GB834455A - Improvements in apparatus for dense-phase fluidization - Google Patents
Improvements in apparatus for dense-phase fluidizationInfo
- Publication number
- GB834455A GB834455A GB1692/57A GB169257A GB834455A GB 834455 A GB834455 A GB 834455A GB 1692/57 A GB1692/57 A GB 1692/57A GB 169257 A GB169257 A GB 169257A GB 834455 A GB834455 A GB 834455A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- dust
- flared portion
- tube
- gas
- 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.)
- Expired
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
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- 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
- B01J8/245—Spouted-bed technique
-
- 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
- B01J8/44—Fluidisation grids
-
- 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
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00761—Discharging
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
An apparatus for carrying out a fluidized bed process comprises a lower flared portion 3, Fig. 1, forming an intake for a part of the fluidizing medium, the upper part of the flared portion being spaced from the walls of the main part of the apparatus, the space being bridged <PICT:0834455/III/1> <PICT:0834455/III/2> by a grate 6 which slopes from the walls downwardly towards the flared portion. The grate may be formed by radial or concentric members having overlapping portions, so that fine particles are prevented from passing into the chamber 7. The fluidizing medium which enters through pipe 5 may have a different ratio of air to steam oxygen to steam or oxygen to carbon dioxide from that which is passed through line 2. A Venturi 4 may be interposed between line 2 and flared portion 3. Gas passing from the chamber 8 may be passed through pipe 21, Fig. 4, into a cyclone separator 50, the clean gas passing out through pipe 22 whilst the dust falls down tube 23. An inert gas or gas manufactured in the apparatus and extracted by compressor 25 after cooling, is fed at 24 into tube 23 to maintain the dust in a slightly fluidized state. After passing through valve 26 into chamber 27, the dust meets gasifying agents arriving through tube 28. These carry the dust through tube 29, 2a back into the chamber 8. The apparatus may be used for the production of hydrogen from producer gas containing steam by reduction with iron which may be produced by reducing iron oxide with producer gas. Specification 723,332, Swiss Specifications 292,727, 292,859, and French Specification 1,050,572 are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR834455X | 1956-01-19 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB834455A true GB834455A (en) | 1960-05-11 |
Family
ID=9297112
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1692/57A Expired GB834455A (en) | 1956-01-19 | 1957-01-16 | Improvements in apparatus for dense-phase fluidization |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB834455A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4045005A (en) * | 1974-12-13 | 1977-08-30 | General Atomic Company | Blending device |
GB2133716A (en) * | 1983-01-11 | 1984-08-01 | Coal Ind | Classifying material withdrawn from fluidised bed |
US5213768A (en) * | 1987-06-30 | 1993-05-25 | Bp Chemicals Ltd. | Fluidized bed apparatus and process for feeding gas to a fluidized bed apparatus |
US5513445A (en) * | 1993-01-13 | 1996-05-07 | Fasti Farrag & Stipsits Gmbh | Method of operating a drier for powdered, granulated and pourable materials and a drier operating in accordance with the method |
FR2805178A1 (en) * | 2000-02-21 | 2001-08-24 | Westinghouse Electric Cy Llc | FLUIDIZED BED REACTOR |
WO2002036256A1 (en) * | 2000-10-31 | 2002-05-10 | Huettlin Herbert | Device for treating particulate material |
WO2013104834A1 (en) | 2012-01-13 | 2013-07-18 | Carbona Oy | Grid for a fluidized bed gasifier |
-
1957
- 1957-01-16 GB GB1692/57A patent/GB834455A/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4045005A (en) * | 1974-12-13 | 1977-08-30 | General Atomic Company | Blending device |
GB2133716A (en) * | 1983-01-11 | 1984-08-01 | Coal Ind | Classifying material withdrawn from fluidised bed |
US5213768A (en) * | 1987-06-30 | 1993-05-25 | Bp Chemicals Ltd. | Fluidized bed apparatus and process for feeding gas to a fluidized bed apparatus |
US5513445A (en) * | 1993-01-13 | 1996-05-07 | Fasti Farrag & Stipsits Gmbh | Method of operating a drier for powdered, granulated and pourable materials and a drier operating in accordance with the method |
FR2805178A1 (en) * | 2000-02-21 | 2001-08-24 | Westinghouse Electric Cy Llc | FLUIDIZED BED REACTOR |
WO2002036256A1 (en) * | 2000-10-31 | 2002-05-10 | Huettlin Herbert | Device for treating particulate material |
WO2013104834A1 (en) | 2012-01-13 | 2013-07-18 | Carbona Oy | Grid for a fluidized bed gasifier |
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