In
recent years,
the fight against climate change and the mitigation
of the impact of fluorinated gases (F-gases) on the atmosphere is
a global concern. Development of technologies that help to efficiently
separate and recycle hydrofluorocarbons (HFCs) at the end of the refrigeration
and air conditioning equipment life is a priority. The technological
development is important to stimulate the F-gas capture, specifically
difluoromethane (R-32) and 1,1,1,2-tetrafluoroethane (R-134a), due
to their high global warming potential. In this work, the COSMO-RS
method is used to analyze the solute–solvent interactions and
to determine Henry’s constants of R-32 and R-134a in more than
600 ionic liquids. The three most performant ionic liquids were selected
on the basis of COSMO-RS calculations, and F-gas absorption equilibrium
isotherms were measured using gravimetric and volumetric methods.
Experimental results are in good agreement with COSMO-RS predictions,
with the ionic liquid tributyl(ethyl)phosphonium diethyl phosphate,
[P2444][C2C2PO4], being
the salt presenting the highest absorption capacities in molar and
mass units compared to salts previously tested. The other two ionic
liquids selected, trihexyltetradecylphosphonium glycinate, [P66614][C2NO2], and trihexyl(tetradecyl)phosphonium
2-cyano-pyrrole, [P66614][CNPyr], may be competitive as
far as their absorption capacities are concerned. Future works will
be guided on evaluating the performance of these ionic liquids at
an industrial scale by means of process simulations, in order to elucidate
the role in process efficiency of other relevant absorbent properties
such as viscosity, molar weight, or specific heat