Electrolysis cell and electrolysis tank
US-9506157-B2 · Nov 29, 2016 · US
US10385465B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10385465-B2 |
| Application number | US-201815908999-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 1, 2018 |
| Priority date | Sep 8, 2015 |
| Publication date | Aug 20, 2019 |
| Grant date | Aug 20, 2019 |
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To provide a method capable of efficiently producing an ion exchange membrane for alkali chloride electrolysis which has high current efficiency, little variation in current efficiency and high alkaline resistance. This is a method for producing an ion exchange membrane 1 having a layer (C) 12 containing a fluorinated polymer (A) having carboxylic acid type functional groups, by immersing an ion exchange membrane precursor film having a precursor layer (C′) containing a fluorinated polymer (A′) having groups convertible to carboxylic acid type functional groups, in an aqueous alkaline solution comprising an alkali metal hydroxide, a water-soluble organic solvent and water, wherein the proportion of structural units having carboxylic acid type functional groups in the fluorinated polymer (A) is from 13.0 to 14.50 mol %; in the layer (C) 12, the value of resistivity is from 4.0×103 to 25.0×103 Ω·cm, and the variation in resistivity is at most 4.0×103 Ω·cm, and the concentration of the water-soluble organic solvent is from 1 to 60 mass % in the alkaline aqueous solution.
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What is claimed is: 1. A production method for an ion exchange membrane for alkali chloride electrolysis, which is a method for producing an ion exchange membrane for alkali chloride electrolysis having a layer containing a fluorinated polymer having carboxylic acid type functional groups, by immersing an ion exchange membrane precursor film having a precursor layer containing a fluorinated polymer having groups convertible to carboxylic acid type functional groups, in an alkaline aqueous solution containing an alkali metal hydroxide, a water-soluble organic solvent and water, and subjecting the groups convertible to carboxylic acid type functional groups to hydrolysis treatment to convert them to carboxylic acid type functional groups, wherein the proportion of structural units having the carboxylic acid type functional groups in the fluorinated polymer having the carboxylic acid type functional groups, is from 13.10 to 14.50 mol %, in all structural units (100 mol %) in the fluorinated polymer having the carboxylic acid type functional groups, in the layer containing a fluorinated polymer having carboxylic acid type functional groups, the following value of resistivity is from 4.0×10 3 to 25.0×10 3 Ω·cm, and the following variation in resistivity is at most 4.0×10 3 Ω·cm, and the concentration of the water-soluble organic solvent is from 1 to 60 mass % in the alkaline aqueous solution (100 mass %): Value of resistivity and variation in resistivity: Five points in the ion exchange membrane for alkali chloride electrolysis are randomly selected; at the respective points, the resistivity in the layer containing a fluorinated polymer having carboxylic acid type functional groups is measured; and the average value of the resistivity at the 5 points in the ion exchange membrane for alkali chloride electrolysis is taken as the value of the resistivity, and further, the value twice the standard deviation in the resistivity at the 5 points in the ion exchange membrane for alkali chloride electrolysis is taken as the variation in the resistivity. 2. The production method for an ion exchange membrane for alkali chloride electrolysis according to claim 1 , wherein the concentration of the water-soluble organic solvent is from 5 to 50 mass % in the alkaline aqueous solution (100 mass %). 3. The production method for an ion exchange membrane for alkali chloride electrolysis according to claim 1 , wherein the concentration of the alkali metal hydroxide is from 1 to 60 mass % in the alkaline aqueous solution (100 mass %). 4. The production method for an ion exchange membrane for alkali chloride electrolysis according to claim 1 , wherein the concentration of the alkali metal hydroxide is from 5 to 50 mass % in the alkaline aqueous solution (100 mass %). 5. The production method for an ion exchange membrane for alkali chloride electrolysis according to claim 1 , wherein the alkali metal hydroxide is sodium hydroxide or potassium hydroxide. 6. The production method for an ion exchange membrane for alkali chloride electrolysis according to claim 1 , wherein the water-soluble organic solvent is at least one member selected from the group consisting of aprotic water-soluble organic solvents, alcohols and aminoalcohols. 7. The production method for an ion exchange membrane for alkali chloride electrolysis according to claim 6 , wherein the water-soluble organic solvent is at least one member selected from the group consisting of dimethyl sulfoxide, methyl alcohol, ethyl alcohol, propyl alcohol, 1-methoxy-2-propanol, triethanolamine, diethanolamine, isopropanolamine, triisopropanolamine, dimethylaminoethanol and diethylaminoethanol. 8. The production method for an ion exchange membrane for alkali chloride electrolysis according to claim 1 , which is a method for producing an ion exchange membrane for alkali chloride electrolysis further having a layer containing a fluorinated polymer having sulfonic acid type functional groups, wherein the ion exchange membrane precursor film further has a precursor layer containing a fluorinated polymer having groups convertible to sulfonic acid type functional groups, the ion exchange membrane precursor film is immersed in the alkaline aqueous solution, and the groups convertible to carboxylic acid type functional groups are subjected to hydrolysis treatment and converted to carboxylic acid type functional groups, and at the same time, the groups convertible to sulfonic acid type functional groups are subjected to hydrolysis treatment and converted to sulfonic acid type functional groups. 9. The production method for an ion exchange membrane for alkali chloride electrolysis according to claim 1 , wherein the ion exchange membrane for alkali chloride electrolysis further has a layer comprising inorganic particles and a binder, on at least one outermost layer. 10. A production method for an alkali chloride electrolysis apparatus, which comprises mounting an ion exchange membrane for alkali chloride electrolysis obtained by the production method for an ion exchange membrane for alkali chloride electrolysis as defined in claim 1 , in an electrolytic cell comprising a cathode and an anode, so as to partition the inside of the electrolytic cell into a cathode chamber on the cathode side and an anode chamber on the anode side.
Films, membranes or diaphragms · CPC title
in diaphragm cells · CPC title
Tetrafluoroethene · CPC title
containing fluorine · CPC title
based on organic materials · CPC title
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