Ex Parte DENK et al - Page 2


         Appeal No. 2002-0952                                                       
         Application No. 08/929,108                                                 

         of beer.”  Further details of this appealed subject matter are             
         recited in representative claim 45, the only independent claim             
         on appeal, reproduced below:                                               
                   45.  A method for raising the filtrate throughput                
              in a crossflow membrane filter in a filter module of a                
              filtration plant during the filtration of beer by                     
              releasing a covering layer built up on a filter                       
              membrane from the filter membrane, wherein beer is                    
              passed through the filter membrane from an unfiltrate                 
              side of the membrane to a filtrate side of the                        
              membrane thereby building up a cake of materials on                   
              the unfiltrate side of the membrane and thereby                       
              creating a transmembrane pressure over the filter                     
              membrane, the method comprising the steps of:                         
                   a) interrupting the flow of beer through the                     
              filter membrane;                                                      
                   b) separating the filter module from the                         
              filtration plant;                                                     
                   c) removing the beer from the filter module                      
              while maintaining circulation of the beer in the                      
              plant;                                                                
                   d) introducing into the filter module an agent                   
              for dissolving chemical bonds between the cake of                     
              materials and the membrane;                                           
                   e) maintaining said agent within the filter                      
              module in a concentration, at a temperature and for a                 
              time sufficient to loosen the cake of materials from                  
              the membrane without completely dissolving the cake of                
              materials;                                                            
                   f) back flushing the membrane with rinsing                       
              liquid from the filtrate side to the unfiltrate side                  
              of the membrane to remove the cake of materials from                  
              the membrane and into the filter module;                              
                   g) removing the cake of materials from the                       
              filter module;                                                        
                   h) connecting the filter module with the                         
              filtration plant;                                                     
                   i) resuming the flow of beer through the filter                  
              membrane; and                                                         
                   j) repeating steps a) to i) in the same                          
              filtration run.                                                       


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