Ex parte CHERUVU et al. - Page 4




               Appeal No.      95-2035                                                                                                
               Serial No.      08/083,864                                                                                             
                       contacting in a first gas phase, fluidized bed reaction zone under polymerization                              
                       conditions, a gaseous monomeric composition comprising a major proportion of                                   
                       ethylene and, optionally, hydrogen, with a catalyst as hereinafter defined, the                                
                       hydrogen/ethylene molar ratio (H /C  ratio) being no higher than about 0.35 and the                            
                                                          2  2                                                                        
                       ethylene partial pressure being no higher than about 100 psia, to produce said HMW                             
                       component associated with catalyst particles, transferring said HMW component                                  
                       associated with catalyst particles to a second gas phase, fluidized bed reaction zone into                     
                       which is also fed hydrogen and a gaseous monomeric composition comprising a major                              
                       proportion of ethylene, under polymerization conditions including a H /C  ratio of at                          
                                                                                                 2  2                                 
                       least about 0.6 and at least about 1.5 times that in said first reaction zone, and an                          
                       ethylene partial pressure of at least 1.7 times that in said first reaction zone, to produce                   
                       said LMW component deposited on and within the HMW component associated with                                   
                       catalyst particles, said catalyst is selected from the group consisting of 1), 2) and 3),                      
                       wherein 1) is a supported Ti/Mg complex precursor prepared by the interacting of a                             
                       previously dried hydroxyl-containing, solid, inorganic carrier slurried in a non-polar                         
                       solvent with a dialkylmagnesium such that no substantial excess of magnesium remains                           
                       in the slurry, and subsequently reacting the resulting supported Mg-containing                                 
                       intermediate with at least sufficient titanium tetrachloride to react with the hydroxyl                        
                       groups on the carrier and form said precursor containing substantially no free TiCl ,                          
                                                                                                              4                       
                       said precursor being used together with a hydrocarbyl aluminum cocatalyst; 2) is a                             
                       supported Ti/Mg complex precursor prepared by treating a magnesium oxide (MgO)                                 
                       support with an organic acid, reacting the treated support with titanium tetrachloride,                        
                       and pre-reducing the catalyst with an aluminum alkyl, said precursor being used                                
                       together with a hydrocarbyl aluminum cocatalyst; and 3) is a catalyst comprising                               
                       chromium oxide and tetravalent titanium supported on a refractory oxide in which at                            
                       least 75% of its pore volume is in pores of about 200 to 500 Angstroms average pore                            
                       diameter.                                                                                                      

                       According to appellants, claims 5, 6 and 12 are to be individually considered separately from                  

               claims 1-4, 13 and 14 (Brief page 3).                                                                                  

                       The prior art reference of record relied upon by the examiner in rejecting the appealed claims is:             

               Bailey et al. (Bailey)                  4,461,873                      Jul. 24, 1984                                   

                                                              ISSUES                                                                  


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