Ex parte RUSSELL et al. - Page 9




          Appeal No. 1997-4285                                       Page 9           
          Application No. 08/420,852                                                  


          The waste stream is first held in one of two holding tanks 14,              
          16.  Then, the waste stream is transferred to a third holding               
          tank 18 where its pH is adjusted to approximately 5.0, as                   
          shown at 20.  By way of example, pH adjustment is accomplished              
          by adding either lime or hydrosulfuric acid to make the waste               
          stream more basic or acidic,                                                
          respectively.  After pH adjustment, ferrous sulfate and                     
          hydrogen peroxide are continuously added to the waste stream                
          in a mixer reactor 22 as shown at 24, 26.  The ferrous sulfate              
          is first added in the reactor 22 in an amount based on the                  
          initial phenol concentration in the waste stream.  The                      
          hydrogen peroxide is added into the mixer reactor 22 after the              
          ferrous sulfate.  The iron in the ferrous sulfate catalyzes                 
          the hydrogen peroxide causing it to oxidize the phenol in the               
          waste stream.  The pH and the amount of unoxidized hydrogen                 
          peroxide is sensed at 28 and 30, respectively, shortly after                
          the waste stream leaves the mixer reactor 22.  Oxidation of                 
          the hydrogen peroxide can be sensed by measuring its oxidation              
          reduction potential (ORP), a process which would be well                    
          familiar to a person skilled in the art.                                    









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