http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-101336764-B1
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-041 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2461 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00907 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-1241 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2475 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00835 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00783 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2458 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2453 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00844 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00873 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-2479 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-1058 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-142 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-0283 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B3-38 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-24 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-0093 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-249 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-24 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B3-38 |
| filingDate | 2011-10-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2013-12-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2013-12-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | KR-101336764-B1 |
| titleOfInvention | Hydrogen production module by reaction separation simultaneous process and water production reactor using the same |
| abstract | The present invention relates to a hydrogen production module using a reaction separation simultaneous process and a water production reactor using the same. More specifically, a first reforming catalyst, a unit cell including a second reforming catalyst facing a hydrogen separation membrane, and a plurality of unit cells Laminated and mounted in the pressure chamber to provide a hydrogen production apparatus capable of high pressure operation. The hydrogen production module may produce hydrogen using hydrocarbons, carbon monoxide and alcohol as raw materials. In particular, the reforming catalyst is all composed of a porous metal plate type to maximize the heat transfer effect required for the reaction. The reactant penetrates through the first reforming catalyst, and then separates hydrogen at the same time as the reaction passes through the gap between the opposing hydrogen separation membrane and the second reforming catalyst. Accordingly, high-purity hydrogen can be obtained at the same time as securing high efficiency and securing the equilibrium conversion of the reaction temperature. |
| priorityDate | 2011-10-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 38.