DK1464384T3 - Horisontal kemisk reaktor især for methanolsyntese - Google Patents

Horisontal kemisk reaktor især for methanolsyntese

Info

Publication number
DK1464384T3
DK1464384T3 DK04006216T DK04006216T DK1464384T3 DK 1464384 T3 DK1464384 T3 DK 1464384T3 DK 04006216 T DK04006216 T DK 04006216T DK 04006216 T DK04006216 T DK 04006216T DK 1464384 T3 DK1464384 T3 DK 1464384T3
Authority
DK
Denmark
Prior art keywords
chemical reactor
methanol synthesis
horizontal chemical
reactor especially
horizontal
Prior art date
Application number
DK04006216T
Other languages
Danish (da)
English (en)
Inventor
Giorgio Pagani
Umberto Zardi
Enrico Rizzi
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 DK1464384T3 publication Critical patent/DK1464384T3/da

Links

Classifications

    • 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
    • F28D7/10—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 one within the other, e.g. concentrically
    • F28D7/12—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 one within the other, e.g. concentrically the surrounding tube being closed at one end, e.g. return type
    • 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
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • B01J8/0085—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction promoting uninterrupted fluid flow, e.g. by filtering out particles in front of the catalyst layer
    • 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
    • B01J8/0446—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 flow within the beds being predominantly vertical
    • B01J8/0476—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 flow within the beds being predominantly vertical in two or more otherwise shaped beds
    • B01J8/0484—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 flow within the beds being predominantly vertical in two or more otherwise shaped beds the beds being placed next to each other
    • 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
    • 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
    • F28D7/06—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 having a single U-bend
    • 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
    • B01J2208/00203—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
    • B01J2208/0053—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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00805—Details of the particulate material
    • B01J2208/00814—Details of the particulate material the particulate material being provides in prefilled containers
    • 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
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00884—Means for supporting the bed of particles, e.g. grids, bars, perforated plates
    • 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
    • B01J2219/18—Details relating to the spatial orientation of the reactor
    • B01J2219/182—Details relating to the spatial orientation of the reactor horizontal
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2280/00—Mounting arrangements; Arrangements for facilitating assembling or disassembling of heat exchanger parts
    • F28F2280/02—Removable elements
    • 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)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Fluid Mechanics (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
DK04006216T 2003-03-20 2004-03-16 Horisontal kemisk reaktor især for methanolsyntese DK1464384T3 (da)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN03107444 2003-03-20

Publications (1)

Publication Number Publication Date
DK1464384T3 true DK1464384T3 (da) 2005-12-27

Family

ID=32831754

Family Applications (1)

Application Number Title Priority Date Filing Date
DK04006216T DK1464384T3 (da) 2003-03-20 2004-03-16 Horisontal kemisk reaktor især for methanolsyntese

Country Status (7)

Country Link
US (1) US7279138B2 (fr)
EP (1) EP1464384B1 (fr)
AT (1) ATE302057T1 (fr)
AU (1) AU2004201132A1 (fr)
DE (1) DE602004000055T2 (fr)
DK (1) DK1464384T3 (fr)
RU (1) RU2004108028A (fr)

Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6983852B2 (en) * 2002-10-10 2006-01-10 Specialized Tech Inc. Desanding apparatus and system
EP2292326A1 (fr) 2009-09-02 2011-03-09 Methanol Casale S.A. Réacteur isothermique à calandre vertical
US9464851B2 (en) 2010-12-09 2016-10-11 Provides Metalmeccanica S.R.L. Heat exchanger
US9909405B2 (en) 2012-02-13 2018-03-06 Specialized Desanders Inc. Desanding apparatus and a method of using same
US9327214B2 (en) 2012-02-13 2016-05-03 Specialized Desanders Inc. Desanding apparatus and a method of using same
US9938812B2 (en) 2012-02-13 2018-04-10 Specialized Desanders Inc. Desanding apparatus and a method of using same
CA2836437A1 (fr) 2013-12-16 2015-06-16 Specialized Desanders Inc. Appareil de desablage et son procede d'utilisation
EP2957339A1 (fr) 2014-06-17 2015-12-23 Casale SA Reacteur catalytique horizontal à ecoulement radial
US10076739B1 (en) 2014-07-22 2018-09-18 Precision Combustion, Inc. Chemical reactor for use with overly reactive chemicals
DK3400099T3 (da) 2016-01-07 2020-06-02 Total Raffinage Chimie Fremgangsmåde til methanolsyntese under anvendelse af en indiumoxidbaseret katalysator
EP3400098B1 (fr) 2016-01-07 2019-12-04 Total Raffinage Chimie Procédé de synthèse de méthanol utilisant un catalyseur d'oxyde d'indium supporté et leurs catalyseurs supportés
DE102017203058A1 (de) * 2017-02-24 2018-08-30 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Wärmeübertrager und Reaktor
EP3404005A1 (fr) 2017-05-17 2018-11-21 Total Research & Technology Feluy Procédé d'oligomérisation d'éthylène à partir d'un flux dilué
WO2018210826A1 (fr) 2017-05-17 2018-11-22 Total Research & Technology Feluy Procédé d'aromatisation d'éthylène à partir d'un flux dilué
WO2018210827A1 (fr) 2017-05-17 2018-11-22 Total Research & Technology Feluy Procédé de valorisation de mto-ocp pour maximiser la sélectivité en propylène
EP3593900A1 (fr) 2018-07-10 2020-01-15 Total Raffinage Chimie Composition catalytique à base de cuivre et de fer pour la conversion de gaz de synthèse en alcools supérieurs et procédé utilisant une telle composition catalytique
US11491468B2 (en) 2018-09-06 2022-11-08 Total Se Noble metal promoted supported indium oxide catalyst for the hydrogenation of CO2 to methanol and process using said catalyst
WO2020157057A1 (fr) 2019-02-01 2020-08-06 Total S.A. Composition catalytique à base de cuivre-fer comprenant des zéolites, procédé de production d'une telle composition catalytique et procédé utilisant une telle composition catalytique pour la conversion de gaz de synthèse en alcools supérieurs
US11306049B2 (en) 2019-02-01 2022-04-19 Total Se Process using catalytic composition for the conversion of syngas to higher alcohols
US20230391698A1 (en) 2020-11-17 2023-12-07 Total Energies Onetech Process for methanol synthesis from co2-rich syngas
DE102022131061A1 (de) 2022-11-23 2024-05-23 PACE-Tec GmbH Vorrichtung zum Behandeln, Spülvorrichtung zum Spülen und Trocknungsvorrichtung zum Trocknen von partikelförmigen Feststoffen sowie Verfahren zum Behandeln, Spülen und/oder Trocknen von derartigen Feststoffen

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Publication number Priority date Publication date Assignee Title
US2483178A (en) * 1946-07-29 1949-09-27 Phillips Petroleum Co Catalyst vessel
US2505850A (en) * 1946-08-20 1950-05-02 Phillips Petroleum Co Seal slot for catalyst bed screens in catalyst chambers
GB670299A (en) 1948-11-02 1952-04-16 Metallgesellschaft Ag Process of and apparatus for producing hydrocarbons
AT306745B (de) 1971-05-24 1973-04-25 Chemie Linz Ag Vorrichtung zur Durchführung von Hochdrucksynthesen, beispielsweise der Ammoniaksynthese
RO58713A2 (fr) 1972-04-24 1975-08-26 Inst De Proiectare Tehnologica Appareil multifonctionnel pour matieres pulverulentes
DE2449789B1 (de) 1974-10-19 1976-03-11 Deggendorfer Werft Eisenbau Mehrstufiger Horden-Reaktor
DE3310772A1 (de) 1983-03-24 1984-09-27 Interatom Internationale Atomreaktorbau Gmbh, 5060 Bergisch Gladbach Methanol-synthese-reaktor mit niedrig siedendem kuehlmittel
US4919909A (en) * 1984-12-03 1990-04-24 Societe Chimique De La Grande Paroisse Reactor for catalytic synthesis and process for using the reactor
US4696799A (en) * 1986-07-15 1987-09-29 The M. W. Kellogg Company Ammonia synthesis converter
WO1995024961A1 (fr) * 1994-03-14 1995-09-21 Methanol Casale S.A. Reacteur horizontal destine a la synthese exothermique heterogene, notamment a la synthese du methanol
ZA955492B (en) * 1994-07-18 1996-02-13 Methanol Casale Sa Catalyst-seal support device in particular for exothermic heterogeneous catalytic synthesis reactors
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US6132687A (en) * 1998-05-21 2000-10-17 Kellogg Brown & Root, Inc. Horizontal ammonia converter adapted for high activity catalyst

Also Published As

Publication number Publication date
US7279138B2 (en) 2007-10-09
ATE302057T1 (de) 2005-09-15
RU2004108028A (ru) 2005-09-10
EP1464384A1 (fr) 2004-10-06
US20040184976A1 (en) 2004-09-23
AU2004201132A1 (en) 2004-10-07
DE602004000055T2 (de) 2006-06-29
EP1464384B1 (fr) 2005-08-17
DE602004000055D1 (de) 2005-09-22

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