GB1410201A - Centrifugal ore concentration - Google Patents

Centrifugal ore concentration

Info

Publication number
GB1410201A
GB1410201A GB5146372A GB5146372A GB1410201A GB 1410201 A GB1410201 A GB 1410201A GB 5146372 A GB5146372 A GB 5146372A GB 5146372 A GB5146372 A GB 5146372A GB 1410201 A GB1410201 A GB 1410201A
Authority
GB
United Kingdom
Prior art keywords
slurry
ore
passage
shaft
interior
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
GB5146372A
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.)
Deringer D C
Original Assignee
Deringer D C
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 Deringer D C filed Critical Deringer D C
Publication of GB1410201A publication Critical patent/GB1410201A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B5/00Other centrifuges
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B5/00Other centrifuges
    • B04B5/04Radial chamber apparatus for separating predominantly liquid mixtures, e.g. butyrometers
    • B04B5/0442Radial chamber apparatus for separating predominantly liquid mixtures, e.g. butyrometers with means for adding or withdrawing liquid substances during the centrifugation, e.g. continuous centrifugation
    • B04B2005/0457Radial chamber apparatus for separating predominantly liquid mixtures, e.g. butyrometers with means for adding or withdrawing liquid substances during the centrifugation, e.g. continuous centrifugation having three-dimensional spirally wound separation channels

Landscapes

  • Centrifugal Separators (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

1410201 Centrifugal ore concentration D C DERINGER 8 Nov 1972 [13 Dec 1971] 51463/ 72 Heading B2P An ore is concentrated by feeding a slurry of the ore through a hollow helicoidal member rotating about its longitudinal axis, whereby a density distribution of particles in the slurry is formed across the width of the interior of the member, and a fraction of the slurry containing concentrated ore particles is tapped off from the outer periphery of the interior of the member whilst the latter is rotated. An ore concentrator, Fig. 1 comprises a pump 12, preferably of the pulsating type, which feeds the ore slurry under pressure via a surge chamber 42 to the upper end of a hollow shaft 26 which is rotated by a motor 54 through a belt and pulley arrangement. Alternatively the slurry may be fed to the shaft by gravity. The shaft 26 consists of sections 48, 116, 114, 118 and 62. The section 114 is in the form of a frusto-conical drum Fig. 4, which does not communicate with the sections 116 and 118 and which carries a hollow helicoidal member 88 to form a centrifuge subassembly 44. The slurry flows through an opening 122 in shaft section 116 via a curved tube 126 to the interior of the member 88 where fractionation of the particles take place by centrifugal force. The member 88 may be in the form of a helicoidal tube but preferably it comprises a plurality of hollow ceramic blocks 140 of trapezoidal cross-section, Figs. 5 and 6, each having a triangularly shaped opening 142 therein, the openings 142 defining a helicoidal passage 94 when the blocks are connected in end to end relation by a cable or rod extending through aligned openings 150 through the wall of the blocks. The blocks are wrapped with glass fibre tape 152. At one or more points along the inner periphery of the passage 94 there is provided a flow-divider 132, Fig. 5, which deflects an outer branch of the slurry stream containing ore concentrate into a discharge branch 134 connected by a tube 90 (92) rotatable with the member 88 to a compartment 76 (78) of a concentrate launder subassembly 68 secured to the frame 30 of the concentrator. The inner branch of the slurry stream containing the tailings is discharged via a drain tube 96 which is connected to the outlet end of the passage 94 in the member 88 and which opens into a tailings launder 98 secured to the frame 30. Water from a line 40 may be fed via a stuffing box 34 to the interior of the shaft sections 62, 118 and through a supply line 112 helically arranged around the drum 114 and enters the passage 94 in the member 88 in the same direction as the slurry via tapping tubes 120a. 120b, 120c, connected between the line 112 and the member 88. The water may be used to dilute the slurry or for introducing additives therein. Alternatively a solvent may be introduced through the line 112 if blockage of the passage 94 occurs.
GB5146372A 1971-12-13 1972-11-08 Centrifugal ore concentration Expired GB1410201A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US20738671A 1971-12-13 1971-12-13

Publications (1)

Publication Number Publication Date
GB1410201A true GB1410201A (en) 1975-10-15

Family

ID=22770332

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5146372A Expired GB1410201A (en) 1971-12-13 1972-11-08 Centrifugal ore concentration

Country Status (5)

Country Link
US (1) US3786919A (en)
JP (1) JPS4866504A (en)
CA (1) CA979397A (en)
DE (1) DE2256860A1 (en)
GB (1) GB1410201A (en)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3877634A (en) * 1973-05-25 1975-04-15 Du Pont Cell washing centrifuge apparatus and system
SE440071B (en) * 1979-08-17 1985-07-15 Scania Dental Centrifuge type apparatus for separating solid particles from the waste water
US4741537A (en) * 1985-09-03 1988-05-03 Adam Alvin R Teeing device
US5656163A (en) 1987-01-30 1997-08-12 Baxter International Inc. Chamber for use in a rotating field to separate blood components
US5792372A (en) * 1987-01-30 1998-08-11 Baxter International, Inc. Enhanced yield collection systems and methods for obtaining concentrated platelets from platelet-rich plasma
US5370802A (en) * 1987-01-30 1994-12-06 Baxter International Inc. Enhanced yield platelet collection systems and methods
DE3734776C1 (en) * 1987-10-14 1989-03-23 Hans-Juergen Dipl-Chem D Kraus Centrifuge for continuously separating a mixture
WO1993012887A1 (en) * 1991-12-23 1993-07-08 Baxter International Inc. Centrifugal processing system with direct access drawer
US6007725A (en) * 1991-12-23 1999-12-28 Baxter International Inc. Systems and methods for on line collection of cellular blood components that assure donor comfort
US5804079A (en) * 1991-12-23 1998-09-08 Baxter International Inc. Systems and methods for reducing the number of leukocytes in cellular products like platelets harvested for therapeutic purposes
WO1993012888A1 (en) * 1991-12-23 1993-07-08 Baxter International Inc. Centrifuge with separable bowl and spool elements providing access to the separation chamber
US5549834A (en) * 1991-12-23 1996-08-27 Baxter International Inc. Systems and methods for reducing the number of leukocytes in cellular products like platelets harvested for therapeutic purposes
US5427695A (en) * 1993-07-26 1995-06-27 Baxter International Inc. Systems and methods for on line collecting and resuspending cellular-rich blood products like platelet concentrate
US5525218A (en) * 1993-10-29 1996-06-11 Baxter International Inc. Centrifuge with separable bowl and spool elements providing access to the separation chamber
JP4836270B2 (en) * 2006-03-31 2011-12-14 独立行政法人産業技術総合研究所 Fine particle classification method and apparatus
DE102010052301A1 (en) 2010-11-23 2012-05-24 Gea Mechanical Equipment Gmbh Process for processing a product in a centrifugal field
CN103301659B (en) * 2013-05-16 2015-04-15 山东莱芜煤矿机械有限公司 Material stabilization device of concentrator

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2730299A (en) * 1953-11-27 1956-01-10 Combined Metals Reduction Comp Coiled tube continuous centrifuge
GB873494A (en) * 1957-03-08 1961-07-26 Selahaddin Rastgeldi Method and means for centrifuging
US3628343A (en) * 1968-10-04 1971-12-21 Harold M Bradbury Method for rotational energy exchange crystallization and material separation

Also Published As

Publication number Publication date
JPS4866504A (en) 1973-09-12
DE2256860A1 (en) 1973-06-20
CA979397A (en) 1975-12-09
US3786919A (en) 1974-01-22

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee