DK1773483T3 - Fremgangsmåde til gennemförsel af heterogent katalyserede exoterme - Google Patents

Fremgangsmåde til gennemförsel af heterogent katalyserede exoterme

Info

Publication number
DK1773483T3
DK1773483T3 DK05753654T DK05753654T DK1773483T3 DK 1773483 T3 DK1773483 T3 DK 1773483T3 DK 05753654 T DK05753654 T DK 05753654T DK 05753654 T DK05753654 T DK 05753654T DK 1773483 T3 DK1773483 T3 DK 1773483T3
Authority
DK
Denmark
Prior art keywords
product
gas
synthesis
partial flow
warm portion
Prior art date
Application number
DK05753654T
Other languages
English (en)
Inventor
Anton Josef Hipp
Original Assignee
Ammonia 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 Ammonia Casale Sa filed Critical Ammonia Casale Sa
Application granted granted Critical
Publication of DK1773483T3 publication Critical patent/DK1773483T3/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
    • B01J8/04—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
    • B01J8/0496—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
    • B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
    • B01J8/067—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
    • C01C1/0458—Separation of NH3
    • C01C1/047—Separation of NH3 by condensation
    • 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
    • C07C29/1516—Multisteps
    • 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
    • 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
    • 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
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00194—Tubes
    • 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
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00256—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles in a heat exchanger for the heat exchange medium separate from 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
    • 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
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
    • 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
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
    • 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
    • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00004—Scale aspects
    • B01J2219/00006—Large-scale industrial plants
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00018—Construction aspects
    • B01J2219/00024—Revamping, retrofitting or modernisation of existing plants
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00027—Process aspects
    • B01J2219/0004—Processes in series
    • 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
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • 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)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
DK05753654T 2004-05-28 2005-05-28 Fremgangsmåde til gennemförsel af heterogent katalyserede exoterme DK1773483T3 (da)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102004028200A DE102004028200B3 (de) 2004-05-28 2004-05-28 Verfahren zur Durchführung heterogen katalytischer exothermer Gasphasenreaktionen für die Methanolsynthese
PCT/EP2005/005775 WO2005115607A1 (de) 2004-05-28 2005-05-28 Verfahren zur durchführung heterogen katalytischer exothermer gasphasenreaktionen

Publications (1)

Publication Number Publication Date
DK1773483T3 true DK1773483T3 (da) 2008-06-09

Family

ID=34971871

Family Applications (1)

Application Number Title Priority Date Filing Date
DK05753654T DK1773483T3 (da) 2004-05-28 2005-05-28 Fremgangsmåde til gennemförsel af heterogent katalyserede exoterme

Country Status (12)

Country Link
US (1) US7683099B2 (da)
EP (1) EP1773483B1 (da)
CN (1) CN100518920C (da)
AT (1) ATE385438T1 (da)
AU (1) AU2005247609A1 (da)
BR (1) BRPI0511587B1 (da)
CA (1) CA2568297A1 (da)
DE (2) DE102004028200B3 (da)
DK (1) DK1773483T3 (da)
MX (1) MXPA06013857A (da)
RU (1) RU2381058C2 (da)
WO (1) WO2005115607A1 (da)

Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0710022D0 (en) * 2007-05-25 2007-07-04 Johnson Matthey Plc Methonal process
EP2011564A1 (en) * 2007-07-06 2009-01-07 Methanol Casale S.A. Process and plant for synthesis of methanol with H2 recovery from purge of synthesis loop
DE102008049622B4 (de) 2008-09-30 2012-10-31 Lurgi Gmbh Verfahren und Anlage zur Herstellung von Methanol
WO2015193440A1 (en) * 2014-06-20 2015-12-23 Haldor Topsøe A/S Serial methanol reactors
AU2015336514B2 (en) * 2014-10-20 2020-02-20 Mitsubishi Gas Chemical Company, Inc. Method for producing methanol and apparatus for producing methanol
EP3218448A1 (en) * 2014-11-14 2017-09-20 SABIC Global Technologies B.V. Multi stage fischer-tropsch reactor and methods of producing hydrocarbons
DE102015208128A1 (de) * 2015-04-30 2016-11-03 Thyssenkrupp Ag Asymmetrische Kreislaufkaskaden in der Gaskatalyse
DE102015210801A1 (de) 2015-06-12 2016-12-15 Thyssenkrupp Ag Mehrdruckverfahren zur Herstellung von Ammoniak ohne Anreicherung von Inertgas
CN107922297A (zh) 2015-08-12 2018-04-17 托普索公司 用于从低质量合成气生产甲醇的新方法
TW201736264A (zh) * 2015-12-16 2017-10-16 托普索公司 在多反應系統中自非惰性合成氣體製備氨之方法
DK3441381T3 (da) * 2016-04-07 2020-05-25 Mitsubishi Gas Chemical Co Fremgangsmåde til fremstilling af methanol og indretning til fremstilling af methanol
DE102016107124A1 (de) 2016-04-18 2017-10-19 Thyssenkrupp Ag NH3 Synthesekonfiguration für Großanlagen
WO2017220570A1 (en) * 2016-06-20 2017-12-28 Haldor Topsøe A/S Interstage removal of ammonia
CN107974318B (zh) * 2016-10-25 2020-04-03 中国石化工程建设有限公司 复合塔式甲烷化装置及甲烷化工艺
EP3401300B1 (de) * 2017-05-12 2021-06-23 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Verfahren zur herstellung von methanol
EP3401299B1 (de) * 2017-05-12 2021-11-03 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Reaktor zum durchführen exothermer gleichgewichtsreaktionen
CN109205558B (zh) * 2017-07-06 2020-08-04 中国石化工程建设有限公司 一种用于煤制天然气的变换装置及变换方法
KR20240096891A (ko) 2018-06-12 2024-06-26 토프쉐 에이/에스 메탄올 제조를 위한 과정 및 플랜트
DE102018129639A1 (de) * 2018-11-23 2020-05-28 Thyssenkrupp Ag Vorrichtung und Verfahren zur katalytischen Herstellung von Ammoniak aus Synthesegas
DE102019201172A1 (de) * 2019-01-30 2020-07-30 Siemens Aktiengesellschaft Reaktorkaskade und Verfahren zum Betreiben einer Reaktorkaskade
CN118145674B (zh) * 2024-03-28 2026-04-21 南京聚拓化工科技有限公司 一种双极单循环氨合成方法

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GB1105614A (en) 1964-04-22 1968-03-06 Ici Ltd Catalytic converter
DE3266054D1 (en) * 1981-11-19 1985-10-10 Ici Plc Synthesis process and reactor
CH672078A5 (da) * 1986-06-02 1989-10-31 Ammonia Casale Sa
US4867959A (en) * 1986-11-20 1989-09-19 Santa Fe Braun, Inc. Process for synthesizing ammonia
DE3643858A1 (de) 1986-12-22 1988-06-30 Uhde Gmbh Verfahren und vorrichtung zur temperaturregelung von katalysatorbetten in ammoniaksyntheseanlagen
DE8717724U1 (de) 1987-03-18 1989-10-05 Uhde Gmbh, 4600 Dortmund Zweistufiger Ammoniakkonverter mit wenigstens einem Katalysatorbett mit in dessen Inneren angeordneten Wärmetauscher
EP0359952A3 (en) 1988-08-05 1990-07-18 Ammonia Casale S.A. System for the improvement of reactors for the synthesis of methanol and reactors obtained therefrom
GB9023465D0 (en) * 1990-10-29 1990-12-12 Shell Int Research Process for the production of methanol
DE4100632C1 (da) * 1991-01-11 1992-04-23 Uhde Gmbh, 4600 Dortmund, De
ATE156778T1 (de) * 1991-07-09 1997-08-15 Ici Plc Synthesegaserzeugung
DE4416425A1 (de) * 1994-05-10 1995-11-16 Metallgesellschaft Ag Verfahren zur Erzeugung von Methanol
DE19605572A1 (de) 1996-02-15 1997-08-21 Metallgesellschaft Ag Verfahren zum Erzeugen von Methanol
DE19644216A1 (de) * 1996-10-24 1998-04-30 Metallgesellschaft Ag Verfahren zum Erzeugen von Methanol aus Erdgas
DK173023B1 (da) * 1997-04-21 1999-11-15 Topsoe Haldor As Fremgangsmåde og reaktor til fremstilling af ammoniak
GB9904649D0 (en) 1998-05-20 1999-04-21 Ici Plc Methanol synthesis
WO2000026139A1 (en) * 1998-10-30 2000-05-11 Haldor Topsøe A/S Process and converter for the preparation of ammonia
DE10057863C2 (de) 2000-11-21 2002-10-24 Uhde Gmbh Mehrdruckverfahren zur Herstellung von Ammoniak
RU2198838C1 (ru) * 2002-01-29 2003-02-20 Писаренко Елена Витальевна Способ получения метанола

Also Published As

Publication number Publication date
DE502005002766D1 (de) 2008-03-20
US7683099B2 (en) 2010-03-23
RU2381058C2 (ru) 2010-02-10
MXPA06013857A (es) 2007-04-25
US20070293590A1 (en) 2007-12-20
BRPI0511587A (pt) 2008-01-02
EP1773483B1 (de) 2008-02-06
CN100518920C (zh) 2009-07-29
DE102004028200B3 (de) 2005-12-15
RU2006146212A (ru) 2008-07-20
ATE385438T1 (de) 2008-02-15
EP1773483A1 (de) 2007-04-18
CA2568297A1 (en) 2005-12-08
AU2005247609A1 (en) 2005-12-08
BRPI0511587B1 (pt) 2015-09-08
CN1972743A (zh) 2007-05-30
WO2005115607A1 (de) 2005-12-08

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