Single or dual layer ammonia slip catalyst
US-2016367938-A1 · Dec 22, 2016 · US
US8940270B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-8940270-B2 |
| Application number | US-201113997473-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 27, 2011 |
| Priority date | Dec 28, 2010 |
| Publication date | Jan 27, 2015 |
| Grant date | Jan 27, 2015 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
To provide a sulfur trioxide decomposition catalyst, particularly, a sulfur trioxide decomposition catalyst capable of lowering the temperature required when producing hydrogen by an S—I cycle process. A sulfur trioxide decomposition catalyst comprising a composite oxide of vanadium and at least one metal selected from the group consisting of transition metal and rare earth elements is provided. Also, a sulfur dioxide production process comprising decomposing sulfur trioxide into sulfur dioxide and oxygen by using the sulfur trioxide decomposition catalyst above, is provided. Furthermore, a hydrogen production process, wherein the reaction of decomposing sulfur trioxide into sulfur dioxide and oxygen by an S—I cycle process is performed by the above-described sulfur dioxide production process, is provided.
Opening claim text (preview).
The invention claimed is: 1. A sulfur dioxide production process, comprising decomposing sulfur trioxide into sulfur dioxide and oxygen with a sulfur trioxide decomposition catalyst, wherein the sulfur trioxide decomposition catalyst comprises a composite oxide of vanadium and at least one metal selected from the group consisting of transition metal and rare earth elements. 2. The process as claimed in claim 1 , wherein said at least one metal is selected from the group consisting of copper (Cu), chromium (Cr), titanium (Ti), zirconium (Zr), lanthanum (La), cerium (Ce), neodymium (Nd) and a combination thereof. 3. The process as claimed in claim 1 , wherein in said composite oxide, the atom ratio between said at least one metal and vanadium is from 1:9 to 9:1. 4. The process as claimed in claim 1 , wherein said at least one metal is cerium (Ce), and in said composite oxide, the atom ratio (cerium:vanadium) between cerium and vanadium is from 0.4:1 to less than 1:1. 5. The process as claimed in claim 4 , wherein in said composite oxide, the atom ratio (cerium:vanadium) between cerium and vanadium is from 0.8:1 to 0.95:1. 6. The process as claimed in claim 1 , wherein said composite oxide is supported on a support. 7. The process as claimed in claim 6 , wherein said support is selected from the group consisting of silica, alumina, zirconia, titania and a combination thereof. 8. The process as claimed in claim 7 , wherein said support is a porous silica support having a pore structure. 9. The process as claimed in claim 1 , wherein said decomposition is performed at a temperature of 800° C. or less. 10. The process as claimed in claim 1 , wherein said decomposition is performed at a temperature of 700° C. or less. 11. A hydrogen production process comprising splitting water into hydrogen and oxygen, wherein the process comprises decomposing sulfuric acid into water, sulfur dioxide and oxygen through a reaction represented by the following formula (X1) and out of the elementary reactions represented by the following formulae (X1-1) and (X1-2), which are elementary reactions of the reaction represented by the following formula (X1), the elementary reaction of formula (X1-2) being performed by the process claimed in claim 1 : H 2 SO 4 →H 2 O+SO 2 +½O 2 (X1) H 2 SO 4 →H 2 O+SO 3 (X1-1) SO 3 →SO 2 +½O 2 . (X1-2) 12. The hydrogen production process as claimed in claim 11 , wherein the hydrogen production process is an S—I cycle process, a Westinghouse cycle process, an Ispra-Mark 13 cycle process, or a Los Alamos science laboratory cycle process.
the hydrogen being generated from the water as a result of cycles of reactions, e.g. sulfur-iodine cycle · CPC title
X-ray diffraction · CPC title
Vanadium · CPC title
in several steps · CPC title
Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.