WO2002051779A3 - Verfahren zur herstellung von alkoholen durch hydrierung von carbonylverbindungen - Google Patents

Verfahren zur herstellung von alkoholen durch hydrierung von carbonylverbindungen Download PDF

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Publication number
WO2002051779A3
WO2002051779A3 PCT/EP2001/015264 EP0115264W WO02051779A3 WO 2002051779 A3 WO2002051779 A3 WO 2002051779A3 EP 0115264 W EP0115264 W EP 0115264W WO 02051779 A3 WO02051779 A3 WO 02051779A3
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WO
WIPO (PCT)
Prior art keywords
carbonyl compounds
producing alcohols
hydrogenating carbonyl
hydrogenating
hydrogen
Prior art date
Application number
PCT/EP2001/015264
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English (en)
French (fr)
Other versions
WO2002051779A2 (de
Inventor
Daniel Ostgard
Monika Berweiler
Stefan Roeder
Original Assignee
Degussa
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
Priority claimed from DE10065029A external-priority patent/DE10065029A1/de
Application filed by Degussa filed Critical Degussa
Priority to JP2002552881A priority Critical patent/JP2004526686A/ja
Priority to AU2002240870A priority patent/AU2002240870A1/en
Priority to EP01988069A priority patent/EP1343744A2/de
Publication of WO2002051779A2 publication Critical patent/WO2002051779A2/de
Publication of WO2002051779A3 publication Critical patent/WO2002051779A3/de

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D315/00—Heterocyclic compounds containing rings having one oxygen atom as the only ring hetero atom according to more than one of groups C07D303/00 - C07D313/00
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
    • C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
    • C07C29/14—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group
    • C07C29/141—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group with hydrogen or hydrogen-containing gases
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
    • C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
    • C07C29/147—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof
    • C07C29/149—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof with hydrogen or hydrogen-containing gases
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/04—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having no double bonds between ring members or between ring members and non-ring members
    • C07D307/06—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having no double bonds between ring members or between ring members and non-ring members with only hydrogen atoms or radicals containing only hydrogen and carbon atoms, directly attached to ring carbon atoms
    • C07D307/08—Preparation of tetrahydrofuran
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B2200/00—Indexing scheme relating to specific properties of organic compounds
    • C07B2200/07—Optical isomers

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

Abstract

Ein Verfahren zur Herstellung von Alkoholen durch katalytische Hydrierung von Carbonylverbindungen mit Wasserstoff oder Wasserstoff enthaltenden Gasen in Gegenwart eines Hydrierkatalysators nach Raney, wobei der Katalysator in Form von Hohlkörpern eingesetzt wird. Als katalytisch aktive Bestandteile werden bevorzugt Nickel, Kobalt, Kupfer, Eisen, Platin, Palladium oder Ruthenium verwendet.
PCT/EP2001/015264 2000-12-23 2001-12-21 Verfahren zur herstellung von alkoholen durch hydrierung von carbonylverbindungen WO2002051779A2 (de)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP2002552881A JP2004526686A (ja) 2000-12-23 2001-12-21 カルボニル化合物の水素化によるアルコールの製法
AU2002240870A AU2002240870A1 (en) 2000-12-23 2001-12-21 Method for producing alcohols by hydrogenating carbonyl compounds
EP01988069A EP1343744A2 (de) 2000-12-23 2001-12-21 Verfahren zur herstellung von alkoholen durch hydrierung von carbonylverbindungen

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DE10065029.5 2000-12-23
DE10065029A DE10065029A1 (de) 2000-12-23 2000-12-23 Verfahren zur Herstellung von Alkoholen durch Hydrierung von Carbonylverbindungen
EPPCT/EP01/12567 2001-10-31
EP0112567 2001-10-31

Publications (2)

Publication Number Publication Date
WO2002051779A2 WO2002051779A2 (de) 2002-07-04
WO2002051779A3 true WO2002051779A3 (de) 2003-03-06

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2001/015264 WO2002051779A2 (de) 2000-12-23 2001-12-21 Verfahren zur herstellung von alkoholen durch hydrierung von carbonylverbindungen

Country Status (5)

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US (1) US6486366B1 (de)
JP (1) JP2004526686A (de)
CN (1) CN1487911A (de)
AU (1) AU2002240870A1 (de)
WO (1) WO2002051779A2 (de)

Families Citing this family (135)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1127613A1 (de) * 2000-02-18 2001-08-29 Degussa AG Geformter Festbettraney-Kupferkatalysator zur Verwendung bei der Dehydrierung von Alkoholen
DE10101646A1 (de) * 2001-01-16 2002-07-18 Degussa Verfahren zur Herstellung von gesättigten organischen Verbindungen
TWI301480B (en) * 2001-11-16 2008-10-01 Shell Int Research Process for the hydrogenation of acetone
AU2003276139A1 (en) * 2003-10-22 2005-05-19 Degussa Ag The use of ir, near ir, visible and uv radiation for the preparation of catalysts
US6919489B1 (en) * 2004-03-03 2005-07-19 Eastman Chemical Company Process for a cyclohexanedimethanol using raney metal catalysts
CA2496839A1 (en) 2004-07-19 2006-01-19 Woodland Chemical Systems Inc. Process for producing ethanol from synthesis gas rich in carbon monoxide
FR2876693B1 (fr) * 2004-10-15 2007-01-26 Roquette Freres Procede de preparation de l-iditol
EP1809596A1 (de) * 2004-11-10 2007-07-25 Degussa GmbH Festbetthydrierung von fettsäurenitrilen zu fettaminen
WO2006050749A1 (en) * 2004-11-12 2006-05-18 Degussa Gmbh Process for modifiying catalysts and the use of the catalysts
US7041857B1 (en) * 2005-09-07 2006-05-09 Air Products And Chemicals, Inc. Hydrogenation of acetone
WO2007028411A1 (en) * 2005-09-08 2007-03-15 Evonik Degussa Gmbh The production and use of supported activated base metal catalysts for organic transformation
CN101346302B (zh) 2005-12-21 2013-07-10 维仁特公司 用于重整含氧化合物的催化剂及方法
BRPI0710578B1 (pt) 2006-04-05 2016-11-29 Woodland Biofuels Inc método de produção de etanol a partir de gás de síntese
DE102006019044A1 (de) * 2006-04-25 2007-10-31 Merck Patent Gmbh Antioxidantien
GB2437517A (en) 2006-04-27 2007-10-31 Danisco Sweeteners Oy Catalytic hydrogenation of sugar to sugar alcohol, using increasing reaction temperature and/or addition of monocarboxylic acid to maintain catalyst activity
US20100288975A1 (en) 2006-12-20 2010-11-18 Cortright Randy D Reactor system for producing gaseous products
DE102007009981A1 (de) * 2007-03-01 2008-09-04 Evonik Degussa Gmbh Aus hohlen Formen bestehende Mischoxidkatalysatoren
ES2817876T3 (es) 2007-03-08 2021-04-08 Virent Inc Síntesis de combustibles líquidos a partir de hidrocarburos oxigenados
US8680317B2 (en) 2008-07-31 2014-03-25 Celanese International Corporation Processes for making ethyl acetate from acetic acid
US8637714B2 (en) 2008-07-31 2014-01-28 Celanese International Corporation Process for producing ethanol over catalysts containing platinum and palladium
US8501652B2 (en) 2008-07-31 2013-08-06 Celanese International Corporation Catalysts for making ethanol from acetic acid
US8309772B2 (en) 2008-07-31 2012-11-13 Celanese International Corporation Tunable catalyst gas phase hydrogenation of carboxylic acids
US8304586B2 (en) 2010-02-02 2012-11-06 Celanese International Corporation Process for purifying ethanol
US7816565B2 (en) 2008-07-31 2010-10-19 Celanese International Corporation Direct and selective production of acetaldehyde from acetic acid utilizing a supported metal catalyst
US8471075B2 (en) 2008-07-31 2013-06-25 Celanese International Corporation Processes for making ethanol from acetic acid
US8338650B2 (en) 2008-07-31 2012-12-25 Celanese International Corporation Palladium catalysts for making ethanol from acetic acid
US8309773B2 (en) 2010-02-02 2012-11-13 Calanese International Corporation Process for recovering ethanol
US8546622B2 (en) 2008-07-31 2013-10-01 Celanese International Corporation Process for making ethanol from acetic acid using acidic catalysts
WO2010025241A2 (en) 2008-08-27 2010-03-04 Virent Energy Systems, Inc. Synthesis of liquid fuels from biomass
US8697924B2 (en) 2008-09-05 2014-04-15 Shell Oil Company Liquid fuel compositions
US8178715B2 (en) * 2008-12-31 2012-05-15 Celanese International Corporation Integrated process for the production of vinyl acetate from acetic acid via acetaldehyde
SG173818A1 (en) 2009-02-25 2011-09-29 Grace W R & Co Process for making 1, 2-propane diol from hydrogenation of glycerol
US8450535B2 (en) 2009-07-20 2013-05-28 Celanese International Corporation Ethanol production from acetic acid utilizing a cobalt catalyst
US8680321B2 (en) 2009-10-26 2014-03-25 Celanese International Corporation Processes for making ethanol from acetic acid using bimetallic catalysts
US8710277B2 (en) 2009-10-26 2014-04-29 Celanese International Corporation Process for making diethyl ether from acetic acid
US9303226B2 (en) 2009-12-31 2016-04-05 Shell Oil Company Direct aqueous phase reforming of bio-based feedstocks
US9447347B2 (en) 2009-12-31 2016-09-20 Shell Oil Company Biofuels via hydrogenolysis-condensation
US8211821B2 (en) 2010-02-01 2012-07-03 Celanese International Corporation Processes for making tin-containing catalysts
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
CA2787419A1 (en) 2010-02-02 2011-08-11 Celanese International Corporation Preparation and use of a catalyst for producing ethanol comprising a crystalline support modifier
US8932372B2 (en) 2010-02-02 2015-01-13 Celanese International Corporation Integrated process for producing alcohols from a mixed acid feed
US8460405B2 (en) 2010-02-02 2013-06-11 Celanese International Corporation Ethanol compositions
US8858659B2 (en) 2010-02-02 2014-10-14 Celanese International Corporation Processes for producing denatured ethanol
US8541633B2 (en) 2010-02-02 2013-09-24 Celanese International Corporation Processes for producing anhydrous ethanol compositions
US8728179B2 (en) 2010-02-02 2014-05-20 Celanese International Corporation Ethanol compositions
US8747492B2 (en) 2010-02-02 2014-06-10 Celanese International Corporation Ethanol/fuel blends for use as motor fuels
US8314272B2 (en) 2010-02-02 2012-11-20 Celanese International Corporation Process for recovering ethanol with vapor separation
US8344186B2 (en) 2010-02-02 2013-01-01 Celanese International Corporation Processes for producing ethanol from acetaldehyde
US8575403B2 (en) 2010-05-07 2013-11-05 Celanese International Corporation Hydrolysis of ethyl acetate in ethanol separation process
US8222466B2 (en) 2010-02-02 2012-07-17 Celanese International Corporation Process for producing a water stream from ethanol production
US8680343B2 (en) 2010-02-02 2014-03-25 Celanese International Corporation Process for purifying ethanol
US8754267B2 (en) 2010-05-07 2014-06-17 Celanese International Corporation Process for separating acetaldehyde from ethanol-containing mixtures
US8569551B2 (en) 2010-05-07 2013-10-29 Celanese International Corporation Alcohol production process integrating acetic acid feed stream comprising water from carbonylation process
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
US9428704B2 (en) 2010-05-12 2016-08-30 Shell Oil Company Direct aqueous phase reforming and aldol condensation to form bio-based fuels
AU2011253083B2 (en) 2010-05-12 2014-08-21 Shell Internationale Research Maatschappij B.V. Process including hydrogenolysis of biomass followed by dehydrogenation and aldol condensation to produce alkanes
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
US8846988B2 (en) 2010-07-09 2014-09-30 Celanese International Corporation Liquid esterification for the production of alcohols
CN103619791B (zh) 2010-07-09 2015-06-24 国际人造丝公司 纯化乙醇产物的方法
US8664454B2 (en) 2010-07-09 2014-03-04 Celanese International Corporation Process for production of ethanol using a mixed feed using copper containing catalyst
WO2012148509A1 (en) 2011-04-26 2012-11-01 Celanese International Corporation Process for producing ethanol using a stacked bed reactor
US8710279B2 (en) 2010-07-09 2014-04-29 Celanese International Corporation Hydrogenolysis of ethyl acetate in alcohol separation processes
US9272970B2 (en) 2010-07-09 2016-03-01 Celanese International Corporation Hydrogenolysis of ethyl acetate in alcohol separation processes
IL207945A0 (en) 2010-09-02 2010-12-30 Robert Jansen Method for the production of carbohydrates
JP5818244B2 (ja) * 2011-03-25 2015-11-18 国立研究開発法人物質・材料研究機構 金属触媒構造体及びその製造方法
US8350098B2 (en) 2011-04-04 2013-01-08 Celanese International Corporation Ethanol production from acetic acid utilizing a molybdenum carbide catalyst
US9024084B2 (en) 2011-04-26 2015-05-05 Celanese International Corporation Reduced energy alcohol separation process having controlled pressure
US9000232B2 (en) 2011-04-26 2015-04-07 Celanese International Corporation Extractive distillation of crude alcohol product
US9024085B2 (en) 2011-04-26 2015-05-05 Celanese International Corporation Process to reduce ethanol recycled to hydrogenation reactor
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
US8686200B2 (en) 2011-04-26 2014-04-01 Celanese International Corporation Process to recover alcohol from an acidic residue stream
US9000233B2 (en) 2011-04-26 2015-04-07 Celanese International Corporation Process to recover alcohol with secondary reactors for hydrolysis of acetal
US8927788B2 (en) 2011-04-26 2015-01-06 Celanese International Corporation Process to recover alcohol with reduced water from overhead of acid column
US9073816B2 (en) 2011-04-26 2015-07-07 Celanese International Corporation Reducing ethyl acetate concentration in recycle streams for ethanol production processes
US8907141B2 (en) 2011-04-26 2014-12-09 Celanese International Corporation Process to recover alcohol with secondary reactors for esterification of acid
US8927784B2 (en) 2011-04-26 2015-01-06 Celanese International Corporation Process to recover alcohol from an ethyl acetate residue stream
US8927787B2 (en) 2011-04-26 2015-01-06 Celanese International Corporation Process for controlling a reboiler during alcohol recovery and reduced ester formation
US8933278B2 (en) 2011-04-26 2015-01-13 Celanese International Corporation Process for producing ethanol and reducing acetic acid concentration
US8686199B2 (en) 2011-04-26 2014-04-01 Celanese International Corporation Process for reducing the concentration of acetic acid in a crude alcohol product
US8884081B2 (en) 2011-04-26 2014-11-11 Celanese International Corporation Integrated process for producing acetic acid and alcohol
US9024082B2 (en) 2011-04-26 2015-05-05 Celanese International Corporation Using a dilute acid stream as an extractive agent
CN102850181B (zh) * 2011-06-30 2015-01-14 中国石油化工股份有限公司 一种高碳醇的制备方法
US8895786B2 (en) 2011-08-03 2014-11-25 Celanese International Corporation Processes for increasing alcohol production
US8829253B2 (en) 2011-08-19 2014-09-09 Celanese International Corporation Integrated process for producing ethanol from methanol
US8853466B2 (en) 2011-08-19 2014-10-07 Celanese International Corporation Integrated process for producing ethanol from methanol
US8853467B2 (en) 2011-08-19 2014-10-07 Celanese International Corporation Integrated process for producing ethanol
US8658843B2 (en) 2011-10-06 2014-02-25 Celanese International Corporation Hydrogenation catalysts prepared from polyoxometalate precursors and process for using same to produce ethanol while minimizing diethyl ether formation
US8536382B2 (en) 2011-10-06 2013-09-17 Celanese International Corporation Processes for hydrogenating alkanoic acids using catalyst comprising tungsten
WO2013055785A1 (en) 2011-10-10 2013-04-18 Virdia Ltd Sugar compositions
US8686201B2 (en) 2011-11-09 2014-04-01 Celanese International Corporation Integrated acid and alcohol production process having flashing to recover acid production catalyst
US8704013B2 (en) 2011-11-09 2014-04-22 Celanese International Corporation Integrated process for producing ethanol
US8614359B2 (en) 2011-11-09 2013-12-24 Celanese International Corporation Integrated acid and alcohol production process
US8809599B2 (en) 2011-11-09 2014-08-19 Celanese International Corporation Integrated process for producing ethanol and water balance control
US8809598B2 (en) 2011-11-09 2014-08-19 Celanese International Corporation Producing ethanol using two different streams from acetic acid carbonylation process
US8703868B2 (en) 2011-11-28 2014-04-22 Celanese International Corporation Integrated process for producing polyvinyl alcohol or a copolymer thereof and ethanol
US9000234B2 (en) 2011-12-22 2015-04-07 Celanese International Corporation Calcination of modified support to prepare hydrogenation catalysts
US9233899B2 (en) 2011-12-22 2016-01-12 Celanese International Corporation Hydrogenation catalysts having an amorphous support
US8907139B2 (en) 2011-12-28 2014-12-09 Celanese International Corporation Process for acetal removal in the purification of a crude ethanol product
US8907142B2 (en) 2011-12-29 2014-12-09 Celanese International Corporation Process for promoting catalyst activity for ethyl acetate conversion
WO2013101305A1 (en) 2011-12-30 2013-07-04 Celanese International Corporation Pressure driven distillation for producing and recovering ethanol from hydrogenation process
US8981164B2 (en) 2012-01-06 2015-03-17 Celanese International Corporation Cobalt and tin hydrogenation catalysts
BR112014015584A8 (pt) 2012-01-06 2017-07-04 Celanese Int Corp catalisadores de hidrogenação com suportes modificados com cobalto
CN102584534B (zh) * 2012-01-18 2014-02-19 浙江华康药业股份有限公司 采用雷尼镍与雷尼铜协同催化加氢生产甘露醇的方法
US9353034B2 (en) 2012-02-07 2016-05-31 Celanese International Corporation Hydrogenation process with reduced residence time for vapor phase reactants
US9051235B2 (en) 2012-02-07 2015-06-09 Celanese International Corporation Process for producing ethanol using a molar excess of hydrogen
US9050585B2 (en) 2012-02-10 2015-06-09 Celanese International Corporation Chemisorption of ethyl acetate during hydrogenation of acetic acid to ethanol
US8729317B2 (en) 2012-02-15 2014-05-20 Celanese International Corporation Ethanol manufacturing process over catalyst with cesium and support comprising tungsten or oxides thereof
US8975452B2 (en) 2012-03-28 2015-03-10 Celanese International Corporation Process for producing ethanol by hydrocarbon oxidation and hydrogenation or hydration
US8772553B2 (en) 2012-10-26 2014-07-08 Celanese International Corporation Hydrogenation reaction conditions for producing ethanol
CN103785415B (zh) * 2012-10-31 2016-03-30 中国石油化工股份有限公司 羧酸加氢制备醇的钴铋催化剂
US8957262B2 (en) 2012-11-20 2015-02-17 Celanese International Corporation Olefin hydration for hydrogenation processes
US9000237B2 (en) 2012-12-20 2015-04-07 Celanese International Corporation Ethanol refining process using intermediate reboiler
ES2641449T3 (es) 2013-02-06 2017-11-10 Alantum Europe Gmbh Cuerpo de espuma metálica modificada superficialmente, procedimiento para su producción y su uso
US8975450B2 (en) 2013-03-15 2015-03-10 Celanese International Corporation Ethanol and ethyl acetate production using an acetic acid and acetic anhydride mixed feed
US8926718B2 (en) 2013-03-15 2015-01-06 Celanese International Corporation Thermochemically produced ethanol compositions
CN103980089A (zh) * 2014-05-05 2014-08-13 大连理工大学 一种制备乙醇和异丙醇的方法
CN104478660B (zh) * 2014-11-12 2016-01-20 厦门大学 一种低温制备异丙醇的方法
CN112226466A (zh) 2015-01-07 2021-01-15 威尔迪亚公司 萃取和转化半纤维素糖的方法
JP6959926B2 (ja) * 2016-01-07 2021-11-05 ハルドール・トプサー・アクチエゼルスカベット 糖からエチレングリコールを製造する方法
CA3010748C (en) * 2016-01-07 2023-08-22 Haldor Topsoe A/S Process for the preparation of ethylene glycol from sugars
PL3416740T3 (pl) 2016-02-19 2021-05-17 Intercontinental Great Brands Llc Procesy tworzenia wielu strumieni wartości ze źródeł biomasy
WO2018054740A1 (de) * 2016-09-23 2018-03-29 Basf Se Verfahren zur bereitstellung eines katalysatorfestbetts, das dotierte strukturierte katalysatorformkörper enthält
SG11201901567PA (en) * 2016-09-23 2019-04-29 Basf Se Process for activating a catalyst
TWI787215B (zh) * 2016-11-22 2022-12-21 美商Ｗ Ｒ 康格雷氏公司 降低損耗的催化劑及其製造方法
US20190345185A1 (en) * 2016-12-20 2019-11-14 Archer-Daniels-Midland Company Continuous process for hydrogenation of maltose to maltitol
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CN113024351B (zh) * 2021-03-24 2022-04-26 西南化工研究设计院有限公司 一种异丙醇的生产方法
JPWO2022244797A1 (de) * 2021-05-19 2022-11-24
CN114213214B (zh) * 2021-12-31 2023-06-13 中国林业科学研究院林产化学工业研究所 一种在温和条件下催化脂肪酸制备脂肪醇的方法

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4576926A (en) * 1984-04-23 1986-03-18 California Institute Of Technology Catalytic hollow spheres
EP0724908A1 (de) * 1995-01-06 1996-08-07 Showa Denko Kabushiki Kaisha Edelmetall Raney-Katalysatoren und Herstellung von wasserstoffhaltigen Verbindungen unter Verwendung solcher Katalysatoren
EP0854149A1 (de) * 1997-01-17 1998-07-22 Südzucker Aktiengesellschaft Mannheim/Ochsenfurt Verfahren zur Hydrierung von Zuckern mittels eines Schalenkatalysators
DE19933450A1 (de) * 1999-07-16 2001-01-18 Degussa Metallkatalysatoren

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1278411B (de) * 1963-06-14 1968-09-26 Basf Ag Verfahren zur Herstellung von Katalysatoren oder Katalysatortraegern in Form von Hohlkugeln
DE1300905B (de) * 1964-11-05 1969-08-14 Basf Ag Verwendung perforierter Hohlkugeln als Verdraengungskoerper in Wirbelschichtreaktoren
US3538018A (en) * 1967-07-29 1970-11-03 Basf Ag Binary support system for fluidized catalysts
US3798176A (en) * 1968-07-19 1974-03-19 Osaka Yogyo Co Ltd Method for manufacturing a catalyst and its carrier having a vacant center or a dense center
BE758296A (fr) 1969-11-07 1971-04-01 Rhodiatoce Procede de fabrication d'hexamethylenediamine
DE2101856C3 (de) 1971-01-15 1974-11-07 Kasachskij Gosudarstwenny Uniwersitet Imeni S.M. Kirowa, Alma-Ata (Sowjetunion) Aluminium-Nickel-Legierung, insbesondere zur Verwendung als Katalysator für die Hydrierung von ungesättigten organischen Verbindungen
DE2100373C3 (de) 1971-01-15 1979-04-12 Institut Chimitscheskich Nauk Akademii Nauk Kasachskoj Ssr Katalysator zum Hydrieren von Nitroverbindungen
US4153578A (en) 1978-07-31 1979-05-08 Gaf Corporation Catalyst comprising Raney nickel with adsorbed molybdenum compound
US4637990A (en) * 1978-08-28 1987-01-20 Torobin Leonard B Hollow porous microspheres as substrates and containers for catalysts and method of making same
DE3724156A1 (de) * 1987-07-22 1989-02-02 Norddeutsche Affinerie Verfahren zum herstellen von metallischen oder keramischen hohlkugeln

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4576926A (en) * 1984-04-23 1986-03-18 California Institute Of Technology Catalytic hollow spheres
EP0724908A1 (de) * 1995-01-06 1996-08-07 Showa Denko Kabushiki Kaisha Edelmetall Raney-Katalysatoren und Herstellung von wasserstoffhaltigen Verbindungen unter Verwendung solcher Katalysatoren
EP0854149A1 (de) * 1997-01-17 1998-07-22 Südzucker Aktiengesellschaft Mannheim/Ochsenfurt Verfahren zur Hydrierung von Zuckern mittels eines Schalenkatalysators
DE19933450A1 (de) * 1999-07-16 2001-01-18 Degussa Metallkatalysatoren

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CN1487911A (zh) 2004-04-07

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