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

Separation of aromatics from aliphatics is a challenging process because of the close range
of their boiling points and the formation of several combinations of azeotropes. Until now, no …

The separation of aromatics from fluid catalytic cracking (FCC) diesel is of great significance
for environmental protection. The extraction ability of 1-methyl-2-pyrrolidinone (NMP) …

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

Abstract (Liquid+ liquid) extraction of ethylbenzene from n-octane by using
tetrabutylammonium bromide-based deep eutectic solvents (DESs) containing pyridine …

Solubility and tie-line data for the (water+ phenol+ 1-octanol),(water+ phenol+
cyclohexanone),(water+ phenol+ 2-ethyl-1-hexanol), and (water+ phenol+ isobutyl acetate) …

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 …

Biodiesel has many advantages because it is a biodegradable, nontoxic fuel and its
production results in less particulate matter. For this reason it has been studied in many …

Liquid–liquid equilibrium (LLE) data for the ternary system (cottonseed biodiesel+ glycerol+
ethanol) have been determined at T= 293.15, 313.15 and 333.15 K and atmospheric …

Contradiction between the desulfurization and loss of octane number (ON) for fluid catalytic
cracking (FCC) naphtha is the long-term problem of clean gasoline production. Moreover …