Ex parte REIMANN et al. - Page 2


          Appeal No. 1999-0772                                                        
          Application No. 08/600,165                                                  


          the only other remaining claims, stand withdrawn from further               
          consideration pursuant to 37 CFR § 1.142(b)(1959).  We reverse.             
               The subject matter on appeal relates to a method for                   
          combined production of cement and sulfuric acid by the so-called            
          Müller-Kühne process.  Further details of this appealed subject             
          matter are recited in illustrative claim 12, the sole                       
          independent claim, reproduced below:                                        
                    12.  A method for combined production of cement                   
               and sulfuric acid by Muller-Kuhne [sic] process                        
               comprising:                                                            
                    storing powder components used in the process                     
               separately, the components including waste material,                   
               unprocessed powder components, fuel components, and                    
               residual components;                                                   
                    conditioning the components by comminuting;                       
                    taking a sample of the components and evaluating                  
               the sample for determining its composition;                            
                    formulating a required composition of the feed                    
               mix;                                                                   
                    combining the components for forming the                          
               formulated feed mix;                                                   
                    feeding the mix to a rotary drum kiln;                            
                    transporting a fuel mix comprising liquid and                     
               solid residual materials, separately to the rotary                     
               drum kiln;                                                             
                    burning the fuel mix in a flame, for forming                      
               active carbon;                                                         
                    burning the feed in the flame at a temperature of                 
               over 700°C, for forming CaO and flue gases;                            
                    calcining the CaO at a temperature of over                        
               1,200°C in the presence of SiO2 [sic], Al2O3 [sic],                    
               and Fe2O3 [sic] for forming cement;                                    


                                                                                      
          (paper 14) that the amendment will be entered for purposes of               
          this appeal.                                                                

                                          2                                           



Page:  Previous  1  2  3  4  5  6  7  8  Next 

Last modified: November 3, 2007