http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2714139-C1
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_9f54e08002a7fb005065961427d317bf |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-06 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-08 |
filingDate | 2019-10-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2020-02-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_883069cec125a1b28a79dfe419bc03fb http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f618540b2112933588075c81646a07f4 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0a12b4d1dec26c619f16139dd87efa6c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_af54bbee4cd16f0e8aec27c806f59bb6 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_67f2c6feb97dfc96a7a5dcfc00cd5a52 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_14e803b86eb507a3f4c5633b9e290975 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_339ce5682822cd23579948d151023078 |
publicationDate | 2020-02-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | RU-2714139-C1 |
titleOfInvention | Method of using a catalyst for hydrogenating diolefins during hydrogenation treatment of petroleum feedstock |
abstract | FIELD: oil and gas industry.SUBSTANCE: invention relates to methods of using a catalyst for hydrogenating diolefins during hydrogenation treatment of petroleum feedstock and can be used in oil refining industry. Disclosed is a method of using a catalyst for hydrogenating diolefins in a hydrogenation treatment of petroleum feedstock, wherein the material is passed through a fixed catalyst bed of a catalyst stack consisting of a basic hydroprocessing catalyst, in form of aluminum-nickel-molybdenum and / or aluminum-cobalt-molybdenum catalyst and protective layers arranged above it. Protective layers include: layer A – inert material for removal of mechanical impurities, layer B – catalyst for hydrogenation of diolefins, consisting of modified carrier prepared on the basis of highly porous cellular material with mesh of 10–30 mesh, grafted layer of gamma-aluminum oxide, as well as bimetallic complex compounds of VIII and VI groups metals deposited on the support. Method is characterized by using layer B catalyst prepared on the basis of highly porous cellular material with open porosity of not less than 50 %, having the shape of discs with diameter of 20–50 mm, height of 20–30 mm, in activated state having specific surface of 12–25 m/g, effective pore diameter of 3–6.7 nm, mesh content of 10–30 mesh, mechanical compression strength of not less than 200 N, wherein content of components in calcined at temperature of 550 °C layer B catalyst is, wt%: high-porous cellular material – 73.0–88.1; γ-AlOin the form of grafted layer – 8.0–22.2; nickel and / or cobalt oxide – not less than 0.5; molybdenum oxide – not less than 2.0. Protective layers additionally include layer B – aluminum-nickel-molybdenum or aluminum-molybdenum catalyst of protective layer located under layers A and B, protective layers making 15–25 % of volume of reactor, and content of layer B makes 27–65 vol% of catalysts of protective layers.EFFECT: method of using a catalyst for hydrogenation of diolefins during batch loading in the process of complex hydrotreatment of hydrocarbon material, which enables to achieve absence of diolefins in hydroforming products.3 cl, 2 tbl |
priorityDate | 2019-10-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 37.