DK1216750T3 - Reaktor til eksoterme eller endoterme heterogene reaktioner - Google Patents

Reaktor til eksoterme eller endoterme heterogene reaktioner

Info

Publication number
DK1216750T3
DK1216750T3 DK01129714T DK01129714T DK1216750T3 DK 1216750 T3 DK1216750 T3 DK 1216750T3 DK 01129714 T DK01129714 T DK 01129714T DK 01129714 T DK01129714 T DK 01129714T DK 1216750 T3 DK1216750 T3 DK 1216750T3
Authority
DK
Denmark
Prior art keywords
exothermic
reactor
heterogeneous reactions
endothermic heterogeneous
endothermic
Prior art date
Application number
DK01129714T
Other languages
English (en)
Inventor
Ermanno Filippi
Enrico Rizzi
Mirco Tarozzo
Original Assignee
Methanol Casale Sa
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 Methanol Casale Sa filed Critical Methanol Casale Sa
Application granted granted Critical
Publication of DK1216750T3 publication Critical patent/DK1216750T3/da

Links

Classifications

    • 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
    • C01C1/0423—Cold wall reactors
    • 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
    • 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
    • F28D7/02—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 helically coiled
    • F28D7/028—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 helically coiled the conduits of at least one medium being helically coiled, the coils having a conical configuration
    • 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
    • B01J2208/00141—Coils
    • 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)
  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Thermal Sciences (AREA)
  • Fluid Mechanics (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Saccharide Compounds (AREA)
DK01129714T 2000-12-14 2001-12-13 Reaktor til eksoterme eller endoterme heterogene reaktioner DK1216750T3 (da)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT2000MI002712A IT1319549B1 (it) 2000-12-14 2000-12-14 Reattore per l'effettuazione di reazioni eterogenee esotermiche oendotermiche

Publications (1)

Publication Number Publication Date
DK1216750T3 true DK1216750T3 (da) 2006-11-27

Family

ID=11446237

Family Applications (1)

Application Number Title Priority Date Filing Date
DK01129714T DK1216750T3 (da) 2000-12-14 2001-12-13 Reaktor til eksoterme eller endoterme heterogene reaktioner

Country Status (9)

Country Link
US (1) US6939520B2 (da)
EP (1) EP1216750B1 (da)
JP (1) JP2002233747A (da)
CN (1) CN1222352C (da)
AT (1) ATE334742T1 (da)
AU (1) AU783696B2 (da)
DE (1) DE60121907T2 (da)
DK (1) DK1216750T3 (da)
IT (1) IT1319549B1 (da)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1060788A1 (en) * 1999-06-15 2000-12-20 Methanol Casale S.A. Isothermal catalytic reactor for exothermic or endothermic heterogeneous reactions
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
EP1563900A1 (en) * 2004-02-12 2005-08-17 Methanol Casale S.A. Pseudo-isothermal chemical reactor for heterogenous chemical reactions
US20080237090A1 (en) * 2007-03-30 2008-10-02 Nicholas Musich Process and system for redcuing the olefin content of a hydrocarbon feed gas and production of a hydrogen-enriched gas therefrom
US8608696B1 (en) 2009-02-24 2013-12-17 North Carolina State University Rapid fluid cooling devices and methods for cooling fluids
JP5389525B2 (ja) * 2009-05-15 2014-01-15 日本パイオニクス株式会社 アンモニア分解筒
CN102937388B (zh) * 2011-08-15 2014-11-19 杨永利 用于钻井平台的余热回收换热器
CN105642197A (zh) * 2014-09-24 2016-06-08 楼韧 一种大型反应器及其装置和工艺
EP3212319A1 (en) 2014-10-30 2017-09-06 SABIC Global Technologies B.V. Reactor comprising radially placed cooling plates and methods of using same
WO2016067244A1 (en) 2014-10-31 2016-05-06 Sabic Global Technologies B.V. Reactors for separating wax products from lightweight gaseous products of a reaction
DE102017203196A1 (de) 2017-02-28 2018-08-30 Robert Bosch Gmbh Rohrwendelwärmetauscher und Speicherbehälter mit einem Rohrwendelwärmetauscher
MY189567A (en) * 2017-04-25 2022-02-17 Bin Halim Rasip Amin Reaction chamber for exothermic and endothermic reactions
KR102707884B1 (ko) * 2018-04-13 2024-09-23 플로우서브 피티이. 엘티디. 유체 냉각기, 열 교환기, 밀봉 조립체 및 유체 냉각기 또는 열 교환기를 포함하는 시스템 및 관련 방법
CN113465426B (zh) * 2019-04-23 2022-04-26 山东大学 一种管径变小旋转对称环路热管
CN112007588A (zh) * 2020-08-31 2020-12-01 江苏永大化工机械有限公司 双酚a反应器
JP2024505162A (ja) * 2021-01-28 2024-02-05 トプソー・アクチエゼルスカベット 螺旋流の触媒熱交換反応器

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB391444A (en) * 1931-10-26 1933-04-26 British Celanese Improvements in or relating to the manufacture of acetaldehyde
US2248993A (en) * 1936-05-08 1941-07-15 Houdry Process Corp Apparatus for controlling chemical reactions
FR841683A (fr) 1937-08-05 1939-05-24 Cie Francaise Procedes Houdry Moyens pour le traitement, en phase vapeur, d'hydrocarbures, et autres applications analogues
DE855258C (de) 1949-05-02 1952-11-10 Ici Ltd Verfahren und Apparatur zur Durchfuehrung chemischer Reaktionen
US3110300A (en) * 1961-04-26 1963-11-12 Universal Oil Prod Co Catalytic gas oxidizing and fluid heating apparatus
CA878266A (en) 1969-04-21 1971-08-17 Brants Henry Heat exchanger
US3663179A (en) * 1970-04-20 1972-05-16 Chemical Construction Corp Apparatus for exothermic catalytic reactions
AT362397B (de) 1976-10-13 1981-05-11 Schober Robert Dipl Ing Dr Tec Vorrichtung zur erhoehung des ammoniakaufbaues bei der katalytischen ammoniaksynthese
DE3007202A1 (de) * 1980-02-26 1981-09-10 Linde Ag, 6200 Wiesbaden Methanol-reaktor
DE3217066A1 (de) * 1982-05-06 1983-11-10 Linde Ag, 6200 Wiesbaden Reaktor zur durchfuehrung katalytischer reaktion
DE3318098A1 (de) * 1983-05-18 1984-11-22 Linde Ag, 6200 Wiesbaden Verfahren und reaktor zur durchfuehrung einer endo- oder exothermen reaktion
JPS60150824A (ja) * 1984-01-18 1985-08-08 Toyo Eng Corp 改良反応器
US5080872A (en) * 1985-09-26 1992-01-14 Amoco Corporation Temperature regulating reactor apparatus and method
DE3708957C2 (de) * 1987-03-19 1996-04-25 Linde Ag Reaktor zur katalytischen Umsetzung von in einem Gasstrom enthaltenem H¶2¶S und SO¶2¶ zu elementarem Schwefel
GB2204055B (en) * 1987-04-29 1992-01-02 Shell Int Research Process for the preparation of hydrocarbons
DE4131446A1 (de) * 1991-09-21 1993-06-09 Basf Ag, 6700 Ludwigshafen, De Reaktor und verfahren zur durchfuehrung heterogenkatalytischer gasphasenreaktionen
AU5563394A (en) * 1992-11-20 1994-06-22 Shell Internationale Research Maatschappij B.V. Reactor and process for highly exothermic or endothermic reactions
EP0776692B1 (en) * 1995-12-01 1999-08-11 Dow Corning Corporation Fluidized-bed reactor

Also Published As

Publication number Publication date
US6939520B2 (en) 2005-09-06
AU783696B2 (en) 2005-11-24
DE60121907T2 (de) 2007-04-19
EP1216750A1 (en) 2002-06-26
ATE334742T1 (de) 2006-08-15
ITMI20002712A1 (it) 2002-06-14
US20020085969A1 (en) 2002-07-04
IT1319549B1 (it) 2003-10-20
JP2002233747A (ja) 2002-08-20
AU9723601A (en) 2002-06-20
EP1216750B1 (en) 2006-08-02
DE60121907D1 (de) 2006-09-14
CN1222352C (zh) 2005-10-12
CN1363416A (zh) 2002-08-14

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