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Disclosed are a pressure swing adsorption apparatus for hydrogen purification and a hydrogen purification method using the same. The pressure swing adsorption apparatus for hydrogen purification includes a plurality of adsorption columns connected with a feed supply pipe, a hydrogen storage tank for

Disclosed are a pressure swing adsorption apparatus for hydrogen purification and a hydrogen purification method using the same. The pressure swing adsorption apparatus for hydrogen purification includes a plurality of adsorption columns connected with a feed supply pipe, a hydrogen storage tank for collecting purified hydrogen from the adsorption columns, and valves for opening or closing a plurality of pipes connected to the respective adsorption columns, and the adsorption columns are packed with adsorbent beds of active alumina or silica gel, activated carbon, zeolite 13X, zeolite 5A, and a carbon monoxide-selective adsorbent other than the zeolite 5A, in order to remove carbon dioxide, methane, and carbon monoxide from a hydrogen-containing gas mixture supplied through the feed supply pipe, and the content of carbon monoxide in the discharged hydrogen is minimized through sequential adsorption on the adsorbents in the adsorption columns. The content of carbon monoxide in the purified hydrogen product can be decreased to 10 ppm or less, thus facilitating the production of highly pure hydrogen products.

대표청구항 ▼

1. A pressure swing adsorption apparatus, comprising a plurality of adsorption columns connected with a feed supply pipe, a hydrogen storage tank for collecting purified hydrogen from the adsorption columns, and valves for opening or closing a plurality of pipes respectively connected to the adsorpt

1. A pressure swing adsorption apparatus, comprising a plurality of adsorption columns connected with a feed supply pipe, a hydrogen storage tank for collecting purified hydrogen from the adsorption columns, and valves for opening or closing a plurality of pipes respectively connected to the adsorption columns, wherein the adsorption columns are packed with adsorbent beds of active alumina or silica gel, activated carbon, zeolite 13X, zeolite 5A, and a carbon monoxide-selective adsorbent other than the zeolite 5A, in order to remove water, carbon dioxide, methane, and carbon monoxide from a hydrogen-containing gas mixture supplied through the feed supply pipe, and a content of carbon monoxide in hydrogen that is discharged is minimized through sequential adsorption on the adsorbents in the adsorption columns. 2. The apparatus according to claim 1, wherein the adsorption columns are constructed such that at least two adsorption columns are disposed parallel to each other to continuously produce a highly pure hydrogen product. 3. The apparatus according to claim 1, wherein the adsorbents in the adsorption columns comprise active alumina or silica gel, activated carbon, zeolite 13X, zeolite 5A, and a carbon monoxide-selective adsorbent other than the zeolite 5A, which are sequentially disposed upward. 4. The apparatus according to claim 1, wherein the adsorbents in the adsorption columns comprise active alumina or silica gel, activated carbon, zeolite 13X, zeolite 5A, and a carbon monoxide-selective adsorbent other than the zeolite 5A, which are sequentially disposed upward. 5. The apparatus according to claim 3, wherein a portion of the zeolite 5A, which is one of the adsorbents, is replaced with the carbon monoxide-selective adsorbent other than the zeolite 5A. 6. The apparatus according to claim 3, wherein 1-100% of the activated carbon, which is one of the adsorbents, is replaced with zeolite 13X. 7. The apparatus according to claim 3, wherein the carbon monoxide-selective adsorbent other than the zeolite 5A is a cuprous chloride (CuCl)-impregnated alumina adsorbent. 8. The apparatus according to claim 7, wherein the cuprous chloride-impregnated alumina adsorbent has a Henry's law constant for carbon monoxide, related to adsorption equilibrium at room temperature, at least four times as high as that of the zeolite 5A. 9. A pressure swing adsorption apparatus for obtaining a highly pure hydrogen product through continuous purification using adsorption columns in which active alumina or silica gel, activated carbon, zeolite 13X, zeolite 5A, and a cuprous chloride-impregnated alumina adsorbent are sequentially disposed in order to adsorb impurities from a hydrogen-containing gas mixture. 10. A method of purifying hydrogen using a pressure swing adsorption apparatus, comprising: supplying a hydrogen-containing gas mixture including impurities into an adsorption column packed with a plurality of adsorbents through a feed supply pipe;adsorbing water on active alumina or silica gel, which is disposed at a lowest position in the adsorption column;adsorbing carbon dioxide and a methane component on activated carbon, which is disposed on the active alumina or the silica gel in the adsorption column;adsorbing carbon dioxide, which is not adsorbed by the activated carbon, on zeolite 13X, which is disposed on the activated carbon in the adsorption column;adsorbing carbon monoxide on zeolite 5A, which is disposed on the zeolite 13X in the adsorption column, and adsorbing the methane component, which is not adsorbed by the activated carbon, thereon;adsorbing carbon monoxide, which is not adsorbed by the zeolite 5A, on a carbon monoxide-selective adsorbent other than the zeolite 5A, which is disposed on the zeolite 5A in the adsorption column; andcollecting a hydrogen product, which is purified to high purity via the plurality of adsorbents in the adsorption column, into a hydrogen storage tank. 11. The method according to claim 10, wherein a portion of the zeolite 5A, which is one of the adsorbents, is replaced with the carbon monoxide-selective adsorbent other than the zeolite 5A. 12. The method according to claim 10, wherein a portion of the activated carbon, which is one of the adsorbents, is replaced with zeolite 13X. 13. The method according to claim 10, wherein the carbon monoxide-selective adsorbent other than zeolite 5A is a cuprous chloride (CuCl)-impregnated alumina adsorbent. 14. A method of purifying hydrogen using a pressure swing adsorption apparatus composed of two or more adsorption columns in which a plurality of adsorbents is sequentially disposed and which are disposed parallel to each other, the method comprising sequentially passing a hydrogen-containing gas mixture including impurities of water, carbon dioxide, methane, and carbon monoxide through active alumina or silica gel, activated carbon, zeolite 13X, zeolite 5A, and a carbon monoxide-selective adsorbent other than the zeolite 5A, which are disposed in the adsorption columns, so that the hydrogen-containing gas mixture is purified to highly pure hydrogen containing less than 10 ppm carbon monoxide. 15. The method according to claim 14, wherein adsorption, supply of a purge gas, partial pressure equalization (for supplying a gas), countercurrent depressurization, purging, partial pressure equalization (for receiving a gas), and product pressurization are sequentially conducted through the adsorption columns, in which the countercurrent depressurization is conducted by subjecting two or more adsorption columns to countercurrent depressurization to atmospheric pressure or less. 16. The apparatus according to claim 4, wherein a portion of the zeolite 5A, which is one of the adsorbents, is replaced with the carbon monoxide-selective adsorbent other than the zeolite 5A. 17. The apparatus according to claim 4, wherein a portion of the activated carbon, which is one of the adsorbents, is replaced with zeolite 13X. 18. The apparatus according to claim 4, wherein the carbon monoxide-selective adsorbent other than the zeolite 5A is a cuprous chloride (CuCl)-impregnated alumina adsorbent. 19. The apparatus according to claim 18, wherein the cuprous chloride-impregnated alumina adsorbent has a Henry's law constant for carbon monoxide, related to adsorption equilibrium at room temperature, at least four times as high as that of the zeolite 5A.