EP0123501B1 - Spiral separator incorporating a fluid deflector - Google Patents

Spiral separator incorporating a fluid deflector Download PDF

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Publication number
EP0123501B1
EP0123501B1 EP19840302608 EP84302608A EP0123501B1 EP 0123501 B1 EP0123501 B1 EP 0123501B1 EP 19840302608 EP19840302608 EP 19840302608 EP 84302608 A EP84302608 A EP 84302608A EP 0123501 B1 EP0123501 B1 EP 0123501B1
Authority
EP
European Patent Office
Prior art keywords
stream
spiral separator
separator according
deflector
trough
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
EP19840302608
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German (de)
French (fr)
Other versions
EP0123501A1 (en
Inventor
Philip John Giffard
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.)
Mineral Deposits Ltd
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Mineral Deposits Ltd
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 Mineral Deposits Ltd filed Critical Mineral Deposits Ltd
Priority claimed from AU27077/84A external-priority patent/AU575046B2/en
Publication of EP0123501A1 publication Critical patent/EP0123501A1/en
Application granted granted Critical
Publication of EP0123501B1 publication Critical patent/EP0123501B1/en
Expired legal-status Critical Current

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    • 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
    • B03B5/626Helical separators

Definitions

  • This invention relates to an improved spiral separator and to a method of spiral separation which is of particular use in the separation of minerals.
  • Spiral separators are extensively used for the wet gravity separation of solids according to their specific gravity, for example for separating various kinds of mineral sands from silica sands.
  • Such separators commonly comprise a vertical column about which there are supported one or more helical troughs.
  • a "pulp" or slurry of the materials to be separated and water is introduced to the upper end of a trough and as the pulp descends the helix, centrifugal forces act on the less dense particles in a radially outwards direction while the more dense particles segregate to the bottom of the flow and after slowing through close approach to the working surface of the trough gravitate towards the vertical column.
  • CA-A-961005 discloses a spiral separator in which fresh water from a separate channel of the trough is fed into the main channel of the trough to replace water which has been lost in extracting particulate material from the separator.
  • a spiral separator including at least one helical trough having a trough floor extending between an inner periphery and an outer periphery, said trough being arranged to receive a pulp stream of water and particles at its upper end and to separate particles of different densities as the stream moves downwardly along said trough, said separator being characterised by the inclusion of at least one deflector located adjacent said outer periphery and having at least one surface contoured for deflecting a portion of the low solids high velocity stream component in a fan-like spray from the outer periphery of the pulp stream back across said stream towards said inner periphery.
  • a method for rediluting a pulp stream flowing downwardly along the helical trough of a spiral separator comprising the deflection of a portion of the low solids high velocity stream component in a fan-like spray from the outer periphery of said pulp stream back across said stream towards its inner periphery.
  • an adjustable deflector is located on an outer wall of the helical trough to deflect the stream component in said fan-like spray. This is not the same mechanism as a normal wash water supply which is deliberately applied as small radial outflow across the segregated stream.
  • the spiral separator 1 includes helical trough 2 supported from a vertical column 3.
  • the helical trough 2 in cross-section comprises an upright inner wall 4, a support web 5 whereby the lip of the inner wall 4 is connected with the column 1, an upright outer wall 6 terminating in a lip 7 and a trough floor 8 extending between the inner wall 4 and the outer wall 6.
  • the trough working surface comprises an inner portion 9 and an outer portion 10 inclined at a greater angle to the helix radial direction and thus slopes more steeply upwardly and outwardly.
  • the profile of the bottom of the trough is such that the mass of water in the slurry moves radially outward and upward. This causes thinning of the water layer at the inner portion 11 of the flow and a water build-up at the low solids, high velocity stream at the flow periphery 12.
  • a deflector 13 is attached to the outer wall 6 to deflect a portion of the water from the flow periphery 12 into the inner portion 11 to reinstate the water quantities necessary to permit the designed separation mechanism to proceed.
  • the deflector 13 is adjustable by rotation about a radial axis 14 and has an under-surface 15 suitably contoured to deflect the water in a fan-like spray 16 across the trough.
  • the undersurface 15 is arcuate in contour when viewed in both radial and tangential directions with respect to the trough.
  • the deflector 13 preferably permits the stream to be rediluted to a considerable depth and across a broad band at the inner portion 9 of the trough floor.
  • the sharpened leading end 17 of the deflector 13 points upstream and the degree of redilution may be controlled by rotation of the deflector 13 about the axis 14.
  • the outer surface 18 of the deflector 13 is contoured generally to conform to the trough wall 6 and to permit rotation of the deflector 13 over the range required.
  • the axis 14 may be spaced at any desired distance from the leading end 17 of the deflector 13 depending upon the amount of deflection required.
  • FIG. 3 to 6 A second embodiment of the invention is shown in Figures 3 to 6 where corresponding features have been given corresponding reference numerals for ease of description.
  • the helical trough descends in a lefthand spiral rather than the right-hand spiral of the first embodiment.
  • the flow is deflected predominantly from the inwardly directed concave surface 15 which extends from the leading end 17 where it is tangential to the stream to a trailing end 18 where it is directed radially inwardly.
  • the flow can also be deflected from the upper surface 19 in a fan-like spray from its trailing end 20. In other embodimemts the flow can be deflected entirely from the upper surface.
  • the deflector of the second embodiment may also be adjustable as previously described but is illustrated in a fixed position on the trough wall, just beneath a flexible edge cover 21 with its lower surface 22 spaced above the trough floor to allow solids to pass under the deflector.
  • the tapered configuration of the deflector with its sharpened leading end provides no abrupt edge which would otherwise tend to collect rubbish.

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  • Cyclones (AREA)
  • Centrifugal Separators (AREA)

Description

  • This invention relates to an improved spiral separator and to a method of spiral separation which is of particular use in the separation of minerals.
  • Spiral separators are extensively used for the wet gravity separation of solids according to their specific gravity, for example for separating various kinds of mineral sands from silica sands.
  • Separators of the kind under discussion are shown, for example, in our Australian Patent Application 82717/82. Such separators commonly comprise a vertical column about which there are supported one or more helical troughs. In operation, a "pulp" or slurry of the materials to be separated and water is introduced to the upper end of a trough and as the pulp descends the helix, centrifugal forces act on the less dense particles in a radially outwards direction while the more dense particles segregate to the bottom of the flow and after slowing through close approach to the working surface of the trough gravitate towards the vertical column.
  • During operation of a spiral separator there is a general migration of water from the inner portion of smaller radius of the flow to the outer portion of the flow. However, particularly when there are high proportions of high specific gravity particles present in the pulp, the total water supply at the inner portion can be used up before segregation is completed. As this takes place there is an accumulation of particles at the inner portion which, while it does not prevent the stream from continuing to move, changes the effective shape of the volute cross section and separation proceeds no further.
  • CA-A-961005 discloses a spiral separator in which fresh water from a separate channel of the trough is fed into the main channel of the trough to replace water which has been lost in extracting particulate material from the separator.
  • According to the present invention in one aspect there is provided a spiral separator including at least one helical trough having a trough floor extending between an inner periphery and an outer periphery, said trough being arranged to receive a pulp stream of water and particles at its upper end and to separate particles of different densities as the stream moves downwardly along said trough, said separator being characterised by the inclusion of at least one deflector located adjacent said outer periphery and having at least one surface contoured for deflecting a portion of the low solids high velocity stream component in a fan-like spray from the outer periphery of the pulp stream back across said stream towards said inner periphery.
  • According to another aspect of the invention there is provided a method for rediluting a pulp stream flowing downwardly along the helical trough of a spiral separator comprising the deflection of a portion of the low solids high velocity stream component in a fan-like spray from the outer periphery of said pulp stream back across said stream towards its inner periphery.
  • Preferably, an adjustable deflector is located on an outer wall of the helical trough to deflect the stream component in said fan-like spray. This is not the same mechanism as a normal wash water supply which is deliberately applied as small radial outflow across the segregated stream.
  • Some embodiments of the invention will now be described, by way of examples, with reference to the accompanying drawings, in which:-
    • Figure 1 is a sectional perspective view of part of a spiral separator looking upstream and showing one embodiment of the rediluting method and apparatus in use, 0
    • Figure 2 is a radial section view taken on line 2-2 of Figure 1,
    • Figure 3 is an incomplete section through a helical trough looking downstream in a tangential direction and showing another embodiment of the invention,
    • Figure 4 is a plan view taken on line 4-4 of Figure 3,
    • Figure 5 is a radial sectional view taken on line 5-5 of Figure 3, and
    • Figure 6 is a section taken on line 6-6 of Figure 5,
  • As shown in Figure 1 the spiral separator 1 includes helical trough 2 supported from a vertical column 3.
  • The helical trough 2 in cross-section comprises an upright inner wall 4, a support web 5 whereby the lip of the inner wall 4 is connected with the column 1, an upright outer wall 6 terminating in a lip 7 and a trough floor 8 extending between the inner wall 4 and the outer wall 6. The trough working surface comprises an inner portion 9 and an outer portion 10 inclined at a greater angle to the helix radial direction and thus slopes more steeply upwardly and outwardly.
  • The profile of the bottom of the trough is such that the mass of water in the slurry moves radially outward and upward. This causes thinning of the water layer at the inner portion 11 of the flow and a water build-up at the low solids, high velocity stream at the flow periphery 12.
  • In accordance with the invention, a deflector 13 is attached to the outer wall 6 to deflect a portion of the water from the flow periphery 12 into the inner portion 11 to reinstate the water quantities necessary to permit the designed separation mechanism to proceed.
  • As shown in Figure 2 the deflector 13 is adjustable by rotation about a radial axis 14 and has an under-surface 15 suitably contoured to deflect the water in a fan-like spray 16 across the trough. The undersurface 15 is arcuate in contour when viewed in both radial and tangential directions with respect to the trough. The deflector 13 preferably permits the stream to be rediluted to a considerable depth and across a broad band at the inner portion 9 of the trough floor. The sharpened leading end 17 of the deflector 13 points upstream and the degree of redilution may be controlled by rotation of the deflector 13 about the axis 14. The outer surface 18 of the deflector 13 is contoured generally to conform to the trough wall 6 and to permit rotation of the deflector 13 over the range required. The axis 14 may be spaced at any desired distance from the leading end 17 of the deflector 13 depending upon the amount of deflection required.
  • A second embodiment of the invention is shown in Figures 3 to 6 where corresponding features have been given corresponding reference numerals for ease of description. In this embodiment the helical trough descends in a lefthand spiral rather than the right-hand spiral of the first embodiment.
  • In this embodiment the flow is deflected predominantly from the inwardly directed concave surface 15 which extends from the leading end 17 where it is tangential to the stream to a trailing end 18 where it is directed radially inwardly. However, in this embodiment the flow can also be deflected from the upper surface 19 in a fan-like spray from its trailing end 20. In other embodimemts the flow can be deflected entirely from the upper surface.
  • The deflector of the second embodiment may also be adjustable as previously described but is illustrated in a fixed position on the trough wall, just beneath a flexible edge cover 21 with its lower surface 22 spaced above the trough floor to allow solids to pass under the deflector. The tapered configuration of the deflector with its sharpened leading end provides no abrupt edge which would otherwise tend to collect rubbish.
  • Although the invention has been described with reference to specific examples, it will be appreciated by those skilled in the art that the invention may be embodied in many other forms without departing from the scope of the present invention as defined in the appended claims.

Claims (20)

1. A spiral separator (1) including at least one helical trough (2) having a trough floor (8) extending between an inner periphery (4) and an outer periphery (6), said trough (2) being arranged to receive a pulp stream of water and particles at its upper end and to separate particles of different densities the stream moves downwardly along said trough (2), said separator (1) being characterised by the inclusion of at least one deflector (13) located adjacent said outer periphery (6) and having at least one surface contoured for deflecting a portion of the low solids high velocity stream component in a fan-like spray (16) from the outer periphery of the pulp stream back across said stream towards said inner periphery.
2. A spiral separator according to claim 1, wherein said outer periphery is defined by an outer wall (6) and said deflector (13) is located on said wall (6).
3. A spiral separator according to claim 2, wherein said deflector (13) has an outer surface (18) contoured to conform to said outer wall (6).
4. A spiral separator according to any preceding claim, wherein said deflector (13) is adjustable to vary the amount of stream deflected.
5. A spiral separator according to claim 4, wherein said deflector (13) is mounted for rotation about an axis (14) extending radially with respect to said trough (2), thereby to vary the amount of stream deflected.
6. A spiral separator according to any preceding claim, wherein said deflector (13) has a contoured undersurface (15) for deflecting said stream in said fan-like spray (16).
7. A spiral separator according to claim 6, wherein said undersurface (15) is arcuate in contour when viewed in both radial and tangential directions with respect to said trough (2).
8. A spiral separator according to claim 7, wherein said deflector (13) has a sharpened leading end (17) pointing upstream.
9. A spiral separator according to any preceding claim, wherein said trough floor (8) has a portion (10) which slopes more steeply closer to said outer periphery.
10. A spiral separator according to claim 9, wherein said trough floor (8) includes an inner portion (9) adjacent said inner periphery and a more steeply inclined outer portion (10) between said inner portion and said outer periphery.
11. A spiral separator according to claim 10, wherein said deflector (13) is able to deflect said stream component substantially to said inner portion (9) to redilute the pulp stream to a substantial depth across said inner portion (9).
12. A spiral separator according to any preceding claim, wherein said deflector (13) has a contoured upper surface (19) for deflecting said stream in a fan-like spray.
13. A spiral separator according to claim 12, wherein said deflector (13) also includes an inwardly directed contoured surface (18) for deflecting said stream in a fan-like spray.
14. A spiral separator according to claim 13, wherein said inwardly directed surface (18) . extends from a leading end (17) where it is tangential to the stream to a trailing edge (20) where it is directed radially inwards.
15. A spiral separator according to claim 14, wherein said inwardly directed surface (18) is concave.
16. A spiral separator according to claim 12, wherein said deflector (13) has a sharpened leading end pointing upstream.
17. A spiral separator according to claim 6, wherein said undersurface (15) is concave.
18. A spiral separator according to claim 17 wherein said undersurface (15) extends from a leading end where it is tangential to the stream to a trailing edge where it is directed radially inwards.
19. A method for rediluting a pulp stream flowing downwardly along the helical trough (2) of a spiral separator (1) characterized by deflecting a portion of the low solids high velocity stream component in a fan-like spray from the outer periphery of the pulp stream back across said stream towards its inner periphery.
20. A method according to claim 19 wherein a substantial portion of said stream component is deflected towards said inner periphery in a fan-like spray to redilute said pulp stream to a substantial depth.
EP19840302608 1983-04-18 1984-04-17 Spiral separator incorporating a fluid deflector Expired EP0123501B1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
AUPF893683 1983-04-18
AU8936/83 1983-04-18
AU27077/84A AU575046B2 (en) 1983-04-18 1984-04-18 Spiral separator incorporating fluid deflector

Publications (2)

Publication Number Publication Date
EP0123501A1 EP0123501A1 (en) 1984-10-31
EP0123501B1 true EP0123501B1 (en) 1987-07-15

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EP19840302608 Expired EP0123501B1 (en) 1983-04-18 1984-04-17 Spiral separator incorporating a fluid deflector

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7686170B2 (en) * 2002-05-17 2010-03-30 Edi Rail Pty Ltd Deflector for spiral separator, and method of spiral separation
CN102240593A (en) * 2011-06-21 2011-11-16 广州粤有研矿物资源科技有限公司 Spiral concentrator

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB586777A (en) * 1944-10-17 1947-03-31 Ira Boyd Humphreys Concentrator and method of concentration
US3891546A (en) * 1971-09-08 1975-06-24 Ira B Humphreys Helical chute concentrator and method of concentrating
US3753491A (en) * 1971-12-28 1973-08-21 United States Steel Corp Apparatus for supplying wash water to a spiral concentrator
CA961005A (en) * 1972-08-22 1975-01-14 Ronald G. Fuller Helical concentrator with restraining lip
NZ199986A (en) * 1981-03-18 1985-07-31 Mineral Deposits Ltd Spiral separator:profile of working surface varies as spiral descends

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EP0123501A1 (en) 1984-10-31

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