GB1015812A - Improvements relating to the treatment of particulate material, to separate components of different specific gravities - Google Patents
Improvements relating to the treatment of particulate material, to separate components of different specific gravitiesInfo
- Publication number
- GB1015812A GB1015812A GB3641963A GB3641963A GB1015812A GB 1015812 A GB1015812 A GB 1015812A GB 3641963 A GB3641963 A GB 3641963A GB 3641963 A GB3641963 A GB 3641963A GB 1015812 A GB1015812 A GB 1015812A
- Authority
- GB
- United Kingdom
- Prior art keywords
- specific gravity
- flow rate
- fluidized bed
- bed
- mass flow
- 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
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B4/00—Separating by pneumatic tables or by pneumatic jigs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B4/00—Separating by pneumatic tables or by pneumatic jigs
- B03B4/005—Separating by pneumatic tables or by pneumatic jigs the currents being pulsating, e.g. pneumatic jigs; combination of continuous and pulsating currents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B4/00—Separating by pneumatic tables or by pneumatic jigs
- B03B4/06—Separating by pneumatic tables or by pneumatic jigs using fixed and inclined tables ; using stationary pneumatic tables, e.g. fluidised beds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/28—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
- B03B5/46—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using dry heavy media; Devices therefor
Landscapes
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
1,015,812. Pneumatic separators. HEAD WRIGHTSON & CO. Ltd. Sept. 8, 1964 [Sept. 16, 1963], No. 36419/63. Heading B2H. [Also in Division F4] Components of different specific gravities are separated from particulate material, e.g. small coal, by delivering the material into a fluidized bed of discrete solid particles comprising an exogenous medium composed of controlled proportions of at least two materials of markedly different specific gravities, and by maintaining the bed in fluidized condition by a gaseous medium applied thereto in such a manner as to give, and retain in, the bed a specific gravity effective to cause separation of the particulate material into two fractions of different specific gravities, continuous measurement of the effective specific gravity of the fluidized bed being made. The fluidized bed materials may be selected from sand, magnetite and ferrosilicon. The gaseous medium may be in the form of a hot or unheated gas and may be applied to the bed in a continuous or pulsed manner. The apparatus, which may also serve to dry the particulate material, is substantially as described in Fig. 7 of Specification 971,583 with the following modifications: (i) The gas supply for feed line 13 is combustion gases from a furnace 17 whereas that for feed lines 12 and 15 is air supplied from a blower 23 and heated in a heat exchanger 22 by the combustion gases. The line 15 may have an independent air supply. The line 51 is a bypass for air not passed along the lines 12, 15. (ii) Only one cyclone 21 is used to separate dust from the hot gas. (iii) Bunkers 40, 42 serve to supply the fluidized bed materials (in this case two) to the hopper 38 via feed control devices 43, 44, e.g. rotary seals or electromagnetically vibrated feeders. The devices 43, 44 are in turn controlled through a mass flow rate indicator 45. In operation, the mass flow rate of fluidizing gas lies within predetermined limits and the devices 43, 44 are set to deliver from the bunkers 40, 42 the necessary proportions of materials to maintain the bed at the required specific gravity. When dip-tubes 27 detect an increase or decrease in the specific gravity, a controller 26 causes the valve 25 respectively to open or close in order to vary the flow rate of fluidizing gas so as to restore the specific gravity to its desired value. If, in order to maintain the desired specific gravity, the mass flow rate of gas has been automatically reduced below, or increased above, the predetermined limits, as the indicator 45 moves below the lower control limit, or above the upper control limit, a control signal automatically actuates the feed control device 43 and/or device 44 to vary the relative proportions of the fluidized bed materials thereby requiring an increased or decreased mass flow rate of fluidizing gas to produce the required specific gravity. As soon as the mass flow rate has increased above the lower control limit or decreased below the upper control limit, the devices 43, 44 revert to their original settings. The hopper 38 may be equipped with upper and lower level controllers which, by automatic control of the devices 43, 44, ensure that the necessary amount of fluidized bed particles is present in the circuit.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE653141D BE653141A (en) | 1963-09-16 | ||
GB3641963A GB1015812A (en) | 1963-09-16 | 1963-09-16 | Improvements relating to the treatment of particulate material, to separate components of different specific gravities |
NL6410307A NL6410307A (en) | 1963-09-16 | 1964-09-04 | |
FR988170A FR1413226A (en) | 1963-09-16 | 1964-09-15 | Improvements in methods and apparatus for separating material into fractions of different respective densities |
DEP1272A DE1272251B (en) | 1963-09-16 | 1964-09-15 | Method and device for sorting grainy material based on the density differences in the grain composition of the feed material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3641963A GB1015812A (en) | 1963-09-16 | 1963-09-16 | Improvements relating to the treatment of particulate material, to separate components of different specific gravities |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1015812A true GB1015812A (en) | 1966-01-05 |
Family
ID=10387968
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3641963A Expired GB1015812A (en) | 1963-09-16 | 1963-09-16 | Improvements relating to the treatment of particulate material, to separate components of different specific gravities |
Country Status (5)
Country | Link |
---|---|
BE (1) | BE653141A (en) |
DE (1) | DE1272251B (en) |
FR (1) | FR1413226A (en) |
GB (1) | GB1015812A (en) |
NL (1) | NL6410307A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DK154955B (en) * | 1975-12-09 | 1989-01-09 | Richter Gedeon Vegyeszet | PROCEDURE AND APPARATUS FOR FLUIDIZATION, PRINCIPLES FOR DRYING OF GOODS |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1587201A (en) * | 1976-07-16 | 1981-04-01 | Exxon Research Engineering Co | Utilisation of solid material containing combustible matter |
JPS58115047A (en) * | 1981-12-28 | 1983-07-08 | 石川島播磨重工業株式会社 | Powder raw material baking equipment |
CN108296007B (en) * | 2018-02-07 | 2023-01-20 | 唐山开远科技有限公司 | Fluidized bed drying separator and complete equipment matched with same |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1001570B (en) * | 1957-01-24 | The Dorr Company Stamford, Conn (V St A) | Device for treating finely divided solid particles in a fluidized bed process |
-
0
- BE BE653141D patent/BE653141A/xx unknown
-
1963
- 1963-09-16 GB GB3641963A patent/GB1015812A/en not_active Expired
-
1964
- 1964-09-04 NL NL6410307A patent/NL6410307A/xx unknown
- 1964-09-15 FR FR988170A patent/FR1413226A/en not_active Expired
- 1964-09-15 DE DEP1272A patent/DE1272251B/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DK154955B (en) * | 1975-12-09 | 1989-01-09 | Richter Gedeon Vegyeszet | PROCEDURE AND APPARATUS FOR FLUIDIZATION, PRINCIPLES FOR DRYING OF GOODS |
Also Published As
Publication number | Publication date |
---|---|
NL6410307A (en) | 1965-03-17 |
DE1272251B (en) | 1968-07-11 |
BE653141A (en) | |
FR1413226A (en) | 1965-10-08 |
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