| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_07d1677a8ad5f7707ebda0e633dbcbdf |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-08
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-0277
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-1235
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-148
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1022
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B2203-0475 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10K1-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10K1-005
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10K1-08
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-32
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G57-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G7-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01B3-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10K1-32 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10K1-32
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10K1-08
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10K1-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00 |
| filingDate |
2015-10-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b9aa11336b41f762ff9ee3463847acda
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3bf66f4d2db79e95cc774385cf27c07e |
| publicationDate |
2017-05-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
WO-2017072548-A1 |
| titleOfInvention |
Process for producing a hydrocarbon product flow from a gaseous hydrocarbonaceous feed flow and related installation |
| abstract |
The process comprises : - introducing the feed flow (14) in a synthesis gas generation unit (16) to form a synthesis gas flow (32) and introducing the synthesis gas flow (32) in a Fischer-Tropsch synthesis unit (18); - at least partially removing carbon dioxide from a first flow (44) formed from a Fischer-Tropsch tail gas flow (38) to form a carbon dioxide depleted flow (50); - forming a tail gas recycle flow (36) from the carbon dioxide depleted flow (50); - introducing the tail gas recycle flow (36) in the synthesis gas generation unit (16) and/or in the synthesis gas flow (32). The process comprises adjusting the carbon dioxide content in the tail gas recycle flow (36) to control the hydrogen to carbon monoxide molar ratio in the synthesis gas flow (32) to a target hydrogen to carbon monoxide molar ratio. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-10266775-B2 |
| priorityDate |
2015-10-26-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |