Catalysts for petrochemical catalysis
US-11795123-B2 · Oct 24, 2023 · US
US2016243530A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016243530-A1 |
| Application number | US-201615144476-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 2, 2016 |
| Priority date | Jul 25, 2012 |
| Publication date | Aug 25, 2016 |
| Grant date | — |
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The present invention relates to a catalyst for the thermochemical generation of hydrogen from water and/or the thermochemical generation of carbon monoxide from carbon dioxide comprising a solid solution of cerium dioxide and uranium dioxide.
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1 . A method for the generation of hydrogen from water and/or the generation of carbon monoxide from carbon dioxide comprising: reducing at least part of a catalyst at a first elevated temperature to produce diatomic oxygen; contacting the catalyst with at least one of water and carbon dioxide at a second elevated temperature; and oxidising the at least partially reduced catalyst to generate the hydrogen and/or the carbon monoxide; wherein the second elevated temperature may be the same or different from the first elevated temperature; and wherein the catalyst comprises a solid solution of cerium dioxide and uranium dioxide. 2 . The method of claim 1 , wherein completion of oxidation of the catalyst is accomplished in less than 20 minutes. 3 . The method of claim 1 , wherein the catalyst further comprises zirconium dioxide. 4 . The method of claim 1 , wherein the catalyst consists essentially of cerium dioxide and uranium dioxide. 5 . The method of claim 1 , wherein the catalyst is free of zirconium dioxide. 6 . The method of claim 1 , wherein the catalyst was produced by dissolving a cerium salt, a uranium salt and optionally a zirconium salt in water; and then precipitating at a pH of at least 8 by addition of a base to form a precipitate, and calcining the precipitate. 7 . The method of claim 1 , wherein the second elevated temperature is lower than the first elevated temperature. 8 . The method of claim 1 , wherein the first elevated temperature is from 600° C. to 1200° C. 9 . The method of claim 1 , wherein the first elevated temperature is from 1000° C. to 1200° C. 10 . The method of claim 1 , wherein the second elevated temperature is from 600° C. to 1000° C. 11 . The method of claim 1 , wherein the second elevated temperature is from 600° C. to 900° C. 12 . The method of claim 1 , wherein the first and or second elevated temperature is obtained by heating using solar energy. 13 . The method of claim 1 , wherein a molar ratio of cerium and uranium is from 50 to 0.05. 14 . The method of claim 13 , wherein the molar ratio of cerium and uranium is from 10 to 0.1. 15 . The method of claim 1 , wherein the solid solution has a fluorite crystal structure. 16 . The method of claim 1 , wherein a total amount of cerium dioxide, uranium dioxide and optionally zirconium dioxide in the solid solution is at least 95.0 wt % based on the weight of the solid solution. 17 . The method of claim 16 , wherein the total amount of cerium dioxide, uranium dioxide and optionally zirconium dioxide in the solid solution is at least 99.0 wt % based on the weight of the solid solution. 18 . The method of claim 1 , wherein a molar ratio of cerium and uranium is from 10 to 1; the solid solution has a fluorite crystal structure; a total amount of cerium dioxide and uranium dioxide in the solid solution is at least 99.0 wt %; and wherein the catalyst is free of zirconium dioxide. 19 . The method of claim 17 , wherein the catalyst consists essentially of cerium dioxide and uranium dioxide.
characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title
characterised by their physical properties · CPC title
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
Precipitation · CPC title
Cyclic methods · CPC title
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