CATALYST FOR GAS DESULPHURISATION, METHOD OF PRODUCTION AND METHOD OF GAS DESULPHURISATION WITH USING THIS CATALYST

FIELD: chemistry. ^ SUBSTANCE: there is disclosed selective oxidation catalyst of gas hydrogen sulphide to element sulphur on carbon carrier containing natural ferric oxide. Herewith catalyst is additionally introduced with ferric oxide in amount 0.5-2.0 wt % and magnesium oxide in amount 0.1-0.5 wt...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Hauptverfasser: MAKSIMOV JURIJ VASIL'EVICH, GURKO ALEKSANDR ALEKSANDROVICH, PEREDERIJ MARGARITA ALEKSEEVNA, SMIRNOV VLADIMIR VALENTINOVICH, TSODIKOV MARK VENIAMINOVICH, KARASEVA MARIJA SERGEEVNA
Format: Patent
Sprache:eng ; 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 MAKSIMOV JURIJ VASIL'EVICH
GURKO ALEKSANDR ALEKSANDROVICH
PEREDERIJ MARGARITA ALEKSEEVNA
SMIRNOV VLADIMIR VALENTINOVICH
TSODIKOV MARK VENIAMINOVICH
KARASEVA MARIJA SERGEEVNA
description FIELD: chemistry. ^ SUBSTANCE: there is disclosed selective oxidation catalyst of gas hydrogen sulphide to element sulphur on carbon carrier containing natural ferric oxide. Herewith catalyst is additionally introduced with ferric oxide in amount 0.5-2.0 wt % and magnesium oxide in amount 0.1-0.5 wt % on metal basis. Substrate is high-ash microcellular carbon carrier made of low-caking fossil coal by crushing, water granulation, drying, carbonisation in inert medium, and gas-vapour activation. Besides, there are described method of catalyst production and method of gas desulphurisation. ^ EFFECT: production of new catalyst ensuring comprehensive adsorption catalytic removal of hydrogen sulphide in gas, improved engineering-and-economical performance ensured with temperature reduction, higher sulphur content and catalyst service life. ^ 5 cl, 2 tbl, 31 ex
format Patent
fullrecord <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_RU2350387C2</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>RU2350387C2</sourcerecordid><originalsourceid>FETCH-epo_espacenet_RU2350387C23</originalsourceid><addsrcrecordid>eNrjZCh2dgxx9IkMDlFw8w9ScHcMVnBxDQ71CfAIDfIMdgzx9PfTUfB1DfHwd1Hwd1MICPJ3CXUGiSo4-rkgSWDTqBDuGeKhEBrs6eeuEOLhGawAs4qHgTUtMac4lRdKczMouLmGOHvophbkx6cWFyQmp-allsQHhRoZmxoYW5g7GxkToQQAPa04vQ</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>CATALYST FOR GAS DESULPHURISATION, METHOD OF PRODUCTION AND METHOD OF GAS DESULPHURISATION WITH USING THIS CATALYST</title><source>esp@cenet</source><creator>MAKSIMOV JURIJ VASIL'EVICH ; GURKO ALEKSANDR ALEKSANDROVICH ; PEREDERIJ MARGARITA ALEKSEEVNA ; SMIRNOV VLADIMIR VALENTINOVICH ; TSODIKOV MARK VENIAMINOVICH ; KARASEVA MARIJA SERGEEVNA</creator><creatorcontrib>MAKSIMOV JURIJ VASIL'EVICH ; GURKO ALEKSANDR ALEKSANDROVICH ; PEREDERIJ MARGARITA ALEKSEEVNA ; SMIRNOV VLADIMIR VALENTINOVICH ; TSODIKOV MARK VENIAMINOVICH ; KARASEVA MARIJA SERGEEVNA</creatorcontrib><description>FIELD: chemistry. ^ SUBSTANCE: there is disclosed selective oxidation catalyst of gas hydrogen sulphide to element sulphur on carbon carrier containing natural ferric oxide. Herewith catalyst is additionally introduced with ferric oxide in amount 0.5-2.0 wt % and magnesium oxide in amount 0.1-0.5 wt % on metal basis. Substrate is high-ash microcellular carbon carrier made of low-caking fossil coal by crushing, water granulation, drying, carbonisation in inert medium, and gas-vapour activation. Besides, there are described method of catalyst production and method of gas desulphurisation. ^ EFFECT: production of new catalyst ensuring comprehensive adsorption catalytic removal of hydrogen sulphide in gas, improved engineering-and-economical performance ensured with temperature reduction, higher sulphur content and catalyst service life. ^ 5 cl, 2 tbl, 31 ex</description><language>eng ; rus</language><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; SEPARATION ; THEIR RELEVANT APPARATUS ; TRANSPORTING</subject><creationdate>2009</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=20090327&amp;DB=EPODOC&amp;CC=RU&amp;NR=2350387C2$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=20090327&amp;DB=EPODOC&amp;CC=RU&amp;NR=2350387C2$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>MAKSIMOV JURIJ VASIL'EVICH</creatorcontrib><creatorcontrib>GURKO ALEKSANDR ALEKSANDROVICH</creatorcontrib><creatorcontrib>PEREDERIJ MARGARITA ALEKSEEVNA</creatorcontrib><creatorcontrib>SMIRNOV VLADIMIR VALENTINOVICH</creatorcontrib><creatorcontrib>TSODIKOV MARK VENIAMINOVICH</creatorcontrib><creatorcontrib>KARASEVA MARIJA SERGEEVNA</creatorcontrib><title>CATALYST FOR GAS DESULPHURISATION, METHOD OF PRODUCTION AND METHOD OF GAS DESULPHURISATION WITH USING THIS CATALYST</title><description>FIELD: chemistry. ^ SUBSTANCE: there is disclosed selective oxidation catalyst of gas hydrogen sulphide to element sulphur on carbon carrier containing natural ferric oxide. Herewith catalyst is additionally introduced with ferric oxide in amount 0.5-2.0 wt % and magnesium oxide in amount 0.1-0.5 wt % on metal basis. Substrate is high-ash microcellular carbon carrier made of low-caking fossil coal by crushing, water granulation, drying, carbonisation in inert medium, and gas-vapour activation. Besides, there are described method of catalyst production and method of gas desulphurisation. ^ EFFECT: production of new catalyst ensuring comprehensive adsorption catalytic removal of hydrogen sulphide in gas, improved engineering-and-economical performance ensured with temperature reduction, higher sulphur content and catalyst service life. ^ 5 cl, 2 tbl, 31 ex</description><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</subject><subject>PERFORMING OPERATIONS</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>SEPARATION</subject><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2009</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZCh2dgxx9IkMDlFw8w9ScHcMVnBxDQ71CfAIDfIMdgzx9PfTUfB1DfHwd1Hwd1MICPJ3CXUGiSo4-rkgSWDTqBDuGeKhEBrs6eeuEOLhGawAs4qHgTUtMac4lRdKczMouLmGOHvophbkx6cWFyQmp-allsQHhRoZmxoYW5g7GxkToQQAPa04vQ</recordid><startdate>20090327</startdate><enddate>20090327</enddate><creator>MAKSIMOV JURIJ VASIL'EVICH</creator><creator>GURKO ALEKSANDR ALEKSANDROVICH</creator><creator>PEREDERIJ MARGARITA ALEKSEEVNA</creator><creator>SMIRNOV VLADIMIR VALENTINOVICH</creator><creator>TSODIKOV MARK VENIAMINOVICH</creator><creator>KARASEVA MARIJA SERGEEVNA</creator><scope>EVB</scope></search><sort><creationdate>20090327</creationdate><title>CATALYST FOR GAS DESULPHURISATION, METHOD OF PRODUCTION AND METHOD OF GAS DESULPHURISATION WITH USING THIS CATALYST</title><author>MAKSIMOV JURIJ VASIL'EVICH ; GURKO ALEKSANDR ALEKSANDROVICH ; PEREDERIJ MARGARITA ALEKSEEVNA ; SMIRNOV VLADIMIR VALENTINOVICH ; TSODIKOV MARK VENIAMINOVICH ; KARASEVA MARIJA SERGEEVNA</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_RU2350387C23</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; rus</language><creationdate>2009</creationdate><topic>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</topic><topic>PERFORMING OPERATIONS</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>SEPARATION</topic><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>MAKSIMOV JURIJ VASIL'EVICH</creatorcontrib><creatorcontrib>GURKO ALEKSANDR ALEKSANDROVICH</creatorcontrib><creatorcontrib>PEREDERIJ MARGARITA ALEKSEEVNA</creatorcontrib><creatorcontrib>SMIRNOV VLADIMIR VALENTINOVICH</creatorcontrib><creatorcontrib>TSODIKOV MARK VENIAMINOVICH</creatorcontrib><creatorcontrib>KARASEVA MARIJA SERGEEVNA</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>MAKSIMOV JURIJ VASIL'EVICH</au><au>GURKO ALEKSANDR ALEKSANDROVICH</au><au>PEREDERIJ MARGARITA ALEKSEEVNA</au><au>SMIRNOV VLADIMIR VALENTINOVICH</au><au>TSODIKOV MARK VENIAMINOVICH</au><au>KARASEVA MARIJA SERGEEVNA</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>CATALYST FOR GAS DESULPHURISATION, METHOD OF PRODUCTION AND METHOD OF GAS DESULPHURISATION WITH USING THIS CATALYST</title><date>2009-03-27</date><risdate>2009</risdate><abstract>FIELD: chemistry. ^ SUBSTANCE: there is disclosed selective oxidation catalyst of gas hydrogen sulphide to element sulphur on carbon carrier containing natural ferric oxide. Herewith catalyst is additionally introduced with ferric oxide in amount 0.5-2.0 wt % and magnesium oxide in amount 0.1-0.5 wt % on metal basis. Substrate is high-ash microcellular carbon carrier made of low-caking fossil coal by crushing, water granulation, drying, carbonisation in inert medium, and gas-vapour activation. Besides, there are described method of catalyst production and method of gas desulphurisation. ^ EFFECT: production of new catalyst ensuring comprehensive adsorption catalytic removal of hydrogen sulphide in gas, improved engineering-and-economical performance ensured with temperature reduction, higher sulphur content and catalyst service life. ^ 5 cl, 2 tbl, 31 ex</abstract><oa>free_for_read</oa></addata></record>
fulltext fulltext_linktorsrc
identifier
ispartof
issn
language eng ; rus
recordid cdi_epo_espacenet_RU2350387C2
source esp@cenet
subjects CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY
PERFORMING OPERATIONS
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
SEPARATION
THEIR RELEVANT APPARATUS
TRANSPORTING
title CATALYST FOR GAS DESULPHURISATION, METHOD OF PRODUCTION AND METHOD OF GAS DESULPHURISATION WITH USING THIS CATALYST
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-29T06%3A38%3A20IST&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=MAKSIMOV%20JURIJ%20VASIL'EVICH&rft.date=2009-03-27&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3ERU2350387C2%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