Electrodialysis for aqueous solution of base

Claim 2

In an electrodialysis process for aqueous base-containing solutions the improvement which comprises using a sulfonic acid group-free cation-exchange membrane which is a copolymer of ethylene and an unsaturated carboxylic acid or a salt thereof having an ion-exchange capacity of 0.7 to 3 m equivalent/g (dry resin).

Claim 3

The electrodialysis process of claim 1 which is an electrolytic dialysis.

Claim 4

The electrodialysis process of claim 1, where the aqueous base-containing solution is an aqueous solution of alkali metal hydroxide, ammonia or an amine.

Claim 5

The electrodialysis process of claim 1, wherein the cation-exchange membrane is made of copolymer of ethylene and an unsaturated carboxylic acid or salt thereof wherein the unsaturated carboxylic acid is acrylic acid, methacrylic acid, itaconic acid, maleic acid, fumaric acid or a precursor thereof, and a molar ratio of the unsaturated carboxylic acid to ethylene is in a range of 0.02 to 0.15.

Claim 6

The electrodialysis process of claim 1, wherein the copolymer of ethylene and an unsaturated carboxylic acid or salt thereof has units having the formula ##STR2## wherein X represents hydrogen or methyl; Y represents hydrogen or a metal atom; m/l (molar ratio) is 0.02 to 0.15 and n is 0 to 10.

Claim 7

The electrodialysis process of claim 5, wherein the copolymer has the unit formula in which Y is H, Na or Zn; and m/l (molar ratio) is 0.03 to 0.12

Claim 8

The electrodialysis process of claim 1, wherein the cation-exchange membranes of the copolymer and anion-exchange membranes are alternatively arranged between an anode and a cathode to form a diluting compartment partitioned with the cation-exchange membrane in the cathode side and the anion-exchange membrane in the anode side and an ajacent concentrating compartment partitioned with the anion-exchange membrane in the cathode side and the cation-exchange membrane in the anode side; and the aqueous base-containing solution is fed to the diluting compartment and the concentrated aqueous base-containing solution is obtained from the concentrating compartment.

Claim 9

The electrodialysis process of claim 2 which is electrolytic dialysis, wherein an anolyte compartment and a catholyte compartment are formed by partition between an anode and a cathode with the cation-exchange membrane of the copolymer and an alkali chloride aqueous solution is fed to the anolyte compartment and the electrolysis is conducted by applying the current to obtain alkali hydroxide from the catholyte compartment.

Claim 10

The electrodialysis process of claim 8, wherein a diaphragm having high oxidation and chlorine resistance is disposed between the anode and the cation-exchange membrane.

Claim 11

The electrodialysis process of claim 9, wherein the diaphragm is a fluorine-containing cation-exchange membrane of a copolymer of tetrafluoroethylene and a sulfonated or carboxylated perfluorovinyl ether.

Claim 12

The electrodialysis process of claim 1, wherein the cation-exchange membrane of the copolymer is reinforced with a support

Claim 13

The electrodialysis process of claim 1, wherein the cation-exchange membrane is made of the copolymer of ethylene and an unsaturated carboxylic acid or salt thereof, which copolymer has a glass transition temperature of at least 20° C below the temperature for the electrodialysis.