GB1000717A - Process for the centrifugal separation of minerals - Google Patents
Process for the centrifugal separation of mineralsInfo
- Publication number
- GB1000717A GB1000717A GB1932764A GB1932764A GB1000717A GB 1000717 A GB1000717 A GB 1000717A GB 1932764 A GB1932764 A GB 1932764A GB 1932764 A GB1932764 A GB 1932764A GB 1000717 A GB1000717 A GB 1000717A
- Authority
- GB
- United Kingdom
- Prior art keywords
- vessel
- slurry
- basket
- pipe
- heavier fractions
- 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
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/48—Washing granular, powdered or lumpy materials; Wet separating by mechanical classifiers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/12—Centrifuges in which rotors other than bowls generate centrifugal effects in stationary containers
Landscapes
- Centrifugal Separators (AREA)
- Paper (AREA)
Abstract
1,000,717. Centrifugal separators. BETEILIGUNGSUND PATENTVERWALTUNGS G.m.b.H. May 8, 1964 [May 11, 1963], No. 19327/64. Heading B2P. Fine-grained minerals are separated from a slurry by means of a collecting basket 2, Fig. 1, which rotates in a stationary vessel 1 containing the slurry and is provided on its inside with grooves in which the heavier fractions of the minerals separated by centrifugal force collect, the slurry being removed from the vessel after separation while the basket is rotating after which the heavier fractions are removed from the basket. The basket is mounted on a shaft 3 driven by a motor 4 and carrying at its lower end a stirrer 5 which produces rotation of the slurry in the vessel 1. Turbulence is produced in the stream of the rotating slurry by means of vertical baffle strips 6 fixedly arranged in the vessel 1. The slurry is fed from a tank 10 through a valve 11. A 3-way cock 12 serves to close the vessel outlet 9 or to connect it via a pipe 13 to a collecting tank for the heavier fractions or via a pipe 14 to a second vessel 1 situated at a lower level thereby to feed the latter by gravity with slurry discharged from the first vessel, the pipe 14 from the second vessel being connected to a third vessel or to a collecting tank. After discharge of the slurry from the vessel and before the heavier fractions are removed from the basket, the vessel is rinsed with clear water introduced through pipes 15, 16 and nozzles 17. The rinsing water may be recirculated into the vessel by connecting the pipe 13 via a pump to a return pipe. The heavier fractions may be removed from the grooves in the basket 2 by means of a scraping tool or, as shown, by means of spray water or compressed air supplied through a pipe 18 and nozzles 19. The basket 2 may rotate at a lower speed during removal of the heavier fractions. The vessel may be rinsed out with clear water after removal of the heavier fractions and the rinsing water directed to the collecting tank for heavier fractions. In Fig. 2, two pressure vessels 20 provided with lids 22 are arranged side by side on the same level. The slurry is forced from one vessel to the other by means of compressed air fed through a valve 23. A mushroom-shaped screening body is provided over the outlet 9 to prevent compressed air being blown straight into the pipe 26. The same slurry may be fed several times to the same vessel. In a modification of Fig. 2, the vessels have no baffle strips. In a further modification, the vessels 1 or 20 may be formed with an approximately horizontal bottom 28, Fig. 4, and with a tangential outlet 29 arranged in the direction of rotation of the rotating basket 2.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB71857A DE1177571B (en) | 1963-05-11 | 1963-05-11 | Process for centrifugal weight separation of minerals using a basket separator |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1000717A true GB1000717A (en) | 1965-08-11 |
Family
ID=6977205
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1932764A Expired GB1000717A (en) | 1963-05-11 | 1964-05-08 | Process for the centrifugal separation of minerals |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1177571B (en) |
GB (1) | GB1000717A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2121325A (en) * | 1982-06-07 | 1983-12-21 | Fsp | Cleaning centrifuge |
-
1963
- 1963-05-11 DE DEB71857A patent/DE1177571B/en active Pending
-
1964
- 1964-05-08 GB GB1932764A patent/GB1000717A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2121325A (en) * | 1982-06-07 | 1983-12-21 | Fsp | Cleaning centrifuge |
Also Published As
Publication number | Publication date |
---|---|
DE1177571B (en) | 1964-09-10 |
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