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AR052003A1 - Reactor quimico - Google Patents

Reactor quimico

Info

Publication number
AR052003A1
AR052003A1 ARP050103128A ARP050103128A AR052003A1 AR 052003 A1 AR052003 A1 AR 052003A1 AR P050103128 A ARP050103128 A AR P050103128A AR P050103128 A ARP050103128 A AR P050103128A AR 052003 A1 AR052003 A1 AR 052003A1
Authority
AR
Argentina
Prior art keywords
bed
supported
catalytic
housing
catalytic bed
Prior art date
Application number
ARP050103128A
Other languages
English (en)
Inventor
Ermanno Filippi
Enrico 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 AR052003A1 publication Critical patent/AR052003A1/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
    • B01J8/0407—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 cylindrical annular shaped beds
    • B01J8/0415—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 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
    • B01J8/0496—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
    • 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
    • F28D7/16—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 in parallel spaced relation
    • 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
    • B01J2208/00106—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
    • B01J2208/00212—Plates; Jackets; Cylinders
    • B01J2208/00221—Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
    • 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
    • B01J2208/00548—Flow
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Fluid Mechanics (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Un reactor químico radial (10, 110, 210, 310,) para reacciones catalíticas que comprende: una carcasa 812) sustancialmente cilíndrica, un primer lecho catalítico 8189 que tiene una seccion transversal con forma sustancialmente de anillo, coaxialmente soportada en dicho carcasa (12) y que tiene un lado de entrada (20) de gases reactivos y un lado de salida (21) de mezcla de reaccion; una pluralidad de intercambiadores de calor (22) soportados y distribuidos en una porcion respectiva con forma sustancialmente de anillo de dicho primer lecho catalítico (18); al menos un segundo lecho catalítico (28) con una seccion transversal con forma sustancialmente de anillo, soportado en dicha carcasa (12) coaxialmente a dicho primer lecho (18) y a una distancia predeterminada de dicho primer lecho, dicho segundo lecho catalítico (28) teniendo un lado de entrada (30) de mezcla de reaccion y un lado de salida (31) de productos de reaccion gaseosos; una pluralidad de intercambiadores de calor (32) soportados y distribuidos en una porcion respectiva con forma sustancialmente de anillo he dicho segundo lecho catalítico (28).
ARP050103128A 2004-07-29 2005-07-27 Reactor quimico AR052003A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP04017905A EP1623755A1 (en) 2004-07-29 2004-07-29 Fixed-bed catalytic reactor

Publications (1)

Publication Number Publication Date
AR052003A1 true AR052003A1 (es) 2007-02-28

Family

ID=34925970

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP050103128A AR052003A1 (es) 2004-07-29 2005-07-27 Reactor quimico

Country Status (15)

Country Link
US (1) US7780925B2 (es)
EP (2) EP1623755A1 (es)
CN (1) CN100563808C (es)
AR (1) AR052003A1 (es)
AT (1) ATE448015T1 (es)
AU (1) AU2005266550B2 (es)
BR (1) BRPI0513803A (es)
CA (1) CA2575346C (es)
DE (1) DE602005017630D1 (es)
DK (1) DK1768773T3 (es)
EG (1) EG25079A (es)
MX (1) MX2007001173A (es)
RU (1) RU2361657C2 (es)
UA (1) UA87511C2 (es)
WO (1) WO2006010565A1 (es)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101143729B (zh) * 2007-09-05 2010-04-14 湖南安淳高新技术有限公司 多床层轴径向合成塔
US7867460B2 (en) * 2007-11-26 2011-01-11 Kellogg Brown & Root Llc Efficiency of ammonia processes
GB0918246D0 (en) * 2009-10-19 2009-12-02 Davy Process Techn Ltd Apparatus
US9126168B2 (en) 2010-12-15 2015-09-08 Exxonmobil Research And Engineering Company Catalyst bed platform with center support pipe
GB201107073D0 (en) * 2011-04-27 2011-06-08 Davy Process Techn Ltd Process
GB201107070D0 (en) * 2011-04-27 2011-06-08 Davy Process Techn Ltd FT process using can reactor
GB201107072D0 (en) 2011-04-27 2011-06-08 Davy Process Techn Ltd Process
CN104069777B (zh) * 2014-07-14 2015-12-16 南京博扬化工科技有限公司 一种等温绝热径向复合式反应器
CN105771810A (zh) * 2014-12-25 2016-07-20 中国石油天然气股份有限公司 一种用于苯与甲醇烷基化的反应器及进料方式
PT3374074T (pt) * 2015-11-13 2021-03-03 Johnson Matthey Plc Aparelho e processo para a produção de formaldeído
WO2018029081A1 (de) 2016-08-09 2018-02-15 Thyssenkrupp Industrial Solutions Ag Verfahren zur herstellung von ammoniak sowie ammoniaksynthesekonverter
DE102016114710A1 (de) * 2016-08-09 2018-02-15 Thyssenkrupp Ag Plattenwärmetauscher, Synthesevorrichtung und Verfahren zur Herstellung eines Produkts
DE102016221967A1 (de) 2016-11-09 2018-05-09 Thyssenkrupp Ag Verfahren zur Herstellung von Ammoniak sowie Ammoniaksynthesekonverter
EP3713663B1 (en) * 2017-11-21 2022-08-24 Casale SA Chemical reactor with adiabatic catalytic beds and axial flow
AR113649A1 (es) 2017-12-20 2020-05-27 Haldor Topsoe As Convertidor de flujo axial enfriado
DE102018007737A1 (de) 2018-10-01 2020-04-02 Hitachi Zosen Inova Etogas Gmbh Festbettanordnung
CN113244801A (zh) * 2021-05-19 2021-08-13 南京国昌化工科技有限公司 一种多流体混合设备

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH666198A5 (it) * 1985-09-13 1988-07-15 Ammonia Casale Sa Reattore per sintesi catalitiche dell'ammoniaca, metanolo ed alcoli superiori.
FR2622475B1 (fr) * 1987-10-28 1990-01-26 Azote & Prod Chim Procede de synthese catalytique heterogene, en phase gazeuse sous haute pression et reacteur de mise en oeuvre
DK167242B1 (da) * 1989-02-16 1993-09-27 Topsoe Haldor As Apparat og fremgangsmaade til exoterme reaktioner
RU2156160C2 (ru) * 1995-04-11 2000-09-20 Флориалл Холдингс Лимитед Способ и реактор для гетерогенного экзотермического синтеза формальдегида
RU2136359C1 (ru) * 1997-07-14 1999-09-10 Институт катализа им.Г.К.Борескова СО РАН Реактор для проведения гетерогенного экзотермического синтеза
DE69901799T2 (de) * 1998-03-05 2002-10-10 Haldor Topsoe A/S, Lyngby Verfahren und vorrichtung zur herstellung von ammonia
JP2001038195A (ja) * 1999-06-28 2001-02-13 Basf Ag 熱交換板を備えた反応器
EP1236505A1 (en) * 2001-02-27 2002-09-04 Methanol Casale S.A. Method for carrying out chemical reactions in pseudo-isothermal conditions
EP1310475A1 (en) * 2001-11-11 2003-05-14 Methanol Casale S.A. Process and plant for the heterogeneous synthesis of chemical compounds
EP1442786A1 (en) * 2003-01-29 2004-08-04 Methanol Casale S.A. Pseudo isothermal radial reactor
EP1477220A1 (en) * 2003-05-16 2004-11-17 Methanol Casale S.A. Chemical reactor
DE10361517A1 (de) * 2003-12-23 2005-07-28 Basf Ag Verfahren zur Herstellung von Formaldehyd
US7740687B2 (en) * 2007-02-13 2010-06-22 Iacx Energy Llc Pressure swing adsorption method and system for separating gas components

Also Published As

Publication number Publication date
AU2005266550B2 (en) 2010-11-11
EP1768773A1 (en) 2007-04-04
RU2007107174A (ru) 2008-09-10
UA87511C2 (ru) 2009-07-27
RU2361657C2 (ru) 2009-07-20
BRPI0513803A (pt) 2008-05-13
EP1623755A1 (en) 2006-02-08
MX2007001173A (es) 2007-09-25
US20080008633A1 (en) 2008-01-10
CA2575346C (en) 2012-11-13
ATE448015T1 (de) 2009-11-15
CN100563808C (zh) 2009-12-02
US7780925B2 (en) 2010-08-24
CN101001691A (zh) 2007-07-18
CA2575346A1 (en) 2006-02-02
DE602005017630D1 (de) 2009-12-24
DK1768773T3 (da) 2010-03-08
WO2006010565A1 (en) 2006-02-02
EP1768773B1 (en) 2009-11-11
AU2005266550A1 (en) 2006-02-02
EG25079A (en) 2011-07-31

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