Poly(ionic liquids) (PolyILs) with excellent mechanical stability and strong CO
2 affinity have emerged as an exciting platform for membrane carbon capture. This study aims to systematically evaluate the effect of fluorine content on structure characteristics and CO
2/gas separation properties of novel anionic PolyIL membranes. First, ionic liquid of 1-ethyl-3-methylimidazolium 3-acryloxypropylsulfonyl(-perfluoroalkyl-[sulfonimide]) with 3, 5 or 9 fluorine groups (or EF3, EF5 and EF9, respectively) were prepared via Sulfur(VI) Fluoride Exchange (SuFEx) click chemistry. These ILs can be cross-linked with 2 mol% of poly(ethylene glycol) diacrylate (PEGDA) to obtain mechanically stable PolyILs (ie. PolyEF) membrane for CO
2 separation application. Characterization of these PolyEF membranes is systematically investigated via FTIR, DSC, TGA, XRD, gas sorption and permeation apparatus. For example, increasing the flourine content between PolyEF3 and PolyEF9 increases the glass transition temperature from -39 to -12
oC, and increases the counterion d-spacing from 0.43 to 0.48 nm, respectively, and enhances CO
2 permeability from 17 to 35 Barrer, and CO
2/N
2 from 10 to 17, respectively. Interestingly, free EF ionic liquid loaded PolyEFs exhibit reduction in T
g but enhancement in counterion d-spacing and simultaneous improvement in gas permeability and CO
2/gas selectivity for all samples. For instance, addition of 57wt% of EF3 in PolyEF3 decreases the T
g from -39 to -67
oC, respectively, but enhances CO
2 permeability from 17 to 260 Barrer, and CO
2/N
2 from 10 to 28, respectively. Direct correlation between polymer transition temperature and gas transport properties can be satisfactorily described by the Vogel-Fulcher-Tammann (VFT) equation. This systematic study highlights the attractive CO
2/gas separation properties of polyanionic liquid membranes, providing insight into the design of polyILs membranes for practical CO
2 capture applications.
