Ex Parte LAINE et al - Page 16


               Appeal No. 2001-0065                                                                                                   
               Application 09/048,289                                                                                                 
                       The two published papers do not provide “recognition” in the art of the invention.                             
               The statement that they are in part  “of interest to the pulp and paper trade” (Pikka                                  
               declaration, page 2, paragraph 4, lines 3-4) does not indicate (1) if any peer review or                               
               other screening for merit occurred, as is usually the case for, e.g. academic publications                             
               or (2) what other considerations went into the decision to publish the articles                                        
               (presumably the other part).                                                                                           
                       Turning now to the substance of the papers from the bleaching conference, we                                   
               initially note that they are not declaratory evidence, per se.  The data presented in the                              
               publications would have best been provided in declaration form, comparing the closest                                  
               prior art directly, and illustrating the benefits of the invention.                                                    
                       We look to the declaration, pages 2-3, paragraphs 4 and 5 for the Appellants’                                  
               interpretation of the articles.  According to declarant Pikka, the processes are according                             
               to or relate to the practice of the invention and:                                                                     
                       This procedure results in a higher yield, savings in bleaching chemicals, and                                  
                       improved cleanliness, improved heat economy, reduced foaming tendency, and a                                   
                       lower consumption of anti-foaming agent, compared to if screening is before the                                
                       oxygen delignification, and by recirculating the rejects directly back to the fiber                            
                       line – rather than treating them with an additional reactor – the costs associated                             
                       with the additional reactor are eliminated, yet the results are just as                                        
                       advantageous. (Pikka declaration, page 3, lines 3-9, relating to Exhibit C)                                    
               and                                                                                                                    
                       As reported in this paper [Exhibit D], actual tests and observations show that by                              
                       practicing the method of claim 1 of the above-identified application utilizing the                             
                       apparatus of claim 18 it is possible to have a significant positive impact on the                              
                       quality of the pulp in the operation and economy of the entire delignification                                 
                       process.  The quality of the pulp produced is good with the pulp going to                                      
                       bleaching so clean that it does not cause problems in bleaching.  Because                                      
                       oxygen delignification is a mild fiberizer of shives, the quality of the fibers                                
                       produced is good and there is improved yield.  Also there is improved heat                                     
                       economy (typically a savings of 50 – 100 Adt of steam per ton of pulp) compared                                
                       to if screening takes place before oxygen delignification, and there is a large                                

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