CS258104B2 - Reactor for catalyzed reactions with through flow of gaseous reaction components in radial directions stepeise through particular chambers filled with catalyst - Google Patents

Reactor for catalyzed reactions with through flow of gaseous reaction components in radial directions stepeise through particular chambers filled with catalyst Download PDF

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Publication number
CS258104B2
CS258104B2 CS837077A CS707783A CS258104B2 CS 258104 B2 CS258104 B2 CS 258104B2 CS 837077 A CS837077 A CS 837077A CS 707783 A CS707783 A CS 707783A CS 258104 B2 CS258104 B2 CS 258104B2
Authority
CS
Czechoslovakia
Prior art keywords
reaction
reactor
gas
catalyst
wall
Prior art date
Application number
CS837077A
Other languages
Czech (cs)
English (en)
Other versions
CS707783A2 (en
Inventor
Kozo Ohsaki
Jun Zanma
Hiroshi Watanabe
Original Assignee
Toyo Engineering Corp
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 Toyo Engineering Corp filed Critical Toyo Engineering Corp
Publication of CS707783A2 publication Critical patent/CS707783A2/cs
Publication of CS258104B2 publication Critical patent/CS258104B2/cs

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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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00—Ammonia; Compounds thereof
    • C01C1/02—Preparation, purification or separation of ammonia
    • C01C1/04—Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • C01C1/0417—Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in the reactor
    • 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
    • B01J8/0285—Heating or cooling the reactor
    • 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
    • B01J8/0403—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 fluid flow within the beds being predominantly horizontal
    • 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
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132—Tubes
    • 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
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
CS837077A 1982-09-28 1983-09-28 Reactor for catalyzed reactions with through flow of gaseous reaction components in radial directions stepeise through particular chambers filled with catalyst CS258104B2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57167639A JPS5959242A (ja) 1982-09-28 1982-09-28 反応方法およびそのための反応器

Publications (2)

Publication Number Publication Date
CS707783A2 CS707783A2 (en) 1987-12-17
CS258104B2 true CS258104B2 (en) 1988-07-15

Family

ID=15853499

Family Applications (1)

Application Number Title Priority Date Filing Date
CS837077A CS258104B2 (en) 1982-09-28 1983-09-28 Reactor for catalyzed reactions with through flow of gaseous reaction components in radial directions stepeise through particular chambers filled with catalyst

Country Status (13)

Country Link
US (1) US4594227A (ja)
JP (1) JPS5959242A (ja)
KR (1) KR870000086B1 (ja)
BR (1) BR8305307A (ja)
CA (1) CA1204916A (ja)
CS (1) CS258104B2 (ja)
DD (1) DD210846A5 (ja)
DE (1) DE3334775A1 (ja)
FR (1) FR2533460B1 (ja)
GB (1) GB2127321B (ja)
IN (2) IN159980B (ja)
MY (1) MY8700158A (ja)
NL (1) NL8303295A (ja)

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DE3605792A1 (de) * 1985-09-27 1987-04-02 Gutehoffnungshuette Man Stehender reaktor fuer katalytische exotherme und endotherme reaktionen, insbesondere zur herstellung von methanol, ammoniak, synthesegas und hoeheren alkoholen
US5192512A (en) * 1987-01-21 1993-03-09 Institut Francais Du Petrole Apparatus for performing chemical reactions under pressure in a multi-stage reaction zone with external intermediary thermal conditioning
DK155979C (da) * 1987-05-20 1989-10-30 Haldor Topsoe As Fordelingselement til fordeling af gas til en reaktor
US4909808A (en) * 1987-10-14 1990-03-20 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Steam reformer with catalytic combustor
DE4135018A1 (de) * 1990-11-30 1992-06-04 Otto Oeko Tech Verfahren und vorrichtung zur stroemungsfuehrung in radialstromreaktoren
EP0539834A1 (de) * 1991-10-23 1993-05-05 OTTO OEKO-TECH GMBH & CO. KG Verfahren und Vorrichtung zur Strömungsführung in Radialstromreaktoren
DE4217317A1 (de) * 1992-05-26 1993-12-02 Metallgesellschaft Ag Kontaktkessel zur quasi-isothermen katalytischen Umsetzung von SO¶2¶ zu SO¶3¶ und Verfahren zum Betreiben desselben
US5520891A (en) * 1994-02-01 1996-05-28 Lee; Jing M. Cross-flow, fixed-bed catalytic reactor
US5869011A (en) * 1994-02-01 1999-02-09 Lee; Jing Ming Fixed-bed catalytic reactor
US5989500A (en) * 1997-07-02 1999-11-23 Phillips Petroleum Company Reactor heat exchange system
US6185268B1 (en) * 1997-08-29 2001-02-06 Kabushiki Kaisha Toshiba Main steam pressure disturbance preventing apparatus of nuclear power plant
US6620386B1 (en) 1998-07-09 2003-09-16 Stone & Webster, Inc. Radial flow reactor
US6171570B1 (en) * 1998-10-12 2001-01-09 Kellogg Brown & Root, Inc. Isothermal ammonia converter
CN1292221C (zh) * 1999-07-21 2006-12-27 斯通－韦伯斯特有限公司 横流式传热装置和增强的横流式传热方法
US6772830B1 (en) 1999-07-21 2004-08-10 Stone & Webster, Inc. Enhanced crossflow heat transfer
ATE284269T1 (de) * 1999-09-02 2004-12-15 Haldor Topsoe As Reaktor zur katalytischen selektiven oxidation eines wasserkohlenstoffes
US20040161381A1 (en) * 1999-12-02 2004-08-19 Thomsen Soren Gyde Process and reactor for carrying out non-adiabatic catalytic reactions
ES2427927T3 (es) * 1999-12-02 2013-11-04 Haldor Topsoe A/S Proceso para realización de reacciones catalíticas no adiabáticas
EP1153653A1 (en) * 2000-05-11 2001-11-14 Methanol Casale S.A. Reactor for exothermic or endothermic heterogeneous reactions
EP1221339A1 (en) * 2001-01-05 2002-07-10 Methanol Casale S.A. Catalytic reactor with heat exchanger for exothermic and endothermic heterogeneous chemical reactions
JP2002273203A (ja) * 2001-03-16 2002-09-24 Toyo Eng Corp 改良された触媒の抜き出し構造を有する反応器
GB0113078D0 (en) 2001-05-30 2001-07-18 Kvaerner Process Tech Ltd Process and plant
US7081230B2 (en) * 2002-11-15 2006-07-25 Kellogg Brown & Root Llc Split-flow, vertical ammonia converter
KR20060081728A (ko) * 2005-01-10 2006-07-13 삼성에스디아이 주식회사 연료 전지 시스템, 개질기 및 버너
DE102005049457A1 (de) * 2005-10-15 2007-05-16 Degussa Vorrichtung zur Durchführung chemischer Reaktionen
CN200954444Y (zh) * 2006-09-27 2007-10-03 吕仲明 径向折流板壳式反应器
DE102006060507A1 (de) * 2006-12-19 2008-06-26 Basf Se Reaktor zur Durchführung einer Reaktion zwischen zwei fluiden Edukten an einem Katalysatorbett mit Vorvermischen der fluiden Edukte in einer Einmischvorrichtung
DE102006060509A1 (de) * 2006-12-19 2008-06-26 Basf Se Reaktor zur Durchführung einer kontinuierlichen Oxidehydrierung sowie Verfahren
DE202007006812U1 (de) * 2007-05-11 2008-09-18 Man Dwe Gmbh Kühlrohrreaktor
CN101977680A (zh) * 2008-01-28 2011-02-16 弗雷穆特·J·马罗尔德 多列式热板和配备多列式热板的换热器
KR20110047224A (ko) * 2008-08-11 2011-05-06 우데 게엠베하 얇은 촉매 베드를 포함한 수직 실린더 반응기
EP2246109A1 (en) * 2009-04-29 2010-11-03 Methanol Casale S.A. Isothermal tube reactor
US9950305B2 (en) * 2011-07-26 2018-04-24 Battelle Memorial Institute Solar thermochemical processing system and method
CN102698659B (zh) * 2012-03-28 2013-12-25 中国石油化工股份有限公司 一种甲醇合成反应器结构
WO2014151340A1 (en) * 2013-03-15 2014-09-25 Caloris Acquisition, Llc Liquid to liquid multi-pass countercurrent heat exchanger
CN104399413B (zh) * 2014-11-18 2016-03-16 安徽新月化工设备有限公司 一种可控移热反应器
AU2015352038B2 (en) 2014-11-24 2018-11-08 Unisa A fixed bed reactor
CN105582856B (zh) * 2016-02-29 2019-08-16 南京敦先化工科技有限公司 一种双球腔可控移热变换反应器及其co反应方法
CN109012507A (zh) * 2018-09-30 2018-12-18 中石化宁波工程有限公司 可变温等温变换反应器
US11754349B2 (en) * 2019-03-08 2023-09-12 Hamilton Sundstrand Corporation Heat exchanger
CN114713147A (zh) * 2020-12-22 2022-07-08 中国石油化工股份有限公司 环氧化物的制备装置以及环氧化物的制备方法
JP2023103558A (ja) * 2022-01-14 2023-07-27 株式会社日立製作所 メタネーション反応器
KR20240061766A (ko) 2022-11-01 2024-05-08 (주)에이티엠코리아 개선된 필터장치를 포함하는 광경화 코팅액 제조장치

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US2835560A (en) * 1954-02-23 1958-05-20 Braun & Co C F Catalytic reactor
US2715570A (en) * 1954-06-03 1955-08-16 Sun Oil Co Rotary converter sealing devices
GB822630A (en) * 1956-11-16 1959-10-28 Distillers Co Yeast Ltd Method of carrying out catalytic reactions
US3249405A (en) * 1962-01-31 1966-05-03 Phillips Petroleum Co Catalytic reforming apparatus
GB1140071A (en) * 1965-03-24 1969-01-15 Ici Ltd Catalytic reactors
AT299981B (de) * 1970-04-21 1972-07-10 Chemie Linz Ag Vorrichtung zur Erzielung einer gleichmäßigen Gasverteilung in radial durchströmten Katalysatorlagen in Reaktoren für katalytische, exotherme Hochdrucksynthesen, vorzugsweise der Ammoniaksynthese
US3898049A (en) * 1971-10-05 1975-08-05 Texaco Inc Hydrogenation reactors with improved flow distribution
US4346060A (en) * 1978-07-17 1982-08-24 Pullman Incorporated Radial ammonia converters
JPS5839572B2 (ja) * 1979-04-03 1983-08-31 東洋エンジニアリング株式会社 反応器およびその使用法
US4421723A (en) * 1982-07-20 1983-12-20 Chevron Research Company Method and apparatus for supporting radial reactor centerpipes to accommodate thermal cycling

Also Published As

Publication number Publication date
NL8303295A (nl) 1984-04-16
MY8700158A (en) 1987-12-31
FR2533460A1 (fr) 1984-03-30
US4594227A (en) 1986-06-10
FR2533460B1 (fr) 1986-09-05
JPH0347134B2 (ja) 1991-07-18
IN161165B (ja) 1987-10-10
GB8325811D0 (en) 1983-10-26
DE3334775C2 (ja) 1987-09-10
IN159980B (ja) 1987-06-20
DE3334775A1 (de) 1984-03-29
BR8305307A (pt) 1984-05-08
GB2127321B (en) 1986-04-30
KR870000086B1 (ko) 1987-02-10
GB2127321A (en) 1984-04-11
CA1204916A (en) 1986-05-27
CS707783A2 (en) 1987-12-17
KR840006444A (ko) 1984-11-30
DD210846A5 (de) 1984-06-27
JPS5959242A (ja) 1984-04-05

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