Article ID Journal Published Year Pages File Type
202337 Fluid Phase Equilibria 2014 7 Pages PDF
Abstract

•Solubility data for acetic acid–n-propanol–n-propyl acetate–water system at 293.15 K and 303.15 K.•LLE tie-lines and critical states of LLE for quaternary system have been determined.•The data for two ternary sub-systems with miscibility gap are presented.•The LLE data have been calculated by using UNIFAC and NRTL models.

Solubility and liquid–liquid equilibrium (LLE) for the quaternary system acetic acid–n-propanol–n-propyl acetate–water and for the ternary sub-systems acetic acid–n-propyl acetate–water and n-propanol–n-propyl acetate–water were studied at 293.15 K and 303.15 K and atmospheric pressure. Binodal surfaces and curves, tie-lines, and compositions of critical LLE points were determined. Experimental LLE data were correlated by UNIFAC and NRTL models.

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Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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