http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-103827269-B
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-44 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-202 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1096 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G69-02 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G69-02 |
| filingDate | 2012-07-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2016-02-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2016-02-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-103827269-B |
| titleOfInvention | Integrated selective hydrogenation cracking and fluidized catalytic cracking method |
| abstract | Provide for transforming heavy crude with the integrated approach of production and transport fuel and system.Method comprises hydrocarbon charging is separated into poor aromatic fraction and rich aromatic fraction.The hydrocracking at relatively high pressure of rich aromatic fraction, for being converted into small part difficult degradation aromatic organosulfur and organic nitrogen compound, and for the production of isocrackate logistics.Unconverted bottom stream is circulated to aromatics separating step.Poor aromatic fraction in fluid catalytic cracking conversion zone cracking to produce crackate logistics, light cycle logistics and heavy recycle stock logistics.In certain embodiments can before fluid catalytic cracking the poor aromatic fraction of hydrotreatment. |
| priorityDate | 2011-07-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 37.