http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-H09506542-A
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A62D2101-22 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A62D2101-28 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-8662 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A62D3-38 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-061 |
| classificationIPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A62D101-22 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A62D101-28 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A62D3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-86 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A62D3-38 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-00 |
| filingDate | 1994-10-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 1997-06-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | JP-H09506542-A |
| titleOfInvention | Selective oxidation catalysts for halogenated organics |
| abstract | (57) [Summary] The present invention relates to a method for decomposing a volatile organic compound (VOC 3 ) and a catalyst composition therefor. This method is a metal exchanged, metal impregnated aluminosilicate zeolite, wherein at least one exchanged metal of the zeolite is Ti, V, Cr, Co, Ni, Cu, Fe, Mo, Mn, Pd and Pt. At least one impregnating metal is selected from the group consisting of Ti, V, Cr, Mn, Fe, Co, Ni, Cu, Mo, Pd, and Pt, and an exchange metal and an impregnating metal are selected. The step of contacting the VOCs with the oxygen-containing gas for a contact time sufficient to oxidize the organic compound in the presence of a catalyst, the difference between which changes the temperature required to promote the oxidation of the organic compound. The reaction temperature of the method is about 100 to about 650 ° C., and the contact time is about 0.01 to 20 seconds. Preferably, the reaction temperature is about 150 to about 450 ° C and the contact time is about 0.1 to 1.0 seconds. The CO / CO 2 ratio and the Cl 2 / HCl ratio in the gas effluent are via the selective combination of at least two impregnating metals and at least one exchange metal in the aluminosilicate zeolite or at least 1 in the aluminosilicate zeolite. Of the impregnating metal and at least two exchange metals in combination. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2012210247-A |
| priorityDate | 1993-10-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 71.