Ex Parte Brauchle et al - Page 3

                Appeal 2007-4230                                                                               
                Application 09/984,339                                                                         
                                                                                                              
                      The Examiner relies on the following prior art references as evidence                    
                in rejecting the appealed claims:                                                              
                Heil    US 5,874,051  Feb. 23, 1999                                                            
                Wiesheu   US 5,984,986  Nov. 16, 1999                                                          
                      Claims 1 and 3 stand rejected under 35 U.S.C. § 103(a) as being                          
                unpatentable over Wiesheu in view of Heil.                                                     
                      Wiesheu discloses a steam reforming process wherein a water                              
                vapor/methanol mixture is prepared in a mixture preparation step and the                       
                mixture is supplied to a reforming reactor (Wiesheu, Abstract, col. 2, l.                      
                38- col. 4, l. 7).  The water vapor/methanol mixing ratio is adjusted as a                     
                function of the reforming system load condition and/or load condition                          
                changes thereof (id.).  For example, a carbon monoxide sensor (9, Fig. 1) is                   
                provided to detect the carbon monoxide concentration in the reformate                          
                leaving the reforming reactor.  A regulation unit (7, Fig. 1) is provided for                  
                determining the deviation from a desired carbon monoxide concentration                         
                value and operates to feed a signal to the mixture preparation unit for                        
                adjusting the water vapor/methanol mixture.  A carbon monoxide conversion                      
                step (not shown in Fig. 1) is performed to remove carbon monoxide from the                     
                reformer effluent and is located downstream of the reformer and upstream of                    
                a fuel cell arrangement that would be poisoned thereby (Wiesheu, col. 2, ll.                   
                29-37).                                                                                        
                      The Examiner acknowledges that Wiesheu does not “specifically                            
                disclose the measure of temperature of a reformate gas stream emerging                         
                from a reforming reactor that comprises more than one stage (i.e., additional                  
                oxidation stage), and thus counteracting an aging–related shift in a                           


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