Production method for fluorinated cation exchange membrane

Patent metadata

Field	Value
Publication number	US-11273435-B2
Application number	US-201615173916-A
Country	US
Kind code	B2
Filing date	Jun 6, 2016
Priority date	Dec 25, 2013
Publication date	Mar 15, 2022
Grant date	Mar 15, 2022

Abstract

To provide a method for producing a fluorinated cation exchange membrane, by which a fluorinated cation exchange membrane having a high effect to suppress attachment of the gas to the surface on the cathode side and having an excellent resistance to dropping of inorganic particles from a gas-releasing layer provided on the cathode side can be obtained.A method for producing a fluorinated cation exchange membrane 1 for electrolysis comprising, on at least the cathode side, a layer (α1) 12 containing a perfluorocarbon polymer (A) having carboxylic acid groups or precursor groups of carboxylic acid groups, and a gas-releasing layer (α2) 10 provided on the cathode side of the layer (α1) 12, which comprises applying to the surface of the layer (α1) 12 a coating liquid containing inorganic particles having an average secondary particle size of from 0.5 to 1.5 μm, a binder and a dispersion medium in a mass ratio of the binder to the total mass of the inorganic particles and the binder of from 0.15 to 0.3, to form the gas-releasing layer (α2) 10.

First claim

What is claimed is:

1. A method for producing a fluorinated cation exchange membrane for electrolysis comprising a layer (α1) containing a perfluorocarbon polymer (A) having a carboxylic acid group or a precursor group of a carboxylic acid group, and a gas-releasing layer (α2) provided on a cathode-facing side of the layer (α1), the method comprising:
applying to the cathode-facing side of the layer (α1) a coating liquid consisting of inorganic particles, a binder and a dispersion medium to form the gas-releasing layer (α2),
wherein a mass ratio of the binder to a total mass of the inorganic particles and the binder in the coating liquid is from 0.16 to 0.25,
the inorganic particles have an average primary particle size of from 0.02 to 0.4 μm and an average secondary particle size of from 0.5 to 1.5 μm,
the binder is a fluorinated polymer (C) having sulfonic acid groups, and
the dispersion medium is an alcohol and is free of an aprotic polar solvent.

2. The method according to claim 1 , wherein the inorganic particles are particles of at least one member selected from the group consisting of an oxide, nitride and carbide of a Group 4 element or Group 14 element.

3. The method according to claim 1 , wherein the inorganic particles are particles of SiO 2 , SiC, ZrO 2 or ZrC.

4. The method according to claim 1 , wherein the inorganic particles have the average primary particle size of 0.4 μm.

5. The method according to claim 4 , wherein the inorganic particles are particles of ZrO 2 .

6. The method according to claim 1 , wherein the perfluorocarbon polymer (A) is a copolymer having structural units derived from the monomer (1) and structural units derived from the monomer (2):
CF 2 ═CX 1 X 2   (1)

CF 2 ═CF(OCF 2 CFX 3 ) n O(CF 2 ) m Y  (2)

wherein, in the formula (1), each of X 1 and X 2 which are independent of each other, is a fluorine atom, a chlorine atom or a trifluoromethyl group, and in the formula (2), X 3 is a fluorine atom or a trifluoromethyl group, m is an integer of from 1 to 5, n is 0 or 1, and Y is a precursor group capable of being converted into a carboxylic acid group by hydrolysis.

7. The method according to claim 1 , wherein the layer (α1) has an ion exchange capacity of from 0.7 to 1.1 meq/g dry resin.

8. The method according to claim 1 , wherein the inorganic particles are particles of ZrO 2 .

9. The method according to claim 1 ,
wherein the inorganic particles are particles of SiO 2 , SiC, ZrO 2 or ZrC, and
the inorganic particles have the average secondary particle size of from 0.7 to 1.3 μm.

10. The method according to claim 1 ,
wherein the inorganic particles are particles of ZrO 2 , and
the inorganic particles have the average secondary particle size of from 0.7 to 1.3 μm.

11. The method according to claim 1 , wherein the dispersion medium consists of an alcohol.

12. The method according to claim 1 , wherein the alcohol comprises ethanol, isopropyl alcohol, or both.

13. The method according to claim 1 , wherein the gas-releasing layer (α2) is formed by a method consisting of the applying of the coating liquid to the cathode-facing side of the layer (α1) and then removing the dispersion medium in the coating liquid.

14. The method according to claim 1 , wherein the fluorinated cation exchange membrane further comprises a layer (β1) containing a perfluorocarbon polymer (B) having a sulfonic acid group or a precursor group of a sulfonic acid group on an anode-facing side of the layer (α1).

15. The method according to claim 14 , wherein the fluorinated cation exchange membrane further comprises a gas-releasing layer (β2) provided on an anode-facing side of the layer (β1).

16. The method according to claim 14 , wherein the perfluorocarbon polymer (B) is a copolymer having structural units derived from the monomer (1) and structural units derived from the monomer (3):
CF 2 ═CX 1 X 2   (1)

CF 2 ═CF(OCF 2 CFX 4 ) s O(CF 2 ) t W  (3)

wherein, in the formula (1), each of X 1 and X 2 which are independent of each other, is a fluorine atom, a chlorine atom or a trifluoromethyl group, and in the formula (3), X 4 is a fluorine atom or a trifluoromethyl group, s is an integer of from 1 to 3, t is 0, 1 or 2, and W is a precursor group capable of being converted into a sulfonic acid group by hydrolysis.

17. The method according to claim 14 , wherein the layer (β1) has an ion exchange capacity of from 0.9 to 1.15 meq/g dry resin.

18. The method according to claim 15 , comprising:
laminating the gas-releasing layer (β2), the layer (β1) and the layer (α1) in this order to obtain a composite membrane;
when the composite membrane has precursor groups of carboxylic acid groups and/or precursor groups of sulfonic acid groups, hydrolyzing and converting the precursor groups of carboxylic acid groups and/or the precursor groups of sulfonic acid groups into carboxylic acid groups and/or sulfonic acid groups; and
after the coating liquid is applied to the cathode-facing side of the layer (α1), removing the dispersion medium by heating to form the gas-releasing layer (α2).

19. A method for producing a fluorinated cation exchange membrane for electrolysis comprising a layer (α1) containing a perfluorocarbon polymer (A) having a carboxylic acid group or a precursor group of a carboxylic acid group, and a gas-releasing layer (α2) provided on a cathode-facing side of the layer (α1), the method comprising:
applying to the cathode-facing side of the layer (α1) a coating liquid consisting of inorganic particles, a binder and a dispersion medium to form the gas-releasing layer (α2),
wherein a mass ratio of the binder to a total mass of the inorganic particles and the binder in the coating liquid is from 0.15 to 0.3,
the inorganic particles have an average primary particle size of from 0.02 to 0.4 μm and an average secondary particle size of from 0.5 to 1.5 μm,
the binder is a fluorinated polymer (C) having sulfonic acid groups, and
the dispersion medium is an alcohol and is free of an aprotic polar solvent.

Assignees

• Agc Inc

Inventors

• Kusano Hiromitsu
• Kaneko Takayuki

Classifications

• C25B13/07

  based on ceramics · CPC title

• B01J39/20 Primary

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

• C25B13/08

  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

• C25B13/02

  characterised by shape or form · CPC title