Nanostructured apparatus and methods for producing carbon-containing molecules as a renewable energy resource
US-2017282147-A1 · Oct 5, 2017 · US
US10124323B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10124323-B2 |
| Application number | US-201715828709-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 1, 2017 |
| Priority date | Dec 22, 2016 |
| Publication date | Nov 13, 2018 |
| Grant date | Nov 13, 2018 |
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A nano-nickel catalyst and a hydrogenation device of carbon oxides are provided. The hydrogenation device is configured to reduce the carbon oxides to form low carbon hydrocarbons. The nano-nickel catalyst has a metallic nickel body and a plurality of microstructures connecting with at least one surface of the metallic nickel body. The microstructures are sharp, and have a length-diameter ratio ranging from 2 to 5.
Opening claim text (preview).
What is claimed is: 1. A nano-nickel catalyst, comprising: a metallic nickel body; and a plurality of microstructures connected to the metallic nickel body on at least one surface of the metallic nickel body; wherein the microstructures are sharp, and have a length-diameter ratio ranging from 2 to 5. 2. The nano-nickel catalyst according to claim 1 , wherein the microstructures contain metallic nickel. 3. The nano-nickel catalyst according to claim 2 , wherein the microstructures are made of metallic nickel. 4. The nano-nickel catalyst according to claim 1 , wherein the metallic nickel body is spherical. 5. The nano-nickel catalyst according to claim 1 , wherein the metallic nickel body is porous. 6. The nano-nickel catalyst according to claim 5 , wherein the metallic nickel body is porous, and has an adsorption pore volume ranging from 0.0024 cm 3 /g to 0.0062 cm 3 /g. 7. The nano-nickel catalyst according to claim 1 , wherein the metallic nickel body is solid. 8. The nano-nickel catalyst according to claim 1 , wherein the metallic nickel body is hollow. 9. The nano-nickel catalyst according to claim 1 , wherein the nano-nickel catalyst has a specific surface area ranging from 1.5 m 2 /g to 2.0 m 2 /g. 10. The nano-nickel catalyst according to claim 1 , wherein the nano-nickel catalyst has an ability to reduce carbon dioxide into low-carbon hydrocarbons. 11. The nano-nickel catalyst according to claim 10 , wherein the low-carbon hydrocarbons are selected from a group consisting of methane, ethane, propane, and a combination thereof. 12. A hydrogenation device of carbon oxides, comprising: a first reactor having a first catalyst bed therein; and a second reactor having a second catalyst bed therein, and communicated with the first reactor through a channel; wherein the first catalyst bed and the second catalyst bed both comprise a nano-nickel catalyst according to claim 1 . 13. The hydrogenation device of carbon oxides according to claim 12 , wherein the first catalyst bed has a first catalyst fill rate with a minimum value of 0.3 g/ml, and the second catalyst bed has a second catalyst fill rate with a minimum value of 0.15 g/ml.
Nickel · CPC title
from carbon dioxide with hydrogen · CPC title
with stationary catalyst bed · CPC title
Nickel · CPC title
of CO2 · CPC title
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