Ex Parte Nedez et al - Page 2

                Appeal 2007-3383                                                                             
                Application 10/452,939                                                                       

                      We AFFIRM.                                                                             
                                                INTRODUCTION                                                 
                      Appellants claim a process for eliminating sulphur from a feed                         
                containing hydrogen sulphide and minimal traces of benzene, toluene and/or                   
                xylene (Specification 1).  The method comprises having two reactors in                       
                series wherein in each reactor there is a first, protective catalyst followed by             
                a second catalyst (catalyst A) (Specification 6; claims 1 and 38).                           
                      Claims 1 and 38 are illustrative:                                                      
                      1.  A process for eliminating sulphur from a feed containing hydrogen                  
                sulphide, sulphur dioxide, carbon oxysulphide and/or carbon sulphide and a                   
                minimal quantity of benzene, toluene and/or xylenes, said process                            
                comprising:                                                                                  
                      introducing said feed into a reaction zone comprising two reactors in                  
                series, each reactor containing a bed with a first catalyst, and recovering                  
                elemental sulphur and an effluent that is at least partially free of sulphur,                
                      wherein said first catalyst can be the same or different in each reactor               
                and is at least one catalyst containing a support comprising at least one                    
                compound selected from the group consisting of alumina, titanium oxide and                   
                zirconia, the support further comprising at least one doping element selected                
                from the group consisting of iron, cobalt, nickel, copper and vanadium,                      
                      each of said reactors further comprises a bed with a catalyst A which                  
                is different from said first catalyst and can be the same or different in each               
                reactor, wherein in each reactor said first catalyst is disposed upstream of                 
                catalyst A and acts as a protective layer for said catalyst A, and                           
                      wherein said feed contains 50-50,000 volume ppm of benzene,                            
                toluene and/or xylenes.                                                                      




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