Ex Parte Schwefer et al - Page 2

                Appeal 2007-0280                                                                               
                Application 10/469,392                                                                         
                14, 16-18, and 20-29 are the only claims pending in this application (Br. 2).                  
                We have jurisdiction pursuant to 35 U.S.C. § 134.                                              
                      According to Appellants, the invention is directed to a method of                        
                reducing the content of NOx and N2O in gases, comprising the steps of                          
                adding ammonia as a reducing agent, introducing the gas mixture into a                         
                reaction zone containing one or more iron-laiden zeolites with no pores or                     
                channels having a width greater than or equal to 7 Angströms, and setting a                    
                specified temperature, flow rate, and space velocity to achieve the desired                    
                degree of decomposition of N2O (Br. 2).  Independent claim 14 is                               
                representative of the invention and is reproduced below:                                       
                      14.     A method of reducing the content of NOx and N2O in gases,                        
                      which comprise the steps of:                                                             
                      a)     adding ammonia as a reducing agent which can reduce NOx                           
                      and is gaseous under the reaction conditions to the NOx- and N2O-                        
                      containing gas in an amount of up to 1.33 (8/6) mol per mole of NOx,                     
                                                                                                              
                      b)     introducing the gas mixture into an apparatus having a reaction                   
                      zone containing one or more iron-laden zeolites whose crystal                            
                      structure has no pores or channels having a width greater than or equal                  
                      to 7 Angström,                                                                           
                      c)     setting a temperature from 350 to 450ºC in the reaction zone                      
                      and selecting a flow rate of the gas mixture and/or the amount of                        
                      catalyst by passing the gas over the catalyst at a space velocity of                     
                      from 5 000 to 50 000h-1, based on the catalyst volume, so that the                       
                      desired degree of decomposition of N2O is achieved and the                               
                      temperature and flow rate of the gas mixture are set and/or the amount                   
                      of catalyst is chosen so that at least 50% of the N2O are decomposed                     
                      in the reaction zone.                                                                    




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