Commonly used solvents for separation of aromatics from aliphatics using liquid–liquid
extraction are reviewed in terms of their physical properties and separation performance …

The experimental (liquid+ liquid) equilibrium (LLE) properties for two ternary systems
containing (N-formylmorpholine+ benzene+ n-hexane),(sulfolane+ benzene+ n-hexane) …

A novel method based on unimolecular quantum mechanical calculations has been used to
predict the multicomponent liquid− liquid equilibria (LLE). The recently developed CO …

Extractive distillation (ED) processes are widely used for the separation of aromatic and non-
aromatic hydrocarbons. Approximate boiling points of components and azeotropes in the …

In this work, the separation of benzene from aliphatic hydrocarbons (hexane, or heptane) is
investigated by extraction with 1-ethyl-3-methylpyridinium ethylsulphate ionic …

Liquid+ liquid equilibrium (LLE) results for the ternary mixtures of (solvent+ aromatic
hydrocarbon+ alkane) at different temperatures from (298.15 to 313.15) K are reported …

Liquid− liquid equilibrium (LLE) data for four ternary systems comprising cyclohexane+(
benzene, toluene, ethylbenzene, or cumene)+ sulfolane have been measured at 303.15 K …

The ionic liquid 1-ethyl-3-methylpyridinium ethylsulfate,[EMpy][ESO4], was studied for the
separation of benzene from aliphatic hydrocarbons (octane or nonane) by solvent extraction …

Application of genetic algorithm (GA), which leads to globally optimal binary interaction
parameters from multi-component liquid–liquid equilibrium data, has been recently …

Benzene is a known carcinogen, and is desired to be removed from the gasoline additive for
environmental reason. A benzene removal process from the additive, reformate of catalytic …