Hydrofluorocarbon
refrigerants are being phased out over the next
two decades due to concerns about high global warming potential. In
order to separate refrigerant mixtures that form azeotropes, new technologies
will be required. Currently, fractional distillation is unable to
efficiently separate azeotropic refrigerant mixtures. Extractive distillation
using an ionic liquid as the entrainer offers a solution. Vapor–liquid
equilibria data for refrigerants difluoromethane (HFC-32), pentafluoroethane
(HFC-125), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,1-trifluoroethane
(HFC-143a), chlorodifluoromethane (HCFC-22), propane (HC-290), and
isobutane (HC-600a) and ionic liquid 1-butyl-3-methylimidazolium hexafluorophosphate
([C4C1im][PF6]) was regressed using
the Peng–Robinson equation of state with the van der Waals
1-parameter mixing rule and Boston–Mathias nonideal correction.
Process flow diagrams using ASPEN simulations were prepared for demonstrating
how multicomponent mixtures of these refrigerants can be separated.
Opportunities for measuring and modeling the solubility of new refrigerants
in ionic liquids are discussed, and challenges remain for effectively
separating some azeotropic refrigerant mixtures containing hydrofluorocarbons
and hydrocarbons.