Process to prepare naphthenic hydrocarbons-rich hydrocarbon streams
Preparation of naphthenic hydrocarbon fluids by treatment of a petroleum cut obtained from the effluents of a catalytic cracking or vapour cracking unit. Preparation of a hydrocarbon fluid containing at least 705 wt. of naphthenic hydrocarbons and with an aromatics content less than or equal to 1% c...
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creator | ALBOUY, ARNAUD BORG, FRANCOISE VANHAEREN, XAVIER DENIS, JEANRISTOPHE |
description | Preparation of naphthenic hydrocarbon fluids by treatment of a petroleum cut obtained from the effluents of a catalytic cracking or vapour cracking unit. Preparation of a hydrocarbon fluid containing at least 705 wt. of naphthenic hydrocarbons and with an aromatics content less than or equal to 1% comprising stages of (1) (a) withdrawal from an effluent fractionating column of a non-hydrogenating conversion unit, of a hydrocarbon cut of distillation range 100 - 400[deg]C containing at least 705 vol of cyclic unsaturated hydrocarbons; (2) (b) hydrodesulfuration of the cut to obtain a desulfurized cut with a S content less than 50 ppm wt; (3) (c) controlled hydrogenation of the cut in the presence of H 2 and a catalyst comprising a group VIII metal on a solid support at 80 - 350[deg]C and H 2 partial pressure of 30 - 200X10 5>; (4) (d) recovery of the fluid containing at least 70% wt. of naphthenic hydrocarbons and aromatics less than or equal to 1% wt. An independent claim is also included for the installation to effect the process. |
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Preparation of a hydrocarbon fluid containing at least 705 wt. of naphthenic hydrocarbons and with an aromatics content less than or equal to 1% comprising stages of (1) (a) withdrawal from an effluent fractionating column of a non-hydrogenating conversion unit, of a hydrocarbon cut of distillation range 100 - 400[deg]C containing at least 705 vol of cyclic unsaturated hydrocarbons; (2) (b) hydrodesulfuration of the cut to obtain a desulfurized cut with a S content less than 50 ppm wt; (3) (c) controlled hydrogenation of the cut in the presence of H 2 and a catalyst comprising a group VIII metal on a solid support at 80 - 350[deg]C and H 2 partial pressure of 30 - 200X10 5>; (4) (d) recovery of the fluid containing at least 70% wt. of naphthenic hydrocarbons and aromatics less than or equal to 1% wt. An independent claim is also included for the installation to effect the process.</description><language>eng ; fre ; ger</language><subject>CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; 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>2013</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=20130410&DB=EPODOC&CC=EP&NR=1447437B1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20130410&DB=EPODOC&CC=EP&NR=1447437B1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>ALBOUY, ARNAUD</creatorcontrib><creatorcontrib>BORG, FRANCOISE</creatorcontrib><creatorcontrib>VANHAEREN, XAVIER</creatorcontrib><creatorcontrib>DENIS, JEANRISTOPHE</creatorcontrib><title>Process to prepare naphthenic hydrocarbons-rich hydrocarbon streams</title><description>Preparation of naphthenic hydrocarbon fluids by treatment of a petroleum cut obtained from the effluents of a catalytic cracking or vapour cracking unit. Preparation of a hydrocarbon fluid containing at least 705 wt. of naphthenic hydrocarbons and with an aromatics content less than or equal to 1% comprising stages of (1) (a) withdrawal from an effluent fractionating column of a non-hydrogenating conversion unit, of a hydrocarbon cut of distillation range 100 - 400[deg]C containing at least 705 vol of cyclic unsaturated hydrocarbons; (2) (b) hydrodesulfuration of the cut to obtain a desulfurized cut with a S content less than 50 ppm wt; (3) (c) controlled hydrogenation of the cut in the presence of H 2 and a catalyst comprising a group VIII metal on a solid support at 80 - 350[deg]C and H 2 partial pressure of 30 - 200X10 5>; (4) (d) recovery of the fluid containing at least 70% wt. of naphthenic hydrocarbons and aromatics less than or equal to 1% wt. An independent claim is also included for the installation to effect the process.</description><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>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>2013</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZHAOKMpPTi0uVijJVygoSi1ILEpVyEssyCjJSM3LTFbIqEwByicWJeXnFesWZSZnIIsoFJcUpSbmFvMwsKYl5hSn8kJpbgYFN9cQZw_d1IL8-NTigsTk1LzUknjXAEMTE3MTY3MnQ2MilAAAcx0y3g</recordid><startdate>20130410</startdate><enddate>20130410</enddate><creator>ALBOUY, ARNAUD</creator><creator>BORG, FRANCOISE</creator><creator>VANHAEREN, XAVIER</creator><creator>DENIS, JEANRISTOPHE</creator><scope>EVB</scope></search><sort><creationdate>20130410</creationdate><title>Process to prepare naphthenic hydrocarbons-rich hydrocarbon streams</title><author>ALBOUY, ARNAUD ; BORG, FRANCOISE ; VANHAEREN, XAVIER ; DENIS, JEANRISTOPHE</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_EP1447437B13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; fre ; ger</language><creationdate>2013</creationdate><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>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>ALBOUY, ARNAUD</creatorcontrib><creatorcontrib>BORG, FRANCOISE</creatorcontrib><creatorcontrib>VANHAEREN, XAVIER</creatorcontrib><creatorcontrib>DENIS, JEANRISTOPHE</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>ALBOUY, ARNAUD</au><au>BORG, FRANCOISE</au><au>VANHAEREN, XAVIER</au><au>DENIS, JEANRISTOPHE</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Process to prepare naphthenic hydrocarbons-rich hydrocarbon streams</title><date>2013-04-10</date><risdate>2013</risdate><abstract>Preparation of naphthenic hydrocarbon fluids by treatment of a petroleum cut obtained from the effluents of a catalytic cracking or vapour cracking unit. Preparation of a hydrocarbon fluid containing at least 705 wt. of naphthenic hydrocarbons and with an aromatics content less than or equal to 1% comprising stages of (1) (a) withdrawal from an effluent fractionating column of a non-hydrogenating conversion unit, of a hydrocarbon cut of distillation range 100 - 400[deg]C containing at least 705 vol of cyclic unsaturated hydrocarbons; (2) (b) hydrodesulfuration of the cut to obtain a desulfurized cut with a S content less than 50 ppm wt; (3) (c) controlled hydrogenation of the cut in the presence of H 2 and a catalyst comprising a group VIII metal on a solid support at 80 - 350[deg]C and H 2 partial pressure of 30 - 200X10 5>; (4) (d) recovery of the fluid containing at least 70% wt. of naphthenic hydrocarbons and aromatics less than or equal to 1% wt. An independent claim is also included for the installation to effect the process.</abstract><oa>free_for_read</oa></addata></record> |
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language | eng ; fre ; ger |
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subjects | CHEMISTRY CRACKING HYDROCARBON OILS FUELS LUBRICANTS METALLURGY MINERAL WAXES 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 | Process to prepare naphthenic hydrocarbons-rich hydrocarbon streams |
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