Ex parte HASENBEIN et al. - Page 2




          Appeal No. 1996-3808                                        Page 2           
          Application No. 08/213,832                                                   


               This is an appeal under 35 U.S.C. § 134 from the                        
          examiner’s refusal to allow claims 3, 4 and 9 which are all of               
          the claims remaining in the application.                                     
                                     THE INVENTION                                     
               Appellants’ invention is directed to a method for the                   
          copolymerization of ethylene with up to 4% molar units of C  to              
                                                                      3                
          C  alkenoic acid or ester thereof.  The process provides for a               
           6                                                                           
          continuously operated tubular reactor at a pressure of 500 to                
          5,000 Bar, elevated temperature and the presence of free                     
          radical initiators.  Two reaction zones are provided.  The                   
          first reaction zone has a maximum temperature of 240  C.  Theo                       
          second reaction zone has a maximum temperature of 300  C.o                      
          Additional initiator is metered into the beginning of a second               
          reaction zone after the temperature in the first reaction zone               
                               o        o                                              
          has dropped by from 5  C to 20  C.                                           
                                      THE CLAIMS                                       
               Claims 3 is illustrative of appellants invention and is                 
          reproduced below.                                                            
               3.   A process for the preparation of a copolymer of                    
          ethylene containing up to 4% molar of copolymerized units of a               
          C -C -alkenoic acid or an ester thereof having up to 14 carbon               
           3 6                                                                         
          atoms or a mixture of said monomers in a continuously operated               
          tubular reactor at a pressure of from 500 to 5,000 bar and at                







Page:  Previous  1  2  3  4  5  6  7  8  9  10  Next 

Last modified: November 3, 2007