Process for reducing the production of water in oil wells

Abstract

A process is described for reducing the production of water in oil wells which comprises the injection into the formation around the well of an aqueous solution of one or more polymers selected from those having general formula (1) [ ] wherein: n ranges from 0.70 to 0.98; m ranges from 0.30 to 0.02; n+m=1; X 1 and X 2 , the same or different, are selected from H an CH 3 ; R 1 , R 2 , R 3 , the same or different, are selected from C 1 -C 10 monofunctional hydrocarbyl groups; x ranges from 2 to 5.

1 . A process for reducing the production of water in oil wells which comprises the injection into the form ation around the well of an aqueous solution of one or more polymers selected from those having general formula (I)  
     
       
         
         
             
             
         
       
     
     wherein: 
 n ranges from 0.70 to 0.98;  
 m ranges from 0.30 to 0.02;  
 n+m=1;  
 X 1  and X 2 , the same or different, are selected from H and CH 3 ;  
 R 1 , R 2 , R 3 , the same or different, are selected from C 1 -C 10  monofunctional hydrocarbyl groups;  
 x ranges from 2 to 5.  
 
   
   
       2 . The process according to  claim 1 , characterized in that n ranges from 0.80 to 0.95 and m ranges from 0.20 to 0.05.  
   
   
       3 . The process according to  claim 1 , characterized in that R 1 , R 2 , R 3 , the same or different, are selected from C 1 -C 3  monofunctional alkyl radicals.  
   
   
       4 . The process according to  claim 3 , characterized in that R 1 =R 2 =R 3 =CH 3 .  
   
   
       5 . The process according to  claim 1 , characterized in that x=3.  
   
   
       6 . The process according to  claim 1 , characterized in that the polymer having general formula (I) has a molecular weight ranging from 1.5 to 12 million.  
   
   
       7 . The process according to  claim 1 , characterized in that the concentration of the polymer having general formula (I) in the aqueous solution ranges from 500 to 8000 ppm.  
   
   
       8 . The process according to  claim 7 , characterized in that the concentration of the polymer having general formula (I) in the aqueous solution ranges from 1500 to 5000 ppm.  
   
   
       9 . The process according to  claim 1 , characterized in that in the polymer having general formula (I) n=0.95, m=0.05, x=3, X 1 =H, X 2 =CH 3 , R 1 =CH 3 , R 2 =CH 3 , R 3 =CH 3 .  
   
   
       10 . The process according to  claim 1 , characterized in that in the polymer having general formula (I) n=0.90, m=0.1, x=3, X 1 =H, X 2 =CH 3 , R 1 =CH 3 , R 2 =CH 3 , R 3 =CH 3 .  
   
   
       11 . The process according to  claim 1 , characterized in that it is preceded by an optional pretreatment step (preflush).  
   
   
       12 . The process according to  claim 11 , characterized in that the pretreatment step is effected with an aqueous solution containing a surface-active agent.  
   
   
       13 . The process according to  claim 1 , characterized in that at the end of the above process, an optional overflush step is effected, or a treatment of the formation itself with brine or gas or oil.