PROCESS FOR OBTAINING BENZENES AND A CATALYST

A process is proposed for obtaining benzenes involving catalytic reforming of benzene fractions, subsequent hydroconversion in the presence of a catalyst and extraction of the product thus obtained. The composition of the proposed catalyst is as follows (figures in wt. %): high silicon zeolite in am...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Hauptverfasser: ESIPKO, EVGENY ALEXEEVICH, KASTERIN, VLADIMIR NIKOLAEVICH, BOLDINOV, VLADIMIR ANATOLIEVICH, ZAYASHNIKOV, EVGENY NIKOLAEVICH, KHVOSTENKO, NIKOLAI NIKOLAEVICH, PROKOFIEV, VIKTOR PETROVICH, LAGUTENKO, NIKOLAI MAKAROVICH
Format: Patent
Sprache:eng ; fre ; rus
Schlagworte:
Online-Zugang:Volltext bestellen
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page
container_issue
container_start_page
container_title
container_volume
creator ESIPKO, EVGENY ALEXEEVICH
KASTERIN, VLADIMIR NIKOLAEVICH
BOLDINOV, VLADIMIR ANATOLIEVICH
ZAYASHNIKOV, EVGENY NIKOLAEVICH
KHVOSTENKO, NIKOLAI NIKOLAEVICH
PROKOFIEV, VIKTOR PETROVICH
LAGUTENKO, NIKOLAI MAKAROVICH
description A process is proposed for obtaining benzenes involving catalytic reforming of benzene fractions, subsequent hydroconversion in the presence of a catalyst and extraction of the product thus obtained. The composition of the proposed catalyst is as follows (figures in wt. %): high silicon zeolite in ammonium form 30-55; U-type zeolite 4-10; molybdenum oxide 8-15; palladium oxide 0.3-10; aluminium oxide the remainder. L'invention concerne un procédé qui permet d'obtenir des benzènes par reformage catalytique de fractions de benzènes, puis par hydroconversion effectuée en présence d'un catalyseur, et enfin par extraction du produit obtenu. La composition du catalyseur d'hydroconversion est la suivante (en pourcentage en poids); zéolite à haute teneur en silicone, sous forme ammoniacale, 30-55; zéolite de type U, 4-10; oxyde de molybdène, 8-15; oxyde de palladium, 0,3-10; le reste étant d'oxyde d'aluminium.
format Patent
fullrecord <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_WO9500605A1</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>WO9500605A1</sourcerecordid><originalsourceid>FETCH-epo_espacenet_WO9500605A13</originalsourceid><addsrcrecordid>eNrjZNANCPJ3dg0OVnDzD1Lwdwpx9PTz9HNXcHL1i3L1cw1WcPRzUXBUcHYMcfSJDA7hYWBNS8wpTuWF0twMCm6uIc4euqkF-fGpxQWJyal5qSXx4f6WpgYGZgamjobGRCgBAGoJJQQ</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>PROCESS FOR OBTAINING BENZENES AND A CATALYST</title><source>esp@cenet</source><creator>ESIPKO, EVGENY ALEXEEVICH ; KASTERIN, VLADIMIR NIKOLAEVICH ; BOLDINOV, VLADIMIR ANATOLIEVICH ; ZAYASHNIKOV, EVGENY NIKOLAEVICH ; KHVOSTENKO, NIKOLAI NIKOLAEVICH ; PROKOFIEV, VIKTOR PETROVICH ; LAGUTENKO, NIKOLAI MAKAROVICH</creator><creatorcontrib>ESIPKO, EVGENY ALEXEEVICH ; KASTERIN, VLADIMIR NIKOLAEVICH ; BOLDINOV, VLADIMIR ANATOLIEVICH ; ZAYASHNIKOV, EVGENY NIKOLAEVICH ; KHVOSTENKO, NIKOLAI NIKOLAEVICH ; PROKOFIEV, VIKTOR PETROVICH ; LAGUTENKO, NIKOLAI MAKAROVICH</creatorcontrib><description>A process is proposed for obtaining benzenes involving catalytic reforming of benzene fractions, subsequent hydroconversion in the presence of a catalyst and extraction of the product thus obtained. The composition of the proposed catalyst is as follows (figures in wt. %): high silicon zeolite in ammonium form 30-55; U-type zeolite 4-10; molybdenum oxide 8-15; palladium oxide 0.3-10; aluminium oxide the remainder. L'invention concerne un procédé qui permet d'obtenir des benzènes par reformage catalytique de fractions de benzènes, puis par hydroconversion effectuée en présence d'un catalyseur, et enfin par extraction du produit obtenu. La composition du catalyseur d'hydroconversion est la suivante (en pourcentage en poids); zéolite à haute teneur en silicone, sous forme ammoniacale, 30-55; zéolite de type U, 4-10; oxyde de molybdène, 8-15; oxyde de palladium, 0,3-10; le reste étant d'oxyde d'aluminium.</description><edition>5</edition><language>eng ; fre ; rus</language><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; PEAT ; PERFORMING OPERATIONS ; PETROLEUM, GAS OR COKE INDUSTRIES ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION ; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES ; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS ; REFORMING OF NAPHTHA ; TECHNICAL GASES CONTAINING CARBON MONOXIDE ; THEIR RELEVANT APPARATUS ; TRANSPORTING</subject><creationdate>1995</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=19950105&amp;DB=EPODOC&amp;CC=WO&amp;NR=9500605A1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,778,883,25551,76302</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=19950105&amp;DB=EPODOC&amp;CC=WO&amp;NR=9500605A1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>ESIPKO, EVGENY ALEXEEVICH</creatorcontrib><creatorcontrib>KASTERIN, VLADIMIR NIKOLAEVICH</creatorcontrib><creatorcontrib>BOLDINOV, VLADIMIR ANATOLIEVICH</creatorcontrib><creatorcontrib>ZAYASHNIKOV, EVGENY NIKOLAEVICH</creatorcontrib><creatorcontrib>KHVOSTENKO, NIKOLAI NIKOLAEVICH</creatorcontrib><creatorcontrib>PROKOFIEV, VIKTOR PETROVICH</creatorcontrib><creatorcontrib>LAGUTENKO, NIKOLAI MAKAROVICH</creatorcontrib><title>PROCESS FOR OBTAINING BENZENES AND A CATALYST</title><description>A process is proposed for obtaining benzenes involving catalytic reforming of benzene fractions, subsequent hydroconversion in the presence of a catalyst and extraction of the product thus obtained. The composition of the proposed catalyst is as follows (figures in wt. %): high silicon zeolite in ammonium form 30-55; U-type zeolite 4-10; molybdenum oxide 8-15; palladium oxide 0.3-10; aluminium oxide the remainder. L'invention concerne un procédé qui permet d'obtenir des benzènes par reformage catalytique de fractions de benzènes, puis par hydroconversion effectuée en présence d'un catalyseur, et enfin par extraction du produit obtenu. La composition du catalyseur d'hydroconversion est la suivante (en pourcentage en poids); zéolite à haute teneur en silicone, sous forme ammoniacale, 30-55; zéolite de type U, 4-10; oxyde de molybdène, 8-15; oxyde de palladium, 0,3-10; le reste étant d'oxyde d'aluminium.</description><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</subject><subject>CHEMISTRY</subject><subject>CRACKING HYDROCARBON OILS</subject><subject>FUELS</subject><subject>LUBRICANTS</subject><subject>METALLURGY</subject><subject>MINERAL WAXES</subject><subject>PEAT</subject><subject>PERFORMING OPERATIONS</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</subject><subject>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</subject><subject>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</subject><subject>REFORMING OF NAPHTHA</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1995</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZNANCPJ3dg0OVnDzD1Lwdwpx9PTz9HNXcHL1i3L1cw1WcPRzUXBUcHYMcfSJDA7hYWBNS8wpTuWF0twMCm6uIc4euqkF-fGpxQWJyal5qSXx4f6WpgYGZgamjobGRCgBAGoJJQQ</recordid><startdate>19950105</startdate><enddate>19950105</enddate><creator>ESIPKO, EVGENY ALEXEEVICH</creator><creator>KASTERIN, VLADIMIR NIKOLAEVICH</creator><creator>BOLDINOV, VLADIMIR ANATOLIEVICH</creator><creator>ZAYASHNIKOV, EVGENY NIKOLAEVICH</creator><creator>KHVOSTENKO, NIKOLAI NIKOLAEVICH</creator><creator>PROKOFIEV, VIKTOR PETROVICH</creator><creator>LAGUTENKO, NIKOLAI MAKAROVICH</creator><scope>EVB</scope></search><sort><creationdate>19950105</creationdate><title>PROCESS FOR OBTAINING BENZENES AND A CATALYST</title><author>ESIPKO, EVGENY ALEXEEVICH ; KASTERIN, VLADIMIR NIKOLAEVICH ; BOLDINOV, VLADIMIR ANATOLIEVICH ; ZAYASHNIKOV, EVGENY NIKOLAEVICH ; KHVOSTENKO, NIKOLAI NIKOLAEVICH ; PROKOFIEV, VIKTOR PETROVICH ; LAGUTENKO, NIKOLAI MAKAROVICH</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_WO9500605A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; fre ; rus</language><creationdate>1995</creationdate><topic>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</topic><topic>CHEMISTRY</topic><topic>CRACKING HYDROCARBON OILS</topic><topic>FUELS</topic><topic>LUBRICANTS</topic><topic>METALLURGY</topic><topic>MINERAL WAXES</topic><topic>PEAT</topic><topic>PERFORMING OPERATIONS</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</topic><topic>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</topic><topic>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</topic><topic>REFORMING OF NAPHTHA</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>ESIPKO, EVGENY ALEXEEVICH</creatorcontrib><creatorcontrib>KASTERIN, VLADIMIR NIKOLAEVICH</creatorcontrib><creatorcontrib>BOLDINOV, VLADIMIR ANATOLIEVICH</creatorcontrib><creatorcontrib>ZAYASHNIKOV, EVGENY NIKOLAEVICH</creatorcontrib><creatorcontrib>KHVOSTENKO, NIKOLAI NIKOLAEVICH</creatorcontrib><creatorcontrib>PROKOFIEV, VIKTOR PETROVICH</creatorcontrib><creatorcontrib>LAGUTENKO, NIKOLAI MAKAROVICH</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>ESIPKO, EVGENY ALEXEEVICH</au><au>KASTERIN, VLADIMIR NIKOLAEVICH</au><au>BOLDINOV, VLADIMIR ANATOLIEVICH</au><au>ZAYASHNIKOV, EVGENY NIKOLAEVICH</au><au>KHVOSTENKO, NIKOLAI NIKOLAEVICH</au><au>PROKOFIEV, VIKTOR PETROVICH</au><au>LAGUTENKO, NIKOLAI MAKAROVICH</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>PROCESS FOR OBTAINING BENZENES AND A CATALYST</title><date>1995-01-05</date><risdate>1995</risdate><abstract>A process is proposed for obtaining benzenes involving catalytic reforming of benzene fractions, subsequent hydroconversion in the presence of a catalyst and extraction of the product thus obtained. The composition of the proposed catalyst is as follows (figures in wt. %): high silicon zeolite in ammonium form 30-55; U-type zeolite 4-10; molybdenum oxide 8-15; palladium oxide 0.3-10; aluminium oxide the remainder. L'invention concerne un procédé qui permet d'obtenir des benzènes par reformage catalytique de fractions de benzènes, puis par hydroconversion effectuée en présence d'un catalyseur, et enfin par extraction du produit obtenu. La composition du catalyseur d'hydroconversion est la suivante (en pourcentage en poids); zéolite à haute teneur en silicone, sous forme ammoniacale, 30-55; zéolite de type U, 4-10; oxyde de molybdène, 8-15; oxyde de palladium, 0,3-10; le reste étant d'oxyde d'aluminium.</abstract><edition>5</edition><oa>free_for_read</oa></addata></record>
fulltext fulltext_linktorsrc
identifier
ispartof
issn
language eng ; fre ; rus
recordid cdi_epo_espacenet_WO9500605A1
source esp@cenet
subjects CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY
CHEMISTRY
CRACKING HYDROCARBON OILS
FUELS
LUBRICANTS
METALLURGY
MINERAL WAXES
PEAT
PERFORMING OPERATIONS
PETROLEUM, GAS OR COKE INDUSTRIES
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION
RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES
REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS
REFORMING OF NAPHTHA
TECHNICAL GASES CONTAINING CARBON MONOXIDE
THEIR RELEVANT APPARATUS
TRANSPORTING
title PROCESS FOR OBTAINING BENZENES AND A CATALYST
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-15T14%3A54%3A24IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-epo_EVB&rft_val_fmt=info:ofi/fmt:kev:mtx:patent&rft.genre=patent&rft.au=ESIPKO,%20EVGENY%20ALEXEEVICH&rft.date=1995-01-05&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EWO9500605A1%3C/epo_EVB%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true