Device and method for removing unwanted component included in beverage
US-2017037347-A1 · Feb 9, 2017 · US
US11452985B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11452985-B2 |
| Application number | US-201615550456-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 15, 2016 |
| Priority date | Feb 16, 2015 |
| Publication date | Sep 27, 2022 |
| Grant date | Sep 27, 2022 |
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The invention is to provide a method for producing a metal-supported zeolite for alcoholic beverages capable of efficiently removing unwanted components contained in alcoholic beverages to thereby reduce silver release, and the metal-supported zeolite for alcoholic beverages, and to provide a method for producing alcoholic beverages using the metal-supported zeolite for alcoholic beverages. For solution to problem, the production method for the metal-supported zeolite for alcoholic beverages of the invention is a production method for a metal-supported zeolite for alcoholic beverages for removing unwanted components contained in alcoholic beverages, and includes a first ion-exchange treatment step of processing a zeolite carrying a metal ion with an ammonium ion-containing aqueous solution to thereby exchange the metal ion in the zeolite for an ammonium ion, the zeolite containing a Y-type zeolite as the main ingredient, and a second ion-exchange treatment step of processing the ammonium ion-supported zeolite obtained in the previous ion-exchange treatment step with a silver ion-containing acidic aqueous solution to thereby exchange the ammonium ion therein with a silver ion.
Opening claim text (preview).
The invention claimed is: 1. A method for producing a metal-supported zeolite with silver ion supported as a metal ingredient, comprising: performing a first ion-exchange treatment comprising processing a zeolite carrying a metal ion with an ammonium ion-containing aqueous solution to thereby exchange the metal ion in the zeolite for an ammonium ion, the zeolite comprising a Y-type zeolite in an amount of 80% by mass or more based on the total mass of the metal-supported zeolite, and performing a second ion-exchange treatment comprising processing the ammonium ion-exchanged zeolite obtained in the first ion-exchange treatment with an aqueous silver nitrate solution, wherein said aqueous silver nitrate solution comprises silver in a concentration ranging from 5% by mass to 15% by mass, to thereby exchange the ammonium ion therein with a silver ion wherein the metal-supported zeolite has a silver use ratio of 85% or more, the silver use ratio determined according to the following expression: silver use ratio (%)−[silver supported amount in terms of an oxide thereof in zeolite/charged amount in terms of an oxide thereof (theoretical value)]×100; and wherein the metal-supported zeolite in ultraviolet-visible absorption spectroscopy is in a measurement range of 800 to 200 nm according to a diffuse reflection method of the metal-supported zeolite, the height of the absorption peak UV1 observed between 250 and 270 nm and the height of the absorption peak UV2 observed between 210 nm±10 nm satisfy (UV1/UV2)≤0.2. 2. The method according to claim 1 , wherein the ammonium ion-containing aqueous solution is selected from the group consisting of an aqueous ammonium nitrate solution, an aqueous ammonium chloride solution, an aqueous ammonium sulfate solution, an aqueous ammonium phosphate solution, an aqueous ammonium acetate solution and an aqueous ammonia solution.
Ion-exchange · CPC title
Synthetic zeolitic molecular sieves · CPC title
by methods for altering the composition of fermented solutions or alcoholic beverages not provided for in groups C12G3/02 - C12G3/07 (methods for reducing the alcohol content of fermented solutions or alcoholic beverages C12H3/00; methods for increasing the alcohol content of fermented solutions or alcoholic beverages C12H6/00) · CPC title
After-treatment · CPC title
using at least one organic template directing agent, e.g. an ionic quaternary ammonium compound or an aminated compound · CPC title
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