GB822856A - Process for separating magnetisable particles from contaminating non-magnetisable particles, present in suspension - Google Patents
Process for separating magnetisable particles from contaminating non-magnetisable particles, present in suspensionInfo
- Publication number
- GB822856A GB822856A GB24612/57A GB2461257A GB822856A GB 822856 A GB822856 A GB 822856A GB 24612/57 A GB24612/57 A GB 24612/57A GB 2461257 A GB2461257 A GB 2461257A GB 822856 A GB822856 A GB 822856A
- Authority
- GB
- United Kingdom
- Prior art keywords
- separator
- suspension
- tank
- screen
- magnetic
- 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
- B03B5/28—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
- B03B5/30—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions
- B03B5/44—Application of particular media therefor
- B03B5/447—Application of particular media therefor recovery of heavy media
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Filtration Of Liquid (AREA)
Abstract
822,856. Filters. STAMICARBON N. V. Aug. 2, 1957 [Aug. 4, 1956], No. 24612/57. Class 46. [Also in Group II] Raw coal is separ ated, by means of a magnetite suspension in a separator 1, intc washed coal and shale. The coal fraction with some sepa rating suspension leaves at B and passes across a screen 2, the suspension dripping through and being collected in a tank 3 for return to the separator by a pump 4. The fraction is then passed across a screen 5 where it is cleaned by water sprays 6, 7 before being discharged at D. The shale, which leaves the separator 1 at C, undergoes similar treatment and is discharged at E ; the screens 2, 5 may be of the vibrating type with a mesh of 1mm. The dilute suspension passing through the screens 5 is collected in a tank 8 and supplied by means of a pump 9 to a curved screen 10 consisting of spaced bars having gaps of 0À5 mm. between them. 90% of the magnetite contained in the dilute suspension is collected in a tank 11 beneath the screen 10 and is then passed to a magnetic separator 12 from which a concentrated magnetic suspension is pumped to the collecting tank 3 via a demagnetising coil 14. This suspension together with that from the screens 2 is then pumped to the separator 1. Alternatively, the suspension from magnetic separator 12 may be pumped direct to the separator 1. Water may be added to the separator 1 at G. In the separator 12 also, a dilute non-magnetic fraction which contains only non-magnetisable particles smaller than 0À25 mm. is separated out and supplied to a tank 15 which also receives the overflow fraction from the screen 10 consisting mainly of the non- magnetisable particles larger than the magnetite. The fractions collected in the tank 15 are pumped into a hydrocyclone thickener 17 from which the clarified overflow is led to the sprays 6 and the apex discharge is treated in a second magnetic separator 18. The separated magnetic fraction is returned to the tank 8 and the non-magnetic fraction leaves the system at F. In place of the screen 10, a cyclone separator or a group thereof may be used. Specifications 791,520, 791,857, 791,858 and 791,859 are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL822856X | 1956-08-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB822856A true GB822856A (en) | 1959-11-04 |
Family
ID=19840925
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB24612/57A Expired GB822856A (en) | 1956-08-04 | 1957-08-02 | Process for separating magnetisable particles from contaminating non-magnetisable particles, present in suspension |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB822856A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3687284A (en) * | 1969-11-19 | 1972-08-29 | Stamicarbon | Reconditioning of suspensions used in the separation of minerals |
GB2231505A (en) * | 1989-05-18 | 1990-11-21 | Young Jayne | Separating farm slurry |
US7785474B2 (en) | 2004-12-15 | 2010-08-31 | Orica Australia Pty Ltd | Method for contacting liquid with ion exchange resin |
CN108998102A (en) * | 2018-08-21 | 2018-12-14 | 石宏扬 | A kind of coal chemical industry rough coal gas separating system |
-
1957
- 1957-08-02 GB GB24612/57A patent/GB822856A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3687284A (en) * | 1969-11-19 | 1972-08-29 | Stamicarbon | Reconditioning of suspensions used in the separation of minerals |
GB2231505A (en) * | 1989-05-18 | 1990-11-21 | Young Jayne | Separating farm slurry |
GB2231505B (en) * | 1989-05-18 | 1993-03-10 | Young Jayne | Flowable material treatment |
US7785474B2 (en) | 2004-12-15 | 2010-08-31 | Orica Australia Pty Ltd | Method for contacting liquid with ion exchange resin |
US9011693B2 (en) | 2004-12-15 | 2015-04-21 | Orica Australia Pty Ltd | Water polishing process |
CN108998102A (en) * | 2018-08-21 | 2018-12-14 | 石宏扬 | A kind of coal chemical industry rough coal gas separating system |
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