The efficient separation of CO 2 from other light gases has received growing attentions due to its importance in reducing greenhouse gas emissions and applications in gas purification. In this work, we developed a series of composite membranes composed of ether-functionalized pyridinium-based ionic liquids ([E n Py][NTf 2 ]) and cellulose acetate (CA) polymer matrices to improve CO 2 separation performance. CA + [E n Py][NTf 2 ] and CA + [C n Py][NTf 2 ] composite membranes were fabricated by a casting method. The CO 2 , N 2 and CH 4 permeabilities of the CA + IL composite membranes were measured, and the CO 2 /N 2 and CO 2 /CH 4 permselectivities were further calculated. The results showed that the CA + 40 wt% [E 1 Py] [NTf 2 ] composite membrane exhibits approximately a seven-fold increase in CO 2 permeability with CO 2 / N 2 and CO 2 /CH 4 permselectivities of 32 and 24, respectively. The characterization results showed that the mechanical properties and thermal stabilities of the CA + [E 1 Py][NTf 2 ] composite membranes are affected by both plasticizing effect and affinity of the ILs for the gases, which also lead to the changes in the CO 2 /N 2 and CO 2 /CH 4 permselectivities. Compared with membranes containing the nonfunctionalized analogues [C n Py][NTf 2 ], the addition of [E n Py][NTf 2 ] improves the ideal permselectivities of CA + IL composite membranes, whereas it decreases slightly the gas permeabilities. Scheme 1 The chemical structures of (a) [E n Py][NTf 2 ], (b) [C n Py][NTf 2 ] and (c) cellulose acetate. This journal is