US2004137297A1PendingUtilityA1

Ion exchange membrane and production process therefor

Priority: Dec 26, 2002Filed: Dec 23, 2003Published: Jul 15, 2004
Est. expiryDec 26, 2022(expired)· nominal 20-yr term from priority
Y02E60/50H01M 8/10H01M 8/1004H01M 8/1055C08J 5/2206H01M 8/1018H01M 8/1053Y02P70/50H01M 8/1048H01M 8/1069
47
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Claims

Abstract

There is provided an ion exchange membrane and preparation process thereof. The membrane has a porous film layer having pores with an average pore diameter of 0.01 to 2 μm and a surface layer existent on at least one side of the porous film. The pores of the porous film layer are filled with an ion exchange resin and the surface layer contains (a) an inorganic filler having an average primary particle longest diameter which is 0.1 time or more the average pore diameter of the pores of the porous film layer and 50 μm or less and (b) an ion exchange resin. The membrane is useful for a diaphragm of a direct methanol type fuel cell.

Claims

exact text as granted — not AI-modified
What is claimed is:  
     
         1 . An ion exchange membrane comprising: 
 (A) a porous film layer having pores with an average pore diameter of 0.01 to 2 μm; and    (B) a surface layer existent on at least one side of the porous film, 
 wherein the pores of the porous film layer (A) are filled with an ion exchange resin and the surface layer comprises (a) an inorganic filler having an average primary particle longest diameter which is 0.1 time or more the average pore diameter of the pores of the porous film layer and 50 μm or less and (b) an ion exchange resin.  
   
     
     
         2 . The ion exchange membrane of  claim 1 , wherein the inorganic filler is a lamellar particle having an aspect ratio of 50 to 2,000.  
     
     
         3 . A process for producing the ion exchange membrane of  claim 1 , comprising the steps of: 
 (1) contacting a porous film having pores with an average pore diameter of 0.01 to 2 μm to a suspension containing an inorganic filler having an average primary particle longest diameter which is 0.1 time or more the average pore diameter of the pores of the porous film and 50 μm or less and a polymerizable monomer selected from the group consisting of a polymerizable monomer which provides an ion exchange resin when it is polymerized and a polymerizable monomer which provides an ion exchange resin precursor when it is polymerized in order to infiltrate the suspension into the pores of the porous film and to adhere the suspension to the surface of the porous film;    (2) polymerizing the polymerizable monomer contained in the suspension in the pores and on the surface of the porous film; and    (3) converting the ion exchange resin precursor into an ion exchange resin when the ion exchange resin precursor is obtained by polymerization in the step (2).    
     
     
         4 . A process for producing the ion exchange membrane of  claim 1 , comprising the steps of: 
 (1) contacting a porous film having pores with an average pore diameter of 0.01 to 2 μm to a suspension containing an inorganic filler having an average primary particle longest diameter which is 0.1 time or more the average pore diameter of the pores of the porous film and 50 μm or less, a resin selected from the group consisting of an ion exchange resin and an ion exchange resin precursor, and a solvent in order to infiltrate the suspension into the pores of the porous film and to adhere the suspension to the surface of the porous film;    (2) removing the solvent contained in the suspension in the pores and on the surface of the porous film; and    (3) converting the ion exchange resin precursor into an ion exchange resin when the suspension in the step (2) contains the ion exchange resin precursor.    
     
     
         5 . A diaphragm for a direct methanol type fuel cell which comprises the ion exchange membrane of  claim 1 .  
     
     
         6 . A direct methanol type fuel cell comprising the diaphragm for a direct methanol type fuel cell of  claim 5.

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