Ex Parte DATH et al - Page 12



          Appeal No. 2005-0183                                                        
          Application No. 09/206,218                                                  
                                      APPENDIX                                        

               1. A process for the production of olefins by catalytic                
          cracking, the process comprising feeding a hydrocarbon feedstock            
          containing at least one olefin of C4 or greater over an MFI                 
          crystalline silicate catalyst to produce an effluent containing             
          at least one olefin of C2 or greater by catalytic cracking which            
          is selective towards light olefins in the effluent, whereby for             
          increasing the catalyst stability by limiting formation of coke             
          thereon during the cracking process the catalyst has a                      
          silicon/aluminum atomic ratio of from 300 to 1000, the olefin               
          partial pressure is from 0.1 to 2 bars, and the feedstock                   
          contacts the catalyst at an inlet temperature of from 500 to                
          600BC, wherein the catalyst has been pretreated by heating the              
          catalyst in steam to reduce the tetrahedral aluminum in the                 
          crystalline silicate framework of said catalyst and convert the             
          tetrahedral aluminum to octahedral aluminum in the form of                  
          amorphous alumina causing partial obstruction in the pores of               
          said crystalline silicate framework and thereafter dealuminating            
          the catalyst by treating the catalyst with a complexing agent for           
          aluminum to remove amorphous alumina from the pores of said                 
          crystalline silicate framework and at least partially recover the           
          micropore volume to increase the silicon/aluminum atomic ratio of           
          the catalyst to a value of from 300 to 1000.                                











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