The poisoning of K 2 O, KCl, and K 2 SO 4 on commercial V 2 O 5 −WO 3 /TiO 2 catalysts used for selective catalytic reduction (SCR) of NO x by NH 3 was investigated, respectively. The degree of inactivation observed in these catalysts poisoned with different forms of potassium follows K 2 O ≈ KCl > K 2 SO 4 . At 350 °C, the NO x conversion of the K 2 SO 4 poisoning catalyst (0.5 wt % K) was 53%, while that of the K 2 O and KCl poisoning catalysts was only 2 and 4%, respectively. The atomic ratio of V 5+ /V 4+ (0.76) and the proportion of adsorbed oxygen species (48%) on the surface of the K 2 SO 4 poisoning sample were higher than those of the K 2 O poisoning sample (0.64, 36%) and the KCl poisoning sample (0.66, 36%). The above phenomena were due to the different poisoning mechanisms caused by K 2 O, KCl, and K 2 SO 4 . K 2 O decreased the number of Brønsted and Lewis acid sites and, moreover, reduced V 5+ to V 4+ ; K in KCl preferred to occupy Brønsted acid sites and Cl in KCl reduced Lewis acid sites. SO 4 2− in K 2 SO 4 counteracted the impact of K on the surface acid sites and V 5+ of the poisoned catalyst and generated new Brønsted acid sites.