Ex Parte KHARAZI - Page 3




                    Appeal No. 2001-0772                                                                                                                                  
                    Application No. 09/052,429                                                                                                                            


                              (2)       Claims 6 and 7 are rejected under 35 U.S.C. § 103(a) as unpatentable over the                                                     
                    combined teachings of Unger, Rubber Technology, Kotani and Alia.                                                                                      
                                                                               Discussion                                                                                 
                              (1)       Rejection of claims 1-5                                                                                                           
                              Unger discloses a method for continuously preparing thermo-crosslinkable and/or                                                             
                    thermoplastic elastomer blends by mixing the elastomer with plasticizer oil and other additives,                                                      
                    including carbon black.  The method comprises the following steps (col. 2, lines 25-43):                                                              
                              (a)       continuously premixing the crushed elastomer in an annular zone mixer with                                                        
                                        at least part of said plasticizer oil, and optionally with at least part of said                                                  
                                        other additives, to form a preblend in which said elastomer is decomposed                                                         
                                        and said additives are embedded in the polymer matrix;                                                                            
                              and thereafter                                                                                                                              
                              (b)       completing the mixing of said premix, and optionally of the remainder of said                                                     
                                        additives, in a mixing unit working batchwise or continuously.                                                                    
                                        In the method according to the invention, said annular zone mixer of said first                                                   
                              step (a) has the function of decomposing the elastomer to such an extent that a                                                             
                              mixing with the adjuvants becomes possible.  Thus a large part of the total mixing                                                          
                              process is effected in said annular zone mixer, whereas the function of said mixing                                                         
                              unit of said second step (b), for example an internal or Banbury type mixer or mixing                                                       
                              extruder, is reduced to a simple aftermixing.                                                                                               
                              In Example 4, carbon black is added during the second step of the method (col. 6,                                                           
                    lines 57-64):                                                                                                                                         
                                        The rubber, the plasticizer oil and the other adjuvants were continuously                                                         
                              premixed in an annular zone mixer rotating at 2000 r.p.m. (revolutions per minute).                                                         
                              The resulting blend and the carbon black were then introduced into a kneader which                                                          
                              was working batchwise, for example an internal mixer, or into a mixing extruder                                                             
                              which was working continuously.  There, the elastomer blend was completed.                                                                  


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