US2019118144A1PendingUtilityA1
Bipolar membrane
Est. expiryApr 14, 2036(~9.8 yrs left)· nominal 20-yr term from priority
B01D 67/0006B01D 71/82B01D 2323/46B01D 61/445C08J 5/2287C08J 5/2243C08J 5/2231C08J 2427/06C08J 2353/02B01J 39/04B01D 69/02C08J 2325/18B01D 2325/42C08J 2325/06B01J 41/04C08J 2423/06C08J 5/2275C08J 2325/14C08J 2325/08B01J 39/20B01J 41/14C08J 2423/12B01J 47/12B01D 61/46B01D 69/12B01D 71/28B01D 71/301B01D 69/125B01D 71/281B01D 69/1071B01D 71/262B01D 71/261B01D 69/1213B01D 71/26Y02E60/50C25B 13/08C25B 13/02C08J 5/22B01D 69/106
49
PatentIndex Score
0
Cited by
0
References
0
Claims
Abstract
A bipolar membrane in which a cation-exchange membrane and an anion-exchange membrane are joined to each other, wherein a leakage ratio of gluconic acid at 60° C. is not more than 1.0%, and the cation-exchange membrane is supported by a polyolefin reinforcing member and, further, contains a polyvinyl chloride.
Claims
exact text as granted — not AI-modified1 . A bipolar membrane in which a cation-exchange membrane and an anion-exchange membrane are joined to each other,
wherein a leakage ratio of gluconic acid at 60° C. is not more than 1.0%, and said cation-exchange membrane is supported by a polyolefin reinforcing member and, further, contains a polyvinyl chloride.
2 . The bipolar membrane according to claim 1 , wherein an area ratio of a portion where the cation-exchange membrane and the anion-exchange membrane are peeled off is not more than 20% after the bipolar membrane is dipped in a 6N sodium hydroxide aqueous solution of 25° C. for one hour and then in pure water of 25° C. for another one hour.
3 . The bipolar membrane according to claim 1 , wherein the cation-exchange membrane contains said polyvinyl chloride in an amount of 10 to 45% by mass.
4 . A method of producing a bipolar membrane including a step of forming a cation-exchange membrane, and a step of forming an anion-exchange membrane on the surface of said cation-exchange membrane; wherein
the step of forming said cation-exchange membrane includes: a step of impregnating a polyolefin reinforcing member with a polymerizable composition obtained by mixing a polyvinyl chloride (A) and a polymerization-curable component (B) that contains a monomer (b1) having a cation-exchange group or a monomer (b2) having a reaction group capable of introducing a cation-exchange group; and a step of forming a membrane of a cation-exchange resin that contains the polyvinyl chloride or of a cation-exchange resin precursor resin by polymerization-curing said polymerizable composition at a temperature of not lower than 100° C.; and, further, as required, a step of introducing a cation-exchange group into the cation-exchange resin precursor resin.
5 . The method of producing the bipolar membrane according to claim 4 , further including:
a step of impregnating a polyolefin reinforcing member with the polymerizable composition obtained by mixing the polyvinyl chloride (A) and the monomer (b1) having a cation-exchange group; and a step of forming a membrane of the cation-exchange resin that contains the polyvinyl chloride by the polymerization curing at a temperature of not lower than 100° C.
6 . The method of producing the bipolar membrane according to claim 4 , further including:
a step of impregnating a polyolefin reinforcing member with the polymerizable composition obtained by mixing the polyvinyl chloride (A) and the monomer (b2) having a reaction group capable of introducing a cation-exchange group; a step of forming the membrane of said cation-exchange resin precursor resin by the polymerization curing at a temperature of not lower than 100° C.; and a step of introducing a cation-exchange group by acting a cation-exchange group introducing agent upon said cation-exchange resin precursor resin.
7 . The method of producing the bipolar membrane according to claim 4 , wherein the step of forming the anion-exchange membrane on the surface of said cation-exchange membrane includes:
a step of applying a polar organic solvent solution of the anion-exchange resin on the surface of said cation-exchange membrane; and a step of removing the polar organic solvent.
8 . The method of producing the bipolar membrane according to claim 4 , wherein the step of forming the anion-exchange membrane on the surface of said cation-exchange membrane includes:
a step of applying, on the surface of said cation-exchange membrane, a polar organic solvent solution of an anion-exchange resin precursor resin having a reaction group capable of introducing the anion-exchange group; a step of forming a membrane of said anion-exchange resin precursor resin on the surface of said cation-exchange membrane by removing the polar organic solvent; and a step of introducing the anion-exchange group into said anion-exchange resin precursor resin.
9 . The method of producing the bipolar membrane according to claim 4 , wherein the step of forming the anion-exchange membrane on the surface of said cation-exchange membrane includes:
a step of applying, on the surface of said cation-exchange membrane, a polar organic solvent solution that contains an anion-exchange resin precursor resin having a reaction group capable of introducing the anion-exchange group and an anion-exchange group introducing agent; and a step of removing the polar organic solvent.Cited by (0)
No later patents cite this yet.
References (0)
No backward citations on record.