Methanation Catalyst
US-2016052837-A1 · Feb 25, 2016 · US
US9908104B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9908104-B2 |
| Application number | US-201414901523-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 27, 2014 |
| Priority date | Jun 28, 2013 |
| Publication date | Mar 6, 2018 |
| Grant date | Mar 6, 2018 |
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The invention relates to a catalyst, comprising a catalytic element disposed on a substrate, wherein said substrate has formula Ce 1-x M x O 2 , wherein x is between about 0 and about 0.3, optionally between about 0.01 and about 0.3, and wherein M, if present, is a metallic element other than Ce, when used for catalysing a methanation reaction. There is also described use of the catalyst for catalysing a methanation reaction and a method for methanation of a feedstock including carbon monoxide and hydrogen, said method comprising contacting the feedstock with the catalyst.
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The invention claimed is: 1. A method for methanation of a feedstock including carbon monoxide and hydrogen, said method comprising contacting the feedstock with a catalyst, said catalyst comprising a catalytic element selected from the group consisting of Co, Fe, Pt, Ru, Rh, Pd, Ni and Ir disposed on a substrate, wherein said substrate has formula Ce 1-x M x O 2 , wherein x is between about 0.01 and about 0.3, and wherein M is a metallic element selected from the group consisting of Y, Gd, Sm and alkaline earth metals. 2. The method of claim 1 wherein the feedstock includes coal gasification effluent and/or biomass gasification effluent. 3. The method of claim 1 wherein the feedstock additionally includes a sulfur-containing gas or vapour. 4. The method of claim 3 , comprising a step of depositing the catalytic element on the substrate for reducing poisoning of the catalytic element by the sulfur-containing gas or vapor. 5. The method of claim 4 wherein said depositing is conducted before exposing said catalytic element to the sulfur-containing gas or vapour. 6. The method of claim 4 wherein the depositing is such that the catalytic element is present in discrete regions on the substrate. 7. The method of claim 3 wherein the sulfur-containing gas or vapour includes any one or more of hydrogen sulfide, carbonyl sulfide, sulfur dioxide or an organic thiol. 8. The method of claim 1 wherein the molar ratio of hydrogen to carbon monoxide in the feedstock is between about 4:1 and about 1:1. 9. The method of claim 1 wherein said contacting is conducted at a temperature of between about 250 ° C. and about 750 ° C. 10. The method of claim 1 wherein the temperature and feedstock gas hourly space velocity during said contacting are sufficient to achieve equilibrium conversion of carbon oxides to methane. 11. The method of claim 1 wherein the catalytic element is metallic nickel. 12. The method of claim 1 wherein the substrate is particulate. 13. The method of claim 1 wherein x is between about 0.01 and about 0.25. 14. The method of claim 1 wherein the catalyst includes regions of metallic nickel dispersed on a surface of the substrate. 15. The method of claim 1 wherein the catalyst includes between about 1% and about 40% of the catalytic element by weight. 16. The method of claim 1 wherein the substrate has a specific surface area of between about 10 m 2 /g and about 300 m 2 /g.
of the platinum-group · CPC title
Mixed oxides other than spinels, e.g. perovskite · CPC title
characterised by the composition · CPC title
containing iron · CPC title
of the iron-group · CPC title
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