ES2108063T3 - Procedimiento para la hidrogenacion selectiva de fracciones en bruto con 4 atomos de carbono ricas en butadieno. - Google Patents

Procedimiento para la hidrogenacion selectiva de fracciones en bruto con 4 atomos de carbono ricas en butadieno.

Info

Publication number
ES2108063T3
ES2108063T3 ES92111353T ES92111353T ES2108063T3 ES 2108063 T3 ES2108063 T3 ES 2108063T3 ES 92111353 T ES92111353 T ES 92111353T ES 92111353 T ES92111353 T ES 92111353T ES 2108063 T3 ES2108063 T3 ES 2108063T3
Authority
ES
Spain
Prior art keywords
butadiene
procedure
carbon atoms
hydrogenation
selective hydrogenation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
ES92111353T
Other languages
English (en)
Inventor
Peter Dr Polanek
Dietmar Dr Posselt
Peter Dr Schreyer
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BASF SE filed Critical BASF SE
Application granted granted Critical
Publication of ES2108063T3 publication Critical patent/ES2108063T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C07C5/03Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
    • C07C5/05Partial hydrogenation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00Aliphatic unsaturated hydrocarbons
    • C07C11/02Alkenes
    • C07C11/08Alkenes with four carbon atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
    • C07C2523/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
    • C07C2523/44Palladium

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

SE PRESENTA UN PROCESO PARA LA HIDROGENACION SELECTIVA DE BUTADIENO A BUTENENO EN FASE LIQUIDA O DE RIEGO EN CATALIZADORES SOPORTE DE METAL NOBLE DISPUESTOS DE FORMA FIJA, CON LO QUE UNA CORRIENTE C4 ENRIQUECIDA DE BUTADIENO CON UN CONTENIDO DEL 20 HASTA EL 80% EN PESO DE BUTADIENO SE TRANSFORMA EN CORRIENTE C4 EN DOS ZONAS DE REACCION CONECTADAS UNA DETRAS DE OTRA PARA LA HIDROGENACION, DE FORMA QUE EL PRODUCTO HIDROGENADO DE LA PRIMERA ZONA DE REACCION DE 0,1 HASTA 20% EN PESO Y EL PRODUCTO DE HIDROGENACION DE LA SEGUNDA ZONA DE REACCION DE RESTO DE BUTADIENO 0,005 HASTA 1% EN PESO, SE TRANSFORMA EN CORRIENTE C4, CON LA MEDIDA DE QUE EL CONTENIDO DE BUTADIENO DEL PRODUCTO DE HIDROGENACION DE LA SEGUNDA ZONA DE REACCION SE DISMINUYE AL MENOS EN EL FACTOR 5 EN CONTRAPOSICION CON EL CONTENIDO DE BUTADIENO DEL PRODUCTO DE HIDROGENACION DE LA ZONA DE REACCION PRIMERA.
ES92111353T 1991-07-13 1992-07-03 Procedimiento para la hidrogenacion selectiva de fracciones en bruto con 4 atomos de carbono ricas en butadieno. Expired - Lifetime ES2108063T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE4123246A DE4123246A1 (de) 1991-07-13 1991-07-13 Verfahren zur selektiven hydrierung von butadienreichen roh-c(pfeil abwaerts)4(pfeil abwaerts)-schnitten

Publications (1)

Publication Number Publication Date
ES2108063T3 true ES2108063T3 (es) 1997-12-16

Family

ID=6436070

Family Applications (1)

Application Number Title Priority Date Filing Date
ES92111353T Expired - Lifetime ES2108063T3 (es) 1991-07-13 1992-07-03 Procedimiento para la hidrogenacion selectiva de fracciones en bruto con 4 atomos de carbono ricas en butadieno.

Country Status (7)

Country Link
US (1) US5227553A (es)
EP (1) EP0523482B1 (es)
JP (1) JP3199848B2 (es)
KR (1) KR100230081B1 (es)
DE (2) DE4123246A1 (es)
ES (1) ES2108063T3 (es)
TW (1) TW213898B (es)

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DE19636064A1 (de) * 1996-09-05 1998-03-12 Basf Ag Verfahren zur Hydrierung
DE19839459A1 (de) 1998-08-29 2000-03-02 Basf Ag Katalysator und Verfahren zur Selektivhydrierung ungesättigter Verbindungen in Kohlenwasserstoffströmen
FR2802921B1 (fr) * 1999-12-24 2002-08-23 Inst Francais Du Petrole Production d'isobutene de haute purete et de propylene a partir de coupes d'hydrocarbures a quatre atomes de carbone
FR2810991B1 (fr) 2000-06-28 2004-07-09 Inst Francais Du Petrole Procede pour l'hydrogenation de coupes contenant des hydrocarbures et notamment des molecules insaturees contenant au moins deux doubles liaisons ou au moins une triple liaison
US7038097B2 (en) * 2003-03-04 2006-05-02 Exxonmobil Chemical Patents Inc. Dual bed process using two different catalysts for selective hydrogenation of acetylene and dienes
US7153807B2 (en) * 2003-03-04 2006-12-26 Exxon Mobil Chemical Patents Inc. Catalysts for selective hydrogenation of alkynes and alkadienes
US7115789B2 (en) 2003-03-28 2006-10-03 Exxon Mobil Chemical Patents Inc. Process for removal of alkynes and/or dienes from an olefin stream
US7227047B2 (en) * 2003-08-22 2007-06-05 Exxonmobil Chemical Patents Inc. Butadiene and isobutylene removal from olefinic streams
US7919431B2 (en) 2003-09-03 2011-04-05 Synfuels International, Inc. Catalyst formulation for hydrogenation
US7045670B2 (en) * 2003-09-03 2006-05-16 Synfuels International, Inc. Process for liquid phase hydrogenation
DE102004021128A1 (de) * 2004-04-29 2005-11-24 Oxeno Olefinchemie Gmbh Vorrichtung und Verfahren für die kontinuierliche Umsetzung einer Flüssigkeit mit einem Gas an einem festen Katalysator
US8013197B2 (en) * 2005-02-18 2011-09-06 Synfuels International, Inc. Absorption and conversion of acetylenic compounds
DE102005062699A1 (de) * 2005-12-28 2007-09-06 Oxeno Olefinchemie Gmbh Verfahren zur Feinreinigung von 1-Buten-haltigen Strömen
DE102008002188A1 (de) 2008-06-03 2009-12-10 Evonik Oxeno Gmbh Verfahren zur Abtrennung von 1-Buten aus C4-haltigen Kohlenwasserstoffströmen durch Hydroformylierung
CN102285859B (zh) * 2010-06-18 2014-03-12 中国石油化工股份有限公司 一种高丁二烯含量c4物流的选择加氢工艺
DE102010030990A1 (de) 2010-07-06 2012-01-12 Evonik Oxeno Gmbh Verfahren zur selektiven Hydrierung von mehrfach ungesättigten Kohlenwasserstoffen in olefinhaltigen Kohlenwasserstoffgemischen
EP2404980A1 (en) * 2010-07-08 2012-01-11 Total Raffinage Marketing Hydrocarbon feedstock average molecular weight increase
FR2980194B1 (fr) * 2011-09-20 2013-08-23 IFP Energies Nouvelles Procede de separation du butene-2 d'une coupe c4 contenant du butene-2 et du butene-1 par oligomerisation selective du butene-1
DE102012212317A1 (de) 2012-07-13 2014-01-16 Evonik Industries Ag Thioveretherung von Mercaptanen in C4-Kohlenwasserstoffgemischen
MY174117A (en) 2013-06-25 2020-03-10 Dow Technology Investments Llc Selective hydrogenation process
KR102589091B1 (ko) 2017-07-27 2023-10-16 사빅 글로벌 테크놀러지스 비.브이. 연료 첨가제의 제조 방법
US11427518B2 (en) * 2018-03-19 2022-08-30 Saudi Arabian Oil Company Method of producing a fuel additive
WO2019180585A1 (en) 2018-03-19 2019-09-26 Sabic Global Technologies B.V. Method of producing a fuel additive
US11248181B2 (en) 2018-04-19 2022-02-15 Sabic Global Technologies B.V. Method of producing a fuel additive
EP3790944B1 (en) 2018-05-07 2023-06-14 SABIC Global Technologies B.V. Method of producing a fuel additive
CN112041291B (zh) 2018-05-07 2023-10-20 沙特基础工业全球技术有限公司 生产燃油添加剂的方法
US11697626B2 (en) 2018-05-18 2023-07-11 Sabic Global Technologies B.V. Method of producing a fuel additive with a hydration unit
WO2020058825A1 (en) 2018-09-18 2020-03-26 Sabic Global Technologies B.V. Systems and processes for efficient production of one or more fuel additives
US12037313B2 (en) 2018-11-20 2024-07-16 Sabic Global Technologies B.V. Process and system for producing ethylene and at least one of butanol and an alkyl tert-butyl ether
EP3680224B1 (de) * 2019-01-08 2023-05-24 Evonik Operations GmbH Verfahren zur entfernung mehrfach ungesättigter kohlenwasserstoffe aus c4-kohlenwasserstoffströmen in anwesenheit von mercaptanen, disulfiden und c5-kohlenwasserstoffen
US12264123B2 (en) 2019-03-08 2025-04-01 Sabic Global Technologies B.V. Method of producing a fuel additive
CN112479798A (zh) * 2019-09-12 2021-03-12 南京延长反应技术研究院有限公司 一种基于微界面强化碳四加氢的系统及工艺
EP4660179A1 (de) 2024-06-03 2025-12-10 Evonik Oxeno GmbH & Co. KG Verfahren zur herstellung von hochreinem 1-buten und von hochreinem isobutan

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DD50823A (es) *
DE740478C (de) * 1935-03-22 1943-11-02 Ig Farbenindustrie Ag Verfahren zur Ausfuehrung exotherm verlaufender partiellkatalytischer Hydrierungen von aliphatischen ungesaettigten Kohlenwasserstoffen in der Gasphase in Gegenwart fest angeordneter Katalysatoren
US2402493A (en) * 1944-05-09 1946-06-18 Shell Dev Hydrogenation process
US3113983A (en) * 1959-04-07 1963-12-10 Air Prod & Chem Selective hydrogenation of diolefins
DE1568542C3 (de) * 1966-06-15 1974-07-18 Bayer Ag, 5090 Leverkusen Verfahren zur katalytischen Umwandlung von Butadien- und n-Buten-1-haltigen C tief 4 - Kohlenwasserstoffen
US3478123A (en) * 1967-10-13 1969-11-11 Universal Oil Prod Co Partial hydrogenation of conjugated diolefinic hydrocarbons
FR2051975A5 (es) * 1969-07-02 1971-04-09 Inst Francais Du Petrole
FR2077907A1 (es) * 1970-02-23 1971-11-05 Inst Francais Du Petrole
FR2614295B1 (fr) * 1987-04-22 1989-08-04 Inst Francais Du Petrole Procede d'isomerisation du butene-1 en butenes-2 dans une coupe d'hydrocarbures en c4 contenant du butadiene et des composes sulfures.
FR2642670B1 (fr) * 1989-02-07 1991-05-24 Eurecat Europ Retrait Catalys Procede de reduction d'un catalyseur de raffinage avant sa mise en oeuvr

Also Published As

Publication number Publication date
EP0523482A3 (en) 1993-09-08
DE4123246A1 (de) 1993-01-14
JP3199848B2 (ja) 2001-08-20
TW213898B (es) 1993-10-01
KR930002289A (ko) 1993-02-22
EP0523482B1 (de) 1997-10-29
US5227553A (en) 1993-07-13
DE59208990D1 (de) 1997-12-04
KR100230081B1 (ko) 1999-11-15
JPH05194280A (ja) 1993-08-03
EP0523482A2 (de) 1993-01-20

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