Ex Parte Brauchle et al - Page 5

                Appeal 2007-4230                                                                               
                Application 09/984,339                                                                         
                      Appellants, on the other hand, contend that Heil does not teach or                       
                suggest “setting a steam/hydrocarbon mixing ratio of a mixture generated in                    
                a mixture-preparation stage as a function of a temperature of a reformate gas                  
                stream emerging from a CO oxidation stage of a reforming reactor as claim                      
                1 specifies”; hence, the combination of Wiesheu and Heil do not suggest the                    
                subject matter required by rejected claims 1 and 3 (Br. 5).                                    
                      The issue before us is: Have Appellants identified reversible error in                   
                the Examiner’s obviousness rejection by their assertions in the Brief?  We                     
                answer that question in the affirmative and we reverse the Examiner’s                          
                obviousness rejection.                                                                         
                      The Examiner bears the initial burden, on review of prior art or on any                  
                other ground, of presenting a prima facie case of unpatentability.  In re                      
                Oetiker, 977 F.2d 1443, 1445, 24 USPQ2d 1443, 1444 (Fed. Cir. 1992).                           
                      Here, the Examiner has not established that the combination of the                       
                carbon monoxide oxidation method of Heil with the reforming method of                          
                Wiesheu would have resulted in a process as claimed wherein a                                  
                steam/hydrocarbon mixing ratio of the steam/hydrocarbon mixture generated                      
                in a mixture preparation stage, which mixture is introduced into the reformer                  
                of a reforming reactor, is set as a function of a temperature of a reformate                   
                gas stream emerging from a CO oxidation stage of a reforming reactor for                       
                the reasons stated by Appellants in the Brief.  While Heil discloses adjusting                 
                the temperature in the CO oxidation multi-stage reactor via metering of                        
                oxygen gas and passive cooling using static mixing structures in addition to                   
                the use of cooling circuits (col. 4, ll. 28-49), the Examiner has not                          
                reasonably established that combining the multi- stage CO reactor of Heil                      
                with the reformer of Wiesheu would have resulted in Appellants’ claimed                        

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