OA06340A - Improved device for heat exchange between solid particles and a gas stream. - Google Patents
Improved device for heat exchange between solid particles and a gas stream.Info
- Publication number
- OA06340A OA06340A OA56899A OA56899A OA06340A OA 06340 A OA06340 A OA 06340A OA 56899 A OA56899 A OA 56899A OA 56899 A OA56899 A OA 56899A OA 06340 A OA06340 A OA 06340A
- Authority
- OA
- OAPI
- Prior art keywords
- support
- heat exchange
- solid particles
- stack
- gas stream
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C3/00—Other direct-contact heat-exchange apparatus
- F28C3/10—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
- F28C3/12—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
- F28C3/16—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid the particulate material forming a bed, e.g. fluidised, on vibratory sieves
-
- 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
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/12—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow
- B01J8/125—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow with multiple sections one above the other separated by distribution aids, e.g. reaction and regeneration sections
-
- 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
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/34—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with stationary packing material in the fluidised bed, e.g. bricks, wire rings, baffles
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/19—Details relating to the geometry of the reactor
- B01J2219/194—Details relating to the geometry of the reactor round
- B01J2219/1941—Details relating to the geometry of the reactor round circular or disk-shaped
- B01J2219/1946—Details relating to the geometry of the reactor round circular or disk-shaped conical
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Gas Burners (AREA)
- Carbon And Carbon Compounds (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)
Abstract
1. A device for heat exchange by direct contact of solid particles flowing under gravity and a gaseous stream ascending in a column comprising at least one stage (12) formed of a stack (12a) of packing elements arranged on a support (12b), the device being characterized in that so that a dense fluidized bed is not formed in contact with said support (12b), the opening ratio of the support (12b) is equal to at least 75 % of the porosity of the stack (12a) of packing elements, the loss of pressure of the gaseous stream through this support (12b) being negligible in relation to that through the stack (12a) and the mean velocity of the gaseous stream in the stage (12a) being from 1 to 1.5 times the mean velocity in free fall of the particles.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7827057A FR2436954A1 (en) | 1978-09-21 | 1978-09-21 | IMPROVED THERMAL EXCHANGE DEVICE BETWEEN SOLID PARTICLES AND A GAS CURRENT |
Publications (1)
Publication Number | Publication Date |
---|---|
OA06340A true OA06340A (en) | 1981-06-30 |
Family
ID=9212872
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
OA56899A OA06340A (en) | 1978-09-21 | 1979-09-18 | Improved device for heat exchange between solid particles and a gas stream. |
Country Status (10)
Country | Link |
---|---|
EP (1) | EP0009455B1 (en) |
JP (1) | JPS5543399A (en) |
AT (1) | ATE6441T1 (en) |
AU (1) | AU531780B2 (en) |
BR (1) | BR7905981A (en) |
CA (1) | CA1140732A (en) |
DE (1) | DE2966725D1 (en) |
ES (1) | ES8100477A1 (en) |
FR (1) | FR2436954A1 (en) |
OA (1) | OA06340A (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2452689A1 (en) * | 1979-03-27 | 1980-10-24 | Saint Gobain | PROCESS FOR RECOVERING HEAT FROM FUMES |
FR2486817B1 (en) * | 1980-07-15 | 1985-11-08 | Tunzini Nessi Equip | GAS PURIFICATION PROCESS AND INSTALLATION FOR ITS IMPLEMENTATION |
JPS57174093A (en) * | 1981-04-21 | 1982-10-26 | Syst Nogyo Center:Kk | Methane fermentation method and apparatus |
FR2535734B1 (en) * | 1982-11-05 | 1986-08-08 | Tunzini Nessi Entreprises Equi | METHOD FOR GASIFICATION OF LIGNOCELLULOSIC PRODUCTS AND DEVICE FOR IMPLEMENTING SAME |
CN109556428A (en) * | 2018-12-19 | 2019-04-02 | 中冶焦耐(大连)工程技术有限公司 | A kind of gas-solid heat exchange device and heat-exchange method increasing high-temperature particle bed of material voidage |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB676613A (en) * | 1947-02-14 | 1952-07-30 | Standard Oil Dev Co | An improved process for contacting finely divided solid particles with gases |
LU29320A1 (en) * | 1947-12-29 | |||
US2774661A (en) * | 1951-08-07 | 1956-12-18 | Dorr Co | Method of heat-treating fines in a coarse solids fluidized bed |
DE1667329A1 (en) * | 1964-12-16 | 1971-06-09 | Universal Oil Prod Co | Process for bringing about countercurrent contact between a gas flow and a liquid flow |
FR1469109A (en) * | 1965-12-27 | 1967-02-10 | Saint Gobain | Intermediate product for the manufacture of glass and other silicates, and process and apparatus for its manufacture |
DE1935214A1 (en) * | 1969-07-11 | 1971-01-14 | Metallgesellschaft Ag | Method and apparatus for producing fine-grain coke |
BE758006A (en) * | 1970-06-12 | 1971-04-01 | Brauer Heinz | PROCEDURE FOR STARTING A SWIRL LAYER REACTOR |
JPS543126Y2 (en) * | 1975-11-17 | 1979-02-13 |
-
1978
- 1978-09-21 FR FR7827057A patent/FR2436954A1/en active Granted
-
1979
- 1979-09-18 OA OA56899A patent/OA06340A/en unknown
- 1979-09-19 AU AU50973/79A patent/AU531780B2/en not_active Ceased
- 1979-09-19 JP JP11946779A patent/JPS5543399A/en active Granted
- 1979-09-19 BR BR7905981A patent/BR7905981A/en not_active IP Right Cessation
- 1979-09-20 CA CA000336037A patent/CA1140732A/en not_active Expired
- 1979-09-20 ES ES484331A patent/ES8100477A1/en not_active Expired
- 1979-09-21 EP EP79400670A patent/EP0009455B1/en not_active Expired
- 1979-09-21 DE DE7979400670T patent/DE2966725D1/en not_active Expired
- 1979-09-21 AT AT79400670T patent/ATE6441T1/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
AU531780B2 (en) | 1983-09-08 |
EP0009455B1 (en) | 1984-02-29 |
AU5097379A (en) | 1980-03-27 |
CA1140732A (en) | 1983-02-08 |
ES484331A0 (en) | 1980-11-01 |
FR2436954A1 (en) | 1980-04-18 |
DE2966725D1 (en) | 1984-04-05 |
ATE6441T1 (en) | 1984-03-15 |
ES8100477A1 (en) | 1980-11-01 |
BR7905981A (en) | 1980-05-27 |
JPS5543399A (en) | 1980-03-27 |
FR2436954B1 (en) | 1981-04-17 |
JPH0159519B2 (en) | 1989-12-18 |
EP0009455A1 (en) | 1980-04-02 |
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