Process and reactor for catalytic oxidation of ammonia
US-12459819-B2 · Nov 4, 2025 · US
US9643845B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9643845-B2 |
| Application number | US-201615295978-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 17, 2016 |
| Priority date | Apr 24, 2012 |
| Publication date | May 9, 2017 |
| Grant date | May 9, 2017 |
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A nitrous oxide room temperature purification method, apparatus and system utilizing at least partially oxidized nickel. In an embodiment, a room temperature regenerable N 2 O purifier includes a vessel having an inlet and outlet, an active portion being at least partially filled with a purification material comprising nickel oxide and optional elemental nickel, wherein the weight ratio between the nickel oxide and the optional elemental nickel is equal or higher than 3 and the surface area of the nickel oxide and the optional elemental nickel is equal or higher than 50 m 2 /g.
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What is claimed is: 1. A method for the purification of N 2 O comprising feeding a N 2 O gaseous stream to a vessel having an inlet and outlet, the vessel being at least partially filled with a purification material comprising nickel oxide and optional elemental nickel, the portion being filled with the purification material being a purifier active portion, wherein the weight ratio between the nickel oxide and the optional elemental nickel is equal or higher than 3 and the surface area of the nickel oxide and the optional elemental nickel is equal or higher than 50 m 2 /g. 2. A method according to claim 1 characterized in that it is carried out at room temperature. 3. A method according to claim 2 wherein the weight ratio between the nickel oxide and the optional elemental nickel is equal or higher than 5 and the surface area of the nickel oxide and the optional elemental nickel is equal or higher than 100 m 2 /g. 4. A method according to claim 3 wherein the purification material consists essentially of nickel oxide. 5. A method according to claim 4 wherein the purification material is supported. 6. A method according to claim 5 wherein the purification material is supported on at least one of amorphous silica and magnesium oxide. 7. A method according to claim 1 wherein the purification material consists of nickel oxide and optional elemental nickel. 8. A purification method according to claim 1 wherein the purification phase is alternate to a regeneration phase where the vessel is heated. 9. A method according to claim 1 wherein the active portion delimits a volume having a length L and a width W, wherein the ratio L/W between the length and the width is comprised between 1 and 15. 10. A method according to claim 9 wherein the ratio between measure of the active portion volume and value of the N 2 O flow is between 0.05 and 2 liter/(m 3 /hour).
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