http://rdf.ncbi.nlm.nih.gov/pubchem/patent/SU-1424863-A1

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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J37-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-88
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-883
filingDate 1987-02-16-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 1988-09-23-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5d113df7d1607e04d0135fdae8efaf24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0f5f5eb528ae15f12cb1c430e52e847b
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publicationDate 1988-09-23-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber SU-1424863-A1
titleOfInvention Method of producing catalyst for hydrofining petroleum raw material
abstract The invention relates to catalytic chemistry, in particular the preparation of a catalyst (CT) for the hydrotreatment of petroleum. To increase the degree of purification of the latter, QDs are obtained from, which is peptized with HC1, then with an aqueous solution of SnCl at the rate of 0.2-0.6% tin on a calcined carrier, followed by a hydrocarbon-ammonia molding. Next, Sn-containing Al-Oj is treated with a 5-40% solution of triethylene glycol, calcined, is passed through an ammonia solution of ammonium paramolybdate and nickel nitrate (ratio in terms of oxides: MoOj - 10-14 wt.%, NiO - 3- 6% by weight. These conditions increase the degree of hydrogenation (up to 47%) and hydrodesulfurization (up to 93%) with an increase in the pore volume of QD to 80-120 L and its specific surface area to 275-310 MVr 2 Table 1C
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2801222-C2
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2020209742-A1
priorityDate 1987-02-16-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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Total number of triples: 46.