Catalyst for decomposition of sulfur trioxide and hydrogen production process

US8940270B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-8940270-B2
Application numberUS-201113997473-A
CountryUS
Kind codeB2
Filing dateDec 27, 2011
Priority dateDec 28, 2010
Publication dateJan 27, 2015
Grant dateJan 27, 2015

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

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.

First claim

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.

Assignees

Inventors

Classifications

  • 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

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US8940270B2 cover?
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 pr…
Who is the assignee on this patent?
Takeshima Shinichi, Machida Masato, Toyota Motor Co Ltd, and 1 more
What technology area does this patent fall under?
Primary CPC classification B01J23/8472. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Jan 27 2015 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).