WO2002051533A1 - Catalytic cartridge and application to installations producing catalysed chemical reactions - Google Patents

Catalytic cartridge and application to installations producing catalysed chemical reactions Download PDF

Info

Publication number
WO2002051533A1
WO2002051533A1 PCT/FR2001/004095 FR0104095W WO02051533A1 WO 2002051533 A1 WO2002051533 A1 WO 2002051533A1 FR 0104095 W FR0104095 W FR 0104095W WO 02051533 A1 WO02051533 A1 WO 02051533A1
Authority
WO
WIPO (PCT)
Prior art keywords
cartridge
texture
catalytic
reactor vessel
reaction medium
Prior art date
Application number
PCT/FR2001/004095
Other languages
French (fr)
Inventor
Nathalie Nicolaus
Original Assignee
Messier-Bugatti
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 Messier-Bugatti filed Critical Messier-Bugatti
Publication of WO2002051533A1 publication Critical patent/WO2002051533A1/en

Links

Classifications

    • B01J35/58
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/2475Membrane reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/248Reactors comprising multiple separated flow channels
    • B01J19/2495Net-type reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/0207Chemical 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 flow within the bed being predominantly horizontal
    • B01J8/0235Chemical 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 flow within the bed being predominantly horizontal in a spiral shaped bed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/18Carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00805Details of the particulate material
    • B01J2208/00814Details of the particulate material the particulate material being provides in prefilled containers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00884Means for supporting the bed of particles, e.g. grids, bars, perforated plates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32279Tubes or cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32408Metal
    • B01J2219/32416Metal fibrous
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32425Ceramic
    • B01J2219/32433Carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32466Composition or microstructure of the elements comprising catalytically active material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals

Definitions

  • the object of the invention is to remedy these drawbacks and to this end proposes the use of a catalytic cartridge comprising a coherent two-dimensional texture made of activated carbon fibers supporting catalyst particles or distributed catalytic functions. on the surface of the fibers, the texture being shaped and housed inside a housing.
  • the carbon fiber texture can be produced in different ways to present a two-dimensional and coherent character.
  • a texture will be used in the form of activated carbon fabric.
  • Other types of textures are however usable, for example knitted textures or unidirectional or multidirectional tablecloths. The latter can be obtained by superposition and bonding together of several unidirectional layers, the directions of the superimposed layers being different from each other.
  • the attachment of catalyst particles to the fibers of the activated carbon texture can be carried out by several methods known in themselves, such as cation exchange or liquid impregnation. We can also develop surface functions on activated carbon fibers to confer catalytic properties.
  • the activated carbon fiber texture is advantageously wound in superimposed turns or in the form of a pleated strip.
  • the texture can be placed around a central passage connected to an inlet or outlet of the reaction medium in or out of the cartridge.
  • the central passage can be materialized by a tube with a porous wall closed at one end.
  • a porous support structure in sheet form such as a grid or a porous membrane.
  • Such a support structure also has the advantage of avoiding possible tearing of fibers which can then be entrained in the reaction medium.
  • the invention also relates to an industrial installation comprising a reactor vessel, at least one catalytic cartridge as defined above and means for ensuring circulation of the reaction medium in contact with the texture of activated carbon fibers.
  • the circulation of the reaction medium can be ensured by an agitator inside the reactor vessel, the catalytic cartridge being housed in this vessel.
  • the installation comprises a circulation loop external to the reactor vessel and a pump for circulating the reaction medium in a closed circuit through the reactor vessel and the circulation loop.
  • the catalytic cartridge can then be placed inside the reactor vessel or inside a chamber integrated into the circulation loop.
  • the circulation loop may then have at least two branches arranged in parallel and each comprising a chamber for receiving at least one catalytic cartridge, means being provided for directing the reaction medium selectively towards one or the other branch. It is thus possible to remove and replace a catalytic cartridge without interrupting the circulation of the reaction medium.
  • FIG. 2 is a detail view on an enlarged scale and in section of a chamber containing a catalytic cartridge in the installation of Figure 1;
  • FIG. 3 is a sectional view along the plane III-III of Figure 2;
  • FIG. 4 is a cross-sectional view of an alternative embodiment of a catalytic cartridge according to the invention.
  • FIG. 5 is a sectional view along the plane V-V of Figure 6 of a chamber containing several catalytic cartridges, according to an alternative embodiment of the installation of Figure 1;
  • FIG. 6 is a sectional view along the plane VI-VI of Figure 5;
  • - Figure 7 is a very schematic view of another alternative embodiment of the installation of Figure 1;
  • FIG. 8 is a very schematic view of an installation for carrying out a catalyzed chemical reaction, according to another embodiment of the invention.
  • FIG. 9 is a very schematic view of an installation for carrying out a catalyzed chemical reaction, according to yet another embodiment of the invention.
  • FIG. 1 The installation of FIG. 1 comprises a reactor vessel 10 intended to contain a liquid reaction mixture which can be brought into contact with a gas under pressure.
  • the tank is closed by a cover 12. This can be provided with a passage for the connection of a pipe 13 for supplying a possible reaction gas.
  • An agitator 14 is immersed in the reaction mixture to keep it in motion in the tank 10.
  • the drive of the agitator 14 in rotation is provided by a motor 16 coupled to a rod 15 supporting the agitator 14 through the cover 12.
  • An outlet pipe 17 is connected to a withdrawal orifice located at the bottom of the tank 10 in order to extract the product obtained at the end of the reaction.
  • a circulation loop 20 is connected to the reactor 10, outside of it.
  • the circulation loop 20 comprises a pipe 21 which plugs into the outlet pipe 17 and connects it to an inlet of a chamber 22.
  • a pump 23 is mounted on the pipe 21.
  • the loop 20 also includes a return pipe 24 which connects an outlet from the chamber 22 to the reactor, through a passage formed in the cover 12.
  • the chamber 22 has a bottom 22a into which the pipe 21 opens and a cover 22b provided with a passage communicating with the pipe 24.
  • a catalytic cartridge 30 (FIGS. 1, 2, 3) is housed in the chamber 22.
  • the cartridge 30 comprises a two-dimensional texture 32 made of activated carbon fibers supporting catalyst particles or catalytic functions.
  • the texture 32 is shaped around a central passage materialized by a tube 34 with a porous wall, for example with a multi-perforated wall.
  • the set is housed inside a housing 35 comprising a cylindrical side wall 36 and two end flanges 37, 38.
  • the housing is fixed to an annular flange 25 of the internal wall of the chamber 22.
  • the texture 32 is a strip wound on itself around the central passage 34.
  • the flanges 37, 38 are applied against the edges of the texture 32, these being able to be guided in grooves formed in the internal faces of the flanges.
  • the lower flange 38 located closest to the entry into the chamber 22 is full, while the upper flange 37 has a central opening 37a communicating with the upper end of the tube 34.
  • the reaction mixture entering the chamber 22 passes through the catalytic cartridge passing through openings 36a of the side wall of the housing 36, through the texture 32 and through the wall of the tube 34 to the opening 37a which constitutes the outlet of the cartridge 30, facing the exit from the chamber 22.
  • the wall 36 of the housing can be produced simply in the form of a cage made up of bars connecting the flanges 37, 38.
  • the material of the housing 35 and of the tube 34 is chosen according to the conditions of use, in particular temperature and chemical nature of the reaction mixture.
  • Stainless steel may be used for high temperatures and high pressures, or plastics for lower temperatures and pressures or with corrosive media.
  • the texture 32 made of carbon fibers is a coherent two-dimensional texture, such as a fabric, other types of texture being however usable as indicated above.
  • a carbon fiber texture is obtained directly from carbon threads or fibers from carbon precursor threads or fibers, after heat treatment, or from a carbon precursor threads or fibers texture, heat treatment transformation of the precursor being carried out after completion of the texture.
  • the activation of the carbon fiber texture can be carried out by heat treatment under an oxidizing atmosphere such as water vapor and / or carbon dioxide.
  • the use of a carbon precursor under Rayon shape provides high purity carbon fibers. Processes for obtaining a carbon fiber texture and for activating such a texture are described in documents WO 99/26721 and FR 2,741,363.
  • An activated carbon fiber texture can also be obtained directly from a texture of cellulosic fibers by heat treatment carried out after impregnation of the texture of cellulosic fibers with an agent which promotes the dehydration of cellulose.
  • a texture of carbon fibers in the form of fabric will preferably be used.
  • an activated carbon fiber texture which supports a noble metal in divided form, such as Pd, Pt, Ru, Rh, Ir.
  • the attachment of the catalyst to the fibers of activated carbon can be carried out by cation exchange or by liquid impregnation with a composition containing a compound of the catalyst to be fixed. Reference may be made to document WO 99/26721 of the applicant.
  • surface functions such as carboxylic acids are developed on the activated carbon fibers. This is achieved by performing an oxidative treatment in the liquid phase using chemical agents such as sodium hypochlorite NaOCI or nitric acid HNO 3 .
  • chemical agents such as sodium hypochlorite NaOCI or nitric acid HNO 3 .
  • Other types of catalysts or catalytic functions can of course be used.
  • the activated carbon fiber texture is shaped after fixing the catalyst or developing catalytic functions.
  • the texture can be fixed by one of its faces on a thin porous sheet support structure having a shape memory capacity.
  • Such a structure 33 is for example a grid or a perforated membrane of plastic material such as polypropylene, polyamide, polyurethane, polyester or polyethylene.
  • this support structure also makes it possible: to induce a pressure drop which increases the contact time of the reaction mixture with the texture of activated carbon fibers; retain any fibers torn off or isolated; homogeneously dispersing the reaction mixture on the surface of the fibrous texture by acting as a distribution grid, the structure 33 being located at least on the face of the fibrous texture receiving the reaction mixture; and to reinforce the mechanical resistance of the fibrous texture.
  • the texture 32 can be provided with a holding structure 33 on only one or on each of its faces.
  • the connection between the texture 32 and the holding structure 33 can be achieved for example by gluing. Different techniques can be used such as:
  • FIG. 4 An alternative embodiment of a catalytic cartridge 30 is illustrated in FIG. 4. This alternative differs from the embodiment of FIGS.
  • a single cartridge 30 is introduced into the chamber 22. It is of course possible, as a variant, to house several cartridges simultaneously in the chamber 22 as illustrated by Figures 5 and 6. In this example, three cylindrical cartridges 30 1f 30 2 , 30 3 are arranged side by side, these cartridges being of similar construction to that of cartridge 30.
  • the cartridges 30 ,, 30 2 , 30 3 are fixed at their upper flanges in openings in a transverse wall 26 of the chamber 22. The outlets of the cartridges open at the upper part of the chamber 22 where the return pipe 24 opens.
  • FIG 7 partially illustrates another alternative embodiment of the installation of Figure 1 which differs from the latter in that the circulation loop 20 comprises several, for example two branches 28 ,, 28 2 connected in parallel between the pipes 22 and 24.
  • Each branch 28 detergent28 2 comprises a chamber 22 containing one or more catalytic cartridges.
  • Valves 29 ,, 29 2 mounted on the branches 28 ,, 28- make it possible to control the circulation of the reaction mixture selectively in one and / or the other of the branches.
  • An advantage of using catalytic cartridges, in accordance with the invention consists in the possibility of removing and replacing the catalytic charge from the installation in a very simple manner, in comparison with the prior art in which the charge is supported by grains of activated carbon dispersed within the reaction medium in the reactor vessel.
  • Another significant advantage lies in the absence of filtering at the outlet of the installation during the withdrawal of the desired reaction product.
  • the embodiments described above have the additional advantage of being able to be implemented on existing installations without requiring significant modifications, in particular at the level of the reactor vessels.
  • the invention is however not limited to the case where the catalytic cartridge (s) are inserted in a circulation loop external to the reactor and also encompasses the case where one or more catalytic cartridges are placed in the reactor vessel itself.
  • one or more catalytic cartridges 130 are supported in the reactor vessel 110.
  • the circulation of the reaction mixture to pass it through the catalytic cartridges is carried out by an agitator 114 mounted at the end of a rod 115.
  • the rod 115 passes through the cover 112 of the reactor vessel and is coupled to a motor 116 driving the agitator.
  • several catalytic cartridges 230 are supported in the reactor vessel 210, as in the case of FIG. 8.
  • the circulation of the reaction mixture is carried out by entrainment of the latter. ci in a closed circuit comprising a circulation loop 220 external to the reactor vessel.
  • the reaction loop 220 connects the outlet pipe of the reactor vessel, at the bottom thereof, to a passage formed in the cover 212 of the reactor vessel. This arrangement makes it possible to optionally inject a product into the reaction mixture during its passage through the recirculation loop 220, during the treatment.
  • the cartridges 130 and 230 can be similar to those of FIGS. 2, 3 and 4 or have a different embodiment, but always based on the use of a coherent texture of activated carbon fibers formed inside 'a housing and supporting catalyst particles or catalytic functions.

Abstract

The invention concerns a catalytic cartridge (30) comprising a coherent two-dimensional texture in activated carbon fibres bearing catalyst particles or catalytic functions distributed at the surface of the fibres, the texture being formed and housed inside a casing. The cartridge (30) can be arranged in a chamber (22) integrated to a recycling loop (20) connected on a reactor vessel (10).

Description

Titre de l'inventionTitle of invention
Cartouche catalytique et application à des installations pour la mise en oeuvre de réactions chimiques catalysées.Catalytic cartridge and application to installations for carrying out catalyzed chemical reactions.
Arrière-plan de l'inventionInvention background
Dans des réacteurs industriels destinés à la mise en oeuvre de réactions chimiques catalysées, il est courant d'incorporer le catalyseur en le fixant sous forme divisée sur des grains de charbon actif introduits dans le réacteur, au sein du milieu réactionnel. En fin de réaction, une filtration soignée doit être réalisée pour éviter la présence de grains de charbon actif dans le produit obtenu. Cette étape de filtration entraîne une perte de catalyseur, qui est souvent sous forme de métal, notamment de métal noble, perte généralement de l'ordre de 5 à 15 % en masse. En outre, lorsque le catalyseur doit être remplacé ou renouvelé, la récupération des grains de charbon actif contenus dans le réacteur est une opération longue et délicate.In industrial reactors intended for the implementation of catalyzed chemical reactions, it is common to incorporate the catalyst by fixing it in divided form on grains of activated carbon introduced into the reactor, within the reaction medium. At the end of the reaction, careful filtration must be carried out to avoid the presence of grains of activated carbon in the product obtained. This filtration step leads to a loss of catalyst, which is often in the form of a metal, in particular a noble metal, a loss generally of the order of 5 to 15% by mass. In addition, when the catalyst must be replaced or renewed, the recovery of the activated carbon grains contained in the reactor is a long and delicate operation.
Objet et résumé de l'invention L'invention a pour but de remédier à ces inconvénients et propose à cet effet l'utilisation d'une cartouche catalytique comprenant une texture bidimensionnelle cohérente en fibres de carbone activé supportant des particules de catalyseur ou fonctions catalytiques réparties à la surface des fibres, la texture étant mise en forme et logée à l'intérieur d'un boîtier.OBJECT AND SUMMARY OF THE INVENTION The object of the invention is to remedy these drawbacks and to this end proposes the use of a catalytic cartridge comprising a coherent two-dimensional texture made of activated carbon fibers supporting catalyst particles or distributed catalytic functions. on the surface of the fibers, the texture being shaped and housed inside a housing.
L'utilisation d'une telle texture cohérente mise en forme dans une cartouche rend très aisés l'extraction et le remplacement du catalyseur, puisque cela peut être fait par simple manipulation de la cartouche. En outre, l'entraînement de particules supports de catalyseur est évité, ce qui permet de se passer de l'étape de filtration lors du soutirage du produit de réaction désiré, donc d'éliminer les inconvénients liés à cette filtration.The use of such a coherent texture formed in a cartridge makes it very easy to extract and replace the catalyst, since this can be done by simple manipulation of the cartridge. In addition, the entrainment of catalyst support particles is avoided, which makes it possible to dispense with the filtration step during the withdrawal of the desired reaction product, therefore eliminating the drawbacks associated with this filtration.
La texture en fibres de carbone peut être réalisée de différentes façons pour présenter un caractère bidimensionnel et cohérent. Avantageusement, on utilisera une texture sous forme de tissu de carbone activé. D'autres types de textures sont toutefois utilisables, par exemple des textures tricotées ou des nappes unidirectionnelles ou multidirectionnelles. Ces dernières peuvent être obtenues par superposition et liaison entre elles de plusieurs nappes unidirectionnelles, les directions des nappes superposées étant différentes les unes des autres.The carbon fiber texture can be produced in different ways to present a two-dimensional and coherent character. Advantageously, a texture will be used in the form of activated carbon fabric. Other types of textures are however usable, for example knitted textures or unidirectional or multidirectional tablecloths. The latter can be obtained by superposition and bonding together of several unidirectional layers, the directions of the superimposed layers being different from each other.
La fixation de particules de catalyseur sur les fibres de la texture en carbone activée peut être réalisée par plusieurs procédés connus en eux-mêmes, tels l'échange cationique ou l'imprégnation liquide. On pourra aussi développer des fonctions de surface sur les fibres de carbone activé pour conférer des propriétés catalytiques.The attachment of catalyst particles to the fibers of the activated carbon texture can be carried out by several methods known in themselves, such as cation exchange or liquid impregnation. We can also develop surface functions on activated carbon fibers to confer catalytic properties.
Afin d'offrir une surface de contact élevée avec le milieu réactionnel, la texture en fibres de carbone activé est avantageusement enroulée en spires superposées ou en forme de bande plissée. La texture peut être disposée autour d'un passage central relié à une entrée ou une sortie de milieu réactionnel dans ou hors la cartouche. Le passage central peut être matérialisé par un tube à paroi poreuse obturé à une extrémité.In order to provide a high contact surface with the reaction medium, the activated carbon fiber texture is advantageously wound in superimposed turns or in the form of a pleated strip. The texture can be placed around a central passage connected to an inlet or outlet of the reaction medium in or out of the cartridge. The central passage can be materialized by a tube with a porous wall closed at one end.
Pour faciliter le maintien en forme de la texture, celle-ci peut avoir au moins une de ses faces fixée sur une structure de support poreuse en feuille telle qu'une grille ou une membrane poreuse. Une telle structure de support présente en outre l'avantage d'éviter un éventuel arrachage de fibres pouvant alors être entraînées dans le milieu réactionnel.To facilitate keeping the texture in shape, it can have at least one of its faces fixed to a porous support structure in sheet form such as a grid or a porous membrane. Such a support structure also has the advantage of avoiding possible tearing of fibers which can then be entrained in the reaction medium.
L'invention a aussi pour objet une installation industrielle comprenant une cuve de réacteur, au moins une cartouche catalytique telle que définie ci-dessus et des moyens pour assurer une circulation du milieu réactionnel au contact de la texture en fibres de carbone activé.The invention also relates to an industrial installation comprising a reactor vessel, at least one catalytic cartridge as defined above and means for ensuring circulation of the reaction medium in contact with the texture of activated carbon fibers.
La mise en circulation du milieu réactionnel peut être assurée par un agitateur à l'intérieur de la cuve de réacteur, la cartouche catalytique étant logée dans cette cuve.The circulation of the reaction medium can be ensured by an agitator inside the reactor vessel, the catalytic cartridge being housed in this vessel.
En variante, l'installation comprend une boucle de circulation extérieure à la cuve de réacteur et une pompe pour mettre en circulation le milieu réactionnel en circuit fermé à travers la cuve de réacteur et la boucle de circulation. La cartouche catalytique peut alors être disposée à l'intérieur de la cuve de réacteur ou à l'intérieur d'une chambre intégrée à la boucle de circulation. Cette dernière disposition est avantageuse car elle permet l'utilisation de cartouches catalytiques conforme à l'invention avec des cuves de réacteurs existants, sans modifications importantes de ceux-ci, et elle permet en outre une mise en place et un retrait aisé de la cartouche.As a variant, the installation comprises a circulation loop external to the reactor vessel and a pump for circulating the reaction medium in a closed circuit through the reactor vessel and the circulation loop. The catalytic cartridge can then be placed inside the reactor vessel or inside a chamber integrated into the circulation loop. This latter arrangement is advantageous because it allows the use of catalytic cartridges in accordance with the invention with existing reactor vessels, without significant modifications to them, and it also allows easy installation and removal of the cartridge. .
La boucle de circulation pourra alors présenter au moins deux branches disposées en parallèle et comprenant chacune une chambre pour recevoir au moins une cartouche catalytique, des moyens étant prévus pour diriger le milieu réactionnel sélectivement vers l'une ou l'autre branche. Il est ainsi possible de retirer et remplacer une cartouche catalytique sans interrompre la circulation du milieu réactionnel.The circulation loop may then have at least two branches arranged in parallel and each comprising a chamber for receiving at least one catalytic cartridge, means being provided for directing the reaction medium selectively towards one or the other branch. It is thus possible to remove and replace a catalytic cartridge without interrupting the circulation of the reaction medium.
Brève description des dessinsBrief description of the drawings
L'invention sera mieux comprise à la lecture de la description faite ci-après, à titre indicatif mais non limitatif, en référence aux dessins annexés sur lesquels : - la figurel est une vue très schématique d'une installation pour la réalisation d'une réaction chimique catalysée, selon un mode de mise en oeuvre de l'invention ;The invention will be better understood on reading the description given below, by way of indication but not limitation, with reference to the appended drawings in which: - the figurel is a very schematic view of an installation for the production of a catalyzed chemical reaction, according to an embodiment of the invention;
- la figure 2 est une vue de détail à échelle agrandie et en coupe d'une chambre contenant une cartouche catalytique dans l'installation de la figure 1 ;- Figure 2 is a detail view on an enlarged scale and in section of a chamber containing a catalytic cartridge in the installation of Figure 1;
- la figure 3 est une vue en coupe suivant le plan lll-lll de la figure 2 ;- Figure 3 is a sectional view along the plane III-III of Figure 2;
- la figure 4 est une vue en coupe transversale d'une variante de réalisation d'une cartouche catalytique conforme à l'invention ;- Figure 4 is a cross-sectional view of an alternative embodiment of a catalytic cartridge according to the invention;
- la figure 5 est une vue en coupe selon le plan V-V de la figure 6 d'une chambre contenant plusieurs cartouches catalytiques, selon une variante de réalisation de l'installation de la figure 1 ;- Figure 5 is a sectional view along the plane V-V of Figure 6 of a chamber containing several catalytic cartridges, according to an alternative embodiment of the installation of Figure 1;
- la figure 6 est une vue en coupe selon le plan VI-VI de la figure 5 ; - la figure 7 est une vue très schématique d'une autre variante de réalisation de l'installation de la figure 1 ;- Figure 6 is a sectional view along the plane VI-VI of Figure 5; - Figure 7 is a very schematic view of another alternative embodiment of the installation of Figure 1;
- la figure 8 est une vue très schématique d'une installation pour la réalisation d'une réaction chimique catalysée, selon un autre mode de mise en oeuvre de l'invention ; et- Figure 8 is a very schematic view of an installation for carrying out a catalyzed chemical reaction, according to another embodiment of the invention; and
- la figure 9 est une vue très schématique d'une installation pour la réalisation d'une réaction chimique catalysée, selon encore un autre mode de mise en oeuvre de l'invention.- Figure 9 is a very schematic view of an installation for carrying out a catalyzed chemical reaction, according to yet another embodiment of the invention.
Description détaillée de modes de réalisation de l'inventionDetailed description of embodiments of the invention
L'installation de la figure 1 comprend une cuve de réacteur 10 destinée à contenir un mélange réactionnel liquide pouvant être mis au contact d'un gaz sous pression. La cuve est obturée par un couvercle 12. Celui-ci peut être muni d'un passage pour le raccordement d'une conduite 13 d'amenée d'un gaz réactionnel éventuel. Un agitateur 14 est immergé dans le mélange réactionnel pour maintenir celui-ci en mouvement dans la cuve 10. L'entraînement de l'agitateur 14 en rotation est assuré par un moteur 16 couplé à une tige 15 supportant l'agitateur 14 à travers le couvercle 12. Une conduite de sortie 17 se raccorde à un orifice de soutirage situé au fond de la cuve 10 afin d'extraire le produit obtenu en fin de réaction.The installation of FIG. 1 comprises a reactor vessel 10 intended to contain a liquid reaction mixture which can be brought into contact with a gas under pressure. The tank is closed by a cover 12. This can be provided with a passage for the connection of a pipe 13 for supplying a possible reaction gas. An agitator 14 is immersed in the reaction mixture to keep it in motion in the tank 10. The drive of the agitator 14 in rotation is provided by a motor 16 coupled to a rod 15 supporting the agitator 14 through the cover 12. An outlet pipe 17 is connected to a withdrawal orifice located at the bottom of the tank 10 in order to extract the product obtained at the end of the reaction.
Une boucle de circulation 20 est raccordée au réacteur 10, à l'extérieur de celui-ci. La boucle de circulation 20 comprend une conduite 21 qui se branche sur la conduite de sortie 17 et la relie à une entrée d'une chambre 22. Une pompe 23 est montée sur la conduite 21. La boucle 20 comprend encore une conduite de retour 24 qui relie une sortie de la chambre 22 au réacteur, à travers un passage formé dans le couvercle 12. La chambre 22 présente un fond 22a dans lequel débouche la conduite 21 et un couvercle 22b muni d'un passage communiquant avec la conduite 24.A circulation loop 20 is connected to the reactor 10, outside of it. The circulation loop 20 comprises a pipe 21 which plugs into the outlet pipe 17 and connects it to an inlet of a chamber 22. A pump 23 is mounted on the pipe 21. The loop 20 also includes a return pipe 24 which connects an outlet from the chamber 22 to the reactor, through a passage formed in the cover 12. The chamber 22 has a bottom 22a into which the pipe 21 opens and a cover 22b provided with a passage communicating with the pipe 24.
Une cartouche catalytique 30 (Figures 1, 2, 3) est logée dans la chambre 22. La cartouche 30 comprend une texture bidimensionnelle 32 en fibres de carbone activé supportant des particules de catalyseur ou des fonctions catalytiques. La texture 32 est mise en forme autour d'un passage central matérialisé par un tube 34 à paroi poreuse, par exemple à paroi multiperforée. L'ensemble est logé à l'intérieur d'un boîtier 35 comprenant une paroi latérale cylindrique 36 et deux flasques d'extrémité 37, 38. Le boîtier est fixé sur un rebord annulaire 25 de la paroi interne de la chambre 22.A catalytic cartridge 30 (FIGS. 1, 2, 3) is housed in the chamber 22. The cartridge 30 comprises a two-dimensional texture 32 made of activated carbon fibers supporting catalyst particles or catalytic functions. The texture 32 is shaped around a central passage materialized by a tube 34 with a porous wall, for example with a multi-perforated wall. The set is housed inside a housing 35 comprising a cylindrical side wall 36 and two end flanges 37, 38. The housing is fixed to an annular flange 25 of the internal wall of the chamber 22.
Dans l'exemple illustré, la texture 32 est une bande enroulée sur elle-même autour du passage central 34. Les flasques 37, 38 sont appliqués contre les bords de la texture 32, ceux-ci pouvant être guidés dans des rainures formées dans les faces internes des flasques. Le flasque inférieur 38 situé le plus proche de l'entrée dans la chambre 22 est plein, tandis que le flasque supérieur 37 présente une ouverture centrale 37a communiquant avec l'extrémité supérieure du tube 34. Le mélange réactionnel pénétrant dans la chambre 22 traverse la cartouche catalytique en passant à travers des ouvertures 36a de la paroi latérale du boîtier 36, à travers la texture 32 et à travers la paroi du tube 34 jusqu'à l'ouverture 37a qui constitue la sortie de la cartouche 30, en regard de la sortie de la chambre 22. On notera que la paroi 36 du boîtier pourra être réalisée simplement sous forme d'une cage constituée de barreaux reliant les flasques 37, 38.In the example illustrated, the texture 32 is a strip wound on itself around the central passage 34. The flanges 37, 38 are applied against the edges of the texture 32, these being able to be guided in grooves formed in the internal faces of the flanges. The lower flange 38 located closest to the entry into the chamber 22 is full, while the upper flange 37 has a central opening 37a communicating with the upper end of the tube 34. The reaction mixture entering the chamber 22 passes through the catalytic cartridge passing through openings 36a of the side wall of the housing 36, through the texture 32 and through the wall of the tube 34 to the opening 37a which constitutes the outlet of the cartridge 30, facing the exit from the chamber 22. It will be noted that the wall 36 of the housing can be produced simply in the form of a cage made up of bars connecting the flanges 37, 38.
Le matériau constitutif du boîtier 35 et du tube 34 est choisi en fonction des conditions d'utilisation, notamment température et nature chimique du mélange réactionnel. On pourra utiliser de l'acier inoxydable pour des hautes températures et pressions élevées, ou des matières plastiques pour de plus faibles températures et pressions ou avec des milieux corrosifs.The material of the housing 35 and of the tube 34 is chosen according to the conditions of use, in particular temperature and chemical nature of the reaction mixture. Stainless steel may be used for high temperatures and high pressures, or plastics for lower temperatures and pressures or with corrosive media.
La texture 32 en fibres de carbone est une texture bidimensionnelle cohérente, tel qu'un tissu, d'autres types de textures étant toutefois utilisables comme indiqué plus haut.The texture 32 made of carbon fibers is a coherent two-dimensional texture, such as a fabric, other types of texture being however usable as indicated above.
La réalisation de tissus ou autres textures bidimensionnelles cohérentes en fibres de carbone activé est connue en soi. Une texture en fibres de carbone est obtenue directement à partir de fils ou fibres de carbone issus de fils ou fibres en précurseur de carbone, après traitement thermique, ou à partir d'une texture en fils ou fibres de précurseur de carbone, le traitement thermique de transformation du précurseur étant effectué après réalisation de la texture. L'activation de la texture en fibres de carbone peut être réalisée par traitement thermique sous atmosphère oxydante telle que vapeur d'eau et/ou dioxyde de carbone. L'utilisation d'un précurseur de carbone sous forme rayonne permet d'obtenir des fibres de carbone de grande pureté. Des procédés d'obtention de texture en fibres de carbone et d'activation d'une telle texture sont décrits dans les documents WO 99/26721 et FR 2 741 363. Une texture en fibres de carbone activé peut aussi être obtenue directement à partir d'une texture en fibres cellulosiques par traitement thermique réalisé après imprégnation de la texture en fibres cellulosiques par un agent promoteur de la déshydratation de la cellulose. Un tel procédé est décrit dans le document WO 98/41678. En raison de sa bonne cohésion et de la possibilité de l'obtenir à partir de tissus de précurseurs de carbone relativement aisés à réaliser, une texture en fibres de carbone sous forme de tissu sera de préférence utilisée.The production of fabrics or other two-dimensional textures consistent with activated carbon fibers is known per se. A carbon fiber texture is obtained directly from carbon threads or fibers from carbon precursor threads or fibers, after heat treatment, or from a carbon precursor threads or fibers texture, heat treatment transformation of the precursor being carried out after completion of the texture. The activation of the carbon fiber texture can be carried out by heat treatment under an oxidizing atmosphere such as water vapor and / or carbon dioxide. The use of a carbon precursor under Rayon shape provides high purity carbon fibers. Processes for obtaining a carbon fiber texture and for activating such a texture are described in documents WO 99/26721 and FR 2,741,363. An activated carbon fiber texture can also be obtained directly from a texture of cellulosic fibers by heat treatment carried out after impregnation of the texture of cellulosic fibers with an agent which promotes the dehydration of cellulose. Such a method is described in document WO 98/41678. Because of its good cohesion and the possibility of obtaining it from fabrics of carbon precursors which are relatively easy to produce, a texture of carbon fibers in the form of fabric will preferably be used.
La nature du catalyseur ou des fonctions catalytiques fixées sur la texture 32 dépend de l'application envisagée.The nature of the catalyst or of the catalytic functions attached to texture 32 depends on the application envisaged.
Dans le cas de réactions telles que par exemple l'hydrogénation catalytique, on utilise une texture en fibres de carbone activé supportant un métal noble sous forme divisée, tel que Pd, Pt, Ru, Rh, Ir. La fixation du catalyseur sur les fibres de carbone activé peut être effectuée par échange cationique ou par imprégnation liquide par une composition contenant un composé du catalyseur à fixer. On pourra se référer au document WO 99/26721 de la déposante.In the case of reactions such as, for example, catalytic hydrogenation, an activated carbon fiber texture is used which supports a noble metal in divided form, such as Pd, Pt, Ru, Rh, Ir. The attachment of the catalyst to the fibers of activated carbon can be carried out by cation exchange or by liquid impregnation with a composition containing a compound of the catalyst to be fixed. Reference may be made to document WO 99/26721 of the applicant.
Dans d'autres cas, comme par exemple pour la catalyse acide, des fonctions de surface type acides carboxyliques sont développées sur les fibres de carbone activé. Cela est obtenu en réalisant un traitement oxydant en phase liquide au moyen d'agents chimiques tels que l'hypochlorite de sodium NaOCI ou l'acide nitrique HNO3. D'autres types de catalyseurs ou fonctions catalytiques pourront bien entendu être utilisés.In other cases, such as for example for acid catalysis, surface functions such as carboxylic acids are developed on the activated carbon fibers. This is achieved by performing an oxidative treatment in the liquid phase using chemical agents such as sodium hypochlorite NaOCI or nitric acid HNO 3 . Other types of catalysts or catalytic functions can of course be used.
La texture en fibres de carbone activé est mise en forme après fixation du catalyseur ou développement de fonctions catalytiques. Afin de faciliter cette mise en forme et le maintien ultérieur de la texture dans la forme voulue, la texture peut être fixée par l'une de ses faces sur une structure de support poreuse mince en feuille ayant une capacité de mémoire de forme.The activated carbon fiber texture is shaped after fixing the catalyst or developing catalytic functions. In order to facilitate this shaping and the subsequent maintenance of the texture in the desired shape, the texture can be fixed by one of its faces on a thin porous sheet support structure having a shape memory capacity.
Une telle structure 33 (montrée sur des détails des figures 2 et 3) est par exemple une grille ou une membrane perforée en matière plastique telle que polypropylène, polyamide, polyuréthane, polyester ou polyéthylène.Such a structure 33 (shown in details in FIGS. 2 and 3) is for example a grid or a perforated membrane of plastic material such as polypropylene, polyamide, polyurethane, polyester or polyethylene.
L'utilisation de cette structure de support permet en outre : d'induire une perte de charge qui augmente le temps de contact du mélange réactionnel avec la texture en fibres de carbone activé ; de retenir d'éventuelles fibres arrachées ou isolées ; de disperser de façon homogène le mélange réactionnel à la surface de la texture fibreuse en agissant comme une grille de distribution, la structure 33 étant située au moins sur la face de la texture fibreuse recevant le mélange réactionnel ; et de renforcer la tenue mécanique de la texture fibreuse.The use of this support structure also makes it possible: to induce a pressure drop which increases the contact time of the reaction mixture with the texture of activated carbon fibers; retain any fibers torn off or isolated; homogeneously dispersing the reaction mixture on the surface of the fibrous texture by acting as a distribution grid, the structure 33 being located at least on the face of the fibrous texture receiving the reaction mixture; and to reinforce the mechanical resistance of the fibrous texture.
La texture 32 peut être munie d'une structure de maintien 33 sur l'une seulement ou sur chacune de ses faces. La liaison entre la texture 32 et la structure de maintien 33 peut être réalisée par exemple par collage. Différentes techniques peuvent être utilisées telles que :The texture 32 can be provided with a holding structure 33 on only one or on each of its faces. The connection between the texture 32 and the holding structure 33 can be achieved for example by gluing. Different techniques can be used such as:
- colaminage de la texture 32 et de la structure de maintien 33 entre deux tapis chauffants de manière à réaliser une fusion superficielle de la matière plastique de la structure de maintien sur la texture 32, ou - contre-collage au moyen d'un film de colle (par exemple polyamide), ou d'une colle déposée en poudre sur la texture 32, avec fusion ultérieure de la colle (par exemple polyuréthane réticulable) ou encore par dispersion d'une colle liquide sur la texture 32 suivie d'un calandrage et d'un séchage. Une variante de réalisation d'une cartouche catalytique 30 est illustrée par la figure 4. Cette variante se distingue du mode de réalisation des figures 2 et 3 en ce que la texture 32 en fibres de carbone activé - ainsi que la structure de maintien éventuelle sur laquelle elle est fixée - est sous forme d'une bande plissée disposée autour du passage central 34. Dans le mode de réalisation des figures 2 et 3, une seule cartouche 30 est introduite dans la chambre 22. Il est bien entendu possible, en variante, de loger plusieurs cartouches simultanément dans la chambre 22 comme illustré par les figures 5 et 6. Dans cet exemple, trois cartouches cylindriques 301f 302, 303 sont disposées côte à côte, ces cartouches étant de réalisation similaire à celle de la cartouche 30. Les cartouches 30,, 302, 303 sont fixées au niveau de leur flasques supérieurs dans des ouvertures d'une paroi transversale 26 de la chambre 22. Les sorties des cartouches s'ouvrent à la partie supérieure de la chambre 22 où débouche la conduite de retour 24.- co-laminating of the texture 32 and of the retaining structure 33 between two heating mats so as to achieve a surface fusion of the plastic material of the retaining structure on the texture 32, or - laminating by means of a film of adhesive (for example polyamide), or of an adhesive deposited in powder on texture 32, with subsequent fusion of the adhesive (for example crosslinkable polyurethane) or also by dispersion of a liquid adhesive on texture 32 followed by calendering and drying. An alternative embodiment of a catalytic cartridge 30 is illustrated in FIG. 4. This alternative differs from the embodiment of FIGS. 2 and 3 in that the texture 32 made of activated carbon fibers - as well as the possible holding structure on which it is fixed - is in the form of a pleated strip arranged around the central passage 34. In the embodiment of Figures 2 and 3, a single cartridge 30 is introduced into the chamber 22. It is of course possible, as a variant, to house several cartridges simultaneously in the chamber 22 as illustrated by Figures 5 and 6. In this example, three cylindrical cartridges 30 1f 30 2 , 30 3 are arranged side by side, these cartridges being of similar construction to that of cartridge 30. The cartridges 30 ,, 30 2 , 30 3 are fixed at their upper flanges in openings in a transverse wall 26 of the chamber 22. The outlets of the cartridges open at the upper part of the chamber 22 where the return pipe 24 opens.
La figure 7 illustre partiellement une autre variante de réalisation de l'installation de la figure 1 qui se distingue de cette dernière en ce que la boucle de circulation 20 comprend plusieurs, par exemple deux branches 28,, 282 connectées en parallèle entre les conduites 22 et 24. Chaque branche 28„ 282 comprend une chambre 22 renfermant une ou plusieurs cartouches catalytiques. Des vannes 29,, 292 montées sur les branches 28,, 28- permettent de commander la circulation du mélange réactionnel sélectivement dans l'une et/ou l'autre des branches.Figure 7 partially illustrates another alternative embodiment of the installation of Figure 1 which differs from the latter in that the circulation loop 20 comprises several, for example two branches 28 ,, 28 2 connected in parallel between the pipes 22 and 24. Each branch 28 „28 2 comprises a chamber 22 containing one or more catalytic cartridges. Valves 29 ,, 29 2 mounted on the branches 28 ,, 28- make it possible to control the circulation of the reaction mixture selectively in one and / or the other of the branches.
De la sorte, le retrait ou la mise en place d'une cartouche catalytique peut être réalisé dans l'une des chambres 22 en mettant hors circuit la branche 28, ou 282 qui la comprend, sans interrompre la circulation du milieu réactionnel dans l'autre branche et l'ensemble de la boucle de circulation.In this way, the removal or the installation of a catalytic cartridge can be carried out in one of the chambers 22 by switching off the branch 28, or 28 2 which includes it, without interrupting the circulation of the reaction medium in the other branch and the entire circulation loop.
Un avantage de l'utilisation de cartouches catalytiques, conformément à l'invention, consiste dans la possibilité de retirer et remplacer la charge catalytique de l'installation de façon très simple, en comparaison avec l'art antérieur dans lequel la charge est supportée par des grains de charbon actif dispersés au sein du milieu réactionnel dans la cuve de réacteur.An advantage of using catalytic cartridges, in accordance with the invention, consists in the possibility of removing and replacing the catalytic charge from the installation in a very simple manner, in comparison with the prior art in which the charge is supported by grains of activated carbon dispersed within the reaction medium in the reactor vessel.
Un autre avantage significatif réside dans l'absence de filtrage en sortie de l'installation lors du soutirage de produit de réaction désiré. En outre, les modes de réalisation décrits ci-avant présentent l'intérêt supplémentaire de pouvoir être mis en oeuvre sur des installations existantes sans nécessiter de modifications importantes, en particulier au niveau des cuves de réacteurs.Another significant advantage lies in the absence of filtering at the outlet of the installation during the withdrawal of the desired reaction product. In addition, the embodiments described above have the additional advantage of being able to be implemented on existing installations without requiring significant modifications, in particular at the level of the reactor vessels.
L'invention n'est toutefois pas limitée au cas où la ou les cartouches catalytiques sont insérées dans une boucle de circulation extérieure au réacteur et englobe aussi le cas où une ou plusieurs cartouches catalytiques sont disposées dans la cuve de réacteur elle- même.The invention is however not limited to the case where the catalytic cartridge (s) are inserted in a circulation loop external to the reactor and also encompasses the case where one or more catalytic cartridges are placed in the reactor vessel itself.
Ainsi, dans le mode de réalisation de la figure 8, une ou plusieurs cartouches catalytiques 130 sont supportées dans la cuve de réacteur 110. La mise en circulation du mélange réactionnel pour le faire passer à travers les cartouches catalytiques est réalisée par un agitateur 114 monté à l'extrémité d'une tige 115. La tige 115 traverse le couvercle 112 de la cuve de réacteur et est couplée à un moteur 116 d'entraînement de l'agitateur. Dans un autre mode de réalisation illustré par la figure 9, plusieurs cartouches catalytiques 230 sont supportées dans la cuve de réacteur 210, comme dans le cas de la figure 8. Toutefois, la mise en circulation du mélange réactionnel est réalisée par entraînement de celui-ci dans un circuit fermé comportant une boucle de circulation 220 externe à la cuve de réacteur. La boucle de réaction 220, sur laquelle est montée une pompe 223 raccorde la conduite de sortie de la cuve de réacteur, au fond de celle-ci, à un passage formé dans le couvercle 212 de la cuve de réacteur. Cette disposition permet d'injecter éventuellement un produit dans le mélange réactionnel lors de son passage dans la boucle de recirculation 220, pendant le traitement.Thus, in the embodiment of FIG. 8, one or more catalytic cartridges 130 are supported in the reactor vessel 110. The circulation of the reaction mixture to pass it through the catalytic cartridges is carried out by an agitator 114 mounted at the end of a rod 115. The rod 115 passes through the cover 112 of the reactor vessel and is coupled to a motor 116 driving the agitator. In another embodiment illustrated in FIG. 9, several catalytic cartridges 230 are supported in the reactor vessel 210, as in the case of FIG. 8. However, the circulation of the reaction mixture is carried out by entrainment of the latter. ci in a closed circuit comprising a circulation loop 220 external to the reactor vessel. The reaction loop 220, on which a pump 223 is mounted, connects the outlet pipe of the reactor vessel, at the bottom thereof, to a passage formed in the cover 212 of the reactor vessel. This arrangement makes it possible to optionally inject a product into the reaction mixture during its passage through the recirculation loop 220, during the treatment.
Les cartouches 130 et 230 peuvent être similaires à celles des figures 2, 3 et 4 ou avoir une forme de réalisation différente, mais toujours basée sur l'utilisation d'une texture cohérente en fibres de carbone activé mise en forme à l'intérieur d'un boîtier et supportant des particules de catalyseur ou des fonctions catalytiques. The cartridges 130 and 230 can be similar to those of FIGS. 2, 3 and 4 or have a different embodiment, but always based on the use of a coherent texture of activated carbon fibers formed inside 'a housing and supporting catalyst particles or catalytic functions.

Claims

REVENDICATIONS
1. Cartouche catalytique comprenant une texture bidimensionnelle cohérente (32) en fibres de carbone activé supportant des particules de catalyseur ou fonctions catalytiques réparties à la surface des fibres, la texture étant mise en forme et logée à l'intérieur d'un boîtier (35).1. Catalytic cartridge comprising a coherent two-dimensional texture (32) made of activated carbon fibers supporting catalyst particles or catalytic functions distributed over the surface of the fibers, the texture being shaped and housed inside a housing (35 ).
2. Cartouche selon la revendication 1, caractérisée en ce que la texture (32) est un tissu de carbone activé. 2. Cartridge according to claim 1, characterized in that the texture (32) is an activated carbon fabric.
3. Cartouche selon l'une quelconque des revendications 1 et3. Cartridge according to any one of claims 1 and
2, caractérisée en ce que la texture est en forme de bande enroulée en spires superposées autour d'un passage central (34).2, characterized in that the texture is in the form of a band wound in superimposed turns around a central passage (34).
4. Cartouche selon l'une quelconque des revendications 1 et 2, caractérisée en ce que la texture est en forme de bande plissée disposée autour d'un passage central (34).4. Cartridge according to any one of claims 1 and 2, characterized in that the texture is in the form of a pleated strip arranged around a central passage (34).
5. Cartouche selon l'une quelconque des revendications 3 et 4, caractérisée en ce que le passage central est matérialisé par un tube (34) à paroi poreuse obturé à une extrémité.5. Cartridge according to any one of claims 3 and 4, characterized in that the central passage is materialized by a tube (34) with porous wall closed at one end.
6. Cartouche selon l'une quelconque des revendications 1 à 5, caractérisée en ce que la texture (32) a au moins l'une de ses faces fixée sur une structure de support poreuse en feuille (33).6. Cartridge according to any one of claims 1 to 5, characterized in that the texture (32) has at least one of its faces fixed on a porous support structure in sheet form (33).
7. Cartouche selon la revendication 6, caractérisée en ce que la structure de support (33) est sous forme de grille.7. Cartridge according to claim 6, characterized in that the support structure (33) is in the form of a grid.
8. Cartouche selon la revendication 6, caractérisée en ce que la structure de support (33) est sous forme de membrane poreuse.8. Cartridge according to claim 6, characterized in that the support structure (33) is in the form of a porous membrane.
9. Installation industrielle pour la mise en oeuvre de réaction chimique catalysée comprenant une cuve de réacteur (10 ; 110 ; 210) destinée à recevoir un milieu réactionnel et des moyens de support de particules de catalyseur ou fonctions catalytiques, caractérisée en ce qu'elle comporte au moins une cartouche catalytique (30 ; 130 ; 230) selon l'une quelconque des revendications 1 à 8 et des moyens pour assurer une circulation du milieu réactionnel au contact de la texture en fibres de carbone activé contenue dans la cartouche. 9. Industrial installation for the implementation of catalyzed chemical reaction comprising a reactor vessel (10; 110; 210) intended to receive a reaction medium and means for supporting catalyst particles or catalytic functions, characterized in that it comprises at least one catalytic cartridge (30; 130; 230) according to any one of claims 1 to 8 and means for ensuring a circulation of the reaction medium in contact with the activated carbon fiber texture contained in the cartridge.
10. Installation selon la revendication 9, caractérisée en ce que la cartouche (130) est disposée à l'intérieur de la cuve de réacteur (110) et celle-ci est munie d'un agitateur (114) pour réaliser la mise en circulation du milieu réactionnel.10. Installation according to claim 9, characterized in that the cartridge (130) is disposed inside the reactor vessel (110) and the latter is provided with an agitator (114) for bringing the reaction medium into circulation.
11. Installation selon la revendication 9, caractérisée en ce qu'elle comprend une boucle de circulation (20 ; 220) extérieure à la cuve (10 ; 210) de réacteur et une pompe (23 ; 223) pour mettre en circulation le milieu réactionnel en circuit fermé à travers la cuve de réacteur et la boucle de recirculation.11. Installation according to claim 9, characterized in that it comprises a circulation loop (20; 220) outside the reactor vessel (10; 210) and a pump (23; 223) for circulating the reaction medium in a closed circuit through the reactor vessel and the recirculation loop.
12. Installation selon la revendication 11, caractérisée en ce que la cartouche (230) est disposée à l'intérieur de la cuve de réacteur (210).12. Installation according to claim 11, characterized in that the cartridge (230) is arranged inside the reactor vessel (210).
13. Installation selon la revendication 11, caractérisée en ce que la cartouche (30) est disposée à l'intérieur d'une chambre (22) intégrée à la boucle de recirculation (20).13. Installation according to claim 11, characterized in that the cartridge (30) is arranged inside a chamber (22) integrated into the recirculation loop (20).
14. Installation selon la revendication 13, caractérisée en ce que la boucle de circulation (20) présente au moins deux branches14. Installation according to claim 13, characterized in that the circulation loop (20) has at least two branches
(28„ 282) disposées en parallèle et comprenant chacune une chambre (22) pour recevoir au moins une cartouche catalytique, et des moyens (29,, 292) sont prévus pour diriger le milieu réactionnel sélectivement vers l'une ou l'autre chambre. (28 „28 2 ) arranged in parallel and each comprising a chamber (22) for receiving at least one catalytic cartridge, and means (29 ,, 29 2 ) are provided for directing the reaction medium selectively towards one or the other room.
PCT/FR2001/004095 2000-12-22 2001-12-20 Catalytic cartridge and application to installations producing catalysed chemical reactions WO2002051533A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0016900A FR2818562A1 (en) 2000-12-22 2000-12-22 CATALYTIC CARTRIDGE AND APPLICATION TO PLANTS FOR THE IMPLEMENTATION OF CATALYZED CHEMICAL REACTIONS
FR00/16900 2000-12-22

Publications (1)

Publication Number Publication Date
WO2002051533A1 true WO2002051533A1 (en) 2002-07-04

Family

ID=8858100

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FR2001/004095 WO2002051533A1 (en) 2000-12-22 2001-12-20 Catalytic cartridge and application to installations producing catalysed chemical reactions

Country Status (2)

Country Link
FR (1) FR2818562A1 (en)
WO (1) WO2002051533A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106995944A (en) * 2017-05-18 2017-08-01 江苏田园新材料股份有限公司 A kind of equipment of new production PBT fibres

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3843561A (en) * 1970-05-13 1974-10-22 Universal Oil Prod Co Mat of inorganic oxide fibers,its method of preparation and its impregnation with catalytic materials
US3925252A (en) * 1971-11-05 1975-12-09 Toyota Motor Co Ltd Catalyzer apparatus and method for the production thereof
US5181993A (en) * 1988-09-22 1993-01-26 Nagakazu Furuya Process for converting ferrous ions to ferric ions
WO1994018440A1 (en) * 1993-02-10 1994-08-18 Alfred Buck Device for the catalytic purification of flowing gases, especially exhaust gases of internal combustion engines
US5567392A (en) * 1993-06-28 1996-10-22 Mannesmann Aktiengesellschaft Device for the purification of contaminated exhaust air through heterogeneous catalysis
WO1998016463A1 (en) * 1996-10-16 1998-04-23 Basf Aktiengesellschaft Process for the manufacture of hydrogen peroxide

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3843561A (en) * 1970-05-13 1974-10-22 Universal Oil Prod Co Mat of inorganic oxide fibers,its method of preparation and its impregnation with catalytic materials
US3925252A (en) * 1971-11-05 1975-12-09 Toyota Motor Co Ltd Catalyzer apparatus and method for the production thereof
US5181993A (en) * 1988-09-22 1993-01-26 Nagakazu Furuya Process for converting ferrous ions to ferric ions
WO1994018440A1 (en) * 1993-02-10 1994-08-18 Alfred Buck Device for the catalytic purification of flowing gases, especially exhaust gases of internal combustion engines
US5567392A (en) * 1993-06-28 1996-10-22 Mannesmann Aktiengesellschaft Device for the purification of contaminated exhaust air through heterogeneous catalysis
WO1998016463A1 (en) * 1996-10-16 1998-04-23 Basf Aktiengesellschaft Process for the manufacture of hydrogen peroxide

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106995944A (en) * 2017-05-18 2017-08-01 江苏田园新材料股份有限公司 A kind of equipment of new production PBT fibres

Also Published As

Publication number Publication date
FR2818562A1 (en) 2002-06-28

Similar Documents

Publication Publication Date Title
EP1313544B1 (en) Filtering medium, method for making same
EP0231706B1 (en) Oxidation process and reactor for a gaseous phase oxidizable charge
EP0459916B1 (en) Carbon-carbon composite material friction elements having a differential texture, processes and devices for their fabrication
LU81375A1 (en) CROSS-OVER OR PERMEATION DEVICE FOR SEPARATING A FLUID FROM A MIXTURE OF FLUIDS, CONTAINING SELECTIVELY PERMEABLE HOLLOW FIBERS
WO2007131990A1 (en) Method of synthesising coated organic or inorganic particles
CA2735957A1 (en) Three-dimensional foam photocatalysts structured with carbon or carbonated material
EP2341948A1 (en) Three-dimensional foam photocatalysts structured with carbide and particularly -sic
EP0870534A1 (en) Macroporous support having a permeability gradient and method for its production
EP1145343A2 (en) Gaseous diffusion electrode and use in catalysed electrochemical processes
EP2307127A1 (en) Filtration and predistribution device for a fixed catalytic bed reactor and use thereof
FR2794033A1 (en) PROCESS FOR PURIFYING GASEOUS EFFLUENTS BY PHOTOCATALYSIS, INSTALLATION FOR CARRYING OUT SAID METHOD
EP0495735A1 (en) Process for manufacturing highly permeable porous tubes from carbon-carbon composite material and their uses
FR3098811A1 (en) PHOTORACTOR INCLUDING A PHOTOCATALYTIC TEXTILE PROVIDED WITH OPTICAL FIBERS
WO2002051533A1 (en) Catalytic cartridge and application to installations producing catalysed chemical reactions
EP2066444A1 (en) Method for impregnating a porous body by a suspension and installation to use such a method.
CA1290141C (en) Process, reactor and its use for gaseous phase oxidation of an oxidizable charge
EP0448466A1 (en) Improvements of membrane filters for ultrafiltration or microfiltration of liquids, in particular of water
WO1999053503A1 (en) Device for activating conductivity in porous structures
EP3064268B1 (en) Assembly for collecting a gaseous fluid for a radial reactor
WO2007135054A1 (en) Reagent injector for equipping a water treatment reactor, comprising a nozzle associated with a dispersing member, and corresponding water treatment device
EP3188815B1 (en) Method of selective extraction of platinoids, from a support containing same, with an extraction medium consisting of a supercritical fluid and an organic ligand
EP3161181A1 (en) Chemical vapour deposition device with improved deposition efficiency
FR2768940A1 (en) REGENERABLE FILTER FOR LIQUIDS, ESPECIALLY FOOD
WO2000071469A1 (en) Method and installation for separating heavy metals contained in liquid effluents
JP6018432B2 (en) Solid acid reactor, solid acid catalytic reactor, and method for producing solid acid reactor

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ CZ DE DE DK DK DM DZ EC EE EE ES FI FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ OM PH PL PT RO RU SD SE SG SI SK SK SL TJ TM TN TR TT TZ UA UG US UZ VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

122 Ep: pct application non-entry in european phase
NENP Non-entry into the national phase

Ref country code: JP

WWW Wipo information: withdrawn in national office

Country of ref document: JP