The selectivity of a membrane for CO 2 /CH 4 separation is critical for purification of natural gas, landfill gas, and biogas since CO 2 is the major impurity present in gas mixtures while CH 4 is the major hydrocarbon constituent. The performance of poly(ether-block-amide) (Pebax 2533) membrane and its silver-incorporated form were investigated with respect to their permeation properties for these two gases. Thin-film composite (TFC) membranes of Pebax were prepared by dissolving 20 g of the polymer in 80 mL of 3:7 volumetric ratio of m-cresol/isopropanol solvent mixture, followed by casting on polyvinylidene fluoride (PVDF) ultrafiltration substrate. Silver incorporation was carried out by loading silver tetrafluoroborate (AgBF 4 ) at 36% of the Pebax polymer weight in the same dope solution. Membranes were characterized by Fourier transform infrared (FTIR), X-ray diffraction (XRD), and scanning electron microscopy (SEM) to study intermolecular interactions, crystalline nature, and surface and cross-sectional morphologies, respectively. At a feed pressure of 1 MPa, Pebax gave a CO 2 permeance of 32.8 GPU at a CO 2 /CH 4 selectivity of 15.3, whereas Ag-Pebax exhibited an enhanced selectivity of 36.2, even though its permeance was reduced to 12.1 GPU. The Ag-Pebax membrane was further upscaled as a spiral-wound module of 0.20 m 2 effective area to test its commercial feasibility.