Desulphurisation and upgrading of asphaltenic feeds - by catalytic hydrodesulphurisation followed by alkali metal treatment
A process for the combined desulphurisation and conversion of asphaltene-contg. feeds comprises (a) subjecting the feed to hydrodesulphurisation (HDS) in the presence of and HDS catalyst contg. at least one group VIB and/or VIII metal component on a porous support with a pore dia. of 10-100 (pref. 2...
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creator | JUN.,ROBY BEARDEN C. BAIRD,WILLIAM P. HAMNER,GLEN |
description | A process for the combined desulphurisation and conversion of asphaltene-contg. feeds comprises (a) subjecting the feed to hydrodesulphurisation (HDS) in the presence of and HDS catalyst contg. at least one group VIB and/or VIII metal component on a porous support with a pore dia. of 10-100 (pref. 20-80) Angstroms so that the feed is at least partially desulphurised, (d) contacting the product with an alkali metal at high temp. in the presence of added H2 to remove >=50% of the S content of the initial feed and to convert >=50% of the heavy (>1050 degrees F) fraction into lower-boiling products, and (c) isolating the lower-boiling products and the desulphurised feed. The process is esp. useful for treating petroleum residues contg. >30% asphaltenes. |
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HAMNER,GLEN</creatorcontrib><description>A process for the combined desulphurisation and conversion of asphaltene-contg. feeds comprises (a) subjecting the feed to hydrodesulphurisation (HDS) in the presence of and HDS catalyst contg. at least one group VIB and/or VIII metal component on a porous support with a pore dia. of 10-100 (pref. 20-80) Angstroms so that the feed is at least partially desulphurised, (d) contacting the product with an alkali metal at high temp. in the presence of added H2 to remove >=50% of the S content of the initial feed and to convert >=50% of the heavy (>1050 degrees F) fraction into lower-boiling products, and (c) isolating the lower-boiling products and the desulphurised feed. The process is esp. useful for treating petroleum residues contg. >30% asphaltenes.</description><edition>2</edition><language>eng ; ger</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>1976</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=19761118&DB=EPODOC&CC=DE&NR=2558505A1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19761118&DB=EPODOC&CC=DE&NR=2558505A1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>JUN.,ROBY BEARDEN</creatorcontrib><creatorcontrib>C. BAIRD,WILLIAM</creatorcontrib><creatorcontrib>P. HAMNER,GLEN</creatorcontrib><title>Desulphurisation and upgrading of asphaltenic feeds - by catalytic hydrodesulphurisation followed by alkali metal treatment</title><description>A process for the combined desulphurisation and conversion of asphaltene-contg. feeds comprises (a) subjecting the feed to hydrodesulphurisation (HDS) in the presence of and HDS catalyst contg. at least one group VIB and/or VIII metal component on a porous support with a pore dia. of 10-100 (pref. 20-80) Angstroms so that the feed is at least partially desulphurised, (d) contacting the product with an alkali metal at high temp. in the presence of added H2 to remove >=50% of the S content of the initial feed and to convert >=50% of the heavy (>1050 degrees F) fraction into lower-boiling products, and (c) isolating the lower-boiling products and the desulphurised feed. The process is esp. useful for treating petroleum residues contg. >30% asphaltenes.</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>1976</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNjE0KwjAQRrNxIeod5gIFfwi4FVvxAO7LmEza4DQJyRQpXt4Krly5evDxvrdUr5rKyKkfsy8oPgbAYGFMXUbrQwfRAZbUIwsFb8AR2QIV3CcwKMiTzGM_2Rztb8dF5vgk-3GRH8geBpovIJlQBgqyVguHXGjz5UrBpbmdrxWl2FJJaCiQtHWz1_qot_q0O_yhvAG390gI</recordid><startdate>19761118</startdate><enddate>19761118</enddate><creator>JUN.,ROBY BEARDEN</creator><creator>C. 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HAMNER,GLEN</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_DE2558505A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; ger</language><creationdate>1976</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>JUN.,ROBY BEARDEN</creatorcontrib><creatorcontrib>C. BAIRD,WILLIAM</creatorcontrib><creatorcontrib>P. HAMNER,GLEN</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>JUN.,ROBY BEARDEN</au><au>C. BAIRD,WILLIAM</au><au>P. HAMNER,GLEN</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Desulphurisation and upgrading of asphaltenic feeds - by catalytic hydrodesulphurisation followed by alkali metal treatment</title><date>1976-11-18</date><risdate>1976</risdate><abstract>A process for the combined desulphurisation and conversion of asphaltene-contg. feeds comprises (a) subjecting the feed to hydrodesulphurisation (HDS) in the presence of and HDS catalyst contg. at least one group VIB and/or VIII metal component on a porous support with a pore dia. of 10-100 (pref. 20-80) Angstroms so that the feed is at least partially desulphurised, (d) contacting the product with an alkali metal at high temp. in the presence of added H2 to remove >=50% of the S content of the initial feed and to convert >=50% of the heavy (>1050 degrees F) fraction into lower-boiling products, and (c) isolating the lower-boiling products and the desulphurised feed. The process is esp. useful for treating petroleum residues contg. >30% asphaltenes.</abstract><edition>2</edition><oa>free_for_read</oa></addata></record> |
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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 | Desulphurisation and upgrading of asphaltenic feeds - by catalytic hydrodesulphurisation followed by alkali metal treatment |
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