ATE334742T1 - Reaktor für exotherme oder endotherme heterogene reaktionen - Google Patents

Reaktor für exotherme oder endotherme heterogene reaktionen

Info

Publication number
ATE334742T1
ATE334742T1 AT01129714T AT01129714T ATE334742T1 AT E334742 T1 ATE334742 T1 AT E334742T1 AT 01129714 T AT01129714 T AT 01129714T AT 01129714 T AT01129714 T AT 01129714T AT E334742 T1 ATE334742 T1 AT E334742T1
Authority
AT
Austria
Prior art keywords
exothermic
reactor
endothermic
reactions
heterogeneus
Prior art date
Application number
AT01129714T
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 ATE334742T1 publication Critical patent/ATE334742T1/de

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
    • 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
    • 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)
AT01129714T 2000-12-14 2001-12-13 Reaktor für exotherme oder endotherme heterogene reaktionen ATE334742T1 (de)

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
ATE334742T1 true ATE334742T1 (de) 2006-08-15

Family

ID=11446237

Family Applications (1)

Application Number Title Priority Date Filing Date
AT01129714T ATE334742T1 (de) 2000-12-14 2001-12-13 Reaktor für exotherme oder endotherme heterogene reaktionen

Country Status (9)

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

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1060788A1 (de) * 1999-06-15 2000-12-20 Methanol Casale S.A. Isothermer katalytischer Reaktor für exotherme oder endotherme heterogene Reaktionen
EP1153653A1 (de) * 2000-05-11 2001-11-14 Methanol Casale S.A. Reaktor für exotherme oder endotherme Reaktionen
EP1221339A1 (de) * 2001-01-05 2002-07-10 Methanol Casale S.A. Katalytischer Reaktor mit Wärmetauscher für endothermischer und exothermischer chemischer Reaktionen
EP1563900A1 (de) * 2004-02-12 2005-08-17 Methanol Casale S.A. Chemische Reaktionsvorrichtung unter pseudo-isothermischen Bedingungen für heterogene chemische Reaktionen
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
US10525427B2 (en) 2014-10-30 2020-01-07 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
MX2020010609A (es) * 2018-04-13 2020-10-20 Flowserve Man Co Enfriadores de fluido, intercambiadores de calor, conjuntos y sistemas de sellado incluyendo enfriadores de fluido o intercambiadores de calor y metodos relacionados.
CN113465427B (zh) * 2019-04-23 2022-04-26 山东大学 一种旋转对称环路热管换热装置
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
US20240293787A1 (en) * 2021-01-28 2024-09-05 Topsoe A/S Catalytic heat exchange reactor with helical flow

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
ZA938618B (en) * 1992-11-20 1994-08-04 Shell Res Ltd Reactor and process for highly exothermic of endothermic reactions
DE69603688T2 (de) * 1995-12-01 2000-04-27 Dow Corning Corp., Midland Wirbelschichtbettreaktor

Also Published As

Publication number Publication date
DK1216750T3 (da) 2006-11-27
JP2002233747A (ja) 2002-08-20
US20020085969A1 (en) 2002-07-04
DE60121907D1 (de) 2006-09-14
EP1216750B1 (de) 2006-08-02
CN1363416A (zh) 2002-08-14
IT1319549B1 (it) 2003-10-20
ITMI20002712A1 (it) 2002-06-14
EP1216750A1 (de) 2002-06-26
US6939520B2 (en) 2005-09-06
CN1222352C (zh) 2005-10-12
DE60121907T2 (de) 2007-04-19
AU9723601A (en) 2002-06-20
AU783696B2 (en) 2005-11-24

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