Ex parte NG et al. - Page 2




              Appeal No. 1995-0770                                                                                          
              Application No. 07/929,457                                                                                    



                                                DECISION ON APPEAL                                                          
                     This is a decision on appeal under 35 U.S.C. § 134 from the final rejection of claims                  
              1-21 and 28, all the claims pending in the application.                                                       
                     Appellants’ claims are directed to a process for preparing copolymers of                               
              monomers having unsaturated carbon-to-carbon bonds.  Claims 1 and 4 are                                       
              representative of the claims on appeal and are reproduced below:                                              
              1.     A process for preparing copolymers which comprises, in the order stated: (1)                           
              adding monomers containing unsaturated carbon-to-carbon bonds, two polymerization                             
              initiators, namely a first polymerization initiator with a 10 hour half-life temperature of from              
              about 50EC to about 95EC and a second polymerization initiator with a 10 hour half-life                       
              temperature of from about 85EC to about 130EC, and a solvent to a reaction vessel; (2)                        
              purging the resulting solution with an inert gas; (3) sealing the reaction vessel and                         
              pressurizing it by the addition of an inert gas to a pressure of from about 20 to about 600                   
              kilopascals above ambient atmospheric pressure; (4) maintaining the temperature within                        
              the pressurized reaction vessel at a substantially constant temperature within the range of                   
              from about 50 to about 100EC for a period of from about 60 to about 300 minutes; (5)                          
              thereafter maintaining the temperature within the pressurized reaction vessel at a                            
              substantially constant temperature within the range of from about 80 to about 115EC for a                     
              period of from about 30 to about 300 minutes, wherein the temperature in step 5 is higher                     
              than the temperature in step 4; and (6) subsequently maintaining the temperature within the                   
              pressurized reaction vessel at a substantially constant temperature within the range of from                  
              about 115 to about 160EC for a period of from about 30 to about 180 minutes, wherein the                      
              temperature in step 6 is higher than the temperature in step 5, wherein the resulting                         
              copolymer is substantially free of gel formation                                                              
              4.     A process according to claim 1 wherein the monomers are styrene, ethyl acrylate,                       
              and acrylic acid.                                                                                             
              The examiner relies on the following references:                                                              
              Kamath (Kamath ‘696)                 4,125,696            November 14, 1978                                   

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