AU651160B2 - Mineral processing screen separator - Google Patents
Mineral processing screen separator Download PDFInfo
- Publication number
- AU651160B2 AU651160B2 AU90008/91A AU9000891A AU651160B2 AU 651160 B2 AU651160 B2 AU 651160B2 AU 90008/91 A AU90008/91 A AU 90008/91A AU 9000891 A AU9000891 A AU 9000891A AU 651160 B2 AU651160 B2 AU 651160B2
- Authority
- AU
- Australia
- Prior art keywords
- pulp
- screen
- tank
- impeller
- separator
- 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
- 229910052500 inorganic mineral Inorganic materials 0.000 title claims description 9
- 239000011707 mineral Substances 0.000 title claims description 9
- 239000002245 particle Substances 0.000 claims description 34
- 239000002184 metal Substances 0.000 claims description 30
- 238000000034 method Methods 0.000 claims description 30
- 239000003463 adsorbent Substances 0.000 claims description 23
- 238000012216 screening Methods 0.000 claims description 17
- 230000005484 gravity Effects 0.000 claims description 7
- 238000011084 recovery Methods 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 238000010408 sweeping Methods 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 2
- 239000002250 absorbent Substances 0.000 claims 2
- 230000002745 absorbent Effects 0.000 claims 2
- 239000004576 sand Substances 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 claims 1
- 239000000463 material Substances 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 241000239290 Araneae Species 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 238000005086 pumping Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 238000013019 agitation Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D15/00—Control, e.g. regulation, of pumps, pumping installations or systems
- F04D15/0072—Installation or systems with two or more pumps, wherein the flow path through the stages can be changed, e.g. series-parallel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
- B01D29/114—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements arranged for inward flow filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/76—Handling the filter cake in the filter for purposes other than for regenerating
- B01D29/86—Retarding cake deposition on the filter during the filtration period, e.g. using stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/26—Filters with built-in pumps filters provided with a pump mounted in or on the casing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D1/00—Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps
- F04D1/14—Pumps raising fluids by centrifugal force within a conical rotary bowl with vertical axis
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D7/00—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts
- F04D7/02—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type
- F04D7/04—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type the fluids being viscous or non-homogenous
- F04D7/045—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type the fluids being viscous or non-homogenous with means for comminuting, mixing stirring or otherwise treating
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Paper (AREA)
Description
41571 GEH:PFB0 P/00/011 Regulation 3.2
AUSTRALIA
Patents Act 1990 COMPLETE SPECIFICATION FOR A STANDARD PATENT
ORIGINAL
00 sea* ofA piat 0"0 NL AMRCNCROAINOFSUHARC IIE 0 0 Acua nv ntr STALE GODOUNE Adrs fo erie bes 59N met of plicant:i non o s 1A- FIELD OF THE INVENTION This invention relates to a screen separator for use in adsorbtion cells such as carbon in pulp adsorbtion tanks, carbon in leach tanks, resin in pulp adsorbtion tanks and resin in leach tanks which contain adsorbent particles such as activated carbon or resin and are filled with metal rich solutions or pulps with the screen separators of the tanks being employed to separate the metal rich 0*1-5 adsorbent particles in the tanks from the leaner pulp or leach
C
6. solution, a method of screen separating the adsorbent particles from a pulp and to a process of recovering metal values from the pulp or leach solution in a circuit including a plurality of adsorbtion cells which include the screen separators of the invention.
S"BACKGROUND TO THE INVENTION in general practise, a metal rich pregnant pulp or solution is fed
*C
into a cell of the above type which contains carbon, resin or like adsorbtion particles and where, by one means or another the adsorbtion particles become loaded with the metal values in the pulp. The adsorbent particles are then screen separated from the now leaner pulp which is then either pumped or gravity fed to an adjacent cell in a series of cells where the process is again repeated.
Periodically, in order to achieve counter current movement of the adsorbent particles and pulp a quantity of pulp in any one tank is pumped together with its associated adsorbent upstream to the preceding tank. This arrangement causes back mixing which reduces the efficiency of counter current contacting.
Gravity feed requires that sequential cells in the series be expensively vertically staggered in cascade and pumping involves the not inconsiderable expense of providing and maintaining the pumps and motors required to do this. Often air or oxygen is required in the leaching process and this is generally supplied by means of a blower, compressor or from a pressurised vessel which feeds the air or oxygen to the tank where it is then diffused in one way or another below the surface of the pulp in the tank. Again the provision of compressed air or oxygen and diffusers is expensive.
15 SUMMARY OF THE INVENTION A method of separating adsorbent particles from a pulp in a tank according to the invention includes the steps of locating an open topped closed bottom cylindrical screen in the tank with its open top at substantially the full pulp surface level in the tank, locating a bladed impeller, which includes a shroud S 20 which is fixed to the radially outer edges of the blades and a pulp outlet from the shroud, partially in and out of the screen with its axis of rotation vertical, its lower portion below the full pulp surface level in the tank and its upper portion including the outlet above the full pulp surface level in the tank, rotating the impeller about its axis of rotation to drive pulp in the screen upwardly to and from the shroud outlet into a receptacle above the full pulp surface level in the tank and discharging the pulp from the receptacle to the outside of the tank to a level above the full pulp surface level in the tank.
-3- Further according to the invention the impeller is located on a drive shaft which carries sweep arms which are located adjacent at least one screening surface of the screen with the method including the step of sweeping the screening surface of the screen by means of the sweep arms as the impeller is rotated by the shaft.
A screen separator according to the invention includes an open topped and closed bottom cylindrical screen for axially vertical location, in use, in the tank containing the pulp, said screen being situated in the tank with its open top at or adjacent the full pulp surface lev'el in the tank, a bladed impeller which is located in the screen with its axis of rotation vertical and its blades in and extending above the full pulp surface level in the tank, a shroud which surrounds the radially outer edges of impeller blades to extend vertically over a substantial portion of the length of the impeller with the shroud including at least 15 one pulp outlet which, in use, is located above the full pulp surface level in the tank, drive means, a drive shaft connected to the drive means, and means connecting the drive shaft to the impeller with the impeller being adapted to drive pulp in the screen upwardly within the shroud to and from its outlet above the full pulp surface level in the tank when the impeller is rotated in the screen by the drive shaft.
I FIA Z 0 Still further according to the invention the shroud is attached to the impeller blades for rotation with the impeller.
Yet further according to the invention the screen is annular in cross section with the impeller drive shaft concentrically located in the bore of the screen with the impeller blades attached to structure on the drive shaft and depending from the structure into the screen.
o• a ooooa a Conveniently the drive shaft carries sweep arms which are located parallel to and adjacent the screening surface of the screen so that rotation of the shaft will cause the sweep arms to sweep the/or each screening surface of the screen in use.
Conveniently the screen separator includes a housing which includes a moat which surrounds the impeller between the pulp outlet from the shroud and the full pulp surface level in the tank in use and a conduit for conveying pulp from the moat to an adjacent tank.
A process according to the invention for recovering mineral values from a pulp by means of a series of adsorbtion cells which are located on a surface having a common level with each cell including a tank, a pulp inlet from a common pulp °6 supply line, a pulp outlet conduit the inlet of which is at a higher level than the full pulp surface level in the tank and a screen separator of the invention for 15 lifting screened pulp from within the screen of the separator in the tank to the .o inlet to the outlet conduit includes the steps of charging the tanks on the outside of the screens with metal adsorbent particles, filling the first tank in the series with a mineral rich pulp, agitating the mixture in the tank, screen separating the i K "'ro 4 '71 1 -6metal loaded particles from the remainder of the pulp, lifting the lean pulp from the screen to the inlet to the outlet conduit during the separation process and gravity feeding the lean pulp to a second cell in the series, again screening and lifting the now further leaned pulp from the second cell and feeding it to a third cell in the series and so on, sequentially closing the pulp inlets to the cells 10 when the adsorbent particles in a cell are fully loaded with the pulp 000e SI* metal, discharging the particles from the tank and feeding the particles from the tank discharge to a storage vessel for further processing while continuing to feerj the pulp from the common supply line to the next cell in the series so that the metal recovery 56_ process is continuous.
BRIEF DESCRIPTION OF THE DRAWINGS 0 The invention is now described by way of example only with reference to the drawings in which: FIGURE 1 is a partially schematic sectioned side elevation of one embodiment of the screen separator of the invention located in a tank containing pulp, -7- FIGURE 2 is a partially sectioned perspective view of the impeller of the Figure 1 screen separator, FIGURE 3 is a view similar to that of Figure 1 of a second embodiment of the screen separator of the invention, and 40 FIGURE 4 is a schematic diagram of a series of adsorbtion cells in *see a mineral recovery process.
I
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT The screen separator of the invention is shown in Figure 1 of the drawings to include a support structure 10 which is centrally held over a tank of a conventional adsorbtion cell, not shown, by means a* of suitable bracing ieements which are also not shown in the drawing. The support structure carries a motor 12, a volute 11, a screen arrangement 14, an impeller 16, sweep arms 18 and a drive shaft 20 to which the impeller and sweep arms are connected.
The screen arrangement 14 is annular in cross section, open at the top and closed at the bottom with the inner surface of the screen being upwardly and inwardly tapered as shown in the drawing. The -8screen is constructed from wire mesh which may be clad with a finer screen material or may be a fine guage wedge wire screen.
On small capacity separators the frusto connical inner surface of the screen could be made from sheet metal with only the outer surface of the screen being water pervious. In larger separators both the inner and outer surfaces of the screen are made from 10 screening material. The screen is attached to the underside of the volute 11, which is in turn rigidly attached to the underside of the support structure In larger variations of the screen separator of the invention which include screening material on the inner surface of the screen an impeller 22 could be fixed to the lower end of the drive shaft 20 to drive adsorbent material away from the inner surface of the screen 14.
C
s" 0 A spider 24 is fixed to and projects radially from the lower end of the drive shaft 20 and carries the vertical sweep arms 18 as shown in the drawing. The sweep arms are located in close proximity to the outer surface of the screen so that rotation of the arms by the shaft 20 about the screen surface will agitate and so dislodge solids from the outer surface of the screen to prevent the screen from becoming choked. In the larger variations of the screen separator the spider 24 may, in addition to or in place of the impeller 22, carry inwardly inclined arms for sweeping the inner frusto connical screening surface of the screen 14.
The impeller 16, as is more clearly seen in Figure 2, consists of an A.0 upper disc 26 which is releasibly attached to the shaft 20, four or *ga more impeller blades 28 which are shaped as shown in the drawings, a shroud 30 which surrounds and is attached to the outer edges of the blades between the dotted line positions shown in Figure 1 and a hub portion 32. The impeller is fixed to the shaft 18 so that the lower portions of the blades 28 are located in the screen 4 14 through its open top as shown in the drawing with the lower portion of the impeller hub 32 being situated closely adjacent the 0 inner screening surface of the upper end of the screen.
20 In use, the tank in which the screen separator of the invention is located is charged, on the outside of the screen, with metal adsorbent particles and the tank is filled with a metal rich pulp. As the drive shaft of the separator is rotated the leaner pulp between the inner surfaces of the walls of the screen 14 is driven upwardly and outwardly on the impeller blades 28 by centrifugal and cyclonically induced forces towards the upper portion of the blades to be thrown from the impeller outlets 36 between the under surface of the disc 26 and the upper surface of the shroud above the full surface level 38 of the pulp in the tank in which the screen separator is located. In this manner, a negative pressure is generated in screen 14 which causes pulp in the tank to be drawn U .1 through the screen of screen arrangement 14 with metal loaded «adsorbtion particles above the screen size of the screen being e trapped by the outer screening surfaces of the screen. As mentioned above, the impeller ip rotated by the drive shaft 20 and so are the sweep arms 18 which agitate the solid material free of the screening surfaces of the screen to avoid the possibility of the 4 4 screen becoming choked. A moat 34 is incorporated in the volute 11 to surround the impeller with its base above the surface of the pulp in the tank. The volute includes a run-off launder from tG%, moat for gravity feeding the pulp which is pumped by the impeller 0 into the trough 34 to an adjacent tank so that the pulp level in the adjacent tank need not be vertically lower than the pulp level in the tank from which the pulp is pumped.
In the Figure 3 embodiment of the separator of the invention the base of the screen 14 and its inner wall 40 are made from solid 11 sheet material. It is to be noted that unlike the frusto connical inner wall of the Figure 1 screen the wall 40 of this screen is in the form of a parallel sided tube.
The impeller 16 of the Figure 3 embodiment differs from that of Figure 1 in a number of respects. The first difference is that its hub ,JO 32 is a tube which is concentrically located about the solid inner 6.* GOO screen wall 40 and extends from the impeller disc 26 to a low level )GO* position in the screen tube 14. The bottom end of the hub 32 0 carries radially projecting impeller blades 42 which, on rotation of the impeller, drive pulp in the screen upwardly from its base portion 9,,115 towards the impeller blades 28. This low level impeller is also particularly useful in agitating solids which may have settled out s onto the solid screen base, perhaps due to a loss of flow through 0 0 the separator, back into an upward flow direction in the screen O* 0o towards the impeller 16. The impeller blades 28, in this "20 embodiment of the separator could, in dependence on the torque capabilities of the motor 12, extend further down into the screen than shown in the drawing further to improve the pump action of the impeller. A further difference between the two impellers is that the Figure 3 impeller includes, between the shroud 30 and the hub 32, a frusto connical insert 44 which is fixed to the disc 26 and the -12hub 32. The insert 44 reduces, as seen in the drawing, the effective area of each of the impeller blades 28 from that of the Figure 1 device and, because the insert has substantially the same cone angle as the shroud 30, provides parallel outwardly inclined fluid passages through the impeller which are uniform in cross sectional area over their length to minimise drop in the velocity of the pulp in its upward passage through the impeller. To improve the wear resistance of the impeller all surfaces of the impeller, such as the inner walls of the slurry passages through the impeller, the portion of the hub 32 which is, in use, in contact with the pulp in the screen and the impeller blades 42, could be clad with a wear resistant material such as a suitable rubber or like comp- ,jnd, polyurethane or the like.
s The drive shaft 20 carries, at its lower end adjacent the wiper spider "24, an impeller 46 which is fixed to the shaft with its blades oppositely pitched to the blades 42 in the screen so that as the
S
o* shaft is rotated the impeller 46 will drive the tank pulp downwardly and away from the lower end of the screen wall tube 40. The drive shaft 20 extends downwardly from the wiper spider 24 and carries on its free end yet a further impeller 48 which drives pulp, in the tank in which the separator is located, towards the base of the tank -13to promote suspension of the adsorbent particles in the pulp by agitation.
In use, the Figure 3 screen separator functions in much the same manner as the Figure 1 device with the obvious differences provided by the modified impeller and the impellers 42 and 48.
Obviously, the leaner pulp which is pumped by the impeller into the moat 34, in both embodiments of the separator, is aerated in its passage through atmosphere from the impeller to the moat. The aerated pulp, as with the Figure I separator, is gravity fed through a launder 49 to an adjacent tank in the mineral separation process.
**see: The separator of the invention is not limited to the precise details as herein described. For example, the impeller blades 28 are shown in the drawings of both embodiments of the invention to be vertical but they could equally well be, and preferably are, inclined from the vertical helically towards their lower ends in the direction of the rotation of the impeller so that a turbine effect will assist in sweeping the pulp upwardly on the blades 28. Alternatively, the lower ends of the blades 28 which project from the shroud 30 could be bent forwardly in the direction of rotation of the impeller for the -14same purpose. Additionally, the impeller of the Figure 1 embodiment of the separator of the invention could include the insert 44 and the extended drive shaft and agitating impeller 48 of the Figure 3 impeller.
Figure 4 illustrates 3 adsorbtion cells 50, 52 and 54 which form part of a series of identical cells in a process circuit for recovering metal values from a mineral rich pulp. The cells each include a 0 conventional tank 56 which is well known in the art and has a domed bottom, a separator 58 of the invention, which may be either S: the Figure 1 or 3 type, a pulp inlet 60, a pulp outlet 62 and a drain valve 64 which is located in the base of the tank below the separator 58.
0 o 0 0 0 In the process of the invention the tank inlets 60 are all connected into a common pulp feed line 66 from a source of metal rich pulp.
:o48% Each tank inlet 60 is controlled by a shut-off valve 68.
An important feature of the process circuit of the invention is that tank pulp outlets 62 are connected through shut-off valves 70 and conduits 72 back into the common pulp feed line 66. The feed line includes isolator valves 74,76 and 78 which are interposed between the inlet 60 of an upstream tank 56 and the inlet of the same tank outlet conduit 72 into the line 66 and the inlet 60 to the adjacent downstream tank in the series as shown in Figure 4.
The tank dump or drain valves 64 are connected in series into an open adsorbent particle discharge conduit 79 which leads to a receiver tank, not shown.
In use, each of the tanks 56 in the process series are charged in the conventional manner with mineral adsorbent particles. The ot isolator valves 74, 76 and 78 are shut and the inlet valves 68 to the cells 50 and 52 are opened. A pulp control valve 80 in the line 66 is opened to allow the tank 56 of the cell 50 to fill to its full pulp level with metal rich pulp from the line 66. The screen separator 58 0* is now activated to agitate the pulp and adsorbent particles in the tank to cause the metal values in the solution to attach to the :oo. particles and to pump the leaned screen pulp from the screen to
S
the trough 34 of the separator 58. The inlet valve 68 is adjusted to permit fresh pulp from the line 66 to enter the tank 56 at the same rate at which the separator 58 pumps the leaned pulp from the tank so that a full pulp surface level in the tank is maintained. When the tank 56 of the cell 52 has filled sufficiently its outlet valve 70 and -16the inlet valve to the cell 54 are opened and its separator 58 is activated for further extraction of metal values from the leaned pulp from the cell 50 with the yet leaner pulp being pumped to the cell 54 and so on through the series of cells until the process is continuous throughout the circuit.
When the pre-calculated saturation time of the adsorbent particles in the tank of the cell 50 has been reached the isolator valve 74 is opened and the inlet and outlet valves of the cell 50 are shut.
Conveniently the outlet valve is only shut after the separator has ceased pumping leaned pulp to the cell 54 to reduce the liquid level of the pulp in the cell 50 to a minimum. The open valve 74 permits the high metal value pulp in the line 66 now to enter the cell 52.
The dump valve 64 of the cell 50 is now opened and the metal rich adsorbent particles are pumped through the discharge conduit 79 :to the receiver tank from where the liquids and solids are separated .2e, with the liquid being pumped to waste. The de-watered adsorbent
S
"particles are then further processed for the recovery of their metal values without interruption of the mineral recovery process. The emptied cell 50 is again charged with fresh adsorbent particles.
The isolator valve 74 is progressively closed and fresh pulp is fed to the cell 50 while the circuit process remains operational. In this 17 manner sequential cells in the started to ensure uninterrupted circuit are emptied and again reoperation of the process.
9S 0S 0*
.*SO
e 0*eO
*.SO
0O** *1 S. S 0 5000** .009 0O S. 0 *9 0
SO
0@ 0 oSS**S 0 0 0. 05 e S S S. 5 0 0 55
Claims (10)
1. A method of separating absorbent particles from a pulp in a tank including the steps of locating an open topped closed bottom cylindrical screen in the tank with its open top at substantially the full pulp surface level in the tank, locating a bladed impeller, which includes a shroud which is fixed to the radially outer edges of the blades and a pulp outlet from the shroud, partially in and out of the screen with its axis of rotation vertical, its lower portion below the full pulp surface level in the tank and its upper portion including the outlet above the full pulp surface level in the tank, rotating the impeller about its axis of rotation to drive pulp in the screen upwardly to and from the shroud outlet into a receptacle above the full pulp surface level in the tank and discharging the pulp from the receptacle to the outside of the tank to a level above the full pulp "surface level in the tank. So*Q 15 2. A method as claimed in claim 1 in which the impeller is rotated by means of a drive shaft which additionally carries sweep arms which are located ~adjacent the screening surface of the screen with the method including the step of sweeping the screening surface of the screen by means of the sweep arms as the drive shaft is rotated. 20 3. A method as claimed in either one of claims 1 or 2 in which the screen is annular in cross-section, the impeller drive shaft passes through the bore of the screen and carries in the tank remote from the closed bottom of the screen an agitator impeller and the method includes the step of agitating the pulp in the tank by means of the agitator impeller as the impeller drive shaft is rotated.
4. A method as claimed in claim 3 including a second impeller on the impeller drive shaft which is located in the screen below and spaced from the first impeller and the method includes the step of rotating the second impeller with the first to drive pulp in the screen upwardly towards the first impeller as the impellers are rotated in the screen. .ln -19- A screen separator for separating metal absorbent particles from a pulp in a tank including an open topped and closed bottom cylindrical screen for axially vertical location, in use, in the tank containing the pulp, said screen being situated in the tank with its open top at or adjacent the full pulp surface level in the tank, a bladed impeller which is located in the screen with its axis of rotation vertical and its blades in and extending above the full pulp surface level in the tank, a shroud which surrounds the radially outer edges of impeller blades to extend vertically over a substantial portion of the length of the impeller with the shroud including at least one pulp outlet which, in use, is located above the full pulp surface level in the tank, drive means, a drive shaft connected to the drive means, and means connecting the drive shaft to the impeller with the impeller being adapted to drive pulp in the screen upwardly within the shroud to Sand from its outlet above the full pulp surface level in the tank when the impeller 15 is rotated in the screen by the drive shaft. eo°r ooo
6. A separator as claimed in claim 5 in which the shroud is attached to the sees impeller blades for rotation with the impeller. eo
7. A separator as claimed in either one of claims 5 or 6 in which the screen is annular in cross-section with the impeller drive shaft concentrically located in *ooo the bore of the screen and the drive shaft connecting means is a structure oo which is fixed to the drive shaft above the screen with the impeller blades fixed to the structure to depend therefrom downwardly into the screen. oooo A separator as claimed in claim 7 in which the drive shaft extends oo.. through the bore of the screen and includes radially projecting arms which extend across the closed bottom of the screen and carry sweep arms which are parallel to the outer screening surface of the screen so that rotation of the drive shaft will cause the sweep arms to sweep the screening surface of the screen in use.
9. A separator as claimed in claim 8 including a second impeller on the impeller drive shaft which is located in the screen below and spaced from the S first impeller to drive pulp in the screen upwardly towards the first impeller as the impellers are rotated by the drive shaft in the screen in use. f~v A k-2 A separator as claimed in either one of claims 8 or 9 including an agitator impeller on the drive shaft at a position below and remote from the closed bottom of the screen for agitating pulp in the tank below the screen as the drive shaft is rotated in use.
11. A separator as claimed in any one of claims 5 to 10 in which the separator includes a housing which includes a trough which surrounds the impeller between its pulp outlet and the pulp surface level in the tank and a conduit for conveying, under gravity, pulp which is discharged from the impeller into the trough from the tank to a level on the outside of the tank above the full pulp surface level in the tank.
12. A process for recovering metal values from a pulp by means of a series of adsorption cells which are located on a common surface with each cell o including a tank, a pulp inlet from a common pulp supply line, a pulp outlet .15 conduit the inlet of which is at a higher level than the full pulp surface level in the tank and a screen separator as claimed in any one of claims 5 to 11 for *see lifting screened pulp from within the screen of the separator in the tank to the .trough and the outlet conduit including the steps of charging the cell tanks on the outside of the screens with metal adsorbent particles, filling the first tank in 20 the series with a metal rich pulp, agitating the mixture in the tank, screen separating the metal loaded particles from the remainder of the pulp, lifting the lean pulp from the screen by means of the screen separator to the trough and the outlet conduit during the separation process and gravity feeding the leaner pulp to a second cell in the series, again screening and lifting the now further leaned pulp from the second cell by means of its separator and feeding it to a third cell in the series and so on, sequentially closing the pulp inlets to the cells when the adsorbent particles in a cell are fully loaded with the puip metal, discharging the particles from the tank and feeding the particles from the tank discharge to a storage vessel for further processing while continuing to feed the pulp from the common supply line to the next cell in the series so that the metal recovery process is continuous. -21-
13. A process as claimed in claim 12 in which the common pulp supply line includes a valve between the pulp inlets of adjacent cell tanks in the series and the method includes the step of closing the valve downstream of the cell tank which is being filled with pulp from the common supply line.
14. A process as claimed in claim 12 in which the outlet conduit from each cell tank feeds the leaned pulp from its tank into the common pulp supply line at a position between the valve in the supply line which is downstream of the inlet to the tank and the inlet to the adjacent tank in the series with the recovery process including the step of feeding the leaned pulp from one tank to another through the common pulp supply line while the downstream valve in the supply line is closed. Goes 15. A process for recovering mineral values from pulp substantially as herein described. °ooo o 15 16. A screening method substantially as herein described with reference to the drawings.
17. A screen separator substantially as herein described with reference to and as illustrated in any of the drawings. Dated this 5th day of May 1994 0* 20 ANGLO AMERICAN CORPORATION OF SOUTH AFRICA LIMITED By their Patent Attorneys COLLISON CO. ABSTRACT This invention relates to a screen separator for separating metal adsorbent particles from a pulp and includes a screen separator for separating metal adsorbent particles from a pulp including an open topped and closed bottom cylindrical screen for axially vertical location, in use, in a tank containing pulp with the open top of the screen at or adjacent the full pulp surface level in the tank, an impeller which is located in the screen with its axis of rotation vertical, drive means, and a drive shaft connecting the drive means %a to the impeller with the impeller being adapted to drive pulp in the screen upwardly to a level above the surface level of the full pulp level in the tank when the impeller is rotated in the screen. The °e invention further extends to a method of separating the particles from the pulp by means of the separator and to a metal recover process which employs the separation method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU90008/91A AU651160B2 (en) | 1991-12-23 | 1991-12-23 | Mineral processing screen separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU90008/91A AU651160B2 (en) | 1991-12-23 | 1991-12-23 | Mineral processing screen separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU9000891A AU9000891A (en) | 1993-07-08 |
| AU651160B2 true AU651160B2 (en) | 1994-07-14 |
Family
ID=3763709
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU90008/91A Expired AU651160B2 (en) | 1991-12-23 | 1991-12-23 | Mineral processing screen separator |
Country Status (1)
| Country | Link |
|---|---|
| AU (1) | AU651160B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111214855A (en) * | 2019-12-06 | 2020-06-02 | 骆军辉 | Disc thickener |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4092248A (en) * | 1977-07-18 | 1978-05-30 | Koehler-Dayton, Inc. | Pump-filter assembly |
| US4096057A (en) * | 1976-05-10 | 1978-06-20 | New Energy Sources Company | Apparatus and method for recovery of bituminous products from tar sands |
| US4955482A (en) * | 1985-09-20 | 1990-09-11 | Kamyr, Inc. | Screen cleaning in cil & cip systems |
-
1991
- 1991-12-23 AU AU90008/91A patent/AU651160B2/en not_active Expired
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4096057A (en) * | 1976-05-10 | 1978-06-20 | New Energy Sources Company | Apparatus and method for recovery of bituminous products from tar sands |
| US4092248A (en) * | 1977-07-18 | 1978-05-30 | Koehler-Dayton, Inc. | Pump-filter assembly |
| US4955482A (en) * | 1985-09-20 | 1990-09-11 | Kamyr, Inc. | Screen cleaning in cil & cip systems |
Also Published As
| Publication number | Publication date |
|---|---|
| AU9000891A (en) | 1993-07-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| AU596924B2 (en) | Improved froth flotation method and apparatus | |
| US5238117A (en) | Mineral processing screen separator | |
| US4836611A (en) | Method and apparatus for drilling and separating | |
| US8636149B2 (en) | Method and apparatus for washing sand | |
| FI59438B (en) | MEDICAL EQUIPMENT SUSPENSION TRYCKSAOLL FOER FIBERSUSPENSIONER | |
| KR20150003742A (en) | Rotating Separator | |
| CN1330426C (en) | Auxiliary agitator for a flotation device | |
| US4515607A (en) | Gas, fluid and mineral solids separation and reclamation system | |
| US5385668A (en) | Apparatus for separating particulate material from a liquid medium | |
| US4163723A (en) | Continuously operated liquid-solids separator | |
| AU651160B2 (en) | Mineral processing screen separator | |
| CN206689127U (en) | A kind of sandstone clean separator | |
| GB1484496A (en) | Apparatus for continuously separating debris from beets or other roots or tubers | |
| CN115121383A (en) | Water flow swirler | |
| RU2069098C1 (en) | Screen separator | |
| US4834783A (en) | Rotary separator | |
| AU646869B2 (en) | Apparatus for separating particulate material from a liquid | |
| AU776134B2 (en) | Pulp screen separator | |
| CN106216080B (en) | Hydrocone type sorting equipment and complete sorting system | |
| CN214865604U (en) | Embryo particle separating device for rice processing | |
| CN219185996U (en) | Spiral sand-water separator for sewage treatment | |
| US3700103A (en) | Recovery of minerals | |
| CN114985123B (en) | Bidirectional sorting centrifuge for ore dressing | |
| EP0671968A4 (en) | Method and apparatus for separating solids from liquid containing same. | |
| CN215656267U (en) | Powder particle separator |