http://rdf.ncbi.nlm.nih.gov/pubchem/patent/FR-3076297-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_011e773a3b21737d887a6c7e81d99943 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1074 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-301 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G67-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G7-00 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G47-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G67-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G7-00 |
| filingDate | 2018-01-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0bf5b649f400337b6dddeddc9306cd7b |
| publicationDate | 2019-07-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | FR-3076297-A1 |
| titleOfInvention | INTEGRATED HYDROCRACKING PROCESS TWO STEPS TO MAXIMIZE NAPHTHA PRODUCTION |
| abstract | The invention relates to a process for hydrocracking DSV-type hydrocarbon feedstocks in admixture with a diesel-type feed allowing the improved production of naphtha comprising a) hydrotreating of the operating DSV feed, in the presence of hydrogen and from minus a hydrotreatment catalyst; b) hydrocracking the effluent of a) operating, in the presence of hydrogen and at least one hydrocracking catalyst, c) the gas / liquid separation of the effluent from step b) to produce a liquid effluent and a gaseous effluent comprising at least hydrogen, d) the sending of the gaseous effluent comprising at least hydrogen in a compression step before its recycling in the hydrotreating steps a) and b ) hydrocracking, e) fractionating the liquid effluent into at least one effluent comprising converted hydrocarbon products having boiling points below 180 ° C and an unconverted liquid fraction having a boiling point greater than 180 ° C, f) hydrocracking said unconverted liquid fraction from step e) operating, in the presence of hydrogen and a hydrocracking catalyst, g) hydrotreating the effluent from the step f) mixed with a hydrocarbon liquid feed of diesel type comprising at least 60% by weight of boiling compounds at a boiling point between 120 and 400 ° C, said hydrotreating step g) operating in the presence of hydrogen and at least one hydrotreatment catalyst. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/FR-3104606-A1 |
| priorityDate | 2018-01-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 27.