The separation of non-ideal mixtures using distillation can be an extremely complex process
and there continues to be a need to further improve these techniques. A new method which …

Based on the COSMO-SAC model, 1-ethyl-3-methylimidazolium acetate and 1-ethyl-3-
methylimidazolium p-toluenesulfonate were selected from 30 ILs as entrainers to investigate …

In order to obtain the vapour-liquid equilibrium (VLE) data of the binary and ternary systems
related to the separation of thioglycolic acid (TGA) by-products, in this research, the VLE …

In high purity thioglycolic acid production, isopropyl acetate is used to extract the acid from
intermediates, but it hydrolyzes and forms azeotrope with isopropanol under acidic …

Isopropyl acetate and isopropyl alcohol were azeotropic mixtures with a minimum boiling
point. To break the azeotrope of the above binary system and separate it, dibutyl ether and …

This study investigates the phase equilibrium behavior of the isopropyl acetate (IAC)-
isopropanol (IPA) azeotrope system at 101.3 kPa in the presence of three different …

Heterogeneous azeotropic distillation is a widely used technique in chemical industries for
the purification of alcohols from their aqueous mixtures. This study aims at exploring the …

The vapor–liquid equilibrium (VLE) data for the binary system isopropyl alcohol+ dimethyl
sulfoxide (DMSO), isopropyl acetate+ DMSO, and ternary system isopropyl alcohol+ …

Vapor-liquid equilibrium (VLE) data of isopropyl acetate+ isopropanol, isopropyl acetate+
isopropanol+ 1-hexyl-3-methylimidazolium acetate ([HMIM][Ac]), isopropyl acetate+ …

Contributing to extending the knowledge for the design and operation of biodiesel
production processes, isobaric PTxy vapor-liquid equilibria data of ethanol+ ethyl …