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

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Physical Properties

Property	Value	Unit	Source
ω	0.4610		KDB
Δ_cH°_liquid	[-3545.00; -3539.00]	kJ/mol
Δ_cH°_liquid	-3545.00	kJ/mol	NIST
Δ_cH°_liquid	-3539.00	kJ/mol	NIST
μ	1.80	debye	KDB
Δ_fG°	-310.73	kJ/mol	Joback Calculated Property
Δ_fH°_gas	-485.00 ± 1.00	kJ/mol	NIST
Δ_fH°_liquid	-528.40 ± 0.79	kJ/mol	NIST
Δ_fusH°	15.67	kJ/mol	Joback Calculated Property
Δ_vapH°	[36.90; 44.00]	kJ/mol
Δ_vapH°	42.71	kJ/mol	NIST
Δ_vapH°	44.00 ± 1.00	kJ/mol	NIST
Δ_vapH°	43.40	kJ/mol	NIST
Δ_vapH°	43.70 ± 1.30	kJ/mol	NIST
Δ_vapH°	42.68 ± 0.10	kJ/mol	NIST
Δ_vapH°	42.00 ± 0.10	kJ/mol	NIST
Δ_vapH°	42.00 ± 0.10	kJ/mol	NIST
Δ_vapH°	Outlier 36.90 ± 0.04	kJ/mol	NIST
IE	9.82	eV	Relay (1.0) Calculated Property
log₁₀WS	-1.28		Aq. Solubility Prediction
logP_oct/wat	1.350		Crippen Calculated Property
McVol	102.840	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
P_c	[3060.00; 3064.00]	kPa
P_c	3060.00	kPa	KDB
P_c	3064.00 ± 151.99	kPa	NIST
ρ_c	276.46 ± 9.99	kg/m³	NIST
I_np	[760.00; 818.00]
I_np	784.00		NIST
I_np	780.20		NIST
I_np	802.00		NIST
I_np	783.00		NIST
I_np	792.00		NIST
I_np	796.00		NIST
I_np	806.00		NIST
I_np	782.00		NIST
I_np	781.00		NIST
I_np	Outlier 760.00		NIST
I_np	782.00		NIST
I_np	778.00		NIST
I_np	782.00		NIST
I_np	788.00		NIST
I_np	784.00		NIST
I_np	788.00		NIST
I_np	775.00		NIST
I_np	785.00		NIST
I_np	793.00		NIST
I_np	789.00		NIST
I_np	791.00		NIST
I_np	792.00		NIST
I_np	789.00		NIST
I_np	789.00		NIST
I_np	790.00		NIST
I_np	793.00		NIST
I_np	790.00		NIST
I_np	Outlier 764.00		NIST
I_np	799.00		NIST
I_np	798.00		NIST
I_np	Outlier 764.00		NIST
I_np	790.00		NIST
I_np	791.00		NIST
I_np	778.00		NIST
I_np	779.00		NIST
I_np	803.00		NIST
I_np	801.00		NIST
I_np	803.00		NIST
I_np	788.00		NIST
I_np	778.00		NIST
I_np	776.00		NIST
I_np	804.00		NIST
I_np	802.00		NIST
I_np	798.00		NIST
I_np	802.00		NIST
I_np	802.00		NIST
I_np	808.00		NIST
I_np	808.00		NIST
I_np	800.00		NIST
I_np	805.00		NIST
I_np	802.00		NIST
I_np	794.00		NIST
I_np	805.00		NIST
I_np	801.00		NIST
I_np	800.00		NIST
I_np	797.00		NIST
I_np	781.00		NIST
I_np	800.00		NIST
I_np	781.00		NIST
I_np	781.00		NIST
I_np	800.00		NIST
I_np	805.00		NIST
I_np	785.00		NIST
I_np	781.00		NIST
I_np	781.00		NIST
I_np	806.00		NIST
I_np	802.20		NIST
I_np	790.00		NIST
I_np	802.00		NIST
I_np	802.00		NIST
I_np	803.00		NIST
I_np	800.00		NIST
I_np	802.00		NIST
I_np	802.00		NIST
I_np	802.00		NIST
I_np	802.00		NIST
I_np	804.00		NIST
I_np	804.00		NIST
I_np	774.00		NIST
I_np	791.00		NIST
I_np	782.00		NIST
I_np	779.00		NIST
I_np	800.00		NIST
I_np	785.00		NIST
I_np	787.00		NIST
I_np	804.00		NIST
I_np	802.00		NIST
I_np	778.00		NIST
I_np	778.00		NIST
I_np	778.00		NIST
I_np	778.00		NIST
I_np	Outlier 818.00		NIST
I_np	801.00		NIST
I_np	805.00		NIST
I_np	806.00		NIST
I_np	803.00		NIST
I_np	807.00		NIST
I_np	798.00		NIST
I_np	770.00		NIST
I_np	798.00		NIST
I_np	805.00		NIST
I_np	805.00		NIST
I_np	805.00		NIST
I_np	801.00		NIST
I_np	803.00		NIST
I_np	798.00		NIST
I_np	800.00		NIST
I_np	803.00		NIST
I_np	803.00		NIST
I_np	802.00		NIST
I_np	801.00		NIST
I_np	802.00		NIST
I_np	792.00		NIST
I_np	803.00		NIST
I_np	804.00		NIST
I_np	784.00		NIST
I_np	801.00		NIST
I_np	803.00		NIST
I_np	774.00		NIST
I_np	807.00		NIST
I_np	802.00		NIST
I_np	800.00		NIST
I_np	783.00		NIST
I_np	800.00		NIST
I_np	800.00		NIST
I_np	800.00		NIST
I_np	803.00		NIST
I_np	800.00		NIST
I_np	800.00		NIST
I_np	806.00		NIST
I_np	778.00		NIST
I_np	804.00		NIST
I_np	788.00		NIST
I_np	798.00		NIST
I_np	788.00		NIST
I_np	797.00		NIST
I_np	799.00		NIST
I_np	783.00		NIST
I_np	803.00		NIST
I_np	804.00		NIST
I_np	780.00		NIST
I_np	812.00		NIST
I_np	802.00		NIST
I_np	780.00		NIST
I_np	785.00		NIST
I_np	790.00		NIST
I_np	799.00		NIST
I_np	784.00		NIST
I_np	802.00		NIST
I_np	804.00		NIST
I_np	804.00		NIST
I_np	799.00		NIST
I_np	782.00		NIST
I_np	791.00		NIST
I_np	780.00		NIST
I_np	784.00		NIST
I_np	785.00		NIST
I_np	781.00		NIST
I_np	788.00		NIST
I_np	789.00		NIST
I_np	785.00		NIST
I_np	785.00		NIST
I_np	782.00		NIST
I_np	794.00		NIST
I_np	796.00		NIST
I_np	787.00		NIST
I_np	774.00		NIST
I_np	770.00		NIST
I_np	807.00		NIST
I_np	801.00		NIST
I_np	803.00		NIST
I_np	798.00		NIST
I_np	801.00		NIST
I_np	770.00		NIST
I_np	804.00		NIST
I_np	800.00		NIST
I_np	770.00		NIST
I_np	802.00		NIST
I_np	803.00		NIST
I_np	804.00		NIST
I_np	796.00		NIST
I_np	800.00		NIST
I_np	802.00		NIST
I_np	800.00		NIST
I_np	803.00		NIST
I_np	800.00		NIST
I_np	778.00		NIST
I_np	799.00		NIST
I_np	778.00		NIST
I_np	770.00		NIST
I_np	770.00		NIST
I_np	774.00		NIST
I_np	803.00		NIST
I_np	774.00		NIST
I_np	774.00		NIST
I_np	804.00		NIST
I_np	792.00		NIST
I_np	804.00		NIST
I_np	802.00		NIST
I_np	787.00		NIST
I_np	787.00		NIST
I_np	800.00		NIST
I_np	800.00		NIST
I_np	798.00		NIST
I_np	784.00		NIST
I_np	806.00		NIST
I_np	806.00		NIST
I_np	771.00		NIST
I_np	789.00		NIST
I_np	802.00		NIST
I_np	771.00		NIST
I_np	806.00		NIST
I_np	800.00		NIST
I_np	774.00		NIST
I_np	771.00		NIST
I_np	781.00		NIST
I_np	800.00		NIST
I_np	788.00		NIST
I_np	804.00		NIST
I_np	800.00		NIST
I_np	800.00		NIST
I_np	785.00		NIST
I_np	774.00		NIST
I_np	793.00		NIST
I_np	796.00		NIST
I_np	784.00		NIST
I_np	784.00		NIST
I_np	780.00		NIST
I_np	804.00		NIST
I_np	804.00		NIST
I_np	804.00		NIST
I_np	801.00		NIST
I_np	802.00		NIST
I_np	805.00		NIST
I_np	780.00		NIST
I_np	789.00		NIST
I_np	788.00		NIST
I_np	780.00		NIST
I_np	783.00		NIST
I_np	784.00		NIST
I_np	784.00		NIST
I_np	787.00		NIST
I_np	799.00		NIST
I_np	778.00		NIST
I_np	784.00		NIST
I_np	796.00		NIST
I_np	782.00		NIST
I_np	788.00		NIST
I_np	774.00		NIST
I_np	798.00		NIST
I_np	770.00		NIST
I_np	800.00		NIST
I_np	792.00		NIST
I_np	806.00		NIST
I_np	785.00		NIST
I_np	801.00		NIST
I_np	787.00		NIST
I_np	804.00		NIST
I_np	803.00		NIST
I_np	805.00		NIST
I_np	789.00		NIST
I_np	Outlier 764.00		NIST
I	[990.00; 1081.00]
I	1025.00		NIST
I	1051.00		NIST
I	1054.00		NIST
I	Outlier 1008.00		NIST
I	1032.00		NIST
I	1045.00		NIST
I	1032.00		NIST
I	1058.00		NIST
I	1057.00		NIST
I	1010.00		NIST
I	1044.00		NIST
I	1044.00		NIST
I	1040.00		NIST
I	1026.00		NIST
I	1042.00		NIST
I	1043.00		NIST
I	1045.00		NIST
I	Outlier 1005.00		NIST
I	1028.00		NIST
I	1036.00		NIST
I	1048.00		NIST
I	1035.00		NIST
I	1035.00		NIST
I	1041.00		NIST
I	1049.00		NIST
I	1061.00		NIST
I	1041.00		NIST
I	1033.00		NIST
I	1039.00		NIST
I	1027.00		NIST
I	1052.00		NIST
I	1048.00		NIST
I	1048.00		NIST
I	Outlier 1067.00		NIST
I	Outlier 1073.00		NIST
I	Outlier 1069.00		NIST
I	Outlier 1000.00		NIST
I	1037.00		NIST
I	1029.00		NIST
I	1052.00		NIST
I	1022.00		NIST
I	1022.00		NIST
I	Outlier 1001.00		NIST
I	1023.00		NIST
I	1041.00		NIST
I	1023.00		NIST
I	1030.00		NIST
I	1021.00		NIST
I	1036.00		NIST
I	1037.00		NIST
I	1021.00		NIST
I	1041.00		NIST
I	1057.00		NIST
I	1025.00		NIST
I	1020.00		NIST
I	1024.00		NIST
I	1025.00		NIST
I	1040.40		NIST
I	1039.00		NIST
I	1039.00		NIST
I	1021.00		NIST
I	1023.00		NIST
I	1044.00		NIST
I	1037.00		NIST
I	1040.00		NIST
I	1032.00		NIST
I	1025.00		NIST
I	1031.00		NIST
I	1057.00		NIST
I	1025.00		NIST
I	1032.00		NIST
I	1040.00		NIST
I	1040.00		NIST
I	1046.00		NIST
I	1040.00		NIST
I	1055.00		NIST
I	1034.00		NIST
I	1034.00		NIST
I	1032.00		NIST
I	1044.00		NIST
I	1028.00		NIST
I	1028.00		NIST
I	1056.00		NIST
I	1021.00		NIST
I	1034.00		NIST
I	1042.00		NIST
I	1056.00		NIST
I	1022.00		NIST
I	1047.00		NIST
I	1037.00		NIST
I	1038.00		NIST
I	1041.00		NIST
I	1041.00		NIST
I	1025.00		NIST
I	1043.00		NIST
I	1044.00		NIST
I	1041.00		NIST
I	1037.00		NIST
I	1035.00		NIST
I	1028.00		NIST
I	1048.00		NIST
I	1038.00		NIST
I	1021.00		NIST
I	1033.00		NIST
I	1038.00		NIST
I	1026.00		NIST
I	1040.00		NIST
I	1032.00		NIST
I	1028.00		NIST
I	1029.00		NIST
I	1037.00		NIST
I	1014.00		NIST
I	1042.00		NIST
I	1042.00		NIST
I	1036.00		NIST
I	1054.00		NIST
I	1015.00		NIST
I	1035.00		NIST
I	1046.00		NIST
I	1031.00		NIST
I	1031.00		NIST
I	1038.00		NIST
I	1050.00		NIST
I	1013.00		NIST
I	Outlier 1066.00		NIST
I	1030.00		NIST
I	1025.00		NIST
I	1047.00		NIST
I	1035.00		NIST
I	1057.00		NIST
I	1028.00		NIST
I	1044.00		NIST
I	1038.00		NIST
I	1032.00		NIST
I	1050.00		NIST
I	1036.00		NIST
I	1022.00		NIST
I	1036.00		NIST
I	1040.00		NIST
I	1036.00		NIST
I	1031.00		NIST
I	1025.00		NIST
I	1043.00		NIST
I	1048.00		NIST
I	1030.00		NIST
I	1023.00		NIST
I	1025.00		NIST
I	1031.00		NIST
I	1035.00		NIST
I	1043.00		NIST
I	1033.00		NIST
I	1025.00		NIST
I	1043.00		NIST
I	1033.00		NIST
I	1052.00		NIST
I	1043.00		NIST
I	1043.00		NIST
I	1029.00		NIST
I	1009.00		NIST
I	1025.00		NIST
I	1010.00		NIST
I	1018.00		NIST
I	1025.00		NIST
I	1030.90		NIST
I	1025.00		NIST
I	1060.00		NIST
I	1028.00		NIST
I	1035.00		NIST
I	1035.00		NIST
I	1035.00		NIST
I	1037.00		NIST
I	1035.00		NIST
I	1037.00		NIST
I	1035.00		NIST
I	1037.00		NIST
I	1035.00		NIST
I	1037.00		NIST
I	1028.00		NIST
I	1030.00		NIST
I	1039.00		NIST
I	1036.00		NIST
I	Outlier 1075.00		NIST
I	1060.00		NIST
I	1032.00		NIST
I	1039.00		NIST
I	1033.00		NIST
I	1033.00		NIST
I	Outlier 1002.00		NIST
I	1023.00		NIST
I	1023.00		NIST
I	1050.00		NIST
I	1026.00		NIST
I	Outlier 1076.00		NIST
I	Outlier 1078.00		NIST
I	Outlier 1079.00		NIST
I	1035.00		NIST
I	1040.00		NIST
I	1046.00		NIST
I	1031.00		NIST
I	1022.00		NIST
I	1043.00		NIST
I	1026.00		NIST
I	1043.00		NIST
I	1029.00		NIST
I	1022.00		NIST
I	1037.00		NIST
I	1037.00		NIST
I	1044.00		NIST
I	1028.00		NIST
I	Outlier 990.00		NIST
I	Outlier 1081.00		NIST
I	1043.00		NIST
I	1030.00		NIST
I	1040.00		NIST
I	1028.00		NIST
I	1045.00		NIST
I	1037.00		NIST
I	1042.00		NIST
I	1028.00		NIST
I	1043.00		NIST
I	1032.00		NIST
I	1046.00		NIST
I	1024.00		NIST
I	1043.00		NIST
I	1042.00		NIST
I	1033.00		NIST
I	1022.00		NIST
I	Outlier 1071.00		NIST
I	1056.00		NIST
I	1028.00		NIST
I	1025.00		NIST
I	1047.00		NIST
I	1025.00		NIST
I	1031.00		NIST
I	1047.00		NIST
I	1047.00		NIST
I	1023.00		NIST
I	1044.00		NIST
I	1023.00		NIST
I	1023.00		NIST
I	1046.00		NIST
I	1028.00		NIST
I	1025.00		NIST
I	1028.00		NIST
I	1041.00		NIST
I	1039.00		NIST
I	Outlier 1067.00		NIST
I	1029.00		NIST
I	1023.00		NIST
I	1036.00		NIST
I	1025.00		NIST
I	1037.00		NIST
I	1057.00		NIST
T_boil	[387.95; 394.90]	K
T_boil	394.55	K	Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
T_boil	393.78	K	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
T_boil	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
T_boil	394.13	K	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
T_boil	394.60	K	KDB
T_boil	394.18 ± 0.40	K	NIST
T_boil	393.20	K	NIST
T_boil	393.00	K	NIST
T_boil	394.60	K	NIST
T_boil	393.95 ± 0.50	K	NIST
T_boil	392.15 ± 1.00	K	NIST
T_boil	Outlier 388.65 ± 5.00	K	NIST
T_boil	393.15 ± 1.00	K	NIST
T_boil	394.55 ± 1.00	K	NIST
T_boil	393.15 ± 1.00	K	NIST
T_boil	393.00 ± 1.00	K	NIST
T_boil	394.70 ± 0.50	K	NIST
T_boil	394.15 ± 1.00	K	NIST
T_boil	394.50 ± 2.00	K	NIST
T_boil	393.10 ± 1.00	K	NIST
T_boil	394.70 ± 0.50	K	NIST
T_boil	394.35 ± 0.40	K	NIST
T_boil	393.40 ± 0.50	K	NIST
T_boil	393.30 ± 0.50	K	NIST
T_boil	393.20 ± 0.50	K	NIST
T_boil	393.35 ± 0.50	K	NIST
T_boil	393.45 ± 1.00	K	NIST
T_boil	391.65 ± 1.00	K	NIST
T_boil	392.15 ± 2.00	K	NIST
T_boil	394.90 ± 0.30	K	NIST
T_boil	393.15 ± 1.00	K	NIST
T_boil	393.40 ± 1.00	K	NIST
T_boil	394.65 ± 1.00	K	NIST
T_boil	394.40 ± 1.50	K	NIST
T_boil	391.90 ± 1.00	K	NIST
T_boil	393.15 ± 1.00	K	NIST
T_boil	392.15 ± 1.00	K	NIST
T_boil	393.75 ± 1.00	K	NIST
T_boil	393.80 ± 0.50	K	NIST
T_boil	394.10 ± 1.50	K	NIST
T_boil	394.40 ± 1.00	K	NIST
T_boil	394.25 ± 1.00	K	NIST
T_boil	392.15 ± 1.00	K	NIST
T_boil	Outlier 387.95 ± 1.00	K	NIST
T_boil	Outlier 387.95 ± 1.00	K	NIST
T_c	[558.70; 577.50]	K
T_c	569.98	K	Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
T_c	566.00	K	KDB
T_c	568.80 ± 0.60	K	NIST
T_c	558.70 ± 10.00	K	NIST
T_c	566.00 ± 2.00	K	NIST
T_c	577.50 ± 6.00	K	NIST
T_fus	[170.65; 178.90]	K
T_fus	175.00	K	KDB
T_fus	178.90	K	Aq. Solubility Prediction
T_fus	175.30 ± 0.30	K	NIST
T_fus	170.65 ± 0.70	K	NIST
V_c	0.421	m³/kmol	KDB
Z_c	0.2737480		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	[220.10; 229.70]	J/mol×K	[290.00; 298.15]
C_p,liquid	229.70	J/mol×K	290.00	NIST
C_p,liquid	220.10	J/mol×K	297.20	NIST
C_p,liquid	220.10	J/mol×K	297.20	NIST
C_p,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
Δ_vapH	[35.47; 48.30]	kJ/mol	[323.00; 394.60]

Δ_vapH	42.10 ± 0.10	kJ/mol	323.00	NIST
Δ_vapH	41.80	kJ/mol	324.00	NIST
Δ_vapH	48.30	kJ/mol	333.50	NIST
Δ_vapH	40.20	kJ/mol	362.50	NIST
Δ_vapH	39.40	kJ/mol	382.50	NIST
Δ_vapH	35.47	kJ/mol	394.60	NIST
P_vap	[22.50; 101.31]	kPa	[348.97; 394.13]

P_vap	22.50	kPa	348.97	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	25.00	kPa	351.83	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	27.50	kPa	354.39	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	30.03	kPa	356.76	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	32.51	kPa	359.00	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	35.02	kPa	361.08	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	35.41	kPa	361.56	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	37.52	kPa	363.04	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	40.04	kPa	364.86	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	40.41	kPa	365.24	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	42.51	kPa	366.66	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	45.03	kPa	368.24	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	47.51	kPa	369.87	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	50.00	kPa	371.33	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	50.01	kPa	371.44	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	52.51	kPa	372.86	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	54.40	kPa	373.83	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	55.03	kPa	374.31	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	57.52	kPa	375.67	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	58.98	kPa	376.28	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	60.00	kPa	376.95	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	60.00	kPa	377.21	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	60.00	kPa	377.23	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	65.03	kPa	379.48	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	65.75	kPa	379.65	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	67.53	kPa	380.68	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	70.00	kPa	381.82	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	72.52	kPa	382.96	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	75.01	kPa	384.07	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	77.20	kPa	384.82	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	77.51	kPa	385.13	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	79.99	kPa	386.19	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	82.52	kPa	387.22	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	84.14	kPa	387.65	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	85.02	kPa	388.21	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	87.54	kPa	389.17	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	89.98	kPa	390.12	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	90.84	kPa	390.23	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	92.53	kPa	391.06	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	94.92	kPa	391.95	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	97.45	kPa	392.83	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	100.40	kPa	393.63	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	100.01	kPa	393.71	Solvent Effects on Vapor Liquid Equilibria of the Binary System 1-Hexene + n-Hexane
P_vap	101.30	kPa	393.78	Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
P_vap	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
ρ_l	[847.00; 884.16]	kg/m³	[288.15; 323.15]

ρ_l	884.16	kg/m³	288.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρ_l	879.00	kg/m³	293.00	KDB
ρ_l	878.90	kg/m³	293.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρ_l	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
ρ_l	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
ρ_l	873.62	kg/m³	298.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρ_l	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
ρ_l	868.33	kg/m³	303.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρ_l	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.
ρ_l	863.02	kg/m³	308.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρ_l	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
ρ_l	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
ρ_l	857.70	kg/m³	313.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρ_l	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
ρ_l	852.36	kg/m³	318.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρ_l	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
ρ_l	847.00	kg/m³	323.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
λ	[0.12; 0.15]	W/m×K	[268.57; 363.52]

λ	0.15	W/m×K	268.57	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	273.61	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	278.63	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	283.58	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	288.65	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	293.58	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.14	W/m×K	298.53	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	303.56	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	308.67	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	313.49	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	318.61	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	323.42	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.13	W/m×K	328.48	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	333.46	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	338.50	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	343.51	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	348.54	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	353.36	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	0.12	W/m×K	358.57	Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
λ	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
C_p,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 C_p,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

C_p,gas	149.10	J/mol×K	273.00	Calculated Property
C_p,gas	180.57	J/mol×K	353.78	Calculated Property
C_p,gas	209.37	J/mol×K	434.56	Calculated Property
C_p,gas	235.51	J/mol×K	515.33	Calculated Property
C_p,gas	258.99	J/mol×K	596.11	Calculated Property
C_p,gas	279.84	J/mol×K	676.89	Calculated Property
C_p,gas	298.05	J/mol×K	757.67	Calculated Property
C_p,gas	313.63	J/mol×K	838.44	Calculated Property
C_p,gas	326.61	J/mol×K	919.22	Calculated Property
C_p,gas	336.98	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.65]	kPa	[292.72; 418.65]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is P_vap 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

P_vap	1.33	kPa	292.72	Calculated Property
P_vap	2.97	kPa	306.71	Calculated Property
P_vap	6.11	kPa	320.70	Calculated Property
P_vap	11.68	kPa	334.70	Calculated Property
P_vap	21.01	kPa	348.69	Calculated Property
P_vap	35.86	kPa	362.68	Calculated Property
P_vap	58.46	kPa	376.67	Calculated Property
P_vap	91.55	kPa	390.67	Calculated Property
P_vap	138.36	kPa	404.66	Calculated Property
P_vap	202.65	kPa	418.65	Calculated Property
P_vap	[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 P_vap 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

P_vap	8.60e-06	kPa	175.15	Calculated Property
P_vap	4.62e-03	kPa	219.13	Calculated Property
P_vap	0.25	kPa	263.12	Calculated Property
P_vap	3.65	kPa	307.10	Calculated Property
P_vap	25.25	kPa	351.08	Calculated Property
P_vap	106.95	kPa	395.07	Calculated Property
P_vap	326.95	kPa	439.05	Calculated Property
P_vap	798.47	kPa	483.03	Calculated Property
P_vap	1664.77	kPa	527.02	Calculated Property
P_vap	3099.82	kPa	571.00	Calculated Property
P_vap	[0.13; 100.76]	kPa	[254.80; 394.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap 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

P_vap	0.13	kPa	254.80	Calculated Property
P_vap	0.42	kPa	270.27	Calculated Property
P_vap	1.13	kPa	285.73	Calculated Property
P_vap	2.71	kPa	301.20	Calculated Property
P_vap	5.89	kPa	316.67	Calculated Property
P_vap	11.74	kPa	332.13	Calculated Property
P_vap	21.82	kPa	347.60	Calculated Property
P_vap	38.19	kPa	363.07	Calculated Property
P_vap	63.45	kPa	378.53	Calculated Property
P_vap	100.76	kPa	394.00	Calculated Property

Similar Compounds

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Mixtures

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Sources

KDB Vapor Pressure Data
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
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure

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