Acid gas separation membrane and acid gas separation method using same, acid gas separation module, and acid gas separation apparatus
US-2019111382-A1 · Apr 18, 2019 · US
US11045761B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11045761-B2 |
| Application number | US-201916643228-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 13, 2019 |
| Priority date | Aug 31, 2018 |
| Publication date | Jun 29, 2021 |
| Grant date | Jun 29, 2021 |
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A separation membrane sheet that causes a specific fluid component to selectively permeate therethrough, comprises: a first porous layer; and a resin composition layer formed on the first porous layer. The resin composition layer has a filtration residue fraction of greater than or equal to 20% and less than or equal to 90%; and contains a resin having an ionic group or a salt thereof, and has an ion exchange capacity of greater than or equal to 1 millimole equivalent per 1 g of a dry resin in a filtration residue.
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The invention claimed is: 1. A separation membrane sheet that causes an acidic gas component to selectively permeate therethrough, the separation membrane sheet comprising: a first porous layer; and a resin composition layer formed on the first porous layer, wherein: the resin composition layer has a filtration residue fraction of greater than or equal to 20% and less than or equal to 90%; and contains a resin having an ionic group or a salt thereof, and has an ion exchange capacity of greater than or equal to 1 millimole equivalent per 1 g of a dry resin in a filtration residue. 2. The separation membrane sheet according to claim 1 , further comprising a second porous layer. 3. The separation membrane sheet according to claim 2 , wherein the second porous layer is laminated on an opposite side of the resin composition layer from the first porous layer. 4. The separation membrane sheet according to claim 1 , wherein the ionic group is an ionic group exhibiting acidity. 5. The separation membrane sheet according to claim 4 , wherein the ionic group exhibiting acidity is a carboxyl group. 6. The separation membrane sheet according to claim 1 , wherein the resin composition layer further contains a substance that reversibly reacts with an acidic gas. 7. The separation membrane element comprising the separation membrane sheet according to claim 1 . 8. A separation membrane element, comprising: a perforated central tube; and an element-use laminated body including the separation membrane sheet according to claim 1 , wherein the element-use laminated body is wound around the perforated central tube. 9. A separation membrane module comprising: at least one separation membrane element according to claim 7 ; a source fluid feeding port for feeding a source fluid to the separation membrane sheet; a retentate fluid discharge port for discharging a source fluid that has not permeated through the separation membrane sheet; and a permeate fluid discharge port for discharging the acidic gas that has permeated through the separation membrane sheet. 10. The separation device comprising at least one separation membrane module according to claim 9 . 11. A hydrogen production device comprising at least one separation membrane module according to claim 9 , wherein: the source fluid is a source gas containing hydrogen and carbon dioxide; and the acidic gas contains carbon dioxide. 12. A manufacturing method for a separation membrane sheet that causes an acidic gas to selectively permeate therethrough, the method comprising forming a resin composition layer on a first porous layer, wherein the forming the resin composition layer comprises irradiating an application layer formed on the first porous layer with an electron beam having an irradiation amount of greater than or equal to 10 kGy and less than 1000 kGy; and the resin composition layer has a filtration residue fraction of greater than or equal to 20% and less than or equal to 90%, and the resin composition layer comprises a resin having an ionic group or a salt thereof, and an ionic exchange capacity of greater than or equal to 1 millimole equivalent per 1 g of a dry resin in a filtration residue. 13. The method of claim 12 , wherein: the forming the resin composition layer further comprises obtaining a laminated body by laminating a second porous layer on an opposite side of the application layer from the first porous layer; and irradiating the application layer with the electron beam is a process of irradiating the application layer of the laminated body with an electron beam. 14. The method of claim 12 , wherein the ionic group is an ionic group exhibiting acidity. 15. The method of claim 14 , wherein the ionic group exhibiting acidity is a carboxyl group. 16. The method of claim 12 , wherein the application layer contains a non-crosslinked polymer. 17. The method of claim 16 , wherein the application layer further contains a crosslinked polymer. 18. The method of claim 12 , wherein acidic gas is carbon dioxide and the application layer further comprises at least one compound selected from the group consisting of alkali metal carbonates, alkali metal bicarbonates, alkanolamine, and alkali metal hydroxides. 19. The method of claim 12 , wherein the irradiation amount of the electron beam with which the application layer is irradiated is adjusted by at least one of the number of irradiations and irradiation time of the electron beam. 20. The method of claim 12 , wherein the acidic gas is sulfur oxide and the application layer further comprises at least one compound selected from the group consisting of sulfur-containing compounds, citrates of alkali metals, and transition metal complexes. 21. The method of claim 12 , wherein the acidic gas is nitrogen oxide and the application layer further comprises at least one compound selected from the group consisting of alkali metal nitrites and transition metal complexes.
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