Ex parte HUFTON et al. - Page 14




          Appeal No. 1998-1273                                                        
          Application No. 08/624,148                                                  


                                      APPENDIX                                        
               1.  A process for producing carbon monoxide which                      
          comprises the steps of:                                                     
               (a) reacting a feed stock comprising methane and water                 
                    in the presence of a steam methane reforming                      
                    catalyst at a temperature ranging from 700°C to                   
                    1000°C and a pressure ranging from 2 to 50                        
                    atmospheres to form a reformate comprising hydrogen,              
                    carbon monoxide, carbon dioxide and unreacted                     
                    feedstock;                                                        
               (b) removing water from the reformate to form a water-                 
                    depleted reformate and heating the water-depleted                 
                    reformate to a temperature ranging from 200° to                   
                    500°C to form a heated water-depleted reformate;                  
               (c) introducing the heated water-depleted reformate into               
                    a plurality of reactors operated isothermally in a                
                    predetermined timed sequence and according to the                 
                    following steps which are performed in a cycle                    
                    within each reactor:                                              
                   (1) reacting the heated water-depleted reformate at               
                         a first pressure in a first reactor containing               
                         an admixture of a water adsorbent and a water                
                         gas shift catalyst under reaction conditions                 
                         sufficient to convert carbon dioxide and                     
                         hydrogen to carbon monoxide and to adsorb water              
                         onto       the adsorbent and withdrawing a CO-               
                         enriched stream under a relatively constant flow             
                         rate at the first pressure;                                  
                    (2) countercurrently depressurizing the first                     
                         reactor to a second pressure by withdrawing a                
                         mixture comprising unreacted feedstock, carbon               
                         monoxide and water;                                          
                    (3) countercurrently purging the first reactor at                 
                         the second pressure with a weakly adsorbing                  
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