TY - JOUR
T1 - Vapor-Liquid Equilibrium of Ethyl Lactate Highly Diluted in Ethanol-Water Mixtures at 101.3 kPa. Experimental Measurements and Thermodynamic Modeling Using Semiempirical Models
AU - Puentes, Cristian
AU - Joulia, Xavier
AU - Paricaud, Patrice
AU - Giampaoli, Pierre
AU - Athès, Violaine
AU - Esteban-Decloux, Martine
N1 - Publisher Copyright:
© 2018 American Chemical Society.
PY - 2018/2/8
Y1 - 2018/2/8
N2 - A thermodynamic study of the vapor-liquid equilibrium for the ternary system ethyl lactate-ethanol-water was performed at 101.3 kPa and infinite dilution regarding ethyl lactate, for boiling temperatures ranging from (352.3 to 370.0) K. The experimental measurements were carried out with a recirculation still and the equilibrium compositions of ethyl lactate were determined by gas chromatography. The volatility of ethyl lactate decreases when the ethanol content in the liquid phase is increased. The investigated system was correctly correlated by the NRTL and UNIQUAC models, with an average absolute relative deviation below 10%. The comparison with the results obtained from interaction parameters fitted to experimental data of the binary systems ethyl lactate-ethanol and ethyl lactate-water at 101.3 kPa, proves that the parameters calculated in this work give a better description of the ethyl lactate volatility, a key parameter in distillation, at low concentrations. These latter parameters are therefore recommended for process simulation and optimization in alcoholic beverages production.
AB - A thermodynamic study of the vapor-liquid equilibrium for the ternary system ethyl lactate-ethanol-water was performed at 101.3 kPa and infinite dilution regarding ethyl lactate, for boiling temperatures ranging from (352.3 to 370.0) K. The experimental measurements were carried out with a recirculation still and the equilibrium compositions of ethyl lactate were determined by gas chromatography. The volatility of ethyl lactate decreases when the ethanol content in the liquid phase is increased. The investigated system was correctly correlated by the NRTL and UNIQUAC models, with an average absolute relative deviation below 10%. The comparison with the results obtained from interaction parameters fitted to experimental data of the binary systems ethyl lactate-ethanol and ethyl lactate-water at 101.3 kPa, proves that the parameters calculated in this work give a better description of the ethyl lactate volatility, a key parameter in distillation, at low concentrations. These latter parameters are therefore recommended for process simulation and optimization in alcoholic beverages production.
U2 - 10.1021/acs.jced.7b00770
DO - 10.1021/acs.jced.7b00770
M3 - Article
AN - SCOPUS:85042046465
SN - 0021-9568
VL - 63
SP - 365
EP - 379
JO - Journal of Chemical and Engineering Data
JF - Journal of Chemical and Engineering Data
IS - 2
ER -