DE60018139D1 - Reaktor zur katalytischen Gasphasenoxidation - Google Patents

Reaktor zur katalytischen Gasphasenoxidation

Info

Publication number
DE60018139D1
DE60018139D1 DE60018139T DE60018139T DE60018139D1 DE 60018139 D1 DE60018139 D1 DE 60018139D1 DE 60018139 T DE60018139 T DE 60018139T DE 60018139 T DE60018139 T DE 60018139T DE 60018139 D1 DE60018139 D1 DE 60018139D1
Authority
DE
Germany
Prior art keywords
reactor
gas phase
phase oxidation
catalytic gas
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 - Lifetime
Application number
DE60018139T
Other languages
English (en)
Other versions
DE60018139T2 (de
Inventor
Takeshi Nishimura
Masakatsu Mori
Masatsugu Kitaura
Osamu Dodo
Michio Tanimoto
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.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai Co 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
Application filed by Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Application granted granted Critical
Publication of DE60018139D1 publication Critical patent/DE60018139D1/de
Publication of DE60018139T2 publication Critical patent/DE60018139T2/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/06Chemical 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 in tube reactors; the solid particles being arranged in tubes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0066Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/06Chemical 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 in tube reactors; the solid particles being arranged in tubes
    • B01J8/067Heating or cooling the reactor
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/25Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
    • C07C51/252Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0066Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • F28D7/0083Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium
    • F28D7/0091Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium the supplementary medium flowing in series through the units
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders
    • B01J2208/00221Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/02Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/023Details
    • B01J2208/024Particulate material
    • B01J2208/025Two or more types of catalyst
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2265/00Safety or protection arrangements; Arrangements for preventing malfunction
    • F28F2265/26Safety or protection arrangements; Arrangements for preventing malfunction for allowing differential expansion between elements

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
DE60018139T 1999-11-05 2000-11-01 Reaktor zur katalytischen Gasphasenoxidation Expired - Lifetime DE60018139T2 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP31546999 1999-11-05
JP31546999A JP3646027B2 (ja) 1999-11-05 1999-11-05 接触気相酸化用反応器およびそれを使用した(メタ)アクリル酸の製造方法

Publications (2)

Publication Number Publication Date
DE60018139D1 true DE60018139D1 (de) 2005-03-24
DE60018139T2 DE60018139T2 (de) 2005-07-21

Family

ID=18065741

Family Applications (1)

Application Number Title Priority Date Filing Date
DE60018139T Expired - Lifetime DE60018139T2 (de) 1999-11-05 2000-11-01 Reaktor zur katalytischen Gasphasenoxidation

Country Status (7)

Country Link
US (1) US6994833B1 (de)
EP (1) EP1097745B1 (de)
JP (1) JP3646027B2 (de)
KR (1) KR100454492B1 (de)
CN (1) CN1096879C (de)
DE (1) DE60018139T2 (de)
ZA (1) ZA200005988B (de)

Families Citing this family (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10137534A1 (de) 2001-08-01 2003-02-13 Basf Ag Verfahren zur Herstellung von Maleinsäureanhydrid
JP4028392B2 (ja) * 2002-01-11 2007-12-26 三菱化学株式会社 気相接触酸化方法
AU2003201861A1 (en) * 2002-01-11 2003-07-30 Mitsubishi Chemical Corporation Multipipe reactor, vapor phase catalytic oxidation method using multipipe reactor, and start-up method applied to multipipe reactor
KR100450234B1 (ko) * 2002-07-10 2004-09-24 주식회사 엘지화학 개선된 열교환 시스템을 갖는 촉매 산화 반응기
US7115776B2 (en) 2002-07-18 2006-10-03 Basf Aktiengesellschaft Heterogeneously catalyzed gas-phase partial oxidation of at least one organic compound
TWI302147B (en) * 2003-09-01 2008-10-21 Lg Chemical Ltd Method of producing unsaturated aldehyde and unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system
JP4477640B2 (ja) * 2003-12-24 2010-06-09 エルジー・ケム・リミテッド 固定層触媒酸化反応器における改善された熱制御システムによる不飽和酸の製造方法
TWI292755B (en) * 2003-12-26 2008-01-21 Lg Chemical Ltd Method of producing unsaturated aldehyde and/or unsaturated fatty acid
US7326389B2 (en) * 2003-12-26 2008-02-05 Lg Chem, Ltd. Method of producing unsaturated aldehyde and/or unsaturated acid
CN1988950B (zh) * 2004-05-28 2012-09-05 住友化学株式会社 热交换型反应器
US7371361B2 (en) * 2004-11-03 2008-05-13 Kellogg Brown & Root Llc Maximum reaction rate converter system for exothermic reactions
KR100850857B1 (ko) * 2005-02-01 2008-08-06 주식회사 엘지화학 불포화 지방산의 제조방법
DE102006000996A1 (de) 2006-01-05 2007-07-12 Basf Ag Verfahren der heterogen katalysierten Gasphasen-Partialoxidation wenigstens einer organischen Ausgangsverbindung
WO2007083927A1 (en) * 2006-01-18 2007-07-26 Lg Chem, Ltd. Reactor with improved heat transfer performance
KR100898692B1 (ko) * 2006-01-18 2009-05-22 주식회사 엘지화학 열전달 성능이 향상된 반응기, 이 반응기를 이용한 산화물 제조방법, 및 평행류의 열매체 유속 증가 방법
EP1734030A1 (de) 2006-01-18 2006-12-20 BASF Aktiengesellschaft Verfahren zum Langzeitbetrieb einer heterogen katalysierten partiellen Gasphasenoxidation einer organischen Ausgangsverbindung
KR100847199B1 (ko) 2006-01-31 2008-07-17 주식회사 엘지화학 열전달 성능이 향상된 반응기, 이 반응기를 이용한 산화물 제조방법, 및 평행류의 열매체 유속 증가 방법
US7897813B2 (en) 2006-07-19 2011-03-01 Nippon Shokubai Co., Ltd. Reactor for gas phase catalytic oxidation and a process for producing acrylic acid using it
TWI373375B (en) 2007-03-01 2012-10-01 Rohm & Haas Apparatus and method for dislodging and extracting solid materials from tubes
EP2177500A1 (de) * 2007-07-27 2010-04-21 Nippon Shokubai Co., Ltd. Verfahren zur herstellung von acrylsäure durch zweistufige katalytische dampfphasenoxidation
KR101105336B1 (ko) * 2008-03-31 2012-01-16 롬 앤드 하아스 컴패니 폭연 압력 감소를 위한 방법 및 장치
WO2013004254A1 (en) * 2011-07-01 2013-01-10 Haldor Topsøe A/S Heat exchange reactor
US20140065029A1 (en) * 2012-08-28 2014-03-06 Dynamic Engineering Inc. Symmetrical reactor including a plurality of packed tubes
CN103908929B (zh) * 2012-12-29 2016-12-28 新煤化工设计院(上海)有限公司 一种组合换热式多壳程的甲醇制烯烃固定床生产设备及其生产方法
EP2887001A1 (de) 2013-12-18 2015-06-24 Casale Sa Rohrwärmetauschereinheit für Einbauten von Wärmetauschern oder Reaktoren
WO2016017722A1 (ja) 2014-08-01 2016-02-04 株式会社日本触媒 不活性物質の回収方法及び当該方法により回収された不活性物質を用いたアクリル酸の製造方法
CN106563929B (zh) * 2015-10-08 2019-09-17 利宝地工程有限公司 修复和制造涡轮发动机部件的方法及涡轮发动机部件
CN206258002U (zh) * 2015-12-10 2017-06-16 莱尔德电子材料(深圳)有限公司 热交换器
SG11201809019YA (en) * 2016-04-21 2018-11-29 Rohm & Haas Methods for using macroporous inert materials in monomer production
KR102084768B1 (ko) * 2016-11-01 2020-03-04 주식회사 엘지화학 불포화 알데하이드 및 불포화 카르복실산의 제조 방법
JP6824508B2 (ja) * 2019-04-05 2021-02-03 千住金属工業株式会社 結露装置、フラックス回収装置、はんだ付け装置、水蒸気除去方法、フラックス回収方法及びはんだ処理方法
JP2023522261A (ja) 2020-04-21 2023-05-29 ベーアーエスエフ・エスエー 元素Mo、W、V及びCuを含む触媒活性多元素酸化物を生成する方法
CN114505018B (zh) * 2022-03-30 2023-02-28 山东彩客东奥化学有限公司 一种BDO脱氢生产γ-丁内酯反应生产装置

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2986454A (en) * 1957-07-23 1961-05-30 American Cyanamid Co Tubular catalytic converter
US3147084A (en) * 1962-03-08 1964-09-01 Shell Oil Co Tubular catalytic reactor with cooler
JPS52120268A (en) * 1976-04-02 1977-10-08 Hitachi Ltd Construction of pipe hole section formed by cementing adhesive member to inside of hole expanding
AU529228B2 (en) * 1977-07-13 1983-06-02 Nippon Shokubai Kagaku Kogyo Co. Ltd. Catalytic vapour phase oxidation
JPS6029290B2 (ja) * 1977-07-20 1985-07-10 株式会社日本触媒 接触気相酸化方法
JPS5419480A (en) * 1977-07-14 1979-02-14 Nippon Shokubai Kagaku Kogyo Co Ltd Pultipass reactor
JPS5419479A (en) * 1977-07-13 1979-02-14 Nippon Shokubai Kagaku Kogyo Co Ltd Reactor
US4436146A (en) * 1981-05-20 1984-03-13 Union Carbide Corporation Shell and tube heat exchanger
JPS6068047A (ja) * 1983-09-14 1985-04-18 Mitsubishi Heavy Ind Ltd 多管式反応装置
EP0383224B1 (de) 1989-02-17 1992-09-16 Jgc Corporation Rohrbündelapparat mit einer Zwischenrohrplatte
US5759500A (en) * 1996-01-16 1998-06-02 E. I. Du Pont De Nemours And Company Fluid reactor with catalyst on floating tubesheet
JP3948798B2 (ja) * 1997-10-27 2007-07-25 株式会社日本触媒 アクリル酸の製造方法
DE19806810A1 (de) * 1998-02-18 1999-08-19 Deggendorfer Werft Eisenbau Röhrenreaktor für katalytische Reaktionen

Also Published As

Publication number Publication date
KR20010051326A (ko) 2001-06-25
CN1294939A (zh) 2001-05-16
JP2001129384A (ja) 2001-05-15
US6994833B1 (en) 2006-02-07
CN1096879C (zh) 2002-12-25
EP1097745A1 (de) 2001-05-09
DE60018139T2 (de) 2005-07-21
EP1097745B1 (de) 2005-02-16
JP3646027B2 (ja) 2005-05-11
KR100454492B1 (ko) 2004-10-28
ZA200005988B (en) 2001-05-18

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