Production method for fluorinated cation exchange membrane
US-2016279627-A1 · Sep 29, 2016 · US
US10865282B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10865282-B2 |
| Application number | US-201816219100-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 13, 2018 |
| Priority date | Dec 18, 2017 |
| Publication date | Dec 15, 2020 |
| Grant date | Dec 15, 2020 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
An ion exchange membrane includes: a membrane main body including a fluorine-containing polymer having an ion exchange group; and a coating layer arranged on at least one face of the membrane main body; wherein the coating layer includes inorganic particles and a binder, a mass ratio of the binder to the total mass of the inorganic particles and the binder in the coating layer is more than 0.3 and 0.9 or less, and a surface roughness of the coating layer is 1.20 μm or more.
Opening claim text (preview).
The invention claimed is: 1. An ion exchange membrane comprising: a membrane main body comprising a fluorine-containing polymer having an ion exchange group; and a coating layer arranged on at least one face of the membrane main body; wherein the coating layer comprises inorganic particles and a binder, wherein the average particle size of the inorganic particles is 0.90 μm or more and 2 μm or less, and a mass ratio of the binder to a total mass of the inorganic particles and binder in the coating layer is more than 0.3 and 0.9 or less, and a surface roughness of the coating layer is 1.20 μm or more. 2. The ion exchange membrane according to claim 1 , wherein the inorganic particles are particles comprising at least one mineral selected from the group consisting of oxides of Periodic Table Group IV elements, nitrides of Periodic Table Group IV elements, and carbides of Periodic Table Group IV elements. 3. The ion exchange membrane according to claim 1 , wherein the inorganic particles are particles of zirconium oxide. 4. The ion exchange membrane according to claim 1 , wherein the membrane main body comprises: a layer S comprising a fluorine-containing polymer having a sulfonic acid group; a layer C comprising a fluorine-containing polymer having a carboxylic acid group; and a plurality of strengthening materials arranged inside the layer S and functioning as at least one of reinforcement yarn and sacrifice yarn; wherein A and B, both of which are defined below, satisfy following formula (1): 2.0≤B/A≤5.0 (1) wherein, when the ion exchange membrane is viewed from a top surface, A represents an average cross-sectional thickness of the membrane measured in pure water for a region, in which the strengthening materials do not exist, and B represents an average cross-sectional thickness of the membrane measured in pure water for a region, in which strands of the reinforcement yarn overlap with each other, and for a region, in which the reinforcement yarn overlaps with the sacrifice yarn. 5. A method for producing the ion exchange membrane according to claim 1 , comprising spraying a coating solution comprising inorganic particles, a binder, and a solvent by a spray system, followed by drying thereof to form a coating layer on a surface of the membrane main body, wherein an average droplet size during the spraying is 100 μm or less. 6. The method for producing the ion exchange membrane according to claim 5 , wherein a surface temperature of the membrane main body during the drying is 40° C. or more and equal to or less than a boiling point of the solvent. 7. A method of using the ion exchange membrane according to claim 1 , comprising using the ion exchange membrane in an electrolyzer.
Three or more layers · CPC title
Laminated layers · CPC title
Coextruded layers · CPC title
Oxides · CPC title
with diaphragms · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.