The
sustainable separation process for the recovery of acetonitrile
from wastewater is essential to achieve the circular economy and environmental
protection. In this work, we demonstrate systematically a methodology
to develop an energy-efficient extractive distillation process for
separating the acetonitrile and water azeotrope. First, the separation
performances of candidate entrainers, i.e., ionic liquids (ILs) and
ethylene glycol (EG), were determined using the residue curve maps.
Second, the boundaries of decision variables for optimization procedures
were obtained via the sensitivity analysis, and the nonsorting genetic
algorithm (NSGA-II) was applied to get the optimal operating parameters
of conventional and heat-integrated schemes using EG and three ILs.
Third, three indicators including the total annual cost, gas emissions,
and thermodynamic efficiency were used to evaluate the economic, environmental,
and energy efficiency performances of conventional and intensified
schemes. Using the conventional EG process as a basis, the heat-integrated
scheme using [EMIM][OAC] shows the best performance as it gives the
reductions of 26.3% and 22.1% in the total annual cost and gas emissions,
respectively, and an absolute increase of 0.44 in the second-law efficiency.