http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2005246163-A
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_cd23c354dd49d149991d5e4d2af08b17 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02C20-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02A50-20 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J27-053 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-86 |
| filingDate | 2004-03-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_48b05467f241d89342aa853abfd5a1a3 |
| publicationDate | 2005-09-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | JP-2005246163-A |
| titleOfInvention | Ammonia decomposition catalyst and ammonia decomposition method |
| abstract | PROBLEM TO BE SOLVED: To provide a catalyst for efficiently decomposing ammonia contained in exhaust gas or the like while suppressing by-production of nitrogen oxides and nitrous oxide. A catalyst for decomposing ammonia is composed of iron-containing sulfate zirconia. In the catalyst, the ratio of iron is about 1 to 20 parts by weight with respect to 100 parts by weight of zirconia. The ratio of the sulfate radical may be about 1 to 25 parts by weight with respect to 100 parts by weight of zirconia in terms of SO 4 2− . When a gas to be treated containing ammonia is brought into contact with the catalyst at about 400 to 600 ° C., ammonia in the gas to be treated can be decomposed and removed into nitrogen while suppressing by-production of nitrogen oxides and nitrous oxide. [Selection figure] None |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2008023521-A |
| priorityDate | 2004-03-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 76.