Liquid-liquid equilibrium for the ternary system 1,3-dioxolane-ethyl acetate-ethylene glycol at T = 291.15, 301.15, and 311.15 K

1987 ◽  
Vol 32 (3) ◽  
pp. 354-356
Author(s):  
Bianca Bubani ◽  
Romolo Francesconi
Keyword(s):  
Ternary System ◽  
Ethylene Glycol ◽  
Ethyl Acetate ◽  
Liquid Equilibrium

Vapor−Liquid Equilibrium of the Ternary System Ethyl Acetate + Hexane + Acetone at 101.32 kPa

2002 ◽  
Vol 47 (4) ◽  
pp. 849-854 ◽  
Author(s):  
Jhoany Acosta ◽  
Alberto Arce ◽  
José Martínez-Ageitos ◽  
Eva Rodil ◽  
Ana Soto
Keyword(s):  
Ternary System ◽  
Ethyl Acetate ◽  
Liquid Equilibrium ◽  
Vapor Liquid Equilibrium ◽  
Vapor Liquid

Liquid–Liquid Equilibrium for Ternary System n-Butanol + n-Hexane + Ethylene Glycol at 298.15–323.15 K

2017 ◽  
Vol 63 (1) ◽  
pp. 57-62
Author(s):  
Qingsong Li ◽  
Midong Shi ◽  
Liping Wang ◽  
Gaoyin He ◽  
Fan Gan
Keyword(s):  
Ternary System ◽  
Ethylene Glycol ◽  
Liquid Equilibrium

Vapour-liquid equilibrium in the ternary system cyclohexane-acetic acid-propionic acid

1989 ◽  
Vol 54 (11) ◽  
pp. 2840-2847 ◽  
Author(s):  
Ivona Malijevská ◽  
Alena Maštalková ◽  
Marie Sýsová
Keyword(s):  
Acetic Acid ◽  
Ternary System ◽  
Propionic Acid ◽  
Activity Coefficients ◽  
Error Propagation ◽  
Analytical Techniques ◽  
Liquid Equilibrium ◽  
Consistency Test ◽  
Propagation Law ◽  
Equilibrium Data

Isobaric equilibrium data (P = 101.3 kPa) for the system cyclohexane-acetic acid-propionic acid have been measured by two different analytical techniques. Activity coefficients calculated by simultaneous solving of equations for the chemical and phase equilibria were subjected to a consistency test based on inaccuracies determined from the error propagation law, and were correlated by Wilson’s equation. The activity coefficients measured were compared with those calculated from binary vapour-liquid equilibrium data and with values predicted by the UNIFAC method.

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