Ex Parte Groten - Page 4



          Appeal No. 2005-0766                                                        
          Application No. 09/877,277                                                  

                                       OPINION                                        
               For the reasons set forth in the answer and below, we will             
          sustain each of the rejections advanced on this appeal.                     
               With respect to each of the Section 102 rejections, it is              
          the examiner’s position that both Podrebarac and Gildert                    
          expressly teach all aspects of the here claimed process except              
          for the specific reactions recited in appealed claim 1(b)(i) and            
          (ii) wherein respectively thiophene is converted to n-butyl                 
          mercaptan and mercaptans are reacted with diolefins to form                 
          sulfide products.  According to the examiner, these reactions               
          would inherently occur in the processes of the applied references           
          because the feed stock, catalyst and reaction conditions of these           
          processes correspond to those of the appellant’s claimed process.           
               The appellant contends that the examiner’s above noted                 
          inherency position is not proper.  In support of this view, the             
          appellant presents the following argument on pages 9 and 10 of              
          the brief:                                                                  
                    [N]either of the reactions which are recited in present           
               claim 1 are disclosed or suggested by either reference.                
               There is a reason they do not occur.  Why?  The conditions             
               used in the reaction to hydrodesulfurize, particularly the             
               temperatures, are too harsh.  In the present process the               
               lower zone is between 270 and 450oF and the upper                      
               distillation zone between 130 to 270oF, whereas in ‘020                
               [i.e., Podrebarac] “The distillation column reactor is                 
               advantageously used to react the heavier or higher boiling             
                                          4                                           




Page:  Previous  1  2  3  4  5  6  7  8  9  10  Next 

Last modified: November 3, 2007