Ex parte NACAMULI et al. - Page 2




          Appeal No. 1998-1067                                                        
          Application No. 08/273,933                                                  

               The subject matter on appeal relates to a process for the              
          production of a benzene, toluene and xylene containing product              
          which contains a reduced amount of close-boiling non-                       
          aromatics.  The process includes the step of contacting a                   
          toluene containing feed which includes about 0.2 wt.% to about              
          5 wt.% close-boiling non-aromatics in a disproportionation                  
          zone with an acidic para-selective molecular sieve catalyst                 
          under conditions such that the product contains a reduced                   
          amount of close-boiling non-aromatics compared to the feed and              
          such that at least 40% of the xylene produced is para-xylene.               
          Further details of this appealed subject matter are set forth               
          in representative independent claim 31 which reads as follows:              
               31. A process for the production of a benzene, toluene                 
          and xylene containing product which contains a reduced amount               
          of  close-boiling non-aromatics, comprising:                                
               (a) aromatizing a predominantly paraffinic feedstock                   
               in an aromatization zone over a substantially                          
               nonacidic aromatization catalyst comprising a Group                    
               VIII metal on a molecular sieve support to produce                     
               an aromatization product which comprises a toluene                     
               containing feed which comprises at least about 70%                     
               toluene and from at least about 0.2 wt% to about 5                     
               wt% close-boiling non-aromatics;                                       
               (b) contacting the toluene containing feed in a                        
               disproportionation zone with an acidic para-                           
               selective molecular sieve catalyst under conditions                    
               such that the product contains a reduced amount of                     
               close-boiling non-aromatic compared to the feed and                    
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