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GB465126A - Improvements in or relating to the separation of solid materials of different specific gravities - Google Patents

Improvements in or relating to the separation of solid materials of different specific gravities

Info

Publication number
GB465126A
GB465126A GB30102/35A GB3010235A GB465126A GB 465126 A GB465126 A GB 465126A GB 30102/35 A GB30102/35 A GB 30102/35A GB 3010235 A GB3010235 A GB 3010235A GB 465126 A GB465126 A GB 465126A
Authority
GB
United Kingdom
Prior art keywords
medium
vessels
separating
sink
vessel
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
Application number
GB30102/35A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of GB465126A publication Critical patent/GB465126A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/62Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type
    • B03B5/623Upward current classifiers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/28Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
    • B03B5/30Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions
    • B03B5/36Devices therefor, other than using centrifugal force

Landscapes

  • Extraction Or Liquid Replacement (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

465,126. Separating solid materials. VOOYS, G. J. DE. Oct. 31, 1935, No. 30102. Convention date, Oct. 31, 1934. [Classes 82 (ii) and 117] The sink material from a sink and float separation in a fluid separating medium of higher density than water is separated into fractions of different specific gravities by subjecting it to current treatment in a stream of the same separating medium which is in communication with but operates independently of the main body of the medium used in the initial sink and float separation. A plurality of streams, in series or in parallel, may be employed so that the sink material from the initial separation is separated into more than two fractions. The separating medium may be a solution, a suspension of solids in liquid, e.g. sand in water or a sludge of clay, barytes, and water, or it may be a suspension of solids in gas, e.g. sand in air. The streams used in the current treatment preferably move in closed circuits. The apparatus shown comprises a vessel A in which the initial sink and float treatment is carried out and a delivery vessel D for the heaviest product. These vessels contain separating medium in a substantially static condition, though small currents, preferably controlled by means of adjustable overflows, may exist due to the supply of medium to replace that removed with the separated fractions or due to the recirculation of small quantities of overflowing medium. The lightest material floats in the vessel A and is drawn off by any known means. Between the vessels A and D is provided a vessel comprising tubes B and C, to which the sink material from A passes through a connection E. An upward current of medium is produced in one of the tubes, e.g. the tube B, by any suitable means, for example a screw propeller e, a pump, a turbine, or compressed air. The lighter part of the sink material is carried up the tube B and removed by any suitable means, the liquid passing into the tube C through the connection F, and the heavier fraction sinks into the well H of the delivery vessel D. A plurality of closed circuit separating vessels may be arranged in series or in parallel between the vessels A and D, the currents in the several vessels having uniform velocities of different magnitudes. The upward-current separators may, if desired, be replaced by separating vessels utilizing horizontal currents.
GB30102/35A 1934-10-31 1935-10-31 Improvements in or relating to the separation of solid materials of different specific gravities Expired GB465126A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE465126X 1934-10-31

Publications (1)

Publication Number Publication Date
GB465126A true GB465126A (en) 1937-04-30

Family

ID=6540350

Family Applications (1)

Application Number Title Priority Date Filing Date
GB30102/35A Expired GB465126A (en) 1934-10-31 1935-10-31 Improvements in or relating to the separation of solid materials of different specific gravities

Country Status (1)

Country Link
GB (1) GB465126A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2474774A (en) * 1945-06-01 1949-06-28 American Cyanamid Co Heavy-media separation apparatus
US2545517A (en) * 1946-02-27 1951-03-20 Blue Channel Corp Apparatus for the recovery of crab meat from bony material by gravity liquid separation
US2563332A (en) * 1949-05-10 1951-08-07 Charles B Hebbard Apparatus for multiple separation in heavy density mediae
US2620069A (en) * 1948-10-19 1952-12-02 Karl R Wendt Method of and apparatus for separating materials of different specific gravity
CN111442173A (en) * 2020-05-14 2020-07-24 中海油能源发展股份有限公司工程技术分公司 Automatic separation equipment for light and heavy minerals

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2474774A (en) * 1945-06-01 1949-06-28 American Cyanamid Co Heavy-media separation apparatus
US2545517A (en) * 1946-02-27 1951-03-20 Blue Channel Corp Apparatus for the recovery of crab meat from bony material by gravity liquid separation
US2620069A (en) * 1948-10-19 1952-12-02 Karl R Wendt Method of and apparatus for separating materials of different specific gravity
US2563332A (en) * 1949-05-10 1951-08-07 Charles B Hebbard Apparatus for multiple separation in heavy density mediae
CN111442173A (en) * 2020-05-14 2020-07-24 中海油能源发展股份有限公司工程技术分公司 Automatic separation equipment for light and heavy minerals

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