CL2004000986A1 - Reactor quimico para reacciones cataliticas que en la zona de reaccion comprende un lecho catalitico e intercambiadores de calor. - Google Patents

Reactor quimico para reacciones cataliticas que en la zona de reaccion comprende un lecho catalitico e intercambiadores de calor.

Info

Publication number
CL2004000986A1
CL2004000986A1 CL200400986A CL2004000986A CL2004000986A1 CL 2004000986 A1 CL2004000986 A1 CL 2004000986A1 CL 200400986 A CL200400986 A CL 200400986A CL 2004000986 A CL2004000986 A CL 2004000986A CL 2004000986 A1 CL2004000986 A1 CL 2004000986A1
Authority
CL
Chile
Prior art keywords
catalytic
reactions
catalitic
milk
reaction area
Prior art date
Application number
CL200400986A
Other languages
English (en)
Inventor
Ermanno Filippi
Ernico; 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
Publication of CL2004000986A1 publication Critical patent/CL2004000986A1/es

Links

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
    • B01J8/0403—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 fluid flow within the beds being predominantly horizontal
    • B01J8/0423—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 fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds
    • B01J8/0426—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 fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds the beds being superimposed one above the other
    • B01J8/043—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 fluid flow within the beds being predominantly horizontal through two or more otherwise shaped beds the beds being superimposed one above the other in combination with one 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • 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
    • B01J8/0461—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 cylindrical annular shaped beds
    • B01J8/0469—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 cylindrical annular shaped beds the beds being superimposed one above the 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
    • B01J8/0492—Feeding reactive fluids
    • 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
    • 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
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0006—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the plate-like or laminated conduits being enclosed within a pressure vessel
    • 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
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0012—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the apparatus having an annular form
    • F28D9/0018—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the apparatus having an annular form without any annular circulation of the heat exchange media
    • 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
    • B01J2208/0015—Plates; Cylinders
    • 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
    • B01J2208/00743—Feeding or discharging of solids
    • B01J2208/00761—Discharging
    • 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
    • B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/021—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles comprising a plurality of beds with flow of reactants in parallel
    • B01J2208/022—Plate-type reactors filled with granular catalyst
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (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)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

LA INVENCION DIVULGA UN REACTORR QUIMICO PARA REACCIONES CATALITICAS, QUE COMPRENDE UAN CARCAZA SUSTANCIALMENTE CILINDRICA CERRADA EN LOS EXTREMOS OPUESTOS POR RESPECTIVAS CUBIERTAS Y, AL MENOS UNA ZONA DEE REACCION, EN LA CUAL SE SOPORTA UN RESPECTIVO LECHO CATALITICO Y UNA PLURALIDAD DE INTERCAMBIADORES DE CALOR UBICADOS EN DICHA AL MENOS UNA ZONA DE REACCION..
CL200400986A 2003-05-16 2004-05-07 Reactor quimico para reacciones cataliticas que en la zona de reaccion comprende un lecho catalitico e intercambiadores de calor. CL2004000986A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP03011209A EP1477220A1 (en) 2003-05-16 2003-05-16 Chemical reactor

Publications (1)

Publication Number Publication Date
CL2004000986A1 true CL2004000986A1 (es) 2005-03-11

Family

ID=33016914

Family Applications (1)

Application Number Title Priority Date Filing Date
CL200400986A CL2004000986A1 (es) 2003-05-16 2004-05-07 Reactor quimico para reacciones cataliticas que en la zona de reaccion comprende un lecho catalitico e intercambiadores de calor.

Country Status (13)

Country Link
US (2) US7807115B2 (es)
EP (2) EP1477220A1 (es)
CN (1) CN1791459B (es)
AR (1) AR044285A1 (es)
AU (1) AU2004238016B2 (es)
BR (1) BRPI0410368B1 (es)
CA (1) CA2525876C (es)
CL (1) CL2004000986A1 (es)
MX (1) MXPA05012330A (es)
MY (1) MY142840A (es)
RU (1) RU2346734C2 (es)
UA (1) UA80203C2 (es)
WO (1) WO2004101135A1 (es)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1442786A1 (en) * 2003-01-29 2004-08-04 Methanol Casale S.A. Pseudo isothermal radial reactor
DE10361517A1 (de) * 2003-12-23 2005-07-28 Basf Ag Verfahren zur Herstellung von Formaldehyd
MX2007001173A (es) * 2004-01-15 2007-09-25 Methanol Casale Sa Reactor catalitico de lecho fijo.
EP1707259B1 (en) * 2005-04-01 2018-06-06 Casale Sa Process for the heterogeneous synthesis of chemical compounds
EP2292326A1 (en) * 2009-09-02 2011-03-09 Methanol Casale S.A. Vertical isothermal shell-and-tube reactor
US8759600B2 (en) 2010-06-28 2014-06-24 Uop Llc Reduced fluidization of solid particles in radial flow fluid/solid contacting
FR3009862B1 (fr) * 2013-08-26 2015-09-11 Commissariat Energie Atomique Echangeur de chaleur entre deux fluides, utilisation de l'echangeur avec du metal liquide et du gaz, application a un reacteur nucleaire a neutrons rapides refroidi avec du metal liquide
EP3115338A1 (en) * 2015-07-07 2017-01-11 Casale SA A method for revamping an ammonia converter
WO2017165753A1 (en) 2016-03-24 2017-09-28 Tetra, Technologies, Inc. Improving the temperature stability of polyols and sugar alcohols in brines
MX2018011602A (es) 2016-03-24 2019-01-10 Tetra Tech Salmueras monovalentes con alta densidad y baja tct y usus de ellas.
GB2564063B (en) 2016-03-24 2022-04-06 Tetra Tech High density, low TCT divalent brines and uses thereof
WO2018029081A1 (de) * 2016-08-09 2018-02-15 Thyssenkrupp Industrial Solutions Ag Verfahren zur herstellung von ammoniak sowie ammoniaksynthesekonverter
US11021645B2 (en) 2017-10-24 2021-06-01 Tetra Technologies, Inc Stabilization and reduction of TCT of divalent iodide-containing brines
US10851278B2 (en) 2017-10-24 2020-12-01 Tetra Technologies, Inc. Stabilization and reduction of TCT of brines containing monovalent iodides
US11453817B2 (en) 2017-10-24 2022-09-27 Tetra Technologies, Inc. Stabilization of iodide-containing brines and brine mixtures
AR113649A1 (es) 2017-12-20 2020-05-27 Haldor Topsoe As Convertidor de flujo axial enfriado
CN109908843B (zh) * 2019-04-23 2019-12-31 宁波巨化新材料有限公司 丙醛加氢反应器
EP4286043A1 (en) * 2022-05-31 2023-12-06 Walter Tosto S.p.A. Catalytic reactor with heat exchange unit

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3796547A (en) * 1969-11-26 1974-03-12 Texaco Inc Heat exchange apparatus for catalytic system
AT367722B (de) * 1977-01-31 1982-07-26 Robert Dipl Ing Dr Tec Schober Vorrichtung zur durchfuehrung eines verfahrens zur erhoehung des ammoniakaufbaues bei der katalytischen ammoniaksynthese
EP1060788A1 (en) * 1999-06-15 2000-12-20 Methanol Casale S.A. Isothermal catalytic reactor for exothermic or endothermic heterogeneous reactions
JP2001038195A (ja) * 1999-06-28 2001-02-13 Basf Ag 熱交換板を備えた反応器
EP1153653A1 (en) * 2000-05-11 2001-11-14 Methanol Casale S.A. Reactor for exothermic or endothermic heterogeneous reactions
EP1221339A1 (en) * 2001-01-05 2002-07-10 Methanol Casale S.A. Catalytic reactor with heat exchanger for exothermic and endothermic heterogeneous chemical reactions
US20030039601A1 (en) * 2001-08-10 2003-02-27 Halvorson Thomas Gilbert Oxygen ion transport membrane apparatus and process for use in syngas production
EP1306126A1 (en) * 2001-10-19 2003-05-02 Methanol Casale S.A. Heat exchange unit for isothermal chemical reactors

Also Published As

Publication number Publication date
WO2004101135A1 (en) 2004-11-25
US20070274880A1 (en) 2007-11-29
AU2004238016B2 (en) 2009-10-29
RU2346734C2 (ru) 2009-02-20
CA2525876A1 (en) 2004-11-25
US20100129283A1 (en) 2010-05-27
CN1791459A (zh) 2006-06-21
US8071059B2 (en) 2011-12-06
EP1626802A1 (en) 2006-02-22
US7807115B2 (en) 2010-10-05
CN1791459B (zh) 2010-10-06
CA2525876C (en) 2012-01-17
AR044285A1 (es) 2005-09-07
BRPI0410368B1 (pt) 2013-10-01
MXPA05012330A (es) 2006-01-30
UA80203C2 (en) 2007-08-27
BRPI0410368A (pt) 2006-05-30
AU2004238016A1 (en) 2004-11-25
EP1477220A1 (en) 2004-11-17
MY142840A (en) 2011-01-14
RU2005139156A (ru) 2006-06-10

Similar Documents

Publication Publication Date Title
CL2004000986A1 (es) Reactor quimico para reacciones cataliticas que en la zona de reaccion comprende un lecho catalitico e intercambiadores de calor.
AR048395A1 (es) Reactor quimico seudo-isotermico para reacciones quimicas heterogeneas
DE60021747D1 (de) Reaktor, insbesondere für exotherme reaktionen
BRPI0600235A (pt) processo para preparação de catalisador de óxidos de metais misturados
BR0206827B1 (pt) processos integrados para produção de produtos de hidrocarbonetos e energia, e para produção de gás de sìntese e energia.
BR0215086B1 (pt) sistema catalisador de conversço de hidrocarboneto, e, processo para a oligomerizaÇço de olefinas.
BR0110586A (pt) Processo para a oxidação catalìtica de hidrocarbonetos
DK1284813T3 (da) Reaktor til exoterme eller endoterme heterogene reaktioner
DK1347825T3 (da) Katalytisk reaktor med varmeveksler til endotermiske og exotermiske kemiske reaktioner
CR6919S (es) Contenedor multicompartimiento de reactivos para inhibir la reutilizacion de estos o de objetos similares
AR062692A1 (es) Reactor isotermico
BR0101330B1 (pt) processo para a combustão, em um forno, de produtos de reação formados em uma reação quìmica.
BR0111614B1 (pt) recipiente que pode ser re-fechado, particularmente para produtos fluidos.
BRPI0504146A (pt) processo catalìtico seletivo regenerativo
DE60224586D1 (de) Reaktor für die katalytische oxidation mit verbessertem wärmeaustauschsystem
BR0207668B1 (pt) método para realização de reações quìmicas em falsas condições isotérmicas.
BRPI0408539B8 (pt) processo para a oxidação parcial de acroleína para ácido acrílico em fase gasosa
EA200801451A1 (ru) Способ получения продукта в конденсированной фазе из одного или нескольких газофазных реагентов
IT1319549B1 (it) Reattore per l'effettuazione di reazioni eterogenee esotermiche oendotermiche
BR0104284B1 (pt) processo para proporcionar um reagente a uma zona de reação.
ES2553608T3 (es) Proceso para la síntesis de 4,4'-diamino-difenil-sulfona
AR042959A1 (es) Reactor radial seudo -isotermico
BRPI0620356A2 (pt) processo para controlar a localização de uma reação exotérmica entre dois ou mais reagentes, e, reator regenerativo de fluxo inverso
ATE278460T1 (de) Chemischer reaktor mit wärmetauscher
CL2004000417A1 (es) Metodo para la preparacion de una espuma poliisocianurato, que comprende la mezcla de al menos un isocianato organico y al menos un poliol, en presencia de al menos un hidrocarburo alifatico y al menos un catalizador de trimerizacion; y dicha espuma