Ex parte CORBIN et al. - Page 5




          Appeal No. 1995-4851                                                        
          Application 08/167,656                                                      


          effective amount of at least one metal selected from iron,                  
          manganese, magnesium and nickel, on a fluorinated alumina                   
          support (col. 2, lines 15-24).  The metals can be in a many                 
          forms including fluorides (col. 2, lines 49-57).  The total                 
          fluorine content of the catalyst taken as AlF  corresponds to               
                                                       3                              
          at least 90 wt%, preferably at least 95 wt%, exclusive of the               
          metal (i.e., iron, manganese, magnesium and nickel) (col. 2,                
          lines 39-47).  The metal content of the catalyst, expressed as              
          the divalent oxide, is not more than 50                                     
          wt% (col. 2, line 67 - col. 3, line 1).  The process is said                
          to achieve high selectivity of the above products by                        
          minimizing the formation of trifluorochloroethane, which is                 
          the product recited in appellants’ claims, through catalyst                 
          selection and control of reaction variables (col. 2, lines 1-               
          5).  Regarding control of reaction variables, Manzer states                 
          (col. 3, line 62 - col. 4, line 3):                                         
                    In general, with a given catalyst composition,                    
               the higher the temperature, the greater the                            
               HF/trihaloethylene and/or tetrahaloethane mol ratio,                   
               and the longer the contact time, the greater is the                    
               conversion to fluorinated products and the greater                     
               is the production of polyfluorinated products.  The                    
               above variables can be balanced, one against the                       
               other, so that formation of CClF CH Cl and/or                          
                                               2  2                                   

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