http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2017009158-A1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_78ca80ad4b743c901ec136b21263f093 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_18a8284bc1d41fe092e46c249d6220be |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1044 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2400-30 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-027 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G63-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G69-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G11-02 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G69-08 |
| filingDate | 2015-02-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_91f7e901391a5ebf2c3cea2610600dd6 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b9a67997bb7459d5f1eac578e0c01a17 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bdb54634877116a164bb04f198f5c7dd |
| publicationDate | 2017-01-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | US-2017009158-A1 |
| titleOfInvention | Process for producing btx from a c5-c12 hydrocarbon mixture |
| abstract | The invention relates to a process for producing BTX comprising: (a) contacting a feedstream comprising C5-C12 hydrocarbons in the presence of hydrogen with a reforming catalyst to produce a reformed product stream, wherein the reforming catalyst comprises a hydrogenation metal and a support of an amorphous alumina, (b) contacting the reformed product stream in the presence of hydrogen with a hydrocracking catalyst to produce a hydrocracking product stream comprising BTX, wherein the hydrocracking catalyst comprises a hydrogenation metal and a zeolite and (c) separating the BTX from the hydrocracking product stream, wherein the hydrocracking catalyst comprises 0.01-1 wt %, preferably 0.01-0.5 wt %, of the hydrogenation metal in relation to the total catalyst weight and the zeolite has a pore size of 5-8 A and a silica (SiO2) to alumina (AI2O3) molar ratio of 5-200, preferably 30-120, wherein step (b) or steps (a) and (b)_are performed at a temperature of 425-580° C., a pressure of 300-5000 kPa gauge and a Weight Hourly Space Velocity of 0.1-15 h −1 preferably 0.1-10 h −1 . |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-11028329-B1 |
| priorityDate | 2014-02-25-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 51.