ES2001303A6 - Procedimiento de hidrogenacion - Google Patents

Procedimiento de hidrogenacion

Info

Publication number
ES2001303A6
ES2001303A6 ES8602194A ES8602194A ES2001303A6 ES 2001303 A6 ES2001303 A6 ES 2001303A6 ES 8602194 A ES8602194 A ES 8602194A ES 8602194 A ES8602194 A ES 8602194A ES 2001303 A6 ES2001303 A6 ES 2001303A6
Authority
ES
Spain
Prior art keywords
stage
penultimate
product mixture
stages
catalytic
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
Application number
ES8602194A
Other languages
English (en)
Inventor
Andrew George Hiles
John Earl Logsdon
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.)
Johnson Matthey Davy Technologies Ltd
Original Assignee
Davy Mckee London Ltd
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=25102843&utm_source=***_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=ES2001303(A6) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Davy Mckee London Ltd filed Critical Davy Mckee London Ltd
Publication of ES2001303A6 publication Critical patent/ES2001303A6/es
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C47/00Compounds having —CHO groups
    • C07C47/02Saturated compounds having —CHO groups bound to acyclic carbon atoms or to hydrogen
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/17Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrogenation of carbon-to-carbon double or triple bonds
    • C07C29/175Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrogenation of carbon-to-carbon double or triple bonds with simultaneous reduction of an oxo group

Landscapes

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

Abstract

SE DESCRIBE UN PROCEDIMIENTO CONTINUO DE HIDROGENACION EN ETAPAS MULTIPLES. SE EFECTUA ESTE CUANDO MENOS EN TRES ETAPAS CATALITICAS CONECTADAS EN SERIE. TODAS LAS ETAPAS, HASTA E INCLUYENDO LA PENULTIMA ETAPA, SON OPERADAS ADIABATICAMENTE Y EN LA FASE DE VAPOR. SE ALIMENTA ALDEHIDO (U OTRO COMPUESTO ORGANICO INSATURADO) A TODAS LAS ETAPAS HASTA E INCLUYENDO LA PENULTIMA ETAPA. EL REGIMEN DE SUMINISTRO DEL ALDEHIDO U OTRO COMPUESTO ORGANICO INSATURADO A LA PENULTIMA ETAPA SE CONTROLA EN RELACION CON EL VOLUMEN DE CATALIZADOR EN LA PENULTIMA ETAPA CATALITICA, DE MANERA QUE EL GRADO DE HIDROGENACION EN ESA ETAPA SEA MENOR QUE 100%. EL MATERIAL QUIMICAMENTE INSATURADO RESTANTE EN LA MEZCLA DE PRODUCTO DE LA PENULTIMA ETAPA ES HIDROGENADO, DESPUES DE ENFRIAR LA MEZCLA DE PRODUCTO, EN LA ETAPA CATALITICA FINAL PARA PRODUCIR NA MEZCLA DE PRODUCTO HIDROGENADO EN FORMA SUSTANCIALMENTE COMPLETA. DE ESTA MANERA, EL TIEMPO DE RESIDENCIA DE LOS REACTIVOS Y EL O LOS PRODUCTOS A LAS TEMPERATURAS <<DE PUNTO CALIENTE>> SE REDUCE AL MINIMO, REDUCIENDO ASI LA FORMACION DE SUBPRODUCTOS.
ES8602194A 1985-09-11 1986-09-10 Procedimiento de hidrogenacion Expired ES2001303A6 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US06/774,958 US4626604A (en) 1985-09-11 1985-09-11 Hydrogenation process

Publications (1)

Publication Number Publication Date
ES2001303A6 true ES2001303A6 (es) 1988-05-01

Family

ID=25102843

Family Applications (1)

Application Number Title Priority Date Filing Date
ES8602194A Expired ES2001303A6 (es) 1985-09-11 1986-09-10 Procedimiento de hidrogenacion

Country Status (9)

Country Link
US (1) US4626604A (es)
EP (1) EP0215563B1 (es)
JP (1) JPH0811738B2 (es)
KR (1) KR950004890B1 (es)
AT (1) ATE72218T1 (es)
CA (1) CA1265161A (es)
DE (1) DE3683710D1 (es)
ES (1) ES2001303A6 (es)
MX (1) MX165051B (es)

Families Citing this family (54)

* Cited by examiner, † Cited by third party
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JPS63146835A (ja) * 1986-12-11 1988-06-18 Japan Tobacco Inc ニトリルの還元によるアルコ−ルの製造方法
GB8702654D0 (en) * 1987-02-06 1987-03-11 Davy Mckee Ltd Process
GB8728156D0 (en) * 1987-12-02 1988-01-06 Davy Mckee Ltd Process
DE4025245A1 (de) * 1990-08-09 1992-02-13 Huels Chemische Werke Ag Verfahren zur herstellung von gesaettigten alkoholen aus aldehyden
DE4220783A1 (de) * 1992-06-25 1994-01-05 Hoechst Ag Verfahren zur katalytischen Hydrierung organischer Verbindungen in der Gasphase
US5744655A (en) * 1996-06-19 1998-04-28 The Dow Chemical Company Process to make 2,3-dihalopropanols
DE19806398B4 (de) * 1997-02-18 2017-01-26 Basf Se Verfahren zur Herstellung von Aldehyden
FR2789683B1 (fr) 1999-02-17 2002-02-15 Roquette Freres Procede continu de preparation d'un ose hydrogene de haute purete par hydrogenation catalytique
DE19933691A1 (de) * 1999-07-17 2001-01-18 Phenolchemie Gmbh & Co Kg Verfahren zur Hydrierung von Aceton
US6750374B2 (en) * 1999-08-10 2004-06-15 Huntsman Petrochemical Corporation Manufacture of cyclohexane from benzene and a hydrogen source containing impurities
US20040033171A1 (en) * 2000-07-27 2004-02-19 The Procter & Gamble Company Systems and devices for emitting volatile compositions
DE10052323A1 (de) * 2000-10-21 2002-05-02 Degussa Kontinierliches Verfahren zur Hydrierung
GB0117090D0 (en) * 2001-07-12 2001-09-05 Kvaerner Process Tech Ltd Process
US8252961B2 (en) 2002-04-22 2012-08-28 The Curators Of The University Of Missouri Method of producing lower alcohols from glycerol
US8017816B2 (en) * 2002-04-22 2011-09-13 The Curators Of The University Of Missouri Method of producing lower alcohols from glycerol
US7585990B2 (en) * 2003-07-31 2009-09-08 Cargill, Incorporated Low trans-fatty acid fat compositions; low-temperature hydrogenation, e.g., of edible oils
BRPI0413177A (pt) * 2003-07-31 2006-10-03 Cargill Inc composições gordurosas com teor baixo de ácido trans-graxo; hidrogenação em temperatura baixa, por exemplo, de óleos comestìveis
GB0329152D0 (en) * 2003-12-16 2004-01-21 Davy Process Techn Ltd Process
JP5130957B2 (ja) * 2008-03-03 2013-01-30 エヌ・イーケムキャット株式会社 脂肪族ケトンの接触水素化用白金固定炭素触媒及びそれを使用する脂肪族ケトンからの脂肪族第2級アルコールの製造方法
US8304586B2 (en) 2010-02-02 2012-11-06 Celanese International Corporation Process for purifying ethanol
US8546622B2 (en) 2008-07-31 2013-10-01 Celanese International Corporation Process for making ethanol from acetic acid using acidic catalysts
EP2346798A2 (en) * 2008-10-06 2011-07-27 Badger Licensing, LLC Process for producing cumene
EP2432756B1 (de) * 2009-05-20 2016-12-21 Basf Se Verfahren zur herstellung von fettalkoholen durch hydrierung von fettsäuretriglyceriden an einem kupferhaltigen heterogenen katalysator
DE102009045718A1 (de) * 2009-10-15 2011-04-21 Evonik Oxeno Gmbh Verfahren zur Herstellung von Decanolen durch Hydrierung von Decenalen
US8668750B2 (en) 2010-02-02 2014-03-11 Celanese International Corporation Denatured fuel ethanol compositions for blending with gasoline or diesel fuel for use as motor fuels
US8680343B2 (en) 2010-02-02 2014-03-25 Celanese International Corporation Process for purifying ethanol
US8541633B2 (en) 2010-02-02 2013-09-24 Celanese International Corporation Processes for producing anhydrous ethanol compositions
US8575403B2 (en) 2010-05-07 2013-11-05 Celanese International Corporation Hydrolysis of ethyl acetate in ethanol separation process
CN102413921B (zh) 2010-02-02 2016-05-18 国际人造丝公司 由乙醛生产乙醇的方法
US8747492B2 (en) 2010-02-02 2014-06-10 Celanese International Corporation Ethanol/fuel blends for use as motor fuels
US8728179B2 (en) 2010-02-02 2014-05-20 Celanese International Corporation Ethanol compositions
US8460405B2 (en) 2010-02-02 2013-06-11 Celanese International Corporation Ethanol compositions
US8344186B2 (en) 2010-02-02 2013-01-01 Celanese International Corporation Processes for producing ethanol from acetaldehyde
US8858659B2 (en) 2010-02-02 2014-10-14 Celanese International Corporation Processes for producing denatured ethanol
US8932372B2 (en) 2010-02-02 2015-01-13 Celanese International Corporation Integrated process for producing alcohols from a mixed acid feed
US8754267B2 (en) 2010-05-07 2014-06-17 Celanese International Corporation Process for separating acetaldehyde from ethanol-containing mixtures
US8680342B2 (en) 2010-05-07 2014-03-25 Celanese International Corporation Process for recovering alcohol produced by hydrogenating an acetic acid feed stream comprising water
US8569551B2 (en) 2010-05-07 2013-10-29 Celanese International Corporation Alcohol production process integrating acetic acid feed stream comprising water from carbonylation process
US8710279B2 (en) 2010-07-09 2014-04-29 Celanese International Corporation Hydrogenolysis of ethyl acetate in alcohol separation processes
US9024083B2 (en) 2010-07-09 2015-05-05 Celanese International Corporation Process for the production of ethanol from an acetic acid feed and a recycled ethyl acetate feed
US8664454B2 (en) 2010-07-09 2014-03-04 Celanese International Corporation Process for production of ethanol using a mixed feed using copper containing catalyst
CN103619791B (zh) 2010-07-09 2015-06-24 国际人造丝公司 纯化乙醇产物的方法
US8704008B2 (en) 2010-07-09 2014-04-22 Celanese International Corporation Process for producing ethanol using a stacked bed reactor
US9272970B2 (en) 2010-07-09 2016-03-01 Celanese International Corporation Hydrogenolysis of ethyl acetate in alcohol separation processes
US8592635B2 (en) 2011-04-26 2013-11-26 Celanese International Corporation Integrated ethanol production by extracting halides from acetic acid
US8754268B2 (en) 2011-04-26 2014-06-17 Celanese International Corporation Process for removing water from alcohol mixtures
US9073816B2 (en) 2011-04-26 2015-07-07 Celanese International Corporation Reducing ethyl acetate concentration in recycle streams for ethanol production processes
US8895786B2 (en) 2011-08-03 2014-11-25 Celanese International Corporation Processes for increasing alcohol production
US8809598B2 (en) 2011-11-09 2014-08-19 Celanese International Corporation Producing ethanol using two different streams from acetic acid carbonylation process
WO2013070212A1 (en) 2011-11-09 2013-05-16 Celanese International Corporation Producing ethanol using two different streams from acetic acid carbonylation process
US8907142B2 (en) 2011-12-29 2014-12-09 Celanese International Corporation Process for promoting catalyst activity for ethyl acetate conversion
US9051235B2 (en) 2012-02-07 2015-06-09 Celanese International Corporation Process for producing ethanol using a molar excess of hydrogen
US9000237B2 (en) 2012-12-20 2015-04-07 Celanese International Corporation Ethanol refining process using intermediate reboiler
EP2980276B1 (en) * 2013-03-29 2019-05-08 JX Nippon Oil & Energy Corporation Electrochemical reduction device and production method for hydrogenated product of aromatic compound

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3301909A (en) * 1967-01-31 By iajl
US3288866A (en) * 1966-11-29 Plural stage hydrogenation of alke- nals to alcohols using copper catalyst and then palladium catalyst
US2549416A (en) * 1948-02-04 1951-04-17 Du Pont Preparation of alcohols
US2760994A (en) * 1950-12-30 1956-08-28 Gulf Research Development Co Process for hydrogenating aldehydes
US2771493A (en) * 1953-03-23 1956-11-20 Exxon Research Engineering Co Aldehyde hydrogenation quench
CA1137519A (en) * 1978-08-29 1982-12-14 Chao-Chyan Pai Heterogeneous vapor phase process for the catalytic hydrogenation of aldehydes to alcohols
EP0074193B1 (en) * 1981-08-20 1986-10-29 DAVY McKEE (LONDON) LIMITED Catalytic hydrogenation
US4451677A (en) * 1981-08-20 1984-05-29 Davy Mckee (London) Limited Multistage aldehyde hydrogenation
EP0073129B1 (en) * 1981-08-20 1985-06-19 DAVY McKEE (LONDON) LIMITED Hydrogenation process
JPS5839932A (ja) * 1981-09-03 1983-03-08 Matsushita Electric Works Ltd 光沢計測装置
DE3228881C2 (de) * 1982-08-03 1985-06-13 Basf Ag, 6700 Ludwigshafen Verfahren zur Herstellung von C&darr;3&darr;-C&darr;5&darr;-Alkoholen

Also Published As

Publication number Publication date
EP0215563A2 (en) 1987-03-25
KR950004890B1 (ko) 1995-05-15
DE3683710D1 (de) 1992-03-12
US4626604A (en) 1986-12-02
JPH0811738B2 (ja) 1996-02-07
EP0215563A3 (en) 1988-08-10
JPS62116526A (ja) 1987-05-28
ATE72218T1 (de) 1992-02-15
EP0215563B1 (en) 1992-01-29
KR870003043A (ko) 1987-04-14
CA1265161A (en) 1990-01-30
MX165051B (es) 1992-10-20

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Legal Events

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SA6 Expiration date (snapshot 920101)

Free format text: 2006-09-10