| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a2a99738c564d0d4da77d442ec8f7500 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1022 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G33-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G67-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-16
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-14
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-18
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G49-08
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-332
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-333
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-043
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-12
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G49-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-12
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-62
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-64 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C2-00 |
| filingDate |
2012-03-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_250dffb4c6ec2027e5e94d15bab77f4a
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bd4ab439f031ec2993f91fd4d5b93844
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a116d0ac3f3935d021ddaa123a551803
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6256bf61ae1de0f6d7440128a953b118 |
| publicationDate |
2013-01-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
CA-2833251-A1 |
| titleOfInvention |
Process and system for reducing the olefin content of a fischer-tropsch product stream |
| abstract |
A method is provided for converting synthesis gas to liquid hydrocarbon mixtures useful as distillate fuel and/or lube base oil. The synthesis gas is contacted with a synthesis gas conversion catalyst comprising a Fischer-Tropsch synthesis component in an upstream catalyst bed thereby producing an intermediate hydrocarbon mixture containing olefins and C21+ normal paraffins. The intermediate hydrocarbon mixture is subsequently contacted with a hydroisomerization catalyst and an olefin saturation catalyst, thereby resulting in a product containing no greater than about 25 wt% olefins and containing no greater than about 5 wt% C21+ normal paraffins. The hydroisomerization and olefin saturation catalysts may be in separate beds or mixed in a single bed downstream of the synthesis gas conversion catalyst. |
| priorityDate |
2011-06-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |