Liquid–liquid equilibrium data for water + formic acid + solvent (butyl acetate, ethyl acetate, and isoamyl alcohol) at T = 291.15 K

2016 ◽  
Vol 415 ◽  
pp. 51-57 ◽  
Author(s):  
M. Timedjeghdine ◽  
A. Hasseine ◽  
H. Binous ◽  
O. Bacha ◽  
M. Attarakih
Keyword(s):  
Formic Acid ◽  
Ethyl Acetate ◽  
Butyl Acetate ◽  
Isoamyl Alcohol ◽  
Liquid Equilibrium ◽  
Equilibrium Data

Vapour-liquid equilibria of pyridine + acetate mixtures at 101.325 kPa

1991 ◽  
Vol 56 (12) ◽  
pp. 2773-2785 ◽  
Author(s):  
Antonio Correa ◽  
Antonio Blanco ◽  
Jose Tojo ◽  
Jose M. Correa ◽  
Alberto Arce
Keyword(s):  
Ethyl Acetate ◽  
Binary Mixtures ◽  
Butyl Acetate ◽  
Propyl Acetate ◽  
Liquid Equilibrium ◽  
Pyridine Acetate ◽  
Equilibrium Data

Experimental vapour-liquid equilibrium data for the binary mixtures ethyl acetate + pyridine, n-propyl acetate + pyridine and n-butyl acetate + pyridine have been determined at 101.325 kPa. The Wilson, NRTL, LEMF, UNIQUAC and Effective UNIQUAC equations have been fitted to the data, which have also been used to establish UNIFAC parameters for interaction between CCOO and PYRIDINE groups.

Liquid–liquid equilibrium data for the systems {LTTM+benzene+hexane} and {LTTM+ethyl acetate+hexane} at different temperatures and atmospheric pressure

2013 ◽  
Vol 360 ◽  
pp. 54-62 ◽  
Author(s):  
Agustin S.B. Gonzalez ◽  
María Francisco ◽  
Guillermo Jimeno ◽  
Sara Lago García de Dios ◽  
Maaike C. Kroon
Keyword(s):  
Ethyl Acetate ◽  
Atmospheric Pressure ◽  
Liquid Equilibrium ◽  
Equilibrium Data ◽  
Different Temperatures

Isobaric Vapor-Liquid Equilibria of Hexamethyl Disiloxane + Ethyl Acetate System at Normal Pressure

2011 ◽  
Vol 396-398 ◽  
pp. 968-972
Author(s):  
Wen Lin Zhang ◽  
Nan Meng ◽  
Ru Yi Sun ◽  
Chun Li Li
Keyword(s):  
Experimental Data ◽  
Ethyl Acetate ◽  
Normal Pressure ◽  
Liquid Equilibrium ◽  
Vapor Liquid Equilibrium ◽  
Equilibrium Data ◽  
Vle Data ◽  
Vapor Liquid Equilibria ◽  
Ethyl Acetate System ◽  
Vapor Liquid

Vapor-liquid equilibrium data of hexamethyl disiloxane + ethyl acetate system at 101.3kPa were measured by using double circulating vapor-liquid equilibrium still. The thermodynamic consistency of the VLE data was examined by Herrington method. Experimental data was correlated by NRTL and UNIQUAC parameter models. Both of the models satisfactorily correlated with the VLE data. The result showed that the NRTL model was the most suitable one to represent experimental data satisfactorily and the system had a minimum temperature azeotrope at 350.31 K and the mole azeotropic composition was 0.0330.

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