| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7580a1cdb7bf704802f84446f901fbf7 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G50-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G55-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G29-205 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G17-095
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G17-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G67-16
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-44
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G50-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G55-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G55-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-10
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G29-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10L1-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G67-08 |
| filingDate |
2002-09-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_56697c5fe56750871cc30511abcf3f8a
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0c271fc3733fa1df09c69d2ca9fe19b4
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ccdab25a18aa699c20da494e10c706f8
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_587dac6aaa4829480914a54b13cb7685
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6c954410635a00eb726946a8a970f206 |
| publicationDate |
2004-03-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
FR-2843969-A1 |
| titleOfInvention |
PROCESS FOR RECOVERING A HYDROCARBON LOAD AND REDUCING THE VAPOR VOLTAGE OF SAID LOAD |
| abstract |
A process for upgrading a hydrocarbon feedstock and for reducing the vapor pressure of said feedstock is described, comprising three steps: a step a) consisting in separating said hydrocarbon feedstock into a fraction (O1) essentially comprising compounds containing 5 carbon atoms including at least 2% by weight of pentenes, step b) consisting in bringing said fraction (O1) into contact with a hydrocarbon cut (02) comprising at least in part hydrocarbons having a number of atoms of carbon between 6 and 10, including at least 2% by weight of olefins, and a step c) consisting in separating the effluents from step b) into a gasoline cut (α) whose upper distillation point is lower at 100 ° C and a kerosene cut (β) with a distillation interval of between 100 ° C and 300 ° C. |
| priorityDate |
2002-09-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |