| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ac29389b816db7ae7fa345b16ba89a60 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P30-40
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-4043
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-4006 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-30
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-50
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-332
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-00 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00 |
| filingDate |
2015-03-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9fef269f7f243beb284cc9ffdbd3dfbb |
| publicationDate |
2015-10-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
WO-2015145311-A1 |
| titleOfInvention |
Fischer-tropsch synthesis |
| abstract |
A Fischer-Tropsch synthesis process (10) includes feeding gaseous reactants (20) including at least CO, H 2 and C0 2 into a reactor (14) holding an iron-based catalyst. The H 2 and CO are fed in a H 2 :CO molar ratio of at least 2: 1 and the C0 2 and CO are fed in a C0 2 :CO molar ratio of at least 0.5: 1. The reactor (14) is controlled at an operating temperature in the range from about 260°C to about 300°C. A liquid product (22) and a gaseous product (24) including hydrocarbons, CO, H 2 , water and C0 2 are withdrawn from the reactor (14). |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-3770145-A1
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2021013640-A1 |
| priorityDate |
2014-03-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |