Ex parte STUART et al. - Page 2




          Appeal No. 1997-0581                                                          
          Application No. 08/168,549                                                    

          pending in the application.  Claims 14 through 20 were                        
          canceled subsequent to the final Office action dated November                 
          23, 1994.                                                                     
               Appellants state that only claims 11, 12 and 13 do not                   
          stand or fall with independent claim 1.  See Brief, page 6.                   
          Therefore, for purposes of this appeal, we need only consider                 
          the propriety of the examiner’s rejections of claims 1, 11, 12                
          and 13 consistent with 37 CFR § 1.192(c)(7) and (c)(8)(1995).                 
          Claims 1, 11, 12 and 13 are reproduced below:                                 
               1. A process for the production of low molecular weight                  
          grafted polyolefins comprising;                                               
                    (a) mixing, at an elevated temperature of about 160                 
          to 300EC, in an extruder equipped with an outlet pressure                     
               control device about 0.1 to 20 weight percent of a free                  
               radical initiator, about 0.1 to 30 weight percent of an                  
               ethylenically unsaturated polycarboxylic acid, anhydride,                
          or ester thereof, and the remainder of a polyolefin                           
          containing     at least 93 weight percent C3-C10 olefins,                     
          wherein said elevated temperature is higher than the                          
          atmospheric boiling       point of at least one of the                        
          components thereby producing an     elevated pressure in said                 
          extruder of at least 30 psig, and                                             
                    (b) extruding the resulting molten grafted                          
          polyolefin     having a viscosity of less than 3,000 cP at                    
          190EC.                                                                        

               11. The process according to Claim 1 wherein said molten                 
          grafted polyolefin has a viscosity less than 2,000 cP at                      
          190EC.                                                                        

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