| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_3a4eba1fe6c976b42e8ddc0258ae962b |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-30
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-22
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-20
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G11-05
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G51-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C11-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C15-00 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C4-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G11-05
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G51-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C4-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G69-04 |
| classificationIPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C15-00 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C4-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C4-06 |
| filingDate |
2015-06-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_99484b35f727dc0374a3ed3e55b00da9
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_03f611137776d7875b633807695c86e2
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ff449844f435f34a606a91d318bf59e0
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c739c9be87297b28c2ffabdca1f680af
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3292b243bab5998ee1a20f6703df8f88 |
| publicationDate |
2016-12-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
WO-2016192041-A1 |
| titleOfInvention |
Process for converting naphtha |
| abstract |
Disclosed is a process for converting naphtha. Lower olefin, light aromatic hydrocarbon, and gasoline with high octane number are produced through combining catalytic cracking of naphtha with steam cracking of lower alkane and catalytic cracking of higher alkane and higher olefin. The process increases the yield of product with high value and decreases the yield of product with low value significantly. At the same time, the power consumption is decreased as a whole since most reactants are converted in catalytic cracking at lower temperature. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-112513229-A |
| priorityDate |
2015-06-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |