313.15	858.2
1000.00	318.15	852.8
1000.00	323.15	847.4
1000.00	328.15	842.0
1000.00	333.15	837.0
1000.00	338.15	831.5
1000.00	343.15	825.9
1000.00	348.15	820.3
1000.00	353.15	814.7
1000.00	363.15	801.4
1000.00	373.15	790.1
1000.00	383.15	778.6
1000.00	393.15	766.9
2000.00	298.15	875.0
2000.00	303.15	869.8
2000.00	308.15	864.4
2000.00	313.15	859.1
2000.00	318.15	853.8
2000.00	323.15	848.4
2000.00	328.15	843.3
2000.00	333.15	838.1
2000.00	338.15	832.6
2000.00	343.15	827.1
2000.00	348.15	821.6
2000.00	353.15	816.1
2000.00	363.15	803.0
2000.00	373.15	791.7
2000.00	383.15	780.4
2000.00	393.15	768.8
3000.00	298.15	875.9
3000.00	303.15	870.7
3000.00	308.15	865.3
3000.00	313.15	860.1
3000.00	318.15	854.8
3000.00	323.15	849.5
3000.00	328.15	844.5
3000.00	333.15	839.2
3000.00	338.15	833.8
3000.00	343.15	828.3
3000.00	348.15	822.9
3000.00	353.15	817.4
3000.00	363.15	804.5
3000.00	373.15	793.4
3000.00	383.15	782.2
3000.00	393.15	770.8
3100.00	298.15	876.0
3100.00	303.15	870.7
3100.00	308.15	865.4
3100.00	313.15	860.2
3100.00	318.15	854.9
3100.00	323.15	849.6
3100.00	328.15	844.6
3100.00	333.15	839.3
3100.00	338.15	833.9
3100.00	343.15	828.4
3100.00	348.15	823.0
3100.00	353.15	817.5
3100.00	363.15	804.7
3100.00	373.15	793.6
3100.00	383.15	782.4
3100.00	393.15	771.0
5000.00	298.15	877.5
5000.00	303.15	872.4
5000.00	308.15	867.1
5000.00	313.15	861.9
5000.00	318.15	856.7
5000.00	323.15	851.7
5000.00	328.15	846.6
5000.00	333.15	841.2
5000.00	338.15	835.9
5000.00	343.15	830.7
5000.00	348.15	825.1
5000.00	353.15	819.8
5000.00	363.15	807.9
5000.00	373.15	796.8
5000.00	383.15	785.5
5000.00	393.15	774.5
10000.00	298.15	881.5
10000.00	303.15	876.5
10000.00	308.15	871.4
10000.00	313.15	866.3
10000.00	318.15	861.3
10000.00	323.15	856.7
10000.00	328.15	851.5
10000.00	333.15	846.3
10000.00	338.15	841.2
10000.00	343.15	836.2
10000.00	348.15	830.9
10000.00	353.15	825.7
10000.00	363.15	814.4
10000.00	373.15	804.0
10000.00	383.15	793.5
10000.00	393.15	783.1
15000.00	298.15	885.3
15000.00	303.15	880.4
15000.00	308.15	875.5
15000.00	313.15	870.5
15000.00	318.15	865.8
15000.00	323.15	861.1
15000.00	328.15	856.2
15000.00	333.15	851.1
15000.00	338.15	846.2
15000.00	343.15	841.4
15000.00	348.15	836.2
15000.00	353.15	831.2
15000.00	363.15	820.7
15000.00	373.15	810.8
15000.00	383.15	800.8
15000.00	393.15	790.9
20000.00	298.15	889.0
20000.00	303.15	884.1
20000.00	308.15	879.4
20000.00	313.15	874.5
20000.00	318.15	869.9
20000.00	323.15	865.4
20000.00	328.15	860.5
20000.00	333.15	855.6
20000.00	338.15	850.8
20000.00	343.15	846.1
20000.00	348.15	841.1
20000.00	353.15	836.3
20000.00	363.15	826.7
20000.00	373.15	817.2
20000.00	383.15	807.5
20000.00	393.15	798.0
25000.00	298.15	892.5
25000.00	303.15	887.8
25000.00	308.15	883.1
25000.00	313.15	878.4
25000.00	318.15	874.1
25000.00	323.15	869.4
25000.00	328.15	864.8
25000.00	333.15	860.1
25000.00	338.15	855.5
25000.00	343.15	850.1
25000.00	348.15	846.0
25000.00	353.15	841.4
25000.00	363.15	832.4
25000.00	373.15	823.1
25000.00	383.15	813.8
25000.00	393.15	804.6
30000.00	298.15	896.9
30000.00	303.15	892.3
30000.00	308.15	887.8
30000.00	313.15	883.2
30000.00	318.15	879.0
30000.00	323.15	874.5
30000.00	328.15	870.0
30000.00	333.15	865.4
30000.00	338.15	861.0
30000.00	343.15	855.7
30000.00	348.15	851.8
30000.00	353.15	847.4
30000.00	363.15	837.7
30000.00	373.15	828.7
30000.00	383.15	819.6
30000.00	393.15	810.7
35000.00	298.15	901.4
35000.00	303.15	896.9
35000.00	308.15	892.5
35000.00	313.15	888.1
35000.00	318.15	884.1
35000.00	323.15	879.7
35000.00	328.15	875.3
35000.00	333.15	870.8
35000.00	338.15	866.5
35000.00	343.15	861.8
35000.00	348.15	857.7
35000.00	353.15	853.4
35000.00	363.15	842.7
35000.00	373.15	834.0
35000.00	383.15	825.2
35000.00	393.15	816.6
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[149.10; 336.98]	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			2.28430e+01
Coefficient B			5.19040e-01
Coefficient C			-2.08000e-04
Coefficient D			3.10000e-09
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	149.10	J/mol×K	273.00	Calculated Property
Cp,gas	180.57	J/mol×K	353.78	Calculated Property
Cp,gas	209.37	J/mol×K	434.56	Calculated Property
Cp,gas	235.51	J/mol×K	515.33	Calculated Property
Cp,gas	258.99	J/mol×K	596.11	Calculated Property
Cp,gas	279.84	J/mol×K	676.89	Calculated Property
Cp,gas	298.05	J/mol×K	757.67	Calculated Property
Cp,gas	313.63	J/mol×K	838.44	Calculated Property
Cp,gas	326.61	J/mol×K	919.22	Calculated Property
Cp,gas	336.98	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[292.72; 418.65]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.49602e+01
Coefficient B			-3.54866e+03
Coefficient C			-5.08630e+01
Temperature range, min.			292.72
Temperature range, max.			418.65
Pvap	1.33	kPa	292.72	Calculated Property
Pvap	2.97	kPa	306.71	Calculated Property
Pvap	6.11	kPa	320.70	Calculated Property
Pvap	11.68	kPa	334.70	Calculated Property
Pvap	21.01	kPa	348.69	Calculated Property
Pvap	35.86	kPa	362.68	Calculated Property
Pvap	58.46	kPa	376.67	Calculated Property
Pvap	91.55	kPa	390.67	Calculated Property
Pvap	138.36	kPa	404.66	Calculated Property
Pvap	202.65	kPa	418.65	Calculated Property
Pvap	[8.60e-06; 3099.82]	kPa	[175.15; 571.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			6.66105e+01
Coefficient B			-6.89506e+03
Coefficient C			-7.55898e+00
Coefficient D			4.55093e-06
Coefficient E			0.00000e+00
Temperature range, min.			175.15
Temperature range, max.			571.00
Pvap	8.60e-06	kPa	175.15	Calculated Property
Pvap	4.62e-03	kPa	219.13	Calculated Property
Pvap	0.25	kPa	263.12	Calculated Property
Pvap	3.65	kPa	307.10	Calculated Property
Pvap	25.25	kPa	351.08	Calculated Property
Pvap	106.95	kPa	395.07	Calculated Property
Pvap	326.95	kPa	439.05	Calculated Property
Pvap	798.47	kPa	483.03	Calculated Property
Pvap	1664.77	kPa	527.02	Calculated Property
Pvap	3099.82	kPa	571.00	Calculated Property
Pvap	[0.13; 100.76]	kPa	[254.80; 394.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45797e+01
Coefficient B			-3.47562e+03
Coefficient C			-4.52840e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			254.80
Temperature range, max.			394.00
Pvap	0.13	kPa	254.80	Calculated Property
Pvap	0.42	kPa	270.27	Calculated Property
Pvap	1.13	kPa	285.73	Calculated Property
Pvap	2.71	kPa	301.20	Calculated Property
Pvap	5.89	kPa	316.67	Calculated Property
Pvap	11.74	kPa	332.13	Calculated Property
Pvap	21.82	kPa	347.60	Calculated Property
Pvap	38.19	kPa	363.07	Calculated Property
Pvap	63.45	kPa	378.53	Calculated Property
Pvap	100.76	kPa	394.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.01]	N/m	[175.15; 394.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.50942e-02
Coefficient B			-1.04500e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			175.15
Temperature range, max.			394.15
γ	0.04	N/m	175.15	Calculated Property
γ	0.03	N/m	199.48	Calculated Property
γ	0.03	N/m	223.82	Calculated Property
γ	0.03	N/m	248.15	Calculated Property
γ	0.03	N/m	272.48	Calculated Property
γ	0.02	N/m	296.82	Calculated Property
γ	0.02	N/m	321.15	Calculated Property
γ	0.02	N/m	345.48	Calculated Property
γ	0.02	N/m	369.82	Calculated Property
γ	0.01	N/m	394.15	Calculated Property

Similar Compounds

Find more compounds similar to Butanoic acid, ethyl ester.

Mixtures

• Carbon dioxide + Butanoic acid, ethyl ester
• Butanoic acid, ethyl ester + Ethane, 1,2-dichloro-
• Butane, 1,4-dichloro- + Butanoic acid, ethyl ester
• Butanoic acid, ethyl ester + Propane, 1,3-dichloro-
• Pentane, 1,5-dichloro- + Butanoic acid, ethyl ester
• Butanoic acid, ethyl ester + Hexane, 1,6-dichloro-
• 1,4-Butanediol + Butanoic acid, ethyl ester
• 1,6-DIBROMOHEXANE + Butanoic acid, ethyl ester
• Pentane, 1,5-dibromo- + Butanoic acid, ethyl ester
• Butanoic acid, ethyl ester + Butane, 1,4-dibromo-
• Propane, 1,3-dibromo- + Butanoic acid, ethyl ester
• Ethane, 1,2-dibromo- + Butanoic acid, ethyl ester
• Butanoic acid, ethyl ester + Water
• Butanoic acid + Butanoic acid, ethyl ester + Water
• 1-Hexene + Butanoic acid, ethyl ester
• n-Hexane + Butanoic acid, ethyl ester
• n-Hexane + 1-Hexene + Butanoic acid, ethyl ester
• Butanoic acid, ethyl ester + Heptane
• Butanoic acid, ethyl ester + Nonane
• 1-Propanol + Butanoic acid, ethyl ester

Find more mixtures with Butanoic acid, ethyl ester.

Sources

• KDB Vapor Pressure Data
• 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).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Cheméo Relay (1.0)
• Crippen Method
• Vapor liquid equilibria of carbon dioxide with isopropyl acetate, diethyl carbonate and ethyl butyrate at elevated pressures
• Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
• Temperature dependence of limiting activity coefficients, Henry's law constants, and related infinite dilution properties of C4-C6 isomeric n-alkyl ethanoates/ethyl n-alkanoates in water. Measurement, critical compilation, correlation, and recommended 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
• 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
• Acoustic and volumetric study of renewable oxygenated fuel additives at (298.15-323.15) K: Isomeric butanediols with ethylbutyrate
• Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
• Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
• Density, Viscosity, and Refractive Index Data for a Ternary System of Wine Congeners (Ethyl Butyrate + Diethyl Succinate + Isobutanol) in the Temperature Range from 288.15 to 323.15 K and at Atmospheric Pressure
• Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
• Densities, Viscosities, and Surface and Interfacial Tensions of the Ternary Mixture Water + Ethyl Butyrate + Methanol at 303.15 K.
• Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
• Vapor-Liquid Equilibrium Data of the Carbon Dioxide + Ethyl Butyrate and Carbon Dioxide + Propylene Carbonate Systems at Pressures from (1.00 to 13.00) MPa and Temperatures from (313.0 to 373.0) K
• Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
• Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
• Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
• Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
• Fast Determination of Binary Vapor Liquid Equilibrium of CO2-Based Mixtures at Elevated Pressures
• 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.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.