[0001] 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.
[0002] 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.
[0003] 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.
[0004] During operation of a spiral separator there is a general migration of water from
the inner portion or 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.
[0005] According to one aspect of the invention 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 adapted 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 for
deflecting a portion of the low solids high velocity stream component from the outer
periphery of the pulp stream back across said stream towards said inner periphery.
[0006] 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 from
the outer periphery of said pulp stream back across said stream towards its inner
periphery.
[0007] Preferably, an adjustable deflector is located on an outer wall of the helical trough
to deflect the stream component in a fan-like spray. This is not the same mechanism
as a normal wash water supply which is deliberately F applied as a small radial outflow
across the segregated stream.
[0008] Preferred embodiments of the invention will now be described, by way of example only,
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.
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.
Figure 6 is a section taken on line 6-6 of Figure 5.
[0009] As shown in Figure 1 the spiral separator 1 includes helical trough 2 supported from
a vertical column 3.
[0010] The helical trough in cross-section comprises an upright inner wall 4, a support
web 5 whereby the lip of the inner wall 4 is connected with column 1, an upright outer
wall 6 terminating in a lip 7 and a trough floor 8 extending between the inner wall
and the outer wall. 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.
[0011] 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.
[0012] 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.
[0013] 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 preferably permits the stream
to be rediluted to a considerable depth and across a broad band at the inner portion
of the trough floor. The sharpened leading end 17 of the deflector points upstream
and the degree of redilution may be controlled by rotation of the deflector about
the axis 14. The outer surface 28 of the deflector is contoured generally to conform
to the trough wall 6 and to permit rotation of the deflector over the range required.
The axis 14 may be spaced at any desired distance from the leading end 17 of the deflector
depending upon the amount of deflection required.
[0014] 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 left-hand spiral rather than the
right-hand spiral of the first embodiment.
[0015] 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 embodiments the flow can be deflected entirely
from the upper surface.
[0016] 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 defl-ector with its
sharpened leading end provides no abrupt edge which would otherwise tend to collect
rubbish.
[0017] Although the invention has been described with reference to a specific example, it
will be appreciated by those skilled in the art that the invention may be embodied
in many other forms.
1. 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 adapted
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 for deflecting a portion of the low solids high velocity stream component
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 and said deflector is located on said wall.
3. A-spiral separator according to cliam 2 wherein said deflector has an outer surface
contoured to conform,to said outer wall.
4. A spiral separator according to claim 1 wherein said deflector is adjustable to
vary the amount of stream deflected.
5. A spiral separator according to claim 4 wherein said deflector is mounted for rotation
about an axis extending radially with respect to said trough, thereby to vary the
amount of stream deflected.
6. A spiral separator according to claim 1 wherein said deflector has a contoured
undersurface adapted to deflect said stream in a fan-like spray.
7. A spiral separator according to claim 6 wherein said undersurface is arcuate in
contour when viewed in both radial and tangential directions with respect to said
trough.
8. A spiral separator according to claim 7 wherein said deflector has a sharpened
leading end pointing upstream.
9. A spiral separator according to claim 1 wherein said trough floor slopes more steeply
closer to said outer periphery.
10. A spiral separator according to claim 9 wherein said trough floor includes an
inner portion adjacent said inner periphery and a more steeply inclined outer portion
between said inner portion and said outer periphery.
11. A spiral separator according to claim 10 wherein said deflector is able to deflect
said stream component substantially to said inner portion to redilute the pulp stream
to a substantial depth across said inner portion.
12. A-spiral separator according to claim 1 wherein said deflector has a contoured
upper surface adapted to deflect said stream in a fan-like spray.
13. A spiral separator according to claim 12 wherein said deflector also includes
an inwardly directed contoured surface adapted to deflect said stream in a fan-like
spray.
14. A spiral separator according to claim 12 wherein said inwardly directed surface
extends from a leading end where it is tangential to the stream to a trailing edge
where it is directed radially inwards.
15. A spiral separator according to claim 14 wherein said inwardly directed surface
is concave.
16. A spiral separator according to claim 12 wherein said deflector has a sharpened
leading end pointing upstream.
17. A spiral separator according to claim 6 wherein said undersurface is concave.
18. A spiral separator according to claim 17 wherein said undersurface 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
of a spiral separator comprising the deflection of a portion of the low solids high
velocity stream component from the outer periphery of the pulp stream back across
said stream towards its inner periphery.
20. A method according to claim 12 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.