http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-100606385-B1
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P10-143 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P10-134 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C21B13-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C21B13-0033 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C21B13-0086 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B31-30 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C21B13-00 |
| filingDate | 1998-10-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2006-08-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2006-08-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | KR-100606385-B1 |
| titleOfInvention | Method for producing a mixture of iron carbide and granular direct reduced iron |
| abstract | The final product containing iron carbide (Fe 3 C) is produced from an intermediate product consisting of granular direct reduced iron. The intermediate product is fed by an iron ore reduction device which is fed to a carbonization reactor. Liquefied hydrocarbons are transferred to the carbonization reactor at a temperature of 500 to 900 ° C. where at least a portion of the granular, direct reduced iron is flowed. The final product from the carbonization reactor consists of 5 to 90 wt% Fe 3 C. Flowing gases containing methane and hydrogen in addition to hydrocarbons can be added to the carbonization reactor.n n n n Iron carbide, granular direct reducing iron |
| priorityDate | 1997-11-06-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 25.