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
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)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (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 (da)
EP (1) EP1464384B1 (da)
AT (1) ATE302057T1 (da)
AU (1) AU2004201132A1 (da)
DE (1) DE602004000055T2 (da)
DK (1) DK1464384T3 (da)
RU (1) RU2004108028A (da)

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 (en) * 2009-09-02 2011-03-09 Methanol Casale S.A. Vertical isothermal shell-and-tube reactor
EP2649396B1 (en) 2010-12-09 2017-02-22 Provides Metalmeccanica S.r.l. Heat exchanger
US9938812B2 (en) 2012-02-13 2018-04-10 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
US9909405B2 (en) 2012-02-13 2018-03-06 Specialized Desanders Inc. Desanding apparatus and a method of using same
CA2836437A1 (en) 2013-12-16 2015-06-16 Specialized Desanders Inc. An desanding apparatus and a method of using the same
EP2957339A1 (en) 2014-06-17 2015-12-23 Casale SA Radial flow horizontal catalytic reactor
US10076739B1 (en) 2014-07-22 2018-09-18 Precision Combustion, Inc. Chemical reactor for use with overly reactive chemicals
WO2017118573A1 (en) 2016-01-07 2017-07-13 Total Research & Technology Feluy Process for methanol synthesis using an indium oxide based catalyst
EP3400098B1 (en) 2016-01-07 2019-12-04 Total Raffinage Chimie Supported indium oxide catalyst and process for methanol synthesis using the same
DE102017203058A1 (de) * 2017-02-24 2018-08-30 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Wärmeübertrager und Reaktor
WO2018210827A1 (en) 2017-05-17 2018-11-22 Total Research & Technology Feluy Mto-ocp upgrading process to maximize the selectivity to propylene
WO2018210826A1 (en) 2017-05-17 2018-11-22 Total Research & Technology Feluy Process for ethylene aromatisation from diluted stream
EP3404005A1 (en) 2017-05-17 2018-11-21 Total Research & Technology Feluy Process for ethylene oligomerisation from diluted stream
EP3593900A1 (en) 2018-07-10 2020-01-15 Total Raffinage Chimie Copper-iron-based catalytic composition for the conversion of syngas to higher alcohols and process using such catalyst composition
WO2020049081A1 (en) 2018-09-06 2020-03-12 Total S.A. Noble metal promoted supported indium oxide catalyst for the hydrogenation of co2 to methanol and process using said catalyst
EP3917669B1 (en) 2019-02-01 2023-08-16 TotalEnergies OneTech Copper-iron-based catalytic composition comprising zeolites, method for producing such catalytic composition and process using such catalytic composition for the conversion of syngas to higher alcohols
WO2020157049A1 (en) 2019-02-01 2020-08-06 Total S.A. Process using catalytic composition for the conversion of syngas to higher alcohols
AU2021382100A1 (en) 2020-11-17 2023-06-01 Totalenergies 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

Family Cites Families (13)

* Cited by examiner, † Cited by third party
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 (ro) 1972-04-24 1975-08-26 Inst De Proiectare Tehnologica Aparat multifunctional pentru materiale pulverulente
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 (en) * 1994-03-14 1995-09-21 Methanol Casale S.A. Horizontal reactor for heterogeneous exothermic synthesis, in particular for methanol synthesis
ZA955492B (en) * 1994-07-18 1996-02-13 Methanol Casale Sa Catalyst-seal support device in particular for exothermic heterogeneous catalytic synthesis reactors
GB2329597B (en) * 1995-02-15 1999-08-11 Air Liquide Arrangement of a retaining grille of an active material in a vessel,and a vessel so equipped
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
DE602004000055T2 (de) 2006-06-29
ATE302057T1 (de) 2005-09-15
AU2004201132A1 (en) 2004-10-07
DE602004000055D1 (de) 2005-09-22
EP1464384A1 (en) 2004-10-06
US7279138B2 (en) 2007-10-09
RU2004108028A (ru) 2005-09-10
US20040184976A1 (en) 2004-09-23
EP1464384B1 (en) 2005-08-17

Similar Documents

Publication Publication Date Title
DK1464384T3 (da) Horisontal kemisk reaktor især for methanolsyntese
NO20004054D0 (no) Gassomdannelse som anvender syntesegass fremstilt av hydrogen for katalysatorregenerering og hydrokarbonomdannelse
FR2804689B1 (fr) Procede de synthese d'hydrocarbures en presence d'un catalyseur comprenant un metal du groupe viii supporte sur silice-alumine
DK1157968T3 (da) Fremgangsmåde til autoterm, katalytisk dampreformering af carbonhydrider
NO20020587L (no) Kjemisk reaktor og fremgangsmåte for katalytiske reaksjoner med reaktanter i gassfase
NO20030027D0 (no) Elektrokjemisk fremgangsmåte for å måle kjemisk reaksjonsrate
ATE302055T1 (de) Wärmetauscher für isothermische chemische reaktor
MY123600A (en) Highly active fischer-tropsch synthesis using doped, thermally stable catalyst support
AU2003299785A8 (en) Catalyst formulations containing group 11 metals for hydrogen generation
ZA99251B (en) Gas conversion using hydrogen produced from syngas for removing sulfur from gas well hydrocarbon liquids.
HUP0200907A2 (en) Biomass gasifying furnace and system for methanol synthesis using gas produced by gasifying biomass
IT1319258B1 (it) Catalizzatore per la idrodeclorurazione del tetracloruro di carbonio acloroformio.
DE59905380D1 (de) Reaktor für eine katalytische chemische Reaktion, insbesondere Methanolreformierungsreaktor
DE69905406T2 (de) Katalysatorträger
ATE496688T1 (de) Werkzeug zum laden von reaktorrohren
DK1216750T3 (da) Reaktor til eksoterme eller endoterme heterogene reaktioner
NO20024608L (no) Fremgangsmåte for fremstilling av hydrokarboner fra syntesegass i en trefasereaktor
AU2003277384A8 (en) Autothermal reforming catalyst
DK163578C (da) Fremgangsmaade til fremstilling af metanol
ZA200100284B (en) Process and reactor for the preparation of hydrogen and carbon monoxide rich gas.
NO20035720D0 (no) Fremgangsmåte for å oppnå syntesegass ved partiell katalytisk oksydasjon
BR0312087B1 (pt) método e dispositivo para produção de amÈnia a partr de gás de sìntese.
FR2892323B1 (fr) Catalyseur pour la production d'un gaz riche en hydrogene.
NO20030238D0 (no) Karbonmonoksidholdige polymerer avledet fra syntesegass
DE60025787D1 (de) Modularer chemischer Reaktor