The current process to purify contaminated natural gas reserves employs a highly energy-intensive amine scrubbing technology. To satisfy the growing demand for natural gas coupled with the tight regulations on CO₂ emissions, researchers worldwide are investigating the use of polymeric membranes for acid gas removal from natural gas streams, to reduce the energy consumption and carbon emission of the nowadays used technology. Placing a polymeric membrane unit at the upstream of the amine scrubbing column reduces the energy consumption during the regeneration process of saturated amines. Hence, the preparation of polymeric membranes in form of hollow fibers is a key step towards their industrial implementation for natural gas processing. The following study demonstrates the potential separation performance of 6FDA-Durene/6FDA-CARDO (5000:5000) in an integrally skinned defect-free asymmetric hollow fiber geometry. The initial screening studies of the membrane shows good pure-gas performance as it exhibits CO₂/CH₄ selectivity coefficients around 28 and CO₂ permeance between 310 and 350 GPU. Feed pressures of up to 900 psig and stage cuts ranging from 5% to 20% were tested for a quaternary sweet mixed-gas feed to assess the membrane performance under operating conditions that mimic those in industrial settings. Mixed-gas permeance of all gases, and CO₂/CH₄ selectivity remain somewhat constant as the feed pressure increases up to 900 psig. Both mixed-gas CO₂ permeance and CO₂/CH₄ selectivity decline as the stage cut increases. As expected, as CO₂ recovery is maximized, CO₂ purity is minimized and CH₄ loss increases with increasing stage cut. As a result of the trade-off between recovery and purity, the data and analyses reported herein can provide insights into the limitations that certain operating parameters can pose on CO₂ separation performance with similar polymeric hollow fiber membranes.