Ex Parte Assarabowski et al - Page 2



          Appeal No. 2005-1209                                                        
          Application No. 10/078,086                                                  

               The two independent claims 1 and 4 are reproduced below as             
          illustrative of appellants’ apparatus and method, respectively.             
               1.   A polymer electrolyte membrane (PEM) fuel cell power              
               plant burner assembly which burner assembly is operable to             
               combust an anode exhaust gas emanating from a cell stack in            
               the PEM fuel cell assemblage, said burner assembly                     
               comprising:                                                            
               a) a catalytic burner;                                                 
               b) an air/anode exhaust gas mixing station adjacent to and             
               opening into said catalytic burner; and                                
               c) at least one heat exchanger disposed in heat exchange               
               relationship with said catalytic burner, said heat exchanger           
               being operable to convert water contained in said heat                 
               exchanger to a two phase mixture of water and steam by using           
               heat generated by said catalytic burner from a mixture of              
               anode exhaust gas and air which is combusted in said                   
               catalytic burner.                                                      
               4.   A method for producing steam for use in a steam                   
               reformer in a polymer electrolyte membrane (PEM) fuel cell             
               power plant, said method comprising:                                   
               a) the step of providing a catalytic burner which operates             
               at temperatures as high as about 1,700oF (927oC);                      
               b) the step of combusting a fuel cell anode exhaust gas                
               stream in said catalytic burner;                                       
               c) the step of converting a stream of water to a mixture of            
               water and steam with heat produced by combustion of said               
               fuel cell anode exhaust gas stream; and                                
               d) the step of feeding steam from said mixture to a                    
               catalytic fuel reformer in the fuel cell power plant.                  
               The sole prior art reference relied upon by the examiner is:           
          Kaufmann               US 2002/0012893 A1           Jan. 31, 2002           
                                          2                                           




Page:  Previous  1  2  3  4  5  6  7  Next 

Last modified: November 3, 2007