Ex parte TEMPLER et al. - Page 2




          Appeal No. 1997-0229                                                        
          Application No. 08/039,260                                                  


          CFR § 1.116” filed March 13, 1995 (Paper No. 14), which the                 
          examiner entered (advisory action of April 11, 1995, Paper No.              
          15).                                                                        
               Claim 11 is illustrative of the claims on appeal and is                
          reproduced below:                                                           
                    11.  The method of recovering raw material for                    
               the manufacture of paper, pulp board or cardboard                      
               from the residual waste water slurry of a mechanical                   
               clarification or separation apparatus by separating                    
               said slurry into a fiber-rich portion and a filler-                    
               rich portion, which comprises the sequential steps                     
               of                                                                     
                    a) adjusting the solids content of said waste                     
               water slurry to a value of 1 to 5% by weight by                        
               adding mechanically clarified waste water to form a                    
               homogeneous suspension,                                                
                    b) separating the coarse contaminant component                    
               of said suspension by passing it through a 1 to 2 mm                   
               mesh screen,                                                           
                    c) separating the black particle components of                    
               said coarse contaminant component having a particle                    
               size greater than 10 micrometers by centrifugation                     
               in a hydrocyclone or in a plurality of hydrocyclones                   
               connected in series or in parallel, said                               
               hydrocyclones having a nominal diameter of 10 to 100                   
               mm, and accept nozzle diameter of 7 to 14 mm and a                     
               reject nozzle diameter of 2 to 8 mm, the input                         
               pressure on the inlet side of said hydrocyclone or                     
               hydrocyclones being between 0.5 and 6 bar,                             
                    d) fractionally separating the accept component                   
               exiting from the hydrocyclone or hydrocyclones into                    
               a fiber component, an agglomerate component and a                      
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