ATE302057T1 - Horizontaler reaktor, insbesondere für die herstellung von methanol - Google Patents

Horizontaler reaktor, insbesondere für die herstellung von methanol

Info

Publication number
ATE302057T1
ATE302057T1 AT04006216T AT04006216T ATE302057T1 AT E302057 T1 ATE302057 T1 AT E302057T1 AT 04006216 T AT04006216 T AT 04006216T AT 04006216 T AT04006216 T AT 04006216T AT E302057 T1 ATE302057 T1 AT E302057T1
Authority
AT
Austria
Prior art keywords
methanol
production
horizontal reactor
catalytic bed
reactor
Prior art date
Application number
AT04006216T
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 ATE302057T1 publication Critical patent/ATE302057T1/de

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)
AT04006216T 2003-03-20 2004-03-16 Horizontaler reaktor, insbesondere für die herstellung von methanol ATE302057T1 (de)

Applications Claiming Priority (1)

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

Publications (1)

Publication Number Publication Date
ATE302057T1 true ATE302057T1 (de) 2005-09-15

Family

ID=32831754

Family Applications (1)

Application Number Title Priority Date Filing Date
AT04006216T ATE302057T1 (de) 2003-03-20 2004-03-16 Horizontaler reaktor, insbesondere für die herstellung von methanol

Country Status (7)

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

Families Citing this family (22)

* 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 (de) 2009-09-02 2011-03-09 Methanol Casale S.A. Vertikaler isothermer Rohrbündelreaktor
WO2012077143A1 (en) 2010-12-09 2012-06-14 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
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
CA2836437A1 (en) 2013-12-16 2015-06-16 Specialized Desanders Inc. An desanding apparatus and a method of using the same
EP2957339A1 (de) 2014-06-17 2015-12-23 Casale SA Horizontaler katalytischer Reaktor mit radialer Durchströmung
US10076739B1 (en) 2014-07-22 2018-09-18 Precision Combustion, Inc. Chemical reactor for use with overly reactive chemicals
EP3400099B1 (de) 2016-01-07 2020-03-18 Total Raffinage Chimie Verfahren zur synthese von methanol unter verwendung eines indiumoxidbasierten katalysators und katalysator dafür
EP3400098B1 (de) 2016-01-07 2019-12-04 Total Raffinage Chimie Verfahren zur methanolsynthese unter verwendung von geträgertem indiumoxidkatalysator und geträgerter katalysator dafür
DE102017203058A1 (de) * 2017-02-24 2018-08-30 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Wärmeübertrager und Reaktor
WO2018210826A1 (en) 2017-05-17 2018-11-22 Total Research & Technology Feluy Process for ethylene aromatisation from diluted stream
WO2018210827A1 (en) 2017-05-17 2018-11-22 Total Research & Technology Feluy Mto-ocp upgrading process to maximize the selectivity to propylene
EP3404005A1 (de) 2017-05-17 2018-11-21 Total Research & Technology Feluy Verfahren zur oligomerisierung von ethylen aus einem verdünnten strom
EP3593900A1 (de) 2018-07-10 2020-01-15 Total Raffinage Chimie Katalytische zusammensetzung auf kupfer-eisenbasis zur umwandlung von syngas in höhere alkohole und verfahren zur verwendung dieser zusammensetzung
EP3846936A1 (de) 2018-09-06 2021-07-14 Total Se Edelmetallgestützter geträgerter indiumoxid-katalysator zur hydrierung von co2 zu methanol und verfahren mit diesem katalysator
EP3917669B1 (de) 2019-02-01 2023-08-16 TotalEnergies OneTech Kupfer-eisen-basierte katalytische zusammensetzung mit zeolithen, verfahren zur herstellung solch einer katalysatorzusammensetzung und verfahren zur verwendung solch einer katalysatorzusammensetzung zur umwandlung von syngas in höhere alkohole
WO2020157049A1 (en) 2019-02-01 2020-08-06 Total S.A. Process using catalytic composition for the conversion of syngas to higher alcohols
EP4247776B1 (de) 2020-11-17 2025-01-01 Totalenergies Onetech Verfahren zur methanolsynthese aus co2-reichem synthesegas
DE102022131061B4 (de) * 2022-11-23 2025-02-06 PACE-Tec GmbH Vorrichtung zum Behandeln, Spülvorrichtung zum Spülen, Trocknungsvorrichtung zum Trocknen und System zum Behandeln von partikelförmigen Feststoffen sowie Verfahren zum Behandeln, Spülen und/oder Trocknen von derartigen Feststoffen
WO2026032912A1 (en) 2024-08-05 2026-02-12 Totalenergies Onetech Plasma-assisted methanol synthesis process

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
AU2004201132A1 (en) 2004-10-07
DE602004000055T2 (de) 2006-06-29
EP1464384A1 (de) 2004-10-06
US7279138B2 (en) 2007-10-09
DK1464384T3 (da) 2005-12-27
US20040184976A1 (en) 2004-09-23
DE602004000055D1 (de) 2005-09-22
EP1464384B1 (de) 2005-08-17
RU2004108028A (ru) 2005-09-10

Similar Documents

Publication Publication Date Title
DE602004000055D1 (de) Horizontaler Reaktor, insbesondere für die Herstellung von Methanol
DE69810842D1 (de) Herstellung von Azithromycin
DE60216572D1 (de) Katalysator für die wasserstofferzeugung und katalysator für die abgasreinigung
DK1157968T3 (da) Fremgangsmåde til autoterm, katalytisk dampreformering af carbonhydrider
NO20020587D0 (no) Kjemisk reaktor og fremgangsmåte for katalytiske reaksjoner med reaktanter i gassfase
IT1318550B1 (it) Catalizzatore e processo per la sintesi diretta di acqua ossigenata.
JP2004504479A5 (de)
CO5680472A2 (es) Hidrogeno para reformado con vapor de gas natural para dar gas de sintesis
FR2804689B1 (fr) Procede de synthese d'hydrocarbures en presence d'un catalyseur comprenant un metal du groupe viii supporte sur silice-alumine
EP0989621A3 (de) Isothermer mehrstufiger Reaktor für die präferentielle Oxidation von Kohlenmonoxid
ATE294786T1 (de) Katalysator für epoxidierungen und verfahren zu dessen herstellung
DE60111690D1 (de) Katalysator für die Dampfreformierung von Methanol und Methode zur Herstellung von Wasserstoff mit diesem Katalysator
DE60100918D1 (de) Verfahren zur Herstellung eines wasserstoffreichen Gases
MXPA04003704A (es) Proceso y aparato electrolitico.
DE60225100D1 (de) Wasserstoffdurchlässige Membran, Verfahren zu deren Herstellung und Wasserstoff-Gasseparator unter Verwendung derselben
EP1445235A3 (de) Verfahren zur Behandlung von Synthesegas
FR2846965B1 (fr) Procede de fabrication de 1,2-epoxy-3-chloropropane
DE60225712D1 (de) Suspensionsverfahren für die kohlenwasserstoffsynthese mit externer hydroisomerierung in einem abstrom-schlaufenreaktor
DE60121907D1 (de) Reaktor für exotherme oder endotherme heterogene Reaktionen
NO20024989L (no) Fremgangsmåte til å fremstille kodede partikler
NO20053244D0 (no) Katalytisk reaktor og fremgangsmate.
CA2271367A1 (en) Horizontal ammonia converter adapted for high activity catalyst
ATE454358T1 (de) Absorptionsmittel enthaltend aluminiumoxidpellets und verfahren zu ihrer herstellung
DE60117227D1 (de) Herstellungsverfahren eines Katalysators für die Wasserdampfreformierung von Methanol
DE60106212D1 (de) Chemischer reaktor mit wärmetauscher

Legal Events

Date Code Title Description
RER Ceased as to paragraph 5 lit. 3 law introducing patent treaties