FR2652891A2 - Method and device for regulation or control of the level of heat of a pulverulent solid, including a heat exchanger with fluidised or mobile bed compartments - Google Patents
Method and device for regulation or control of the level of heat of a pulverulent solid, including a heat exchanger with fluidised or mobile bed compartments Download PDFInfo
- Publication number
- FR2652891A2 FR2652891A2 FR8913128A FR8913128A FR2652891A2 FR 2652891 A2 FR2652891 A2 FR 2652891A2 FR 8913128 A FR8913128 A FR 8913128A FR 8913128 A FR8913128 A FR 8913128A FR 2652891 A2 FR2652891 A2 FR 2652891A2
- Authority
- FR
- France
- Prior art keywords
- solid
- regulation
- mobile
- zone
- compartment
- 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.)
- Granted
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
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1809—Controlling processes
-
- 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
- F28D13/00—Heat-exchange apparatus using a fluidised 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/00044—Temperature measurement
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
Description
Le brevet principal concerne un procédé de régulation thermique et/ou de débit d'un solide pulvérulent avec échange thermique en lit fluidisé et un dispositif pour la mise en oeuvre de ce procédé. Plus particulièrement, le procédé peut s'appliquer à la régénération de catalyseurs particulièrement chargés en résidus hydrocarbonés et en coke après réaction avec une charge d'hydrocarbures. Elle peut concerner les catalyseurs d'hydrotraitement, d'hydrocraquage ou de craquage catalytique, de réformage ou même toutes masses de contact utilisées par exemple dans les procédés de craquage thermique.The main patent relates to a process for thermal regulation and / or flow rate of a pulverulent solid with heat exchange in a fluidized bed and a device for implementing this process. More particularly, the process can be applied to the regeneration of catalysts which are particularly charged with hydrocarbon residues and with coke after reaction with a hydrocarbon charge. It can relate to hydrotreatment, hydrocracking or catalytic cracking, reforming catalysts or even any contact masses used for example in thermal cracking processes.
L'invention peut également concerner (a) toute réaction de raffinage en présence d'un catalyseur fluidisé ou mobile ou (b) la combustion de charbon.The invention may also relate to (a) any refining reaction in the presence of a fluidized or mobile catalyst or (b) the combustion of coal.
Conformément à la présente addition, le solide circule du haut vers le bas dans le compartiment périphérique, en lit fluidisé. I1 est animé par des premiers moyens de fluidisation (un anneau ou une grille) qui sont adaptés à délivrer dans ce compartiment périphérique une vitesse de fluidisation comprise par exemple entre 1 cm/s et 10 cm/s. I1 traverse ensuite un espace de passage à la base de l'échangeur et remonte dans le compartiment central en lit fluidisé. Des seconds moyens de fluidisation (anneau ou grille) sont en effet adaptés à délivrer, dans le compartiment central de volume généralement plus important une vitesse de fluidisation par exemple comprise entre 0,1 m/s et 1 m/s. La pression de fluidisation est supérieure dans la partie ascendante à la pression de fluidisation dans la partie descendante. On ajuste le débit thermique en jouant sur un différentiel de pression entre les deux compartiments. In accordance with the present addition, the solid circulates from top to bottom in the peripheral compartment, in a fluidized bed. I1 is driven by first fluidization means (a ring or a grid) which are adapted to deliver in this peripheral compartment a fluidization speed of for example between 1 cm / s and 10 cm / s. I1 then crosses a passage space at the base of the exchanger and rises in the central compartment in a fluidized bed. Second fluidization means (ring or grid) are in fact adapted to deliver, in the central compartment of generally larger volume, a fluidization speed for example between 0.1 m / s and 1 m / s. The fluidization pressure is higher in the ascending part than the fluidization pressure in the descending part. The thermal flow is adjusted by playing on a pressure differential between the two compartments.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8913128A FR2652891B2 (en) | 1989-06-16 | 1989-10-05 | METHOD AND DEVICE FOR REGULATING OR CONTROLLING THE THERMAL LEVEL OF A POWDER SOLID COMPRISING A HEAT EXCHANGER WITH FLUIDIZED OR MOBILE BED COMPARTMENTS. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8908159A FR2648550B1 (en) | 1989-06-16 | 1989-06-16 | METHOD AND DEVICE FOR REGULATING OR CONTROLLING THE THERMAL LEVEL OF A POWDER SOLID COMPRISING A HEAT EXCHANGER WITH FLUIDIZED OR MOBILE BED COMPARTMENTS |
FR8913128A FR2652891B2 (en) | 1989-06-16 | 1989-10-05 | METHOD AND DEVICE FOR REGULATING OR CONTROLLING THE THERMAL LEVEL OF A POWDER SOLID COMPRISING A HEAT EXCHANGER WITH FLUIDIZED OR MOBILE BED COMPARTMENTS. |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2652891A2 true FR2652891A2 (en) | 1991-04-12 |
FR2652891B2 FR2652891B2 (en) | 1995-04-14 |
Family
ID=26227407
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR8913128A Expired - Lifetime FR2652891B2 (en) | 1989-06-16 | 1989-10-05 | METHOD AND DEVICE FOR REGULATING OR CONTROLLING THE THERMAL LEVEL OF A POWDER SOLID COMPRISING A HEAT EXCHANGER WITH FLUIDIZED OR MOBILE BED COMPARTMENTS. |
Country Status (1)
Country | Link |
---|---|
FR (1) | FR2652891B2 (en) |
-
1989
- 1989-10-05 FR FR8913128A patent/FR2652891B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
FR2652891B2 (en) | 1995-04-14 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2304128A (en) | Fluid catalyst process and apparatus | |
US4088568A (en) | Catalytic cracking of hydrocarbons | |
US4439533A (en) | Fluid particle backmixed cooling process | |
US4615992A (en) | Catalyst regeneration process with improved catalyst distribution in a fluidized bed | |
US2383636A (en) | Temperature control of catalytic reactions | |
US2390708A (en) | Regenerating contact material | |
US2584391A (en) | Apparatus for effecting fluidized contact between solid particles and fluid mediums | |
KR100247678B1 (en) | Process and apparatus for regenerating cokes deposited- catalyst within flidized layer | |
CA2019103C (en) | Bulk solid temperature or regulating process by means of a fluidized or mobile bed multicompartmented heat exchanger | |
JPH10503545A (en) | FCC catalyst stripper | |
US2386491A (en) | Process for the regeneration of contact materials | |
US2389236A (en) | Catalytic conversion system | |
US3843330A (en) | Regeneration apparatus | |
US2607662A (en) | Stripper for subdivided catalyst particles | |
US8387645B2 (en) | Methods and apparatus for contacting a fluid stream with particulate solids | |
US2385189A (en) | Catalytic reactor | |
US2477751A (en) | Apparatus for suspended catalyst operations | |
US2427112A (en) | Conversion of hydrocarbon oils | |
US2804368A (en) | Fluidized bed catalyst process and apparatus for reaction of hydrocarbons | |
US3198729A (en) | Continuous conversion of hydrocarbons with sensitive catalyst | |
FR2652891A2 (en) | Method and device for regulation or control of the level of heat of a pulverulent solid, including a heat exchanger with fluidised or mobile bed compartments | |
US3309784A (en) | Apparatus for contacting fluidizable solids with gasiform fluids | |
US3629143A (en) | Regenerator for metal halide sludge catalyst | |
US2471085A (en) | Fluid catalyst process for the conversion of hydrocarbons | |
US2799359A (en) | Contacting solids and gases |