http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2019504144-A
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2229-42 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2229-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1074 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01F7-141 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-084 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-0045 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-166 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-036 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-7815 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J21-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G47-20 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G47-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J37-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J37-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J37-03 |
| filingDate | 2016-11-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2019-02-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | JP-2019504144-A |
| titleOfInvention | Process for hydrocracking hydrocarbon feedstocks using a catalyst comprising zeolite and amorphous mesoporous alumina |
| abstract | The present invention is a process for hydrocracking at least one hydrocarbon feedstock, wherein a minimum of 50% by weight of the compounds in the feedstock has an initial boiling point of less than 300 ° C and an end fraction of less than 540 ° C. The aperture is defined by a ring having at least one metal from group VIB and / or at least one metal from group VIII of the periodic table and a ring having 12 oxygen atoms (12MR) Using at least one catalyst comprising at least one zeolite having at least one series of channels and a support comprising at least one binder, wherein the support is prepared from a highly dispersible alumina gel. The hydrocracking process is performed at a temperature of 200 ° C. to 480 ° C. and a total pressure of 1 MPa to 25 MPa, and the volume ratio of hydrogen to hydrocarbon feedstock is 80 to 5000 liters / A liter, hourly space velocity (HSV) is defined by the ratio of the volume of the catalyst loaded in the volumetric flow versus reactor liquid hydrocarbon feedstock is 0.1～50H -1, describes a method To do. |
| priorityDate | 2015-12-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 116.