Water-absorbent resin composition, absorbent material and absorbent article
US-2024424473-A1 · Dec 26, 2024 · US
US9844766B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9844766-B2 |
| Application number | US-201114355134-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 31, 2011 |
| Priority date | Oct 31, 2011 |
| Publication date | Dec 19, 2017 |
| Grant date | Dec 19, 2017 |
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The present invention relates to a method for manufacturing a carbon dioxide absorbent and to the absorbent manufactured by the method. The method comprises: (A) a step of preparing a slurry composition including a carrier composition containing a support, an inorganic binder, and a solvent; (B) a step of preparing solid particles by spray drying the thus-prepared slurry composition; (C) a step of manufacturing a carrier by dry calcining the thus-prepared solid particles; and (D) a step of receiving an amine compound into the pores of the thus-manufactured carrier. According to the absorbent of the present invention, an absorbing reaction and a regenerating reaction at a low temperature range (less than or equal to 100° C. may be conducted, and therefore, the cost for capturing CO 2 in a dry capturing process may be expected to decrease.
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What is claimed is: 1. A method for manufacturing a carbon dioxide absorbent, the method comprising the steps of: (A) preparing a slurry composition including a carrier composition containing a support and an inorganic binder, and a solvent; (B) preparing solid particles by spray drying the prepared slurry composition; (C) manufacturing a carrier by dry calcining the solid particles; and (D) receiving an amine compound into pores of the manufactured carrier. 2. The method of claim 1 , wherein the support comprises at least one of a basic support, a neutral support, and an amphoteric support. 3. The method of claim 2 , wherein the basic support includes calcium oxide, zinc oxide, and magnesium oxide, the neutral support includes carbon molecular sieve or carbon nano tubes, a magnesium and aluminum containing oxide, a magnesium and silicon containing oxide, a calcium and aluminum containing oxide, and the amphoteric support includes alumina, titanium dioxide, zirconium oxide, cesium oxide. 4. The method of claim 1 , wherein a content of the support is in a range of 20 to 85 parts by weight, based on the total weight of the carrier composition. 5. The method of claim 1 , wherein the inorganic binder includes a cement-like inorganic binder, a clay-like inorganic binder, and a ceramic-like inorganic binder. 6. The method of claim 5 , wherein the cement-like inorganic binder is calcium silicate or calcium aluminate, the clay-like inorganic binder is bentonite or kaolinite, and the ceramic-like inorganic binder is alumina sol, silica sol or boehmite. 7. The method of claim 1 , wherein a content of the inorganic binder is in a range of 5 to 50 parts by weight, based on the total weight of the carrier composition. 8. The method of claim 1 , wherein the carrier composition is contained in an amount of 15 to 60 parts by weight, based on the total weight of the slurry composition. 9. The method of claim 1 , wherein the slurry composition further includes one or more organic additives including a dispersant, a defoamer and an organic binder. 10. The method of claim 9 , wherein the dispersant is an anionic dispersant, a cationic dispersant, an amphoteric dispersant or a non-ionic dispersant, the defoamer is a metal soap- or polyester-based material, and the organic binder is one or more selected from the group consisting of a polyvinylalcohol-based material, a polyglycol-based material and methylcellulose. 11. The method of claim 1 , wherein after performing step (A), further comprising: stirring and comminuting the slurry composition; and removing foreign substances from the stirred and comminuted slurry composition. 12. The method of claim 1 , wherein the drying in step (C) is performed under an air atmosphere at 110 to 150° C. 13. The method of claim 1 , wherein the calcining in step (C) is performed under an air, nitrogen, helium or reducing gas atmosphere at 350 to 1000° C. 14. The method of claim 1 , wherein step (D) comprises dissolving the amine compound in a solvent; and mixing the carrier prepared in step (C) with the solvent and stirring the resultant product. 15. The method of claim 14 , wherein the amine compound comprises at least one primary amine compound, at least one piperazine-based cyclic secondary amine compound, at least one cyclic tertiary amine compound, and at least one amine compound polymer. 16. The method of claim 14 , wherein a content of the amine compound is in a range of 5 to 70 parts by weight, based on the weight of the carrier. 17. The method of claim 14 , wherein the solvent is distilled water, an organic solvent or a mixture thereof. 18. The method of claim 14 , wherein the stirring is performed at 30 to 80° C. 19. The method of claim 15 , wherein the at least one primary amine compound is selected from the group consisting of monoethanolamine (MEA), tetraethylenepentamine (TEPA), and tetraethylenetetraamine (TETA). 20. The method of claim 15 , wherein the at least one piperazine-based cyclic secondary amine compound is selected from the group consisting of piperazine and 2-piperidine ethanol. 21. The method of claim 15 , wherein the at least one cyclic tertiary amine compound is 1-(2-hydroxyethyl) piperazine. 22. The method of claim 15 , wherein the at least one amine compound polymer is polyethyleneimine (PEI).
of sorbents or filter aids comprising organic materials · CPC title
Thermal treatment, e.g. calcining or pyrolizing · CPC title
being in the range 100-500 m2/g · CPC title
Carbon dioxide · CPC title
the functional group or the linking, spacer or anchoring group as a whole comprising at least one type of heteroatom selected from a nitrogen, oxygen or sulfur, these atoms not being part of the carrier as such · CPC title
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