Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation

A heavy residual petroleum feed boiling above 650° F.+ (345° C.+) is subjected to hydroconversion at elevated temperature in the presence of hydrogen at a hydrogen pressure not normally higher than 500 psig (3500 kPag) using a dispersed metal-on-carbon catalyst to produce a hydroconverted effluent w...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Hauptverfasser: GORBATY MARTIN L, KALDOR ANDREW, CORCORAN EDWARD W, FERRUGHELLI DAVID T, CUNDY STEPHEN M
Format: Patent
Sprache:eng
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 GORBATY MARTIN L
KALDOR ANDREW
CORCORAN EDWARD W
FERRUGHELLI DAVID T
CUNDY STEPHEN M
description A heavy residual petroleum feed boiling above 650° F.+ (345° C.+) is subjected to hydroconversion at elevated temperature in the presence of hydrogen at a hydrogen pressure not normally higher than 500 psig (3500 kPag) using a dispersed metal-on-carbon catalyst to produce a hydroconverted effluent which is fractionated to form a low boiling fraction and a relatively higher boiling fraction which is subjected to membrane separation to produce a permeate which is low in metals and Microcarbon Residue (MCR) as well as a retentate, containing most of the MCR and metals. The process has the advantage that the hydroconversion may be carried out in low pressure equipment with a low hydrogen consumption as saturation of aromatics is reduced.
format Patent
fullrecord <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_US7931798B2</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>US7931798B2</sourcerecordid><originalsourceid>FETCH-epo_espacenet_US7931798B23</originalsourceid><addsrcrecordid>eNqNjDEOgkAQRWksjHqHuYCFUqCtRkOv1mSBTyRZdjYzC4ZLeGansLKymfn_5ects3c5t8INhwmiPQeK1qBKHQtFJGGPcSCB9q1SPdPzZ88WqHFSW9YxRpaElgYk5w3bnTWZzHt-GTeBwqNJ_QQbDbW4AEPRiUumW2eLznnF5vtXGV0v93O5ReQKGl2DgFQ9bsUx3xXHw2mf_zH5ALqrUKY</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation</title><source>esp@cenet</source><creator>GORBATY MARTIN L ; KALDOR ANDREW ; CORCORAN EDWARD W ; FERRUGHELLI DAVID T ; CUNDY STEPHEN M</creator><creatorcontrib>GORBATY MARTIN L ; KALDOR ANDREW ; CORCORAN EDWARD W ; FERRUGHELLI DAVID T ; CUNDY STEPHEN M</creatorcontrib><description>A heavy residual petroleum feed boiling above 650° F.+ (345° C.+) is subjected to hydroconversion at elevated temperature in the presence of hydrogen at a hydrogen pressure not normally higher than 500 psig (3500 kPag) using a dispersed metal-on-carbon catalyst to produce a hydroconverted effluent which is fractionated to form a low boiling fraction and a relatively higher boiling fraction which is subjected to membrane separation to produce a permeate which is low in metals and Microcarbon Residue (MCR) as well as a retentate, containing most of the MCR and metals. The process has the advantage that the hydroconversion may be carried out in low pressure equipment with a low hydrogen consumption as saturation of aromatics is reduced.</description><language>eng</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; ORGANIC CHEMISTRY ; PEAT ; PETROLEUM, GAS OR COKE INDUSTRIES ; 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</subject><creationdate>2011</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=20110426&amp;DB=EPODOC&amp;CC=US&amp;NR=7931798B2$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=20110426&amp;DB=EPODOC&amp;CC=US&amp;NR=7931798B2$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>GORBATY MARTIN L</creatorcontrib><creatorcontrib>KALDOR ANDREW</creatorcontrib><creatorcontrib>CORCORAN EDWARD W</creatorcontrib><creatorcontrib>FERRUGHELLI DAVID T</creatorcontrib><creatorcontrib>CUNDY STEPHEN M</creatorcontrib><title>Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation</title><description>A heavy residual petroleum feed boiling above 650° F.+ (345° C.+) is subjected to hydroconversion at elevated temperature in the presence of hydrogen at a hydrogen pressure not normally higher than 500 psig (3500 kPag) using a dispersed metal-on-carbon catalyst to produce a hydroconverted effluent which is fractionated to form a low boiling fraction and a relatively higher boiling fraction which is subjected to membrane separation to produce a permeate which is low in metals and Microcarbon Residue (MCR) as well as a retentate, containing most of the MCR and metals. The process has the advantage that the hydroconversion may be carried out in low pressure equipment with a low hydrogen consumption as saturation of aromatics is reduced.</description><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS</subject><subject>CHEMISTRY</subject><subject>CRACKING HYDROCARBON OILS</subject><subject>FUELS</subject><subject>LUBRICANTS</subject><subject>METALLURGY</subject><subject>MINERAL WAXES</subject><subject>ORGANIC CHEMISTRY</subject><subject>PEAT</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</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><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2011</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNjDEOgkAQRWksjHqHuYCFUqCtRkOv1mSBTyRZdjYzC4ZLeGansLKymfn_5ects3c5t8INhwmiPQeK1qBKHQtFJGGPcSCB9q1SPdPzZ88WqHFSW9YxRpaElgYk5w3bnTWZzHt-GTeBwqNJ_QQbDbW4AEPRiUumW2eLznnF5vtXGV0v93O5ReQKGl2DgFQ9bsUx3xXHw2mf_zH5ALqrUKY</recordid><startdate>20110426</startdate><enddate>20110426</enddate><creator>GORBATY MARTIN L</creator><creator>KALDOR ANDREW</creator><creator>CORCORAN EDWARD W</creator><creator>FERRUGHELLI DAVID T</creator><creator>CUNDY STEPHEN M</creator><scope>EVB</scope></search><sort><creationdate>20110426</creationdate><title>Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation</title><author>GORBATY MARTIN L ; KALDOR ANDREW ; CORCORAN EDWARD W ; FERRUGHELLI DAVID T ; CUNDY STEPHEN M</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_US7931798B23</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>2011</creationdate><topic>ACYCLIC OR CARBOCYCLIC COMPOUNDS</topic><topic>CHEMISTRY</topic><topic>CRACKING HYDROCARBON OILS</topic><topic>FUELS</topic><topic>LUBRICANTS</topic><topic>METALLURGY</topic><topic>MINERAL WAXES</topic><topic>ORGANIC CHEMISTRY</topic><topic>PEAT</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</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><toplevel>online_resources</toplevel><creatorcontrib>GORBATY MARTIN L</creatorcontrib><creatorcontrib>KALDOR ANDREW</creatorcontrib><creatorcontrib>CORCORAN EDWARD W</creatorcontrib><creatorcontrib>FERRUGHELLI DAVID T</creatorcontrib><creatorcontrib>CUNDY STEPHEN M</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>GORBATY MARTIN L</au><au>KALDOR ANDREW</au><au>CORCORAN EDWARD W</au><au>FERRUGHELLI DAVID T</au><au>CUNDY STEPHEN M</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation</title><date>2011-04-26</date><risdate>2011</risdate><abstract>A heavy residual petroleum feed boiling above 650° F.+ (345° C.+) is subjected to hydroconversion at elevated temperature in the presence of hydrogen at a hydrogen pressure not normally higher than 500 psig (3500 kPag) using a dispersed metal-on-carbon catalyst to produce a hydroconverted effluent which is fractionated to form a low boiling fraction and a relatively higher boiling fraction which is subjected to membrane separation to produce a permeate which is low in metals and Microcarbon Residue (MCR) as well as a retentate, containing most of the MCR and metals. The process has the advantage that the hydroconversion may be carried out in low pressure equipment with a low hydrogen consumption as saturation of aromatics is reduced.</abstract><oa>free_for_read</oa></addata></record>
fulltext fulltext_linktorsrc
identifier
ispartof
issn
language eng
recordid cdi_epo_espacenet_US7931798B2
source esp@cenet
subjects ACYCLIC OR CARBOCYCLIC COMPOUNDS
CHEMISTRY
CRACKING HYDROCARBON OILS
FUELS
LUBRICANTS
METALLURGY
MINERAL WAXES
ORGANIC CHEMISTRY
PEAT
PETROLEUM, GAS OR COKE INDUSTRIES
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
title Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-02T10%3A09%3A06IST&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=GORBATY%20MARTIN%20L&rft.date=2011-04-26&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EUS7931798B2%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