GALIMBERTI et al. V. ASANUMA et al. - Page 25




            Interference No. 103,303                                                                  


                  particular manner and technique.  The Asanuma                                       
                  process as set out in Example 3 is not specific and                                 
                  hence is unrepeatable and unreproducible--too many                                  
                  essential details are missing.  The specific process                                
                  actually adopted by Asanuma for the "repeats" of                                    
                  Example 3 is utterly unsupported by the text of that                                
                  Example.  Thus, the Asanuma application altogether                                  
                  fails to disclose or suggest the Galimberti process                                 
                  as set out in Galimberti patent claim 2.                                            
                  The following table compares the processes of the                                   
            parties.                                                                                  
            Galimberti et al.'s Claim 2                  Asanuma et al.'s claim 16                    
            A process for the preparation             A process for the                               
            preparation                                                                               
            of the copolymers of claim 1              of the copolymers of claim 1                    
            comprising                                comprising                                      
            polymerization of gaseous                 polymerization of                               
            mixture of propylene and                  propylene and butene                            
            1-butene                                                                                  
            with catalysts obtained from              with catalysts obtained from                    
            isopropyl (cyclopentadienyl-1             isopropyl (cyclopentadienyl-                    
            1                                                                                         
            fluorenyl) hafnium or                     fluorenyl) hafnium or                           
            zirconium         dichloride              zirconium dichloride                            
            where the 1-butene molar ---------                                                        
            content in the gas mixture                                                                
            being continuously fed is                                                                 
            from 1.5 to 10%                                                                           
            the polymerization is                     the polymerization is                           
            conducted in the liquid phase             conducted in the liquid                         
            phase                                                                                     
            at a temperature from -30E to             at a temperature from -100E                     
            to                                                                                        
            70EC.                                     100EC.                                          

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