Four layer cation exchange fluoropolymer membrane

Claim 2

A cation exchange fluoropolymer membrane of high mechanical strength, having integrally laminated layers, consisting essentially of: (a) a main layer made of a perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 1.4 to 2.0 meq/g dry resin and having a thickness of from 50 to 250 μm; (b) a sulfonic acid film surface layer formed on one side of said main layer, made of a perfluorocarbon polymer having sulfonic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.5 meq/g dry resin and having a thickness of from 5 to 50 μm; (c) a carboxylic acid film surface layer formed on the other side of said main layer, made of a perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.3 meq/g dry resin and having a thickness of from 5 to 50 μm, said sulfonic acid film surface layer and carboxylic acid film surface layer constituting the outer-most layers, respectively; and (d) a composite film layer between said main layer and said sulfonic acid film surface layer, which integrally laminates said layers, said composite film layer being made of a perfluorocarbon polymer having both carboxylic acid and sulfonic acid groups and having a thickness of from 5 to 50 μm.

Claim 3

The cation exchange fluoropolymer membrane according to claim 1, wherein the composite film layer is made of a blend comprising a perfluorocarbon polymer having carboxylic acid groups as its ion exchange groups and a perfluorocarbon polynmer having sulfonic acid groups as its ion exchange groups.

Claim 4

The cation exchange fluoropolymer membrane according to claim 1, wherein the composite film layer is made of a blend comprising a perfluorocarbon polymer constituting the main layer and a perfluorocarbon polymer constituting the sulfonic acid film surface layer.

Claim 5

The cation exchange fluoropolymer membrane according to claim 1, wherein the composite film layer is made of a blend comprising 100 parts by weight of a perfluorocarbon polymer having carboxylic groups as its ion exchange groups and from 25 to 400 parts by weight of a perfluorocarbon polymer having sulfonic acid groups as its ion exchange groups.

Claim 6

An electrolytic cell having high current efficiency, which comprises anode and cathode compartments partitioned by a cation exchange fluoropolymer membrane of high mechanical strength, having integrally laminated layers, consisting essentially of: (a) a main layer made of a perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 1.4 to 2.0 meq/g dry resin and having a thickness of from 50 to 250 μm. (b) a sulfonic acid film surface layer formed on one side of said main layer, made of a perfluorocarbon polymer having sulfonic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.5 meq/g dry resin and having a thickness of from 5 to 50 μm, (c) a carboxylic acid film surface layer formed on the other side of said main layer, made of a perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.3 meq/g dry resin and having a thickness of from 5 to 50 μm, said sulfonic acid film surface layer and carboxylic acid film surface layer constituting the outer-most layers, respectively, and (d) a composite film layer between said main layer and said sulfonic acid film surface layer, to integrally laminate said layers, said composite film layer being made of a perfluorocarbon polymer having both carboxylic acid and sulfonic acid groups and having a thickness of from 5 to 50 μm.

Claim 7

An electrolytic cell having high current efficiency, which comprises anode and cathode compartments partitioned by a cation exchange fluoropolymer membrane of high mechanical strength, having integrally laminated layers, consisting essentially of: (a) a main layer made of a perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 1.4 to 2.0 meq/g dry resin and having a thickness of from 50 to 250 μm. (b) a sulfonic acid film surface layer formed on one side of said main layer, made of a perfluorocarbon polymer having sulfonic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.5 meq/g dry resin and having a thickness of from 5 to 50 μm, (c) a carboxylic acid film surface layer formed on the other side of said main layer, made of a perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.3 meq/g dry resin and having a thickness of from 5 to 50 μm, said sulfonic acid film surface layer and carboxylic acid film surface layer constituting the outer-most layers, respectively, and (d) a composite film layer between said main layer and said sulfonic acid film surface layer, to integrally laminate said layers, said composite film layer being made of a perfluorocarbon polymer having both carboxylic acid and sulfonic acid groups and having a thickness of from 5 to 50 μm.

Claim 8

The electrolytic cell according to claim 5, wherein the cation exchange fluoropolymer membrane is disposed so that the carboxylic acid film surface layer faces the cathode and the sulfonic acid film surface layer faces the anode.

Claim 9

The electrolytic cell according to claim 6, wherein an aqueous alkali metal chloride solution is electrolyzed to obtain an alkali metal hydroxide and chlorine.

Claim 10

An electrolytic process for the production of an alkali hydroxide an chlorine by the electrolysis of an alkali chloride, said produced alkali hydroxide having a low content of alkali chloride therein, which comprises electrolyzing an aqueous alkali metal chloride solution in an electrolytic cell at a temperature of from 80 to 120° C. and at a current density of from 10 to 100 A/dm 2 , while supplying a 2.5-5.0 N alkali metal chloride aqueous solution to the anode compartment and water or dilute alkali metal hydroxide aqueous solution to the cathode compartment, and wherein said electrolytic cell has high current efficiency and comprises anode and cathode compartments partitioned by a cation exchange fluoropolymer membrane of high mechanical strength, having integrally laminated layers, consisting essentially of: (a) a main layer made of perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 1.4 to 2.0 meq/g dry resin and having a thickness of from 50 to 250 μm, (b) a sulfonic acid film surface layer formed on one side of said main layer, made of a perfluorocarbon polymer having sulfonic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.5 meq/g dry resin and having a thickness of from 5 to 50 μm, (c) a carboxylic acid film surface layer formed on the other side of said main layer, made of a perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.3 meq/g dry resin and having a thickness of from 5 to 50 μm, said sulfonic acid film surface layer and carboxylic acid film surface layer constituting the outer-most layers, respectively, and (d) a composite film layer between said main layer and said sulfonic acid film surface layer, to integrally laminate said layers, said composite film layer being made of a perfluorocarbon polymer having both carboxylic acid and sulfonic acid groups and having a thickness of from 5 to 50 μm.

Claim 11

An electrolytic process for the production of an alkali hydroxide an chlorine by the electrolysis of an alkali chloride, said produced alkali hydroxide having a low content of alkali chloride therein, which comprises electrolyzing an aqueous alkali metal chloride solution in an electrolytic cell at a temperature of from 80 to 120° C. and at a current density of from 10 to 100 A/dm 2 , while supplying a 2.5-5.0 N alkali metal chloride aqueous solution to the anode compartment and water or dilute alkali metal hydroxide aqueous solution to the cathode compartment, and wherein said electrolytic cell has high current efficiency and comprises anode and cathode compartments partitioned by a cation exchange fluoropolymer membrane of high mechanical strength, having integrally laminated layers, consisting essentially of: (a) a main layer made of perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 1.4 to 2.0 meq/g dry resin and having a thickness of from 50 to 250 μm, (b) a sulfonic acid film surface layer formed on one side of said main layer, made of a perfluorocarbon polymer having sulfonic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.5 meq/g dry resin and having a thickness of from 5 to 50 μm, (c) a carboxylic acid film surface layer formed on the other side of said main layer, made of a perfluorocarbon polymer having carboxylic acid groups as ion exchange groups therefor with an ion exchange capacity of from 0.5 to 1.3 meq/g dry resin and having a thickness of from 5 to 50 μm, said sulfonic acid film surface layer and carboxylic acid film surface layer constituting the outer-most layers, respectively, and (d) a composite film layer between said main layer and said sulfonic acid film surface layer, to integrally laminate said layers, said composite film layer being made of a perfluorocarbon polymer having both carboxylic acid and sulfonic acid groups and having a thickness of from 5 to 50 μm.

Claim 12

The cation exchange fluoropolymer membrane according to claim 1, wherein said main layer of perfluorocarbon polymer has an ion exchange capacity of from 1.4 to 1.9 meq/g dry resin and has a thickness of from 100 to 200 μm.

Claim 13

The cation exchange fluoropolymer membrane according to claim 1, wherein said main layer has a thickness which is at least one-half of the total membrane thickness.

Claim 14

The cation exchange fluoropolymer membrane according to claim 25, wherein said carboxylic acid film surface layer has an ion-exchange capacity of from 0.8 to 1.3 meq/g dry resin and has a thickness of from 10 to 40 μm.

Claim 15

The cation exchange fluoropolymer membrane according to claim 1, wherein said sulfonic acid film surface layer has an ion-exchange capacity of from 0.8 to 1.3 meq/g dry resin and has a thickness of from 10 to 40 μm.

Claim 16

The cation exchange fluoropolymer membrane according to claim 1, wherein said perfluorocarbon polymers are selected from the group consisting of ##STR4## pps wherein X is F or --CF 3 , and Y is selected from the group consisting of: ##STR5## wherein each of x, y and z is from 0 to 10, and each of Z and R f is --F or a perfluoroalkyl group having from 1 to 10 carbon atoms, A is --SO 3 M or --COOM, or a group capable of being converted to one of these groups by hydrolysis and selected from th group consisting of --SO 2 F, --CN, --COF and --COOR, wherein M is H or an alkali metal, and R is an alkyl group having from 1 to 10 carbon atoms.

Claim 17

The cation exchange fluoropolymer membrane according to claim 1, wherein said membrane has a total thickness of from 60 to 350 μm.

Claim 18

The cation exchange fluoropolymer membrane according to claim 1, which further comprises either a reinforcing woven fabric of a cloth or a net, or a non-woven fabric of metallic mesh, perforated sheet or polytetrafluoroethylene.

Claim 19

The electrolytic cell according to claim 5, wherein said anode is made of a platinum group metal or an electro-conductive oxide or electro-conductive reduced oxide thereof.

Claim 20

The electrolytic cell according to claim 16, wherein said metal is selected from the group consisting of platinum, rhodium, ruthenium, palladium and iridium.

Claim 21

The electrolytic cell according to claim 5, wherein said cathode is made of a platinum group metal, an electro-conductive oxide thereof, or an iron group metal.

Claim 22

THe electrolytic cell according to claim 18, wherein said platinum group metal is selected from the group consisting of platinum, rhodium, ruthenium, palladium an iridium; and said iron group metal is selected from the group consisting of iron, cobalt, nickel, Raney nickel, stabilized Raney nickel, stainless steel, and alkali-etching stainless steel.