http://rdf.ncbi.nlm.nih.gov/pubchem/patent/BR-PI0512669-A
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ac29389b816db7ae7fa345b16ba89a60 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_05b300899aadb36fbc75d47f1c84e1e9 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-703 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C1-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-332 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-75 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C1-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-75 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J37-18 |
| filingDate | 2005-12-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ccc0ef3862673ce8781cd4e21300be42 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a67eba3eb3d4a3065603b1845261d503 |
| publicationDate | 2008-04-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | BR-PI0512669-A |
| titleOfInvention | processes for the production of a supported fisher-tropsch catalyst, and for the synthesis of a fisher-tropsch wax product, and, fisher-tropsch wax product |
| abstract | PROCESSES FOR PRODUCING A SUPPORTED FISHER-TROPSCH CATALYST, AND FOR THE SYNTHESIS OF A FISHER-TROPSCH WAX PRODUCT, AND FISHER-TROPSCH WAX PRODUCT Process for producing a Fisher-Tropsch catalyst including one-stage treatment. activation (12) of a supported pre-reduction particulate cobalt nitrate supported Fisher-Tropsch synthesis catalyst precursor containing reducing cobalt oxides, with hydrogen as a reducing gas to reduce cobalt oxides for Co during ammonia and water being formed, the reduction including a period of time when predominantly CoO is reduced to Co. Unreacted hydrogen is withdrawn (20), which includes water and is treated to decrease its point. of dew (14). At least a portion of the unreacted hydrogen removed is taken back to the activation stage (12) as recycled hydrogen (26). An ammonia concentration is maintained at the activation stage (12) at least during the time when predominantly CoO is reduced to Co to less than 250 parts per million by volume ("vppm"). |
| priorityDate | 2005-01-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 30.