The deactivation and regeneration of selective catalytic reduction (SCR) catalysts poisoned bypotassium by a wet-impregnation method was investigated experimentally. Potassium in theform of both chloride and sulfate is a strong poison for the catalyst. The results indicate thatpotassium titrates the active sites for NH
3 adsorption. Simply increasing the operatingtemperature or the vanadium content in the catalyst cannot compensate the loss of catalystactivity: Increasing the temperature hardly increases the conversion of NO for the stronglypoisoned catalysts, and catalysts with high vanadium content become active for oxidizing NH
3to NO, causing a net NO formation. Deactivated catalysts can be regenerated by differentmethods. Sulfation by gaseous SO
2 is efficient provided the poison is first removed by washing.When regenerating by 0.5 M H
2SO
4, the catalyst regains a higher activity than that of the freshcatalyst at temperatures higher than 300
![](/images/entities/deg.gif)
C. Heat treatment of the catalyst at 400
![](/images/entities/deg.gif)
C for 2 hafter poisoning to simulate actual operation has no influence on the regeneration by 0.5 M H
2SO
4.Deactivated catalysts without the heat treatment step regain higher activities than that of thefresh catalyst at all temperatures when regenerated by 1 M NH
4Cl. However, the heat treatmentstep has a negative effect on the regeneration by NH
4Cl.