Ex parte DALY et al. - Page 5




          Appeal No. 1997-0183                                                        
          Application 08/206,623                                                      


          choice,” there is no evidence or convincing reasons of record               
          to support this position.  Kaiser is directed to a catalyst                 
          for the isomerization of alpha-pinene to beta-pinene, with the              
          object of increasing the conversion and retaining the                       
          specificity of the catalyst for beta-pinene formation (col. 1,              
          ll. 5-10 and 55-59).  Neutral to basic conditions must be                   
          maintained to suppress acidic by-product formation which                    
          affects selectivity (col. 1, ll. 67-68; col. 2, ll. 17-24).                 
          Kaiser teaches that the alpha-pinene isomerization process is               
          “acutely acid sensitive” as acidic conditions can                           
          deactivate the catalyst and commercially prepared Group VIII                
          catalysts admixed with a Group IB metal on an alumina support               
          contain residual anions which can form acid during the                      
          isomerization process (col. 3, ll. 4-8 and 13-26).  Kaiser                  
          further teaches that                                                        
               The acidic functionality displayed by the Group                        
               VIII catalyst admixed with Group IB metal on an                        
               alumina support can be suppressed by subjecting the                    
               supported catalyst and Group IB metal to a                             
               neutralization treatment.  This involves treating                      
               the supported catalyst and Group IB metal with at                      
               least about 0.002 weight parts per weight of alumina                   
               of an alkali metal or alkaline earth metal                             
               neutralizing agent provided from an alkali metal or                    
               alkaline earth metal salt or hydroxide inert to the                    
               catalyst.  (Col. 3, ll. 39-48).                                        

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