JP3002756B2 - 反応器への装入前に有機化合物が組込まれている担持金属をベースとする触媒の存在下における、蒸気クラッキングガソリン中のジオレフィンの選択的水素化方法 - Google Patents

反応器への装入前に有機化合物が組込まれている担持金属をベースとする触媒の存在下における、蒸気クラッキングガソリン中のジオレフィンの選択的水素化方法

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Publication number
JP3002756B2
JP3002756B2 JP3172332A JP17233291A JP3002756B2 JP 3002756 B2 JP3002756 B2 JP 3002756B2 JP 3172332 A JP3172332 A JP 3172332A JP 17233291 A JP17233291 A JP 17233291A JP 3002756 B2 JP3002756 B2 JP 3002756B2
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Prior art keywords
catalyst
sulfur
organic
reactor
formula
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Expired - Lifetime
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JP3172332A
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Japanese (ja)
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JPH04226592A (ja
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ジャン・ポール・ボワチオ
パトリック・サラザン
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IFP Energies Nouvelles IFPEN
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IFP Energies Nouvelles IFPEN
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Publication of JPH04226592A publication Critical patent/JPH04226592A/ja
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Expired - Lifetime legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/20Sulfiding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/755Nickel
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/32Selective hydrogenation of the diolefin or acetylene compounds
    • C10G45/34Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
    • C10G45/36Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
JP3172332A 1990-07-13 1991-07-12 反応器への装入前に有機化合物が組込まれている担持金属をベースとする触媒の存在下における、蒸気クラッキングガソリン中のジオレフィンの選択的水素化方法 Expired - Lifetime JP3002756B2 (ja)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9009079 1990-07-13
FR9009079A FR2664610A1 (fr) 1990-07-13 1990-07-13 Hydrogenation selective des essences de vapocraquage sur des catalyseurs a base d'un metal supporte dans lesquels un compose organique a ete incorpore avant chargement dans le reacteur.

Publications (2)

Publication Number Publication Date
JPH04226592A JPH04226592A (ja) 1992-08-17
JP3002756B2 true JP3002756B2 (ja) 2000-01-24

Family

ID=9398791

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3172332A Expired - Lifetime JP3002756B2 (ja) 1990-07-13 1991-07-12 反応器への装入前に有機化合物が組込まれている担持金属をベースとする触媒の存在下における、蒸気クラッキングガソリン中のジオレフィンの選択的水素化方法

Country Status (6)

Country Link
US (1) US5417844A (enExample)
EP (1) EP0466567B1 (enExample)
JP (1) JP3002756B2 (enExample)
AT (1) ATE99354T1 (enExample)
DE (1) DE69100881T2 (enExample)
FR (1) FR2664610A1 (enExample)

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FR2730728B1 (fr) * 1995-02-21 1997-05-23 Inst Francais Du Petrole Procede de separation du p-xylene comportant un pretraitement par hydrogenation selective et par de la terre activee
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FR2770421B1 (fr) * 1997-10-31 1999-12-10 Inst Francais Du Petrole Procede de preparation de catalyseurs utilisables dans les reactions de transformation de composes organiques
FR2770521B1 (fr) * 1997-10-31 1999-12-10 Inst Francais Du Petrole Procede de deshydrogenation d'hydrocarbures aliphatiques satures en hydrocarbures olefiniques
FR2770520B1 (fr) * 1997-10-31 1999-12-10 Inst Francais Du Petrole Procede d'hydrogenation selective des composes insatures
US6368496B1 (en) * 1998-02-03 2002-04-09 Exxonmobil Oil Corporation Decreasing bi-reactive contaminants
FR2785833B1 (fr) * 1998-11-18 2000-12-08 Inst Francais Du Petrole Catalyseur comprenant du nickel et son utilisation dans un procede d'hydrodesulfuration de charges hydrocarbonees
US6977317B1 (en) * 2002-06-25 2005-12-20 Uop Llc Process for the selective hydrogenation of olefins
US6740788B1 (en) 2002-12-19 2004-05-25 Uop Llc Integrated process for aromatics production
FR2854335B1 (fr) * 2003-04-30 2009-03-20 Eurecat Sa Traitement hors site de catalyseurs d'hydrogenation
US7179434B1 (en) 2004-09-08 2007-02-20 Uop Llc Integrated apparatus for aromatics production
US7169368B1 (en) 2004-09-08 2007-01-30 Uop Llc Integrated apparatus for aromatics production
CN101300213B (zh) * 2005-11-10 2011-05-11 环球油品公司 烯烃的选择性加氢方法
US7517824B2 (en) * 2005-12-06 2009-04-14 Exxonmobil Chemical Company Process for steam stripping hydrocarbons from a bromine index reduction catalyst
US7268263B1 (en) 2006-05-18 2007-09-11 Uop Llc Integrated process for aromatics production
US7304193B1 (en) 2006-05-18 2007-12-04 Uop Llc Integrated process for aromatics production
US7288687B1 (en) 2006-05-18 2007-10-30 Uop Llc Integrated process for aromatics production
US7687674B2 (en) 2006-12-28 2010-03-30 Uop Llc Low temperature process for recovering and producing para-xylene and heat exchange network therefore
FR2936962B1 (fr) * 2008-10-10 2011-05-06 Eurecat Sa Procede de regeneration de catalyseurs de traitement d'hydrocarbures.
WO2010072836A1 (en) * 2008-12-24 2010-07-01 Shell Internationale Research Maatschappij B.V. Process for selectively sulfiding a supported nickel catalyst
WO2010123694A2 (en) * 2009-04-22 2010-10-28 Exxonmobil Chemical Patents Inc. Start up procedure in a process for purifying aromatic streams
US8329971B2 (en) * 2009-04-22 2012-12-11 Exxonmobil Chemical Patents Inc. Regeneration of catalyst used in purification of aromatic streams
FR2949077B1 (fr) 2009-08-17 2011-07-22 Inst Francais Du Petrole Procede de preparation d'un catalyseur supporte a base de ni et d'un metal du groupe ib pour l'hydrogenation selective d'hydrocarbures polyinsatures
FR2949078B1 (fr) 2009-08-17 2011-07-22 Inst Francais Du Petrole Procede de preparation d'un catalyseur supporte ni/sn pour l'hydrogenation selective d'hydrocarbures polyinsatures
FR2963344B1 (fr) 2010-07-29 2012-07-27 IFP Energies Nouvelles Procede d'hydrogenation selective en presence d'un catalyseur a base d'un metal du groupe viii prepare au moyen d'au moins un oligosaccharide cyclique
CN102618328B (zh) * 2011-01-31 2015-02-11 北京安耐吉能源工程技术有限公司 一种汽油加工方法
FR2984761B1 (fr) 2011-12-21 2014-12-26 IFP Energies Nouvelles Procede de preparation d'un catalyseur a base d'un metal du groupe viii prepare au moyen d'au moins un additif organique et procede d'hydrogenation selective mettant en oeuvre ledit catalyseur
FR2990882B1 (fr) 2012-05-24 2015-05-15 IFP Energies Nouvelles Procede de preparation d'un catalyseur a base d'un metal du groupe viii et contenant du silicium et procede d'hydrogenation selective mettant en oeuvre ledit catalyseur
FR3022160B1 (fr) 2014-06-13 2021-05-07 Ifp Energies Now Catalyseur a phase active de nickel comalaxee mesoporeux et macroporeux ayant un diametre median macroporeux compris entre 50 et 300 nm et son utilisation en hydrogenation
FR3025728B1 (fr) 2014-09-11 2018-04-20 IFP Energies Nouvelles Catalyseur mesoporeux a base de nickel et son utilisation en hydrogenation.
EA034710B1 (ru) 2015-01-29 2020-03-10 Ламмус Текнолоджи Инк. Производство олефинов c5 из потока углеводородов c5 установки парового крекинга
US10010878B2 (en) 2015-03-03 2018-07-03 Uop Llc High meso-surface area, low Si/Al ratio pentasil zeolite
US9890094B2 (en) 2015-03-03 2018-02-13 Uop Llc High meso-surface area and high acid site density pentasil zeolite for use in xylene conversion
US10336665B2 (en) 2015-03-03 2019-07-02 Uop Llc Yields in xylene isomerization using layer MFI zeolites
US9643897B2 (en) 2015-03-03 2017-05-09 Uop Llc Enhanced propylene production in OTO process with modified zeolites
US9688587B2 (en) 2015-03-03 2017-06-27 Uop Llc Process for oxygenate to olefin conversion using 2-D pentasil zeolite
FR3061196A1 (fr) * 2016-12-22 2018-06-29 IFP Energies Nouvelles Procede d'hydrogenation selective mettant en œuvre un catalyseur a base de nickel prepare au moyen d'un additif comprenant une fonction alcool
FR3061195B1 (fr) * 2016-12-22 2019-06-28 IFP Energies Nouvelles Procede d'hydrogenation selective mettant en œuvre un catalyseur de nickel prepare au moyen d'un additif comprenant une fonction amine, amide, ou un acide amine
FR3061194B1 (fr) 2016-12-22 2019-06-28 IFP Energies Nouvelles Procede d'hydrogenation selective mettant en œuvre un catalyseur a base de nickel prepare au moyen d'un additif comprenant une fonction acide carboxylique
FR3061197A1 (fr) 2016-12-22 2018-06-29 IFP Energies Nouvelles Procede d'hydrogenation selective mettant en œuvre un catalyseur a base de nickel prepare au moyen d'un additif comprenant une fonction ester
DE102017130369A1 (de) 2016-12-22 2018-06-28 IFP Energies Nouvelles Verfahren zur selektiven hydrierung unter verwendung eines nickel-katalysators, hergestellt mittels eines additivs, umfassend eine amin- oder amid-funktion, oder eine aminosäure
FR3064500A1 (fr) 2017-03-29 2018-10-05 IFP Energies Nouvelles Catalyseur en multicouches d'hyrogenation selective
FR3068985A1 (fr) 2017-07-13 2019-01-18 IFP Energies Nouvelles Procede d’hydrogenation des aromatiques mettant en oeuvre un catalyseur obtenu par comalaxage comprenant un support specifique
FR3068982A1 (fr) 2017-07-13 2019-01-18 IFP Energies Nouvelles Procede d'hydrogenation selective mettant en œuvre un catalyseur obtenu par comalaxage comprenant un support specifique
FR3068983B1 (fr) 2017-07-13 2019-07-12 IFP Energies Nouvelles Procede d'hydrogenation selective mettant en œuvre un catalyseur obtenu par impregnation comprenant un support specifique
FR3068984B1 (fr) 2017-07-13 2020-01-17 IFP Energies Nouvelles Procede d'hydrogenation des aromatiques mettant en œuvre un catalyseur obtenu par impregnation comprenant un support specifique.
FR3076747B1 (fr) 2018-01-15 2022-06-10 Ifp Energies Now Procede de preparation d'un catalyseur particulier d'hydrogenation selective et d'hydrogenation des aromatiques par malaxage
FR3087787B1 (fr) 2018-10-25 2020-12-18 Ifp Energies Now Procede d’hydrogenation comprenant un catalyseur prepare par addition d’un compose organique en phase gazeuse
US11459513B2 (en) * 2021-01-28 2022-10-04 Saudi Arabian Oil Company Steam cracking process integrating oxidized disulfide oil additive
EP4424797A1 (de) * 2023-03-02 2024-09-04 OMV Downstream GmbH Verfahren zur reinigung eines synthetischen rohölstroms
EP4424796A1 (de) 2023-03-02 2024-09-04 OMV Downstream GmbH Verfahren zur reinigung eines synthetischen rohölstroms
FR3163283A1 (fr) 2024-06-18 2025-12-19 IFP Energies Nouvelles Catalyseur comprenant du cuivre, du nickel et du soufre pour le traitement de reformat

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Also Published As

Publication number Publication date
US5417844A (en) 1995-05-23
DE69100881D1 (de) 1994-02-10
ATE99354T1 (de) 1994-01-15
EP0466567A1 (fr) 1992-01-15
FR2664610A1 (fr) 1992-01-17
EP0466567B1 (fr) 1993-12-29
JPH04226592A (ja) 1992-08-17
DE69100881T2 (de) 1994-07-28
FR2664610B1 (enExample) 1994-07-13

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