Ion exchange membrane for alkali chloride electrolysis, method for its production and alkali chloride electrolysis apparatus

Patent metadata

Field	Value
Publication number	US-10669641-B2
Application number	US-201816156320-A
Country	US
Kind code	B2
Filing date	Oct 10, 2018
Priority date	Apr 13, 2016
Publication date	Jun 2, 2020
Grant date	Jun 2, 2020

Abstract

To provide an ion exchange membrane for alkali chloride electrolysis whereby it is possible to make the electrolysis voltage low and the current efficiency high at the time of performing electrolysis of an alkali chloride; a method for its production; and an alkali chloride electrolysis apparatus using it. The ion exchange membrane for alkali chloride electrolysis has a layer (C) comprising a fluorinated polymer having carbonic acid functional groups, and a layer (S) comprising a fluorinated polymer having sulfonic acid functional groups; a reinforcing material containing reinforcing threads is disposed in the layer (S); and when measured after the ion exchange membrane for alkali chloride electrolysis is immersed and held in a 32 mass % sodium hydroxide aqueous solution warmed at 90° C. for 16 hours and subsequently immersed in a 32 mass % sodium hydroxide aqueous solution at 25° C. for 3 hours, the AC resistance value A of the layer (S) and the AC resistance value B of the layer (C) satisfy the following formulae at the same time: 1(Ω·cm2)≤A≤10(Ω·cm2) and 200(Ω·cm2)≤B≤450(Ω·cm2).

First claim

What is claimed is:

1. An ion exchange membrane for alkali chloride electrolysis, having a layer (C) comprising a fluorinated polymer having carboxylic acid functional groups, and a layer (S) comprising a fluorinated polymer having sulfonic acid functional groups, wherein a reinforcing material comprising reinforcing threads is disposed in the layer (S), and when measured after the ion exchange membrane for alkali chloride electrolysis is immersed and held in a 32 mass % sodium hydroxide aqueous solution warmed at 90° C. for 16 hours and subsequently immersed in a 32 mass % sodium hydroxide aqueous solution at 25° C. for 3 hours, the AC resistance value A of said layer (S) and the AC resistance value B of said layer (C) satisfy the following formulae at the same time,
1(Ω·cm 2 )≤ A≤ 10(Ω·cm 2 )

170(Ω·cm 2 )≤ B≤ 550(Ω·cm 2 ).

2. The ion exchange membrane for alkali chloride electrolysis according to claim 1 , wherein the ratio (A/B) of the AC resistance value A to the AC resistance value B satisfies the following formula,
A/B≤ 0.03.

3. The ion exchange membrane for alkali chloride electrolysis according to claim 1 , wherein the thickness when dried of the layer (C) is from 1 to 50 μm, and the thickness when dried of the layer (S) is from 30 to 200 μm.

4. The ion exchange membrane for alkali chloride electrolysis according to claim 1 , wherein at least a part of the fluorinated polymer having sulfonic acid functional groups constituting the layer (S) is a polymer having structural units represented by the following formula (U1),

wherein Q 1 is a perfluoroalkylene group which optionally have an etheric oxygen atom, Q 2 is a single bond or a perfluoroalkylene group which optionally have an etheric oxygen atom, R f1 is a perfluoroalkyl group which optionally have an etheric oxygen atom, X 1 is an oxygen atom, a nitrogen atom or a carbon atom, when X 1 is an oxygen atom, a is 0, when X 1 is a nitrogen atom, a is 1, when X 1 is a carbon atom, a is 2, Y 1 is a fluorine atom or a monovalent perfluoro organic group, r is 0 or 1, and M is a hydrogen atom, an alkali metal or a quaternary ammonium base.

5. The ion exchange membrane for alkali chloride electrolysis according to claim 4 , wherein the structural units represented by the formula (U1) are structural units based on a monomer represented by the formula (m1),

wherein R F11 is a single bond or a C 1-6 linear perfluoroalkylene group which may have an etheric oxygen atom, and R F12 is a C 1-6 linear perfluoroalkylene group.

6. The ion exchange membrane for alkali chloride electrolysis according to claim 1 , which further has an inorganic particle layer comprising inorganic particles and a binder, on at least one of the outermost surfaces.

7. A method for producing the ion exchange membrane for alkali chloride electrolysis as according to claim 1 , comprising
a step of obtaining a reinforced precursor membrane having a precursor layer (C′) comprising a fluorinated polymer having groups convertible to carboxylic acid functional groups, a precursor layer (S′) comprising a fluorinated polymer having groups convertible to sulfonic acid functional groups, and a reinforcing material comprising reinforcing threads, disposed in the precursor layer (S′), and
a step of obtaining said ion exchange membrane for alkali chloride electrolysis by contacting the reinforced precursor membrane and an aqueous alkaline solution to convert the groups convertible to carboxylic acid functional groups in the precursor layer (C′) to the carboxylic acid functional groups thereby to form said layer (C), and to convert the groups convertible to sulfonic acid functional groups in the precursor layer (S′) to the sulfonic acid functional groups thereby to form said layer (S).

8. The method for producing the ion exchange membrane for alkali chloride electrolysis according to claim 7 , wherein in the step of obtaining said ion exchange membrane for alkali chloride electrolysis,
as the aqueous alkaline solution, a first aqueous alkaline solution and a second aqueous alkaline solution different from the first aqueous alkaline solution in at least one of the composition and the temperature, are prepared, and
the precursor layer (C′) is brought in contact with the first aqueous alkaline solution, and the precursor layer (S′) is brought in contact with the second aqueous alkaline solution.

9. The method for producing the ion exchange membrane for alkali chloride electrolysis according to claim 8 , wherein the first aqueous alkaline solution comprises an alkali metal hydroxide, a water-soluble organic solvent and water, and in the above first aqueous alkaline solution (100 mass %), the concentration of the alkali metal hydroxide is from 1 to 60 mass %, and the concentration of the water-soluble organic solvent is from 1 to 60 mass %; and the second aqueous alkaline solution comprises an alkali metal hydroxide, a water-soluble organic solvent and water, and in the above second aqueous alkaline solution (100 mass %), the concentration of the alkali metal hydroxide is from 1 to 60 mass %, and the concentration of the water-soluble organic solvent is from 1 to 60 mass %.

10. The method for producing the ion exchange membrane for alkali chloride electrolysis according to claim 8 , wherein the temperature of the first aqueous alkaline solution is from 30 to 95° C., and the temperature of the second aqueous alkaline solution is from 30 to 95° C.

11. The method for producing the ion exchange membrane for alkali chloride electrolysis according to claim 9 , wherein the alkali metal hydroxide is sodium hydroxide or potassium hydroxide.

12. The method for producing the ion exchange membrane for alkali chloride electrolysis according to claim 9 , wherein the water-soluble organic solvent contains at least one member selected from the group consisting of aprotic organic solvents, alcohols and amino alcohols.

Assignees

• Agc Inc

Inventors

• Yamaki Yasushi
• Kaneko Takayuki
• Kusano Hiromitsu
• Nishio Takuo

Classifications

• B01J39/07

  in the weakly acidic form · CPC title

• B01J39/20

  obtained by reactions only involving unsaturated carbon-to-carbon bonds · CPC title

• B01J39/05

  in the strongly acidic form · CPC title

• C25B13/08 Primary

  based on organic materials · CPC title

• B01J47/12

  characterised by the use of ion-exchange material in the form of ribbons, filaments, fibres or sheets, e.g. membranes (electrodialysis or electro-osmosis B01D61/42) · CPC title