Ex parte NATARAJ et al. - Page 17




          Appeal No. 1998-2224                                                        
          Application No. 08/624,147                                                  


                                      APPENDIX                                        
          1.  A process for operating an equilibrium controlled reaction              
          in a system which comprises a plurality of reactors operated                
          isothermally in a predetermined timed sequence wherein the                  
          heating and cooling requirements in a moving reaction mass                  
          transfer zone within each reactor are provided by indirect                  
          heat exchange with a fluid capable of phase change at                       
          temperatures maintained in each reactor during the following                
          cyclic steps:                                                               
          (a) reacting a feedstock at a first pressure in a                           
               first reactor containing an admixture of an                            
               adsorbent and a catalyst suitable for                                  
               conducting the equilibrium controlled                                  
               reaction under reaction conditions sufficient                          
               to convert the feedstock into a more                                   
               adsorbable product which is selectively                                
               adsorbed by the adsorbent and a less                                   
               adsorbable product and withdrawing  the less                           
               adsorbable product in substantially pure form                          
               under a relatively constant flow rate at the                           
               first pressure;                                                        
          (b) countercurrently depressurizing the first                               
               reactor to a second pressure by withdrawing a                          
               mixture comprising unreacted feedstock, a                              
               portion of the less adsorbable product and a                           
               portion of the more adsorbable product;                                
          (c) countercurrently purging the first reactor at                           
          the second pressure with a weakly adsorbing                                 
               purge fluid with respect to the adsorbent wherein                      
               the weakly adsorbing purge fluid is a fluid                            
               other than the less adsorbable product to                              
               desorb the more adsorbable product from the                            
               adsorbent and withdrawing a mixture comprising                         
               unreacted feedstock, a portion of the more                             
               adsorbable product and a portion of the less                           
               adsorbable product;                                                    
                                         17                                           





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