Ex parte FEITELBERG et al. - Page 2


            Appeal No. 1997-4422                                                      
            Application 08/269,797                                                    

                 Appellants’ invention is directed to a reduced ammonia               
            power generation system.  Claims 24 and 38, set forth below,              
            are representative of the claimed subject matter:                         
                 24.  A reduced ammonia power generation system comprising:           
                 a gasification unit;                                                 
                 a hot gas desulfurization system arranged to receive fuel            
            gas from said gasification unit;                                          
                 at least one catalytic reactor arranged to receive fuel              
            gas from said hot gas desulfurization system, said catalytic              
            reactor comprising a water-gas-shift stage for raising the                
            fuel gas temperature, a methanation of CO stage for raising               
            the fuel gas temperature and for consuming H2, and an ammonia             
            decomposition stage for reducing the ammonia content of the               
            fuel gas, in that sequence; [emphasis added]                              
                 a particulate removal system arranged to receive the                 
            reduced ammonia fuel gas from said catalytic reactor; and                 
                 a gas turbine arranged to receive the reduced ammonia fuel           
            gas from said particulate removal system.                                 
                 38.  A reduced ammonia power generation system comprising:           
                 a gasification unit;                                                 
                 a hot gas desulfurization system arranged to receive fuel            
            gas from said gasification unit;                                          
                 at least one catalytic reactor arranged to receive fuel              
            gas from said hot gas desulfurization system, said catalytic              
            reactor comprising a water-gas-shift and methanation stage for            
            raising the fuel gas temperature and for consuming H2 [sic,               
            H2], and an ammonia decomposition stage for reducing the                  
            ammonia content of the fuel gas, in that sequence.  [emphasis             
            added]                                                                    
                 The prior art references of record relied upon by the                
            examiner in rejecting the appealed claims are:                            
            Aldridge et al. (Aldridge) 3,850,841               Nov. 26, 1974          
            Graboski et al. (Graboski) 3,904,386               Sep. 09, 1975          
            Suggitt et al. (Suggitt)            4,202,167           May  13,          
            1980                                                                      
            Kimura et al. (Kimura ‘275) 4,233,275              Nov. 11, 1980          
            Flockenhaus et al.             4,259,312           Mar. 31, 1981          
            (Flockenhaus)                                                             
            Kimura et al. (Kimura ‘749) 4,273,749              Jun. 16, 1981          
            Takahashi et al. (Takahashi) 4,273,748             Jun. 16, 1981          
            Shah et al. (Shah)             4,476,683           Oct. 16, 1984          
            Babu et al. (Babu)             4,699,632           Oct. 13, 1987          
            Deinert                       4,779,412           Oct. 25, 1988          
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