FR3120804B3 - Tubular reactors with graduated catalytic bed for improved heat transfer - Google Patents
Tubular reactors with graduated catalytic bed for improved heat transfer Download PDFInfo
- Publication number
- FR3120804B3 FR3120804B3 FR2102656A FR2102656A FR3120804B3 FR 3120804 B3 FR3120804 B3 FR 3120804B3 FR 2102656 A FR2102656 A FR 2102656A FR 2102656 A FR2102656 A FR 2102656A FR 3120804 B3 FR3120804 B3 FR 3120804B3
- Authority
- FR
- France
- Prior art keywords
- tubular reactor
- particles
- catalytic bed
- diameter
- graduated
- Prior art date
- Legal status (The legal status 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 status listed.)
- Active
Links
- 230000003197 catalytic effect Effects 0.000 title abstract 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 4
- 239000002245 particle Substances 0.000 abstract 4
- 239000003054 catalyst Substances 0.000 abstract 2
- 239000008246 gaseous mixture Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 238000002407 reforming Methods 0.000 abstract 1
- 238000006057 reforming reaction Methods 0.000 abstract 1
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
- B01J8/0242—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 flow within the bed being predominantly vertical
- B01J8/025—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 flow within the bed being predominantly vertical in a cylindrical 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
- 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
- B01J8/0285—Heating or cooling the reactor
-
- 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
- B01J2208/00504—Controlling the temperature by means of a burner
-
- 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
- B01J2208/00654—Controlling the process by measures relating to the particulate material
- B01J2208/00672—Particle size selection
-
- 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
- B01J2208/023—Details
- B01J2208/024—Particulate material
- B01J2208/025—Two or more types of catalyst
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
Réacteur tubulaire pour un procédé de reformage de méthane, de diamètre intérieur D, de longueur L avec une première extrémité ouverte pour introduire un mélange gazeux d’alimentation et l’extrémité opposée ouverte pour l’évacuation du mélange gazeux produit, du catalyseur permettant la réaction de conversion du méthane, sous forme de particules étant disposé dans le réacteur tubulaire, l’apport de chaleur externe nécessaire à la réaction de reformage étant fourni par des brûleurs disposés dans le four où est installé le réacteur tubulaire, caractérisé en ce que au moins deux types de particules de catalyseur de dimensions différentes sont disposés dans le tube formant un lit catalytique graduel dans lequel: - les plus petites particules de diamètre a1 compris entre 2 mm et 10 mm, de préférence entre 4 mm et 8 mm forment une couche annulaire d’épaisseur a au moins égale à a1 plaquée contre la paroi du réacteur tubulaire, - les particules les plus grandes de dimension b1 sont disposées dans la partie centrale du réacteur tubulaire où elles remplissent un espace de forme cylindrique dans l’axe du réacteur, le diamètre b dudit espace cylindrique étant inférieur ou égal à D-2a, Figure de l’abrégé : Fig. 2Tubular reactor for a methane reforming process, of internal diameter D, of length L with a first end open to introduce a gaseous feed mixture and the opposite end open for the evacuation of the gaseous mixture produced, of the catalyst allowing the conversion reaction of methane, in the form of particles, being arranged in the tubular reactor, the external heat input necessary for the reforming reaction being provided by burners arranged in the furnace where the tubular reactor is installed, characterized in that at the at least two types of catalyst particles of different sizes are arranged in the tube forming a gradual catalytic bed in which: - the smallest particles with a diameter a1 of between 2 mm and 10 mm, preferably between 4 mm and 8 mm, form a layer ring of thickness a at least equal to a1 pressed against the wall of the tubular reactor, - the largest particles of dimension b1 are arranged in the central part of the tubular reactor where they fill a space of cylindrical shape in the axis of the reactor , the diameter b of said cylindrical space being less than or equal to D-2a, Figure of the abstract: FIG. 2
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR2102656A FR3120804B3 (en) | 2021-03-17 | 2021-03-17 | Tubular reactors with graduated catalytic bed for improved heat transfer |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR2102656A FR3120804B3 (en) | 2021-03-17 | 2021-03-17 | Tubular reactors with graduated catalytic bed for improved heat transfer |
FR2102656 | 2021-03-17 |
Publications (2)
Publication Number | Publication Date |
---|---|
FR3120804A3 FR3120804A3 (en) | 2022-09-23 |
FR3120804B3 true FR3120804B3 (en) | 2023-08-18 |
Family
ID=83319378
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR2102656A Active FR3120804B3 (en) | 2021-03-17 | 2021-03-17 | Tubular reactors with graduated catalytic bed for improved heat transfer |
Country Status (1)
Country | Link |
---|---|
FR (1) | FR3120804B3 (en) |
-
2021
- 2021-03-17 FR FR2102656A patent/FR3120804B3/en active Active
Also Published As
Publication number | Publication date |
---|---|
FR3120804A3 (en) | 2022-09-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2692701A1 (en) | Exchanger reactor having a bayonet tube allowing operation with pressure differences of the order of 100 bar between the tube side and the shell side. | |
EP2394735B1 (en) | Reactor-exchanger with bayonet tubes and fire tubes suspended from the upper vault of the reactor | |
JP2012519258A (en) | Crimp type coupler, crimping tool and crimping method | |
WO2008132313A2 (en) | Compact exchanger reactor using a plurality of porous burners | |
FR3120804B3 (en) | Tubular reactors with graduated catalytic bed for improved heat transfer | |
EP0252356B1 (en) | Process and furnace for the steam cracking of hydrocarbons for the preparation of olefins and diolefins | |
FR2624115A1 (en) | PROCESS AND APPARATUS FOR CONVERTING HYDROCARBONS | |
EP1458469A1 (en) | Catalytic reactor, corresponding reaction installation and method | |
NO176750B (en) | Reactor for partial catalytic oxidation of hydrocarbons | |
CA2460622A1 (en) | Device and method of providing a relative and controlled waterproof seal between a pipe and a ceramic tube | |
FR3120805B3 (en) | Tubular tube-in-tube reactors with double catalytic bed | |
CN101432225B (en) | Process for producing hydrogen generator | |
FR2931368A1 (en) | NEW BAIONNETTE TUBE EXCHANGER REACTOR SURROUNDED BY CEMENT CHIMNEYS. | |
FR2541390A1 (en) | Nozzle-effect ejector-mixer used particularly as a thermocompressor | |
CH516129A (en) | Process for cooling a fluid and cooling apparatus for its implementation | |
CN210229908U (en) | Tubular reactor | |
US3127248A (en) | Catalyst tube assembly | |
CN204996460U (en) | Chemical engineering reaction tank | |
CH414567A (en) | Process for carrying out thermal reactions and apparatus for carrying out this process | |
CN212429968U (en) | Pipeline erection supporting device for petrochemical engineering construction | |
FR2639354A1 (en) | PROCESS FOR CRACKING A LOWER HYDROCARBON HEAVY HYDROCARBON LOAD AND DEVICE FOR CARRYING OUT SAID METHOD | |
CN210320120U (en) | Component of petrochemical heating furnace | |
EP0321341B1 (en) | Device for fixing pipes passing through a wall | |
RU2005138465A (en) | TUBE CONNECTION | |
CN218530866U (en) | Novel gas-solid continuous reaction device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PLFP | Fee payment |
Year of fee payment: 2 |
|
PLFP | Fee payment |
Year of fee payment: 3 |
|
PLFP | Fee payment |
Year of fee payment: 4 |