http://rdf.ncbi.nlm.nih.gov/pubchem/patent/ES-2643987-T3
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_011e773a3b21737d887a6c7e81d99943 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-202 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2300-1074 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J27-19 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-002 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G69-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-0203 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J37-0207 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J27-19 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J37-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J35-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G69-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-04 |
| filingDate | 2014-10-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2017-11-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9ed685305435972c3cdf600473532aa5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ed564e528d4b7c4aecdbce1987a371c0 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1fb2308d26837ff67c11de037d62df4a |
| publicationDate | 2017-11-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | ES-2643987-T3 |
| titleOfInvention | Vacuum distillation hydrotreatment procedure using a sequence of catalysts |
| abstract | Process for hydrotreating a hydrocarbon load that contains nitrogen compounds with a content greater than 250 ppm by weight and that has a weighted average temperature greater than 380 ° C, comprising the following steps: a) contacting said hydrogen in the presence of hydrocarbon loading with at least one first catalyst comprising an amorphous support based on alumina, phosphorus and an active phase formed by at least one metal of group VIB in the form of oxide and at least one metal of group VIII in the form of oxide, the first catalyst being prepared according to a process that comprises at least one calcination step, b) contacting in the presence of hydrogen the effluent obtained from step a) with at least one second catalyst comprising an amorphous support a alumina base, phosphorous, an active phase formed by at least one group VIB metal and at least one group VIII metal, and at least one organic compound containing oxygen and / or nitrogen, the second catalyst being prepared according to a process comprising the following steps: i) contacting at least one compound of a group VIB metal, at least one compound of a group VIII metal, phosphorus and at least one organic compound containing oxygen and / or nitrogen with the support, so that a catalyst precursor is obtained, ii) drying said catalyst precursor obtained in step i) at a temperature lower than 200 ° C, without subsequently calcine it, so that a hydrotreated effluent is obtained. |
| priorityDate | 2013-11-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 83.