Chemical Properties of LACTIC ACID, ETHYL ESTER (CAS 97-64-3)

InChI

InChI=1S/C5H10O3/c1-3-8-5(7)4(2)6/h4,6H,3H2,1-2H3

InChI Key

LZCLXQDLBQLTDK-UHFFFAOYSA-N

Formula

C5H10O3

SMILES

CCOC(=O)C(C)O

Molecular Weight¹

118.13

CAS

97-64-3

Other Names

• (+-)-ethyl 2-hydroxypropionate
• (+-)-ethyl lactate
• (.+/-.)-Ethyl lactate
• (S)-(-)-ethyl lactate
• (dl) ethyl lactate
• 2-Hydroxypropanoic acid ethyl ester
• Actylol
• Acytol
• DL-ethyl 2-hydroxypropionate
• DL-ethyl lactate
• Ethyl 2-hydroxypropionate
• Ethyl ester of lactic acid
• Ethyl racemic-lactate
• Ethyl «alpha»-hydroxypropionate
• Ethylester kyseliny mlecne
• Eusolvan
• L-ethyl 2-hydroxypropanoate
• L-ethyl lactate
• L-lactic acid, ethyl ester
• Lactate d'ethyle
• NSC 8850
• Propanoic acid, 2-hydroxy-, ethyl ester
• Solactol
• UN 1192
• ethyl 2-hydroxypropanoate
• ethyl lactate

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• 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.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• 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.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.5909		Relay (1.0) Calculated Property
Tig	673.15	K	NCMS SOLV-DB
Tflash,cc	328.15	K	NCMS SOLV-DB
ΔfG°	-458.41	kJ/mol	Joback Calculated Property
ΔfH°gas	-653.86	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	13.64	kJ/mol	Joback Calculated Property
ΔvapH°	57.01	kJ/mol	Relay (1.0) Calculated Property
IE	10.19	eV	Relay (1.0) Calculated Property
log10WS	0.85		Relay (1.0) Calculated Property
logPoct/wat	0.308		NCMS SOLV-DB
McVol	94.620	ml/mol	McGowan Calculated Property
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	3940.66	kPa	Joback Calculated Property
Inp	[764.00; 836.00]
Inp	803.00		NIST
Inp	806.00		NIST
Inp	787.00		NIST
Inp	787.00		NIST
Inp	787.00		NIST
Inp	797.00		NIST
Inp	798.00		NIST
Inp	799.00		NIST
Inp	801.00		NIST
Inp	813.00		NIST
Inp	815.00		NIST
Inp	815.00		NIST
Inp	826.00		NIST
Inp	815.00		NIST
Inp	789.00		NIST
Inp	836.00		NIST
Inp	Outlier 764.00		NIST
Inp	821.00		NIST
Inp	832.00		NIST
Inp	815.00		NIST
Inp	797.00		NIST
Inp	821.00		NIST
Inp	798.00		NIST
Inp	788.00		NIST
Inp	798.00		NIST
Inp	813.00		NIST
Inp	801.00		NIST
Inp	803.00		NIST
Inp	803.00		NIST
Inp	Outlier 764.00		NIST
Inp	821.00		NIST
Inp	801.00		NIST
Ip	[1309.00; 1372.00]
Ip	Outlier 1309.00		NIST
Ip	Outlier 1312.00		NIST
Ip	1340.00		NIST
Ip	1352.00		NIST
Ip	1353.00		NIST
Ip	1342.00		NIST
Ip	1329.00		NIST
Ip	1333.00		NIST
Ip	1333.00		NIST
Ip	1345.00		NIST
Ip	1347.00		NIST
Ip	1347.00		NIST
Ip	1325.00		NIST
Ip	1341.00		NIST
Ip	1339.00		NIST
Ip	1316.00		NIST
Ip	1317.00		NIST
Ip	1353.00		NIST
Ip	1353.00		NIST
Ip	1347.00		NIST
Ip	1331.00		NIST
Ip	1353.00		NIST
Ip	1353.00		NIST
Ip	1339.00		NIST
Ip	1353.00		NIST
Ip	1372.00		NIST
Ip	1356.00		NIST
Ip	1362.00		NIST
Ip	1338.00		NIST
Ip	1334.00		NIST
Ip	1334.00		NIST
Ip	1334.00		NIST
Ip	1349.00		NIST
Ip	1371.00		NIST
Ip	1349.00		NIST
Ip	1349.00		NIST
Ip	1356.00		NIST
Ip	1362.00		NIST
Ip	1331.00		NIST
Ip	1337.00		NIST
Ip	Outlier 1312.00		NIST
Ip	1367.00		NIST
Ip	1355.00		NIST
Ip	1341.00		NIST
Ip	1334.00		NIST
Ip	1339.00		NIST
Ip	1353.00		NIST
Ip	1354.00		NIST
Ip	1353.00		NIST
Ip	1356.00		NIST
Ip	1348.00		NIST
Ip	1363.00		NIST
Ip	1353.00		NIST
Ip	1363.00		NIST
Ip	1348.00		NIST
Ip	1348.00		NIST
Ip	1321.00		NIST
Ip	1363.00		NIST
Ip	1341.00		NIST
Ip	1349.00		NIST
Ip	1364.00		NIST
Ip	1348.00		NIST
Ip	1334.00		NIST
Ip	1338.00		NIST
Ip	1353.00		NIST
Ip	1338.00		NIST
Ip	1371.00		NIST
Ip	1339.00		NIST
Ip	1330.00		NIST
Ip	1356.00		NIST
Ip	1358.00		NIST
Ip	Outlier 1312.00		NIST
Ip	1342.00		NIST
Ip	1347.00		NIST
Ip	1316.00		NIST
Ip	1353.00		NIST
Ip	Outlier 1309.00		NIST
Ip	1340.00		NIST
Tboil	427.03	K	NCMS SOLV-DB
Tc	609.68	K	Relay (1.0) Calculated Property
Tfus	247.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Vc	0.368	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	[0.0014940; 0.0027000]	Pa×s	[298.15; 318.15]
η	0.0023980	Pa×s	298.15	Densities and Viscosities for Binary Mixtures of Ethyl Lactate with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
η	0.0027000	Pa×s	298.15	NCMS SOLV-DB
η	0.0018630	Pa×s	308.15	Densities and Viscosities for Binary Mixtures of Ethyl Lactate with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
η	0.0014940	Pa×s	318.15	Densities and Viscosities for Binary Mixtures of Ethyl Lactate with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
ΔvapH	[49.20; 51.30]	kJ/mol	[367.00; 375.50]
ΔvapH	49.20	kJ/mol	367.00	NIST
ΔvapH	51.30	kJ/mol	375.50	NIST
Pvap	[0.04; 0.69]	kPa	[274.60; 311.30]
Pvap	0.04	kPa	274.60	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.05	kPa	276.60	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.07	kPa	279.60	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.07	kPa	281.40	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.09	kPa	283.60	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.10	kPa	284.60	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.10	kPa	285.80	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.13	kPa	287.60	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.13	kPa	287.60	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.13	kPa	288.40	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.15	kPa	290.20	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.15	kPa	290.30	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.16	kPa	291.10	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.16	kPa	293.15	NCMS SOLV-DB
Pvap	0.19	kPa	293.50	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.24	kPa	296.40	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.28	kPa	298.50	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.37	kPa	301.50	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.38	kPa	302.50	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.45	kPa	304.50	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.48	kPa	305.30	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.53	kPa	307.20	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.58	kPa	308.20	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.63	kPa	310.10	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.63	kPa	310.10	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
Pvap	0.69	kPa	311.30	Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
n0	[1.41050; 1.41500]		[293.15; 298.15]
n0	1.41290		293.15	Vapor liquid equilibria and excess volumes of the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate at 101.325 kPa
n0	1.41050		298.15	Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + Ethyl Lactate and Methyl Acetate + Ethyl Lactate
n0	1.41057		298.15	Isobaric Vapor Liquid Equilibrium of 3-Methyl-1-butanol + Ethyl Lactate and 1-Pentanol + Ethyl Lactate at (13.0 and 101.3) kPa
n0	1.41500		298.15	NCMS SOLV-DB
ρl	[983.94; 1050.05]	kg/m3	[278.15; 338.15]
ρl	1050.05	kg/m3	278.15	Thermophysical Properties of Lactates
ρl	1047.37	kg/m3	280.65	Thermophysical Properties of Lactates
ρl	1044.68	kg/m3	283.15	Thermophysical Properties of Lactates
ρl	1041.96	kg/m3	285.65	Thermophysical Properties of Lactates
ρl	1039.26	kg/m3	288.15	Thermophysical Properties of Lactates
ρl	1039.28	kg/m3	288.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1036.54	kg/m3	290.65	Thermophysical Properties of Lactates
ρl	1033.84	kg/m3	293.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1033.82	kg/m3	293.15	Thermophysical Properties of Lactates
ρl	1031.09	kg/m3	295.65	Thermophysical Properties of Lactates
ρl	1028.08	kg/m3	298.15	Vapor-liquid equilibria of binary and ternary mixtures containing ethyl lactate and effect of ethyl lactate as entrainer
ρl	1028.39	kg/m3	298.15	Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
ρl	1028.08	kg/m3	298.15	Separation Effects of Renewable Solvent Ethyl Lactate on the Vapor Liquid Equilibria of the Methanol + Dimethyl Carbonate Azeotropic System
ρl	1028.37	kg/m3	298.15	Self-aggregation of liquids from biomass in aqueous solution
ρl	1028.39	kg/m3	298.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1028.37	kg/m3	298.15	Thermophysical Properties of Lactates
ρl	1025.63	kg/m3	300.65	Thermophysical Properties of Lactates
ρl	1022.89	kg/m3	303.15	Thermophysical Properties of Lactates
ρl	1022.92	kg/m3	303.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1020.15	kg/m3	305.65	Thermophysical Properties of Lactates
ρl	1017.40	kg/m3	308.15	Thermophysical Properties of Lactates
ρl	1017.42	kg/m3	308.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1014.64	kg/m3	310.65	Thermophysical Properties of Lactates
ρl	1011.90	kg/m3	313.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1011.88	kg/m3	313.15	Thermophysical Properties of Lactates
ρl	1009.12	kg/m3	315.65	Thermophysical Properties of Lactates
ρl	1006.36	kg/m3	318.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	1006.34	kg/m3	318.15	Thermophysical Properties of Lactates
ρl	1003.57	kg/m3	320.65	Thermophysical Properties of Lactates
ρl	1000.78	kg/m3	323.15	Thermophysical Properties of Lactates
ρl	1000.79	kg/m3	323.15	Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
ρl	997.99	kg/m3	325.65	Thermophysical Properties of Lactates
ρl	995.19	kg/m3	328.15	Thermophysical Properties of Lactates
ρl	992.39	kg/m3	330.65	Thermophysical Properties of Lactates
ρl	989.58	kg/m3	333.15	Thermophysical Properties of Lactates
ρl	986.76	kg/m3	335.65	Thermophysical Properties of Lactates
ρl	983.94	kg/m3	338.15	Thermophysical Properties of Lactates
csound,fluid	[1206.90; 1261.10]	m/s	[303.15; 318.15]
csound,fluid	1261.10	m/s	303.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1243.80	m/s	308.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1224.80	m/s	313.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
csound,fluid	1206.90	m/s	318.15	Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
γ	0.03	N/m	298.15	NCMS SOLV-DB

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	1045.06
288.15	100.00	1039.64
293.15	100.00	1034.25
298.15	100.00	1028.78
303.15	100.00	1023.32
308.15	100.00	1017.84
313.15	100.00	1012.33
318.15	100.00	1006.72
323.15	100.00	1001.23
328.15	100.00	995.54
333.15	100.00	989.91
338.15	100.00	984.3
283.15	2500.00	1046.77
288.15	2500.00	1041.39
293.15	2500.00	1036.05
298.15	2500.00	1030.66
303.15	2500.00	1025.21
308.15	2500.00	1019.82
313.15	2500.00	1014.31
318.15	2500.00	1008.86
323.15	2500.00	1003.36
328.15	2500.00	997.8
333.15	2500.00	992.19
338.15	2500.00	986.71
283.15	5000.00	1048.51
288.15	5000.00	1043.21
293.15	5000.00	1037.86
298.15	5000.00	1032.56
303.15	5000.00	1027.24
308.15	5000.00	1021.87
313.15	5000.00	1016.42
318.15	5000.00	1011.01
323.15	5000.00	1005.56
328.15	5000.00	1000.11
333.15	5000.00	994.55
338.15	5000.00	989.18
283.15	7500.00	1050.24
288.15	7500.00	1044.99
293.15	7500.00	1039.7
298.15	7500.00	1034.43
303.15	7500.00	1029.11
308.15	7500.00	1023.84
313.15	7500.00	1018.41
318.15	7500.00	1013.1
323.15	7500.00	1007.68
328.15	7500.00	1002.34
333.15	7500.00	996.87
338.15	7500.00	991.49
283.15	10000.00	1051.88
288.15	10000.00	1046.74
293.15	10000.00	1041.5
298.15	10000.00	1036.23
303.15	10000.00	1031.0
308.15	10000.00	1025.7
313.15	10000.00	1020.39
318.15	10000.00	1015.13
323.15	10000.00	1009.78
328.15	10000.00	1004.46
333.15	10000.00	999.06
338.15	10000.00	993.65
283.15	20000.00	1058.39
288.15	20000.00	1053.28
293.15	20000.00	1048.3
298.15	20000.00	1043.21
303.15	20000.00	1038.26
308.15	20000.00	1033.08
313.15	20000.00	1027.93
318.15	20000.00	1022.87
323.15	20000.00	1017.76
328.15	20000.00	1012.65
333.15	20000.00	1007.62
338.15	20000.00	1002.34
283.15	30000.00	1064.45
288.15	30000.00	1059.46
293.15	30000.00	1054.58
298.15	30000.00	1049.76
303.15	30000.00	1044.91
308.15	30000.00	1039.92
313.15	30000.00	1034.97
318.15	30000.00	1030.04
323.15	30000.00	1025.13
328.15	30000.00	1020.17
333.15	30000.00	1015.4
338.15	30000.00	1010.27
283.15	40000.00	1070.13
288.15	40000.00	1065.24
293.15	40000.00	1060.54
298.15	40000.00	1055.69
303.15	40000.00	1051.19
308.15	40000.00	1046.28
313.15	40000.00	1041.52
318.15	40000.00	1036.74
323.15	40000.00	1031.99
328.15	40000.00	1027.16
333.15	40000.00	1022.5
338.15	40000.00	1017.75
283.15	50000.00	1075.5
288.15	50000.00	1070.74
293.15	50000.00	1066.26
298.15	50000.00	1061.53
303.15	50000.00	1056.95
308.15	50000.00	1052.19
313.15	50000.00	1047.69
318.15	50000.00	1042.96
323.15	50000.00	1038.42
328.15	50000.00	1033.75
333.15	50000.00	1029.24
338.15	50000.00	1024.55
283.15	60000.00	1080.55
288.15	60000.00	1076.04
293.15	60000.00	1071.55
298.15	60000.00	1066.96
303.15	60000.00	1062.52
308.15	60000.00	1057.98
313.15	60000.00	1053.46
318.15	60000.00	1048.96
323.15	60000.00	1044.49
328.15	60000.00	1039.99
333.15	60000.00	1035.71
338.15	60000.00	1031.04
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	1028.45
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
308.00	10000.00	1029.1
308.00	20000.00	1034.4
308.00	30000.00	1042.6
323.00	10000.00	1009.5
323.00	20000.00	1016.8
323.00	30000.00	1023.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[140.07; 304.60]	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			2.73610e+01
Coefficient B			4.63940e-01
Coefficient C			-1.87200e-04
Coefficient D			5.00000e-10
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	140.07	J/mol×K	273.00	Calculated Property
Cp,gas	168.09	J/mol×K	353.78	Calculated Property
Cp,gas	193.66	J/mol×K	434.56	Calculated Property
Cp,gas	216.80	J/mol×K	515.33	Calculated Property
Cp,gas	237.51	J/mol×K	596.11	Calculated Property
Cp,gas	255.78	J/mol×K	676.89	Calculated Property
Cp,gas	271.63	J/mol×K	757.67	Calculated Property
Cp,gas	285.04	J/mol×K	838.44	Calculated Property
Cp,gas	296.04	J/mol×K	919.22	Calculated Property
Cp,gas	304.60	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[318.50; 450.93]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.89834e+01
Coefficient B			-6.73793e+03
Coefficient C			4.18990e+01
Temperature range, min.			318.50
Temperature range, max.			450.93
Pvap	1.33	kPa	318.50	Calculated Property
Pvap	2.78	kPa	333.21	Calculated Property
Pvap	5.47	kPa	347.93	Calculated Property
Pvap	10.25	kPa	362.64	Calculated Property
Pvap	18.40	kPa	377.36	Calculated Property
Pvap	31.73	kPa	392.07	Calculated Property
Pvap	52.79	kPa	406.79	Calculated Property
Pvap	85.05	kPa	421.50	Calculated Property
Pvap	133.05	kPa	436.22	Calculated Property
Pvap	202.65	kPa	450.93	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.02]	N/m	[247.15; 428.15]	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			5.75706e-02
Coefficient B			-9.83000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			247.15
Temperature range, max.			428.15
γ	0.03	N/m	247.15	Calculated Property
γ	0.03	N/m	267.26	Calculated Property
γ	0.03	N/m	287.37	Calculated Property
γ	0.03	N/m	307.48	Calculated Property
γ	0.03	N/m	327.59	Calculated Property
γ	0.02	N/m	347.71	Calculated Property
γ	0.02	N/m	367.82	Calculated Property
γ	0.02	N/m	387.93	Calculated Property
γ	0.02	N/m	408.04	Calculated Property
γ	0.02	N/m	428.15	Calculated Property

Similar Compounds

Find more compounds similar to LACTIC ACID, ETHYL ESTER.

Mixtures

• Thymol + LACTIC ACID, ETHYL ESTER + Water
• caffeine + LACTIC ACID, ETHYL ESTER + Water
• LACTIC ACID, ETHYL ESTER + Vanillic acid + Water
• 2-Propenoic acid, 3-(4-hydroxy-3-methoxyphenyl)- + LACTIC ACID, ETHYL ESTER + Water
• Acetic acid, methyl ester + LACTIC ACID, ETHYL ESTER
• LACTIC ACID, ETHYL ESTER + Methyl Alcohol
• Acetic acid, methyl ester + LACTIC ACID, ETHYL ESTER + Methyl Alcohol
• Aniline + LACTIC ACID, ETHYL ESTER
• Aniline, N-methyl- + LACTIC ACID, ETHYL ESTER
• Benzenamine, N-ethyl- + LACTIC ACID, ETHYL ESTER
• Ethanol + LACTIC ACID, ETHYL ESTER
• 1-Propanol + LACTIC ACID, ETHYL ESTER
• 1-Butanol + LACTIC ACID, ETHYL ESTER
• Propylene Glycol + LACTIC ACID, ETHYL ESTER
• 1,3-Propanediol + LACTIC ACID, ETHYL ESTER
• LACTIC ACID, ETHYL ESTER + Tetrahydrofuran
• 2,5,8,11,14-Pentaoxapentadecane + LACTIC ACID, ETHYL ESTER
• Ethanol, 2-methoxy- + LACTIC ACID, ETHYL ESTER
• LACTIC ACID, ETHYL ESTER + Ethanol, 2-ethoxy-
• Ethanol, 2-butoxy- + LACTIC ACID, ETHYL ESTER

Find more mixtures with LACTIC ACID, ETHYL ESTER.

Sources

• 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).
• 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).
• Cheméo Relay (1.0)
• Crippen Method
• Vapor liquid equilibria and excess volumes of the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate at 101.325 kPa
• Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
• High pressure phase behavior of the binary system (ethyl lactate + carbon dioxide)
• Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
• Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
• Vapor-liquid equilibria of binary and ternary mixtures containing ethyl lactate and effect of ethyl lactate as entrainer
• Partitioning of amino acids in the novel biphasic systems based on environmentally friendly ethyl lactate
• Solubility of high-value compounds in ethyl lactate: Measurements and modelling
• The pqT behaviour of the lactate family
• Self-aggregation of liquids from biomass in aqueous solution
• Comparative studies of intermolecular interaction of aromatic amines with ethyl lactate at different temperatures
• Thermodynamic behaviour of alkyl lactate-alkanol systems
• Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
• Thermophysical Properties of Lactates
• Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
• Separation Effects of Renewable Solvent Ethyl Lactate on the Vapor Liquid Equilibria of the Methanol + Dimethyl Carbonate Azeotropic System
• Density Measurements of CO2-Expanded Liquids
• Vapor-Liquid Equilibrium of Ethyl Lactate Highly Diluted in Ethanol-Water Mixtures at 101.3 kPa. Experimental Measurements and Thermodynamic Modeling Using Semiempirical Models
• Vapor-Liquid Equilibria in the Systems Ethyl Lactate + Ethanol and Ethyl Lactate + Water
• Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + Ethyl Lactate and Methyl Acetate + Ethyl Lactate
• Isobaric Vapor Liquid Equilibrium of 3-Methyl-1-butanol + Ethyl Lactate and 1-Pentanol + Ethyl Lactate at (13.0 and 101.3) kPa
• High-Pressure Phase Behavior of Methyl Lactate and Ethyl Lactate in Supercritical Carbon Dioxide
• Solubility of CO2 in Ethyl Lactate and Modeling of the Phase Behavior of the CO2 + Ethyl Lactate Mixture
• Densities and Viscosities for Binary Mixtures of Ethyl Lactate with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
• Joback Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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