Ex parte HENRICSON - Page 2




          Appeal No. 1998-2133                                                        
          Application No. 08/448,585                                                  


               The claims relate to a method and apparatus for ozone                  
          bleaching of cellulose pulp involving the use of a plurality                
          of fluidizing mixers directly connected in series where ozone               
          is introduced only into the first fluidizing mixer.  Claim 14               
          is representative of the subject matter on appeal:                          
          14. A method of ozone bleaching cellulose pulp having a                     
          consistency of 5-25% using first and second fluidizing mixers,              
          comprising the steps of sequentially:                                       
          (a) in the first fluidizing mixer at a pressure of 6-15 bar                 
          mixing cellulose pulp having a consistency of 5-25% with a                  
          mixture of ozone gas in carrier gas in an amount of 2-5 cubic               
          meters per air dried ton of the cellulose pulp to form a                    
          fluidized mixture of pulp, ozone and carrier gas so that some               
          ozone reacts with pulp to effect bleaching but non-reacted                  
          ozone remains;                                                              
          (b) transferring the mixture of pulp, non-reacted ozone, and                
          carrier gas from the first fluidizing mixer directly to the                 
          second fluidizing mixer;                                                    
          (c) in the second fluidizing mixer, without introducing any                 
          additional ozone therein, refluidizing the mixture of pulp,                 
          non-reacted ozone, and carrier gas from the first fluidizing                
          mixer, the ozone further reacting with the pulp to effect                   
          bleaching, but some residual ozone and carrier gas remaining                
          mixed with the pulp, and discharging the mixture of residual                
          ozone, carrier gas, and pulp from the second fluidizing mixer;              
          (d) maintaining the residual ozone in contact with the pulp                 
          for a time sufficient for further reaction of ozone with the                
          pulp to effect bleaching to take place; and                                 
          (e) separating carrier gas and unreacted ozone from the pulp.               
               The following references are relied upon by the examiner               
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