In
a challenge to develop a process that meets the criteria of
being “green” in the extraction of aromatics, deep eutectic
solvents (DESs) are currently gaining importance as separation media.
This work reports a phosphonium-based DES for the dearomatization
of model diesel components at 25 °C and p =
1 bar. The DES comprising a hydrogen bond acceptor, namely, methyltriphenylphosphonium
bromide, along with ethylene glycol as a hydrogen bond donor, was
formulated with a molar ratio of 1:4. The DES was then used to extract
benzene from representative diesel fuel components, a mixture of n-decane, n-dodecane, and n-hexadecane. Ternary liquid–liquid equilibrium experiments
were then performed at ambient conditions with different benzene concentrations
with the feed varying from 2 to 20 wt %. An absence of the solvent
in the raffinate phase was found in all the tie lines, suggesting
limited solvent recovery costs. Besides, it was also found that all
three ternary systems show type I phase activity with positive slopes,
indicating that the desired removal of benzene requires a small amount
of solvent. The quantum chemical-based COSMO-SAC model was then used
to predict the tie lines giving an average root mean square deviation
value of 1.2%. The mechanism of the extraction process was also extensively
studied with the help of quantitative 1H NMR and Fourier
transform infrared spectroscopy. Higher benzene extraction efficiencies
were observed due to the strong noncovalent interaction between the
DES and benzene.