This work investigates the separation performance of a commercial carbonized polyimide hollow fiber membrane module for post-combustion CO 2 capture applications. In particular, the resilience to water and sulfur and nitrogen oxides (SO x and NO x ) as gas impurities was examined. The membrane exhibited a CO 2 permeance of 660 Gas Permeance Units (GPU) and a CO 2 / N 2 permselectivity of 20 at 50 °C when the permeate side was controlled at 0.2 bar absolute pressure. With an increase in water vapor in the feed stream, this CO 2 permeance decreased slightly, while the CO 2 /N 2 selectivity increased slightly, due to the combination of competitive sorption and concentration polarization. The water vapor permeance was high, which made accurate measurement difficult due to the concentration polarization but a value of 1090 ± 200 GPU was recorded. The membrane was then examined under three mixed gas conditions (i.e. SO 2 /CO 2 /O 2 /N 2 , NO/CO 2 /N 2 , and NO/NO 2 /N 2 ) for a time frame of 30 days. The permeances of SO 2 , O 2 , NO, and NO 2 were 650 ± 50, 155 ± 5, 125 ± 10, and 70 ± 5 GPU at 30 °C, respectively. All of these minor components had a marginal impact on the membrane separation performance during the testing period, indicating strong commercial potential. The higher permeance of SO 2 and NO relative to nitrogen meant that these penetrants were concentrated in the permeate stream, which might lead to issues with downstream corrosion in a humid environment. Conversely, the permeance of NO 2 was low.