Methods and systems for upgrading mixed pyrolysis oil to light aromatics over mixed metal oxide catalysts
US-2024010934-A1 · Jan 11, 2024 · US
US2016296916A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016296916-A1 |
| Application number | US-201514805077-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 21, 2015 |
| Priority date | Apr 7, 2015 |
| Publication date | Oct 13, 2016 |
| Grant date | — |
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A disclosure is related to a composite oxide catalyst for a reverse water gas shift (RWGS) reaction, which is a reaction for obtaining water and carbon monoxide by reacting hydrogen with carbon dioxide, and particularly, to a self-recoverable composite oxide catalyst for a reverse water gas shift reaction, which is composed of a compound of Ce 1-x M x O 2-0.5x (M is one element selected from the group consisting of Y, La, Nd, Sm, and Gd) and Fe 2 O 3 as a composite oxide, thus has an excellent thermal stability at high temperature, and has high carbon dioxide conversion and high carbon monoxide selectivity even under a strong reducing atmosphere, which is a process condition of the reverse water gas shift reaction. Also, the composite oxide exhibits excellent catalytic activity even at the reaction condition of low temperature such as 400° C., and thus enables a large amount of carbon dioxide to be removed at low cost.
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What is claimed is: 1 . A composite oxide catalyst for a reverse water gas shift (RWGS) reaction, wherein the catalyst is composed of a compound of Ce 1-x M x O 2-0.5x and Fe 2 O 3 as a composite oxide, and M is one element selected from the group consisting of Y, La, Nd, Sm, and Gd, and x is in a range of 0≦x≦0.5. 2 . The composite oxide catalyst of claim 1 , wherein M in Ce 1-x M x O 2-0.5x is Gd. 3 . The composite oxide catalyst of claim 1 , wherein the compound of Ce 1-x M x O 2-0.5x is included in a ratio of 10 to 50 mol % based on the entire composite oxide. 4 . The composite oxide catalyst of claim 1 , wherein the catalyst is capable of repeated redox reaction. 5 . The composite oxide catalyst of claim 1 , wherein when the catalyst is used for the reverse water gas shift reaction, the carbon dioxide conversion is 35% or more under a temperature condition of 400° C. 6 . The composite oxide catalyst of claim 1 , wherein when the catalyst is used for the reverse water gas shift reaction, the carbon monoxide selectivity is 80% or more under a temperature condition of 400° C.
Increasing the carbon monoxide content, e.g. reverse water-gas shift [RWGS] · CPC title
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
with rare earths or actinides · CPC title
Grinding · CPC title
Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
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