DK167242B1 - Apparat og fremgangsmaade til exoterme reaktioner - Google Patents

Apparat og fremgangsmaade til exoterme reaktioner Download PDF

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Publication number
DK167242B1
DK167242B1 DK071389A DK71389A DK167242B1 DK 167242 B1 DK167242 B1 DK 167242B1 DK 071389 A DK071389 A DK 071389A DK 71389 A DK71389 A DK 71389A DK 167242 B1 DK167242 B1 DK 167242B1
Authority
DK
Denmark
Prior art keywords
cooling
gas
tubes
temperature
catalyst bed
Prior art date
Application number
DK071389A
Other languages
Danish (da)
English (en)
Other versions
DK71389D0 (da
DK71389A (da
Inventor
Henrik Otto Stahl
Original Assignee
Topsoe Haldor As
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
Publication of DK71389D0 publication Critical patent/DK71389D0/da
Application filed by Topsoe Haldor As filed Critical Topsoe Haldor As
Priority to DK071389A priority Critical patent/DK167242B1/da
Priority to CA002046304A priority patent/CA2046304C/en
Priority to AU51036/90A priority patent/AU627281B2/en
Priority to US07/743,393 priority patent/US5190731A/en
Priority to PCT/DK1990/000034 priority patent/WO1990009234A1/en
Priority to EP90903328A priority patent/EP0458848B1/de
Priority to DE9090903328T priority patent/DE69000483T2/de
Priority to JP50359990A priority patent/JPH0638906B2/ja
Priority to CN90106925A priority patent/CN1031110C/zh
Publication of DK71389A publication Critical patent/DK71389A/da
Priority to KR90702255A priority patent/KR0131401B1/ko
Priority to SU915001565A priority patent/RU2031702C1/ru
Application granted granted Critical
Publication of DK167242B1 publication Critical patent/DK167242B1/da

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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
    • 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
    • B01J8/0278—Feeding reactive fluids
    • 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
    • B01J8/0005—Catalytic processes under superatmospheric pressure
    • 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
    • B01J8/0207—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 flow within the bed being predominantly horizontal
    • B01J8/0214—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 flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
    • 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
    • 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
    • C01C1/0405—Preparation of ammonia by synthesis from N2 and H2 in presence of a catalyst
    • C01C1/0417—Preparation of ammonia by synthesis 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
    • 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
    • C07C29/15—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 oxides of carbon exclusively
    • C07C29/151—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 oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/152—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 oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02—Header boxes; End plates
    • F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
    • F28F9/0273—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes with multiple holes
    • 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)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Fluid Mechanics (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Saccharide Compounds (AREA)
DK071389A 1989-02-16 1989-02-16 Apparat og fremgangsmaade til exoterme reaktioner DK167242B1 (da)

Priority Applications (11)

Application Number Priority Date Filing Date Title
DK071389A DK167242B1 (da) 1989-02-16 1989-02-16 Apparat og fremgangsmaade til exoterme reaktioner
DE9090903328T DE69000483T2 (de) 1989-02-16 1990-02-12 Vorrichtung und verfahren fuer exothermische reaktionen.
AU51036/90A AU627281B2 (en) 1989-02-16 1990-02-12 Exothermic reactions
US07/743,393 US5190731A (en) 1989-02-16 1990-02-12 Process and apparatus for exothermic reactions
PCT/DK1990/000034 WO1990009234A1 (en) 1989-02-16 1990-02-12 Process and apparatus for exothermic reactions
EP90903328A EP0458848B1 (de) 1989-02-16 1990-02-12 Vorrichtung und verfahren für exothermische reaktionen
CA002046304A CA2046304C (en) 1989-02-16 1990-02-12 Process and apparatus for exothermic reactions
JP50359990A JPH0638906B2 (ja) 1989-02-16 1990-02-12 発熱反応のプロセスと装置
CN90106925A CN1031110C (zh) 1989-02-16 1990-08-14 放热反应方法及所用设备
KR90702255A KR0131401B1 (en) 1989-02-16 1990-10-13 Process and apparatus for exothermic reaction
SU915001565A RU2031702C1 (ru) 1989-02-16 1991-08-15 Реактор для проведения экзотермической газофазной реакции и способ проведения экзотермической газофазной реакции

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DK71389 1989-02-16
DK071389A DK167242B1 (da) 1989-02-16 1989-02-16 Apparat og fremgangsmaade til exoterme reaktioner
CN90106925A CN1031110C (zh) 1989-02-16 1990-08-14 放热反应方法及所用设备
CN90106925 1990-08-14

Publications (3)

Publication Number Publication Date
DK71389D0 DK71389D0 (da) 1989-02-15
DK71389A DK71389A (da) 1990-08-17
DK167242B1 true DK167242B1 (da) 1993-09-27

Family

ID=36763884

Family Applications (1)

Application Number Title Priority Date Filing Date
DK071389A DK167242B1 (da) 1989-02-16 1989-02-16 Apparat og fremgangsmaade til exoterme reaktioner

Country Status (10)

Country Link
US (1) US5190731A (de)
EP (1) EP0458848B1 (de)
JP (1) JPH0638906B2 (de)
CN (1) CN1031110C (de)
AU (1) AU627281B2 (de)
CA (1) CA2046304C (de)
DE (1) DE69000483T2 (de)
DK (1) DK167242B1 (de)
RU (1) RU2031702C1 (de)
WO (1) WO1990009234A1 (de)

Families Citing this family (30)

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SG49945A1 (en) 1992-08-27 1998-06-15 Cabot Corp Carbon blacks
DK169696B1 (da) * 1992-12-07 1995-01-16 Topsoe Haldor As Fremgangsmåde til køling af syntesegas i en katalytisk reaktor
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
CN1088618C (zh) * 1996-08-21 2002-08-07 楼寿林 一种接近最佳温度的催化反应改进工艺及其合成反应器
RU2124937C1 (ru) * 1997-04-28 1999-01-20 Акционерное общество "Ново-Уфимский нефтеперерабатывающий завод" Реактор для проведения каталитических процессов
RU2152249C1 (ru) * 1999-02-05 2000-07-10 Закрытое акционерное общество "Каустик" Устройство для ввода реагентов в реактор оксихлорирования этилена
DE19937152B4 (de) * 1999-08-06 2006-09-21 Nucellsys Gmbh Kombiniertes Bauteil zur Nachverbrennung von Anodenabgasen eines Brennstoffzellensystems und zum Verdampfen von dem Brennstoffzellensystem zuzuführenden Edukten
RU2208475C2 (ru) * 2001-04-26 2003-07-20 Институт катализа им. Г.К. Борескова СО РАН Каталитический реактор для получения синтез-газа
US20030039601A1 (en) * 2001-08-10 2003-02-27 Halvorson Thomas Gilbert Oxygen ion transport membrane apparatus and process for use in syngas production
ATE469696T1 (de) 2002-08-27 2010-06-15 Methanol Casale Sa Verfahren zur durchführung von chemischen reaktionen unter pseudo-isothermischen bedingungen
MX2007001173A (es) * 2004-01-15 2007-09-25 Methanol Casale Sa Reactor catalitico de lecho fijo.
EP1610081A1 (de) * 2004-06-25 2005-12-28 Haldor Topsoe A/S Wärmeaustauschprozess und Wärmetauscher
JP2008517864A (ja) * 2004-10-26 2008-05-29 ハルドール・トプサー・アクチエゼルスカベット 吸熱又は発熱接触反応を実施するための反応装置及び方法
US7371361B2 (en) * 2004-11-03 2008-05-13 Kellogg Brown & Root Llc Maximum reaction rate converter system for exothermic reactions
EA009954B1 (ru) * 2006-06-07 2008-04-28 Генрих Семенович Фалькевич Способ осуществления химического превращения сырья
DE102006051899A1 (de) * 2006-10-31 2008-05-15 Bayer Technology Services Gmbh Verfahren und Vorrichtung zur katalytischen Oxidation von SO2-haltigen Gasen mit Sauerstoff
ITMI20070627A1 (it) * 2007-03-29 2008-09-30 Polimeri Europa Spa Dispositivo miscelatore a bassa perdita di carico e suo impiego nella miscelazione di due gas-vapori
EP2070590A1 (de) * 2007-12-11 2009-06-17 Methanol Casale S.A. System zur Unterstützung von Wärmetauschplatten in isothermischen chemischen Reaktoren
RU2481151C2 (ru) * 2008-02-25 2013-05-10 Хальдор Топсеэ А/С Способ проведения синтеза фишера-тропша и реактор для его осуществления
EP2192082B1 (de) * 2008-11-28 2013-07-03 Haldor Topsoe A/S Gleichzeitige Herstellung von Methanol und Ammoniak
US8092755B2 (en) * 2009-04-06 2012-01-10 Lummus Technology Inc. Devices for injection of gaseous streams into a bed of fluidized solids
SI23385A (sl) * 2010-06-09 2011-12-30 Brinox, D.O.O. Nova izvedba procesne komore z distribucijsko ploĺ äśo plina, namenjena uporabi v napravah za obdelavo trdnih delcev
RU2452559C2 (ru) * 2010-08-19 2012-06-10 Общество с ограниченной ответственностью "СинТоп" Реактор паровой и пароуглекислотной конверсии легких углеводородов для получения газа, содержащего водород и окись углерода
BR112013028447A2 (pt) * 2011-06-16 2018-06-19 Haldor Topsoe As método para executar reações catalíticas exotérmicas e reator para utilização no método
US9902668B2 (en) 2013-09-06 2018-02-27 Saudi Basic Industries Corporation Hydrogenation reactor and process
AR113649A1 (es) * 2017-12-20 2020-05-27 Haldor Topsoe As Convertidor de flujo axial enfriado
CN111115578B (zh) * 2019-12-11 2021-09-17 厦门大学 一种适用于大流量高压条件的仲氢富集装置
US12491484B2 (en) 2021-01-15 2025-12-09 CRI, hf Reactor for synthesis of methanol or other products
US11738317B2 (en) * 2021-01-15 2023-08-29 CRI, hf Reactor for synthesizing methanol or other products

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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
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JPS60225632A (ja) * 1984-04-23 1985-11-09 Mitsubishi Heavy Ind Ltd 反応器

Also Published As

Publication number Publication date
CA2046304C (en) 1999-11-02
CN1031110C (zh) 1996-02-28
RU2031702C1 (ru) 1995-03-27
JPH04502426A (ja) 1992-05-07
EP0458848A1 (de) 1991-12-04
AU5103690A (en) 1990-09-05
CA2046304A1 (en) 1990-08-17
DK71389D0 (da) 1989-02-15
JPH0638906B2 (ja) 1994-05-25
WO1990009234A1 (en) 1990-08-23
US5190731A (en) 1993-03-02
DE69000483T2 (de) 1993-06-03
DE69000483D1 (de) 1992-12-24
DK71389A (da) 1990-08-17
CN1059107A (zh) 1992-03-04
AU627281B2 (en) 1992-08-20
EP0458848B1 (de) 1992-11-19

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Legal Events

Date Code Title Description
B1 Patent granted (law 1993)
PBP Patent lapsed