ATE171394T1 - Katalytischer reaktor und verfahren zur durchführung von stark exothermen reaktionen - Google Patents

Katalytischer reaktor und verfahren zur durchführung von stark exothermen reaktionen

Info

Publication number
ATE171394T1
ATE171394T1 AT94309380T AT94309380T ATE171394T1 AT E171394 T1 ATE171394 T1 AT E171394T1 AT 94309380 T AT94309380 T AT 94309380T AT 94309380 T AT94309380 T AT 94309380T AT E171394 T1 ATE171394 T1 AT E171394T1
Authority
AT
Austria
Prior art keywords
reaction
carrying
zone
catalytic reactor
exothermic reactions
Prior art date
Application number
AT94309380T
Other languages
English (en)
Inventor
Jr John C Jubin
Original Assignee
Arco Chem Tech
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 US08/310,546 external-priority patent/US5466836A/en
Application filed by Arco Chem Tech filed Critical Arco Chem Tech
Application granted granted Critical
Publication of ATE171394T1 publication Critical patent/ATE171394T1/de

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
    • B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D301/00—Preparation of oxiranes
    • C07D301/02—Synthesis of the oxirane ring
    • C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
    • C07D301/12—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with hydrogen peroxide or inorganic peroxides or peracids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Epoxy Compounds (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
AT94309380T 1993-12-20 1994-12-15 Katalytischer reaktor und verfahren zur durchführung von stark exothermen reaktionen ATE171394T1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US17114493A 1993-12-20 1993-12-20
US08/310,546 US5466836A (en) 1993-12-20 1994-09-22 Catalytic converter and method for highly exothermic reactions

Publications (1)

Publication Number Publication Date
ATE171394T1 true ATE171394T1 (de) 1998-10-15

Family

ID=22622713

Family Applications (1)

Application Number Title Priority Date Filing Date
AT94309380T ATE171394T1 (de) 1993-12-20 1994-12-15 Katalytischer reaktor und verfahren zur durchführung von stark exothermen reaktionen

Country Status (9)

Country Link
US (1) US5573736A (de)
EP (1) EP0659473B1 (de)
JP (1) JP3597895B2 (de)
CN (1) CN1133630C (de)
AT (1) ATE171394T1 (de)
CA (1) CA2137310C (de)
DE (1) DE69413507T2 (de)
ES (1) ES2121162T3 (de)
RU (1) RU2126799C1 (de)

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US5760253A (en) * 1997-01-29 1998-06-02 Arco Chemical Technology, L.P. Catalytic converter and method for highly exothermic reactions
WO1999025461A1 (fr) * 1997-11-18 1999-05-27 Asahi Kasei Kogyo Kabushiki Kaisha Procede et dispositif de prevention contre le rechauffement general de la planete
US5849937A (en) * 1997-12-19 1998-12-15 Arco Chemical Technology, L.P. Epoxidation process using serially connected cascade of fixed bed reactors
DE19835907A1 (de) * 1998-08-07 2000-02-17 Basf Ag Verfahren zur Umsetzung einer organischen Verbindung mit einem Hydroperoxid
US7033553B2 (en) * 2000-01-25 2006-04-25 Meggitt (Uk) Limited Chemical reactor
EP1122248A1 (de) 2000-02-07 2001-08-08 Degussa AG Verfahren zur Epoxidierung von Olefinen
EP1122246A1 (de) * 2000-02-07 2001-08-08 Degussa AG Verfahren zur Epoxidierung von Olefinen
EP1122247A1 (de) 2000-02-07 2001-08-08 Degussa AG Verfahren zur Epoxidierung von Olefinen
FR2810983B1 (fr) * 2000-06-28 2004-05-21 Solvay Procede de fabrication d'oxiranne au moyen d'un compose peroxyde
FR2810980B1 (fr) * 2000-06-28 2004-05-21 Solvay Procede de fabrication d'oxiranne en presence d'un catalyseur sous forme de particules
EP1221442B1 (de) 2001-01-08 2010-07-28 Evonik Degussa GmbH Verfahren zur Epoxidierung von Olefinen
EP1247805A1 (de) † 2001-03-05 2002-10-09 Degussa AG Verfahren zur epoxidierung von olefinen
EP1247806A1 (de) * 2001-03-05 2002-10-09 Degussa AG Verfahren zur Epoxidierung von Olefinen
EP1258483A1 (de) * 2001-03-05 2002-11-20 Degussa AG Verfahren zur epoxidierung von olefinen
US6608219B2 (en) 2001-06-13 2003-08-19 Degussa Ag Process for the epoxidation of olefins
US6596881B2 (en) 2001-06-13 2003-07-22 Degussa Ag Process for the epoxidation of olefins
US6600055B2 (en) 2001-06-13 2003-07-29 Degussa Ag Process for the epoxidation of olefins
US6749668B2 (en) 2001-06-18 2004-06-15 Degussa Ag Process for the recovery of combustible components of a gas stream
US6532741B2 (en) 2001-06-29 2003-03-18 United Technologies Corporation Gas generator for producing adjustable flow
US6652248B2 (en) 2001-06-29 2003-11-25 United Technologies Corporation Catalyst bed
EP1285915A1 (de) * 2001-08-16 2003-02-26 Degussa AG Kontinuierliches Verfahren zur Herstellung von Epoxiden aus Olefinen und Wasserstoffperoxid
US6610865B2 (en) 2001-08-15 2003-08-26 Degussa Ag Process for the epoxidation of olefins
US6596883B2 (en) 2001-08-23 2003-07-22 Degussa Ag Process for the epoxidation of olefins
AU2002366573A1 (en) * 2001-12-05 2003-06-23 Dow Global Technologies Inc. Process of preparing an olefin oxide from olefin and organic hydroperoxide
US6720436B2 (en) 2002-03-18 2004-04-13 Degussa Ag Process for the epoxidation of olefins
EP1359148A1 (de) * 2002-05-02 2003-11-05 Degussa AG Verfahren zur Epoxidierung von Olefinen
US7141683B2 (en) 2002-05-02 2006-11-28 Degussa Ag Process for the epoxidation of olefins
US6838572B2 (en) 2002-09-30 2005-01-04 Degussa Ag Process for the epoxidation of olefins
US7722847B2 (en) 2002-09-30 2010-05-25 Evonik Degussa Gmbh Aqueous hydrogen peroxide solutions and method of making same
EP1403259A1 (de) * 2002-09-30 2004-03-31 Degussa AG Verfahren zur Epoxidierung von Olefinen
US7169945B2 (en) 2002-11-26 2007-01-30 Degussa Ag Process for the epoxidation of olefins
DE10317520A1 (de) * 2003-04-16 2004-11-04 Basf Ag Verfahren zur Herstellung eines Alkenoxids
DE102004059191B4 (de) * 2004-12-09 2010-07-01 Evonik Degussa Gmbh Vorrichtung und Verfahren zur Herstellung von Chlorsilanen
US20070004926A1 (en) * 2005-06-29 2007-01-04 Basf Aktiengesellschaft Process for producing propylene oxide
KR101485955B1 (ko) * 2007-05-11 2015-01-22 베리 제이. 빌릭 산화올레핀 제조 공장에서의 고선택성 촉매의 개시 방법
JP2009035544A (ja) * 2007-07-11 2009-02-19 Sumitomo Chemical Co Ltd エポキシ化合物の製造装置および製造方法
BRPI0814211A2 (pt) * 2007-07-11 2015-01-27 Sumitomo Chemical Co Método e aparelho para produção de gás misturado, e aparelho e método para produção de composto époxi.
ES2436625T3 (es) * 2009-05-12 2014-01-03 Basf Se Proceso para producir óxido de propileno
CN101885711B (zh) * 2009-05-13 2012-09-05 中国石油化工股份有限公司 环氧丙烷的生产方法
CN101941955B (zh) * 2009-07-06 2012-09-05 中国石油化工股份有限公司 由过氧化氢和丙烯生产环氧丙烷的方法
CN101941954B (zh) * 2009-07-06 2012-09-05 中国石油化工股份有限公司 由过氧化氢和丙烯制备环氧丙烷的方法
GB201102551D0 (en) 2011-02-14 2011-03-30 Davy Process Techn Ltd Reactor
RU2472786C1 (ru) * 2011-05-13 2013-01-20 Закрытое акционерное общество "Химтэк Инжиниринг" Способ получения оксида пропилена
HUE046136T2 (hu) 2015-11-25 2020-02-28 Evonik Operations Gmbh Eljárás 1,2-propándiol elõállítására propénból és hidrogén-peroxidból
TWI707847B (zh) 2015-11-26 2020-10-21 德商贏創運營有限公司 丙烯之環氧化方法
ES2873407T3 (es) * 2015-11-26 2021-11-03 Evonik Operations Gmbh Procedimiento y reactor para la epoxidación de propeno
PL3380459T3 (pl) 2015-11-26 2020-06-01 Evonik Operations Gmbh Sposób epoksydowania olefiny
CN108473453B (zh) 2016-01-19 2020-08-04 赢创运营有限公司 烯烃的环氧化方法
HUE052019T2 (hu) 2016-03-21 2021-04-28 Evonik Operations Gmbh Eljárás propén epoxidálására
EP3246323A1 (de) 2016-05-17 2017-11-22 Evonik Degussa GmbH Integrierter prozess zur herststellung von propenoxid aus propan
EP3406603A1 (de) 2017-05-22 2018-11-28 Evonik Degussa GmbH Verfahren zur epoxidierung von propen
CN108043331A (zh) * 2017-12-21 2018-05-18 红宝丽集团股份有限公司 一种用于1,2-环氧丁烷制备的多段反应装置及1,2-环氧丁烷的制备方法
EP4332233A1 (de) 2022-09-05 2024-03-06 Syensqo Sa Lösungsmittelfreie enzymatische epoxidierung von olefinen
CN119841791A (zh) * 2025-03-18 2025-04-18 中国天辰工程有限公司 一种过氧化氢直接氧化法生产环氧丙烷的方法

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Also Published As

Publication number Publication date
JP3597895B2 (ja) 2004-12-08
JPH07196639A (ja) 1995-08-01
CN1109382A (zh) 1995-10-04
RU2126799C1 (ru) 1999-02-27
DE69413507T2 (de) 1999-02-11
DE69413507D1 (de) 1998-10-29
ES2121162T3 (es) 1998-11-16
EP0659473B1 (de) 1998-09-23
EP0659473A1 (de) 1995-06-28
US5573736A (en) 1996-11-12
RU94043783A (ru) 1996-12-20
CN1133630C (zh) 2004-01-07
CA2137310A1 (en) 1995-06-21
CA2137310C (en) 2004-02-17

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Legal Events

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REN Ceased due to non-payment of the annual fee