PROCESS OF CATALYTIC REFORMING OF GASOLINE FRACTIONS ON ALUMINUM-PLATINUM-RHENIUM CATALYST
FIELD: petroleum processing and petrochemistry. ^ SUBSTANCE: catalytic reforming carried out at temperature in the reforming zone entry not higher than 485°C is supplemented by sulfidizing accomplished by introducing sulfur-containing compounds by doses each constituting 0.001-0.02% sulfur of the we...
Gespeichert in:
| Hauptverfasser: | , , , , |
|---|---|
| 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 | KORONATOV NIKOLAJ NIKOLAEVICH ZALISHCHEVSKIJ GRIGORIJ DAVYDOVICH SOLOVYKH ALEKSANDR IVANOVICH RABINOVICH GEORGIJ LAZAREVICH FERKEL' EVGENIJ VIKTOROVICH |
| description | FIELD: petroleum processing and petrochemistry. ^ SUBSTANCE: catalytic reforming carried out at temperature in the reforming zone entry not higher than 485°C is supplemented by sulfidizing accomplished by introducing sulfur-containing compounds by doses each constituting 0.001-0.02% sulfur of the weight of catalyst, intervals between doses being not less than 1/2 one dose introduction time and at summary amounts of added sulfur 0.02-0.2% sulfur of the weight of catalyst during additional sulfidizing period. Additional sulfidizing is performed one or several times over the service cycle lasting hundreds or thousands hours. One sulfur dose addition time ranges from 0.5 to 1.5 h. ^ EFFECT: increased yield of reforming catalysate. ^ 3 cl, 1 tbl, 7 ex |
| format | Patent |
| fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_RU2281969C1</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>RU2281969C1</sourcerecordid><originalsourceid>FETCH-epo_espacenet_RU2281969C13</originalsourceid><addsrcrecordid>eNrjZIgKCPJ3dg0OVvB3U3B2DHH0iQzxdFYIcnXzD_L19HMHCbs7Bvv7ePq5KrgFOTqHePr7ARX7KTj6hAIVhPrqBvg4hoAZQR6ufp6hvlBjgkN4GFjTEnOKU3mhNDeDgptriLOHbmpBfnxqcUFicmpeakl8UKiRkYWhpZmls6ExEUoAJe0yDA</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>PROCESS OF CATALYTIC REFORMING OF GASOLINE FRACTIONS ON ALUMINUM-PLATINUM-RHENIUM CATALYST</title><source>esp@cenet</source><creator>KORONATOV NIKOLAJ NIKOLAEVICH ; ZALISHCHEVSKIJ GRIGORIJ DAVYDOVICH ; SOLOVYKH ALEKSANDR IVANOVICH ; RABINOVICH GEORGIJ LAZAREVICH ; FERKEL' EVGENIJ VIKTOROVICH</creator><creatorcontrib>KORONATOV NIKOLAJ NIKOLAEVICH ; ZALISHCHEVSKIJ GRIGORIJ DAVYDOVICH ; SOLOVYKH ALEKSANDR IVANOVICH ; RABINOVICH GEORGIJ LAZAREVICH ; FERKEL' EVGENIJ VIKTOROVICH</creatorcontrib><description>FIELD: petroleum processing and petrochemistry. ^ SUBSTANCE: catalytic reforming carried out at temperature in the reforming zone entry not higher than 485°C is supplemented by sulfidizing accomplished by introducing sulfur-containing compounds by doses each constituting 0.001-0.02% sulfur of the weight of catalyst, intervals between doses being not less than 1/2 one dose introduction time and at summary amounts of added sulfur 0.02-0.2% sulfur of the weight of catalyst during additional sulfidizing period. Additional sulfidizing is performed one or several times over the service cycle lasting hundreds or thousands hours. One sulfur dose addition time ranges from 0.5 to 1.5 h. ^ EFFECT: increased yield of reforming catalysate. ^ 3 cl, 1 tbl, 7 ex</description><language>eng ; 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>2006</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&date=20060820&DB=EPODOC&CC=RU&NR=2281969C1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20060820&DB=EPODOC&CC=RU&NR=2281969C1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>KORONATOV NIKOLAJ NIKOLAEVICH</creatorcontrib><creatorcontrib>ZALISHCHEVSKIJ GRIGORIJ DAVYDOVICH</creatorcontrib><creatorcontrib>SOLOVYKH ALEKSANDR IVANOVICH</creatorcontrib><creatorcontrib>RABINOVICH GEORGIJ LAZAREVICH</creatorcontrib><creatorcontrib>FERKEL' EVGENIJ VIKTOROVICH</creatorcontrib><title>PROCESS OF CATALYTIC REFORMING OF GASOLINE FRACTIONS ON ALUMINUM-PLATINUM-RHENIUM CATALYST</title><description>FIELD: petroleum processing and petrochemistry. ^ SUBSTANCE: catalytic reforming carried out at temperature in the reforming zone entry not higher than 485°C is supplemented by sulfidizing accomplished by introducing sulfur-containing compounds by doses each constituting 0.001-0.02% sulfur of the weight of catalyst, intervals between doses being not less than 1/2 one dose introduction time and at summary amounts of added sulfur 0.02-0.2% sulfur of the weight of catalyst during additional sulfidizing period. Additional sulfidizing is performed one or several times over the service cycle lasting hundreds or thousands hours. One sulfur dose addition time ranges from 0.5 to 1.5 h. ^ EFFECT: increased yield of reforming catalysate. ^ 3 cl, 1 tbl, 7 ex</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>2006</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZIgKCPJ3dg0OVvB3U3B2DHH0iQzxdFYIcnXzD_L19HMHCbs7Bvv7ePq5KrgFOTqHePr7ARX7KTj6hAIVhPrqBvg4hoAZQR6ufp6hvlBjgkN4GFjTEnOKU3mhNDeDgptriLOHbmpBfnxqcUFicmpeakl8UKiRkYWhpZmls6ExEUoAJe0yDA</recordid><startdate>20060820</startdate><enddate>20060820</enddate><creator>KORONATOV NIKOLAJ NIKOLAEVICH</creator><creator>ZALISHCHEVSKIJ GRIGORIJ DAVYDOVICH</creator><creator>SOLOVYKH ALEKSANDR IVANOVICH</creator><creator>RABINOVICH GEORGIJ LAZAREVICH</creator><creator>FERKEL' EVGENIJ VIKTOROVICH</creator><scope>EVB</scope></search><sort><creationdate>20060820</creationdate><title>PROCESS OF CATALYTIC REFORMING OF GASOLINE FRACTIONS ON ALUMINUM-PLATINUM-RHENIUM CATALYST</title><author>KORONATOV NIKOLAJ NIKOLAEVICH ; ZALISHCHEVSKIJ GRIGORIJ DAVYDOVICH ; SOLOVYKH ALEKSANDR IVANOVICH ; RABINOVICH GEORGIJ LAZAREVICH ; FERKEL' EVGENIJ VIKTOROVICH</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_RU2281969C13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; rus</language><creationdate>2006</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>KORONATOV NIKOLAJ NIKOLAEVICH</creatorcontrib><creatorcontrib>ZALISHCHEVSKIJ GRIGORIJ DAVYDOVICH</creatorcontrib><creatorcontrib>SOLOVYKH ALEKSANDR IVANOVICH</creatorcontrib><creatorcontrib>RABINOVICH GEORGIJ LAZAREVICH</creatorcontrib><creatorcontrib>FERKEL' EVGENIJ VIKTOROVICH</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>KORONATOV NIKOLAJ NIKOLAEVICH</au><au>ZALISHCHEVSKIJ GRIGORIJ DAVYDOVICH</au><au>SOLOVYKH ALEKSANDR IVANOVICH</au><au>RABINOVICH GEORGIJ LAZAREVICH</au><au>FERKEL' EVGENIJ VIKTOROVICH</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>PROCESS OF CATALYTIC REFORMING OF GASOLINE FRACTIONS ON ALUMINUM-PLATINUM-RHENIUM CATALYST</title><date>2006-08-20</date><risdate>2006</risdate><abstract>FIELD: petroleum processing and petrochemistry. ^ SUBSTANCE: catalytic reforming carried out at temperature in the reforming zone entry not higher than 485°C is supplemented by sulfidizing accomplished by introducing sulfur-containing compounds by doses each constituting 0.001-0.02% sulfur of the weight of catalyst, intervals between doses being not less than 1/2 one dose introduction time and at summary amounts of added sulfur 0.02-0.2% sulfur of the weight of catalyst during additional sulfidizing period. Additional sulfidizing is performed one or several times over the service cycle lasting hundreds or thousands hours. One sulfur dose addition time ranges from 0.5 to 1.5 h. ^ EFFECT: increased yield of reforming catalysate. ^ 3 cl, 1 tbl, 7 ex</abstract><oa>free_for_read</oa></addata></record> |
| fulltext | fulltext_linktorsrc |
| identifier | |
| ispartof | |
| issn | |
| language | eng ; rus |
| recordid | cdi_epo_espacenet_RU2281969C1 |
| 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 OF CATALYTIC REFORMING OF GASOLINE FRACTIONS ON ALUMINUM-PLATINUM-RHENIUM CATALYST |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-24T21%3A23%3A32IST&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=KORONATOV%20NIKOLAJ%20NIKOLAEVICH&rft.date=2006-08-20&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3ERU2281969C1%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 |