Ex parte KOURTAKIS et al. - Page 3




               Appeal No. 1996-3493                                                                                                  
               Application No. 08/451,697                                                                                            


               April 9, 1996) for the examiner’s reasoning in support of the rejection and to the appellants’ brief                  

               (Paper No. 8, filed March 20, 1996) for the appellants’ arguments thereagainst.                                       





                                                        THE INVENTION                                                                

                       Appellants’ claimed invention is directed to an attrition resistant catalyst composition comprising           

               one or more acidic zeolites selected from rho and chabazite which are uniformly admixed to a ratio of                 

               from about 25 to about 75 weight % with one or more particulate binders selected from kaolin,                         

               bentonite, alpha-alumina and titania (brief, page 3).                                                                 

                                                             OPINION                                                                 

                       Bergna discloses acidic zeolite catalysts selected from the group consisting of chabazite,                    

               erionite, ZK-5 and rho which have been modified by depositing thereon at least 0.05 weight % of at                    

               least one element selected from the group consisting of silicon, aluminum, phosphorus and boron, which                

               catalysts are useful for producing dimethylamine (DMA) (col. 4, lines 44-58).  Zeolite rho synthesized                
                                                      +                           +        +             +                        
               in a Na-Cs form is converted to the H -form by exchanging the Na  and Cs  ions for NH  ions and                       
                                                                                                           4                         
               deammoniating by calcination at 400 EC to 800EC (col. 6, lines 57-63).  Zeolite H -rho which was+                               

               further treated with tetraethylorothosilicate before calcination had improved selectivity for DMA (col.               
               14, line 47 - col. 15, line 22).  Ammoniated zeolite chabazite is also converted to its H -form by+                           


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