SCR-Active Material

Abstract

The present invention relates to an SCR-active material, comprising a small-pore zeolite, aluminum oxide and copper, characterized in that it contains 5 to 25 wt-% of aluminum oxide in relation to the entire material and that the copper is present on the aluminum oxide in a first concentration and on the small-pore zeolite in a second concentration.

1 - 21 . (canceled) 
     
     
         22 . An SCR-active material comprising
 (i) small-pore zeolites belonging to the structure type AEI, AFX, CHA (chabazite), ERI (erionite), or KFI,   (ii) aluminum oxide, and   (iii) copper,   
       wherein it contains 5 to 25 wt-% aluminum oxide based on the entire material and the copper is present on the aluminum oxide in a first concentration and on the small-pore zeolite in a second concentration. 
     
     
         23 . The SCR-active material according to  claim 22 , wherein the total amount of copper calculated as CuO and based on the total SCR-active material is 1 to 15 wt-%. 
     
     
         24 . The SCR-active material according to  claim 22 , wherein the first concentration is higher than the second concentration. 
     
     
         25 . The SCR-active material according to  claim 22 , wherein the first concentration is at least 1.5 times higher than the second concentration. 
     
     
         26 . The SCR-active material according to  claim 22 , wherein the zeolite has an atomic ratio of copper to backbone aluminum of 0.25-0.6. 
     
     
         27 . The SCR-active material according to  claim 22 , wherein the small-pore zeolite is an aluminosilicate. 
     
     
         28 . The SCR-active material according to  claim 27 , wherein the small-pore zeolite has an SAR value of 5 to 50. 
     
     
         29 . The SCR-active material according to  claim 22 , wherein the small-pore zeolite is a silicoaluminosilicate or aluminophosphate. 
     
     
         30 . The SCR-active material according to  claim 22 , wherein the average crystallite size (d50) of the small-pore zeolite is 0.1 to 20 μm. 
     
     
         31 . The SCR-active material according to  claim 22 , wherein the small-pore zeolite forms a core and the aluminum oxide forms a shell encasing said core. 
     
     
         32 . The SCR-active material according to  claim 22 , wherein it is present in powder form. 
     
     
         33 . The SCR-active material according to  claim 22 , wherein it is present (A) in the form of a coating on a carrier substrate or (B) in the form of a substrate that was extruded in combination with a matrix component. 
     
     
         34 . The SCR-active material according to  claim 33 , wherein the carrier substrate of (A) comprises a combination of an inert matrix component and the SCR-active material. 
     
     
         35 . The SCR-active material according to  claim 22 , wherein it is present in the form of a coating suspension, said coating suspension further comprises water. 
     
     
         36 . A method for purifying exhaust gas of lean-operated combustion engines, wherein the exhaust gas is passed over an SCR-active material according to  claim 22 . 
     
     
         37 . A device for purifying exhaust gas of lean-operated combustion engines, wherein it comprises an SCR-active material according to  claim 22 , and an injector for providing a reducing agent. 
     
     
         38 . The device according to  claim 37 , wherein the reducing agent is an aqueous urea solution. 
     
     
         39 . The device according to  claim 37 , and further comprising an oxidation catalyst. 
     
     
         40 . The device according to  claim 37 , and further comprising a nitrogen oxide storage catalyst. 
     
     
         41 . A method for the production of the SCR-active material according to  claim 22 , which comprises drying an aqueous suspension of the small-pore zeolites, copper salt, and aluminum oxide or precursor thereof to obtain a dried product, and subsequently calcining the dried product. 
     
     
         42 . The method according to  claim 41 , wherein the drying is by spray drying. 
     
     
         43 . The method according to  claim 41 , wherein the calcining is performed in an air or in an air/water atmosphere at temperatures between 500° C. and 900° C. 
     
     
         44 . The method according to  claim 41 , which comprises placing the small-pore zeolite in water, then adding a soluble copper salt while stirring, and then adding the aluminum oxide or precursor thereof.