Ex Parte Brauchle et al - Page 2

                Appeal 2007-4230                                                                               
                Application 09/984,339                                                                         


                      Appellants’ invention is directed to a method of operating a steam                       
                reforming plant including a mixture preparation stage, a reactor having a                      
                reformer and a carbon monoxide oxidation stage, a control circuit having a                     
                control unit, and a temperature sensor.  A steam/hydrocarbon1 mixture is                       
                prepared in the mixture preparation stage using a temperature of a product                     
                gas leaving the carbon monoxide stage for setting the steam/ hydrocarbon                       
                mixing ratio of the mixture generated in the mixture preparation stage to                      
                counteract an aging-related shift in a temperature profile within the                          
                reforming reactor.  The plant can be a mobile plant used in combination with                   
                fuel cell vehicles for the purposed of supplying hydrogen to the fuel cells                    
                (Specification ¶ 0003).    Claim 1 is illustrative and reproduced below:                       
                      1.  A method for operating a plant for the steam reforming of                            
                hydrocarbons, comprising:                                                                      
                      providing a control circuit including a control unit, a mixture                          
                preparation stage, a reactor having a reformer and a CO oxidation stage, and                   
                a temperature sensor,                                                                          
                      in the mixture-preparation stage, generating a steam/hydrocarbon                         
                mixture from water and at least one hydrocarbon;                                               
                      introducing the prepared steam/hydrocarbon mixture into the reformer                     
                of the reforming reactor; and                                                                  
                      counteracting an aging-related shift in a temperature profile within the                 
                reforming reactor by setting a steam/hydrocarbon mixing ratio of the                           
                steam/hydrocarbon mixture generated in the mixture-preparation stage as a                      
                function of a temperature of a reformate gas stream emerging from the CO                       
                oxidation stage of the reforming reactor.                                                      
                                                                                                              
                1 The term “hydrocarbon” is used by Appellants in a manner that includes                       
                methanol within the scope thereof  (Specification ¶ 0002).                                     
                                                      2                                                        

Page:  Previous  1  2  3  4  5  6  7  Next

Last modified: September 9, 2013