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US3700103A - Recovery of minerals - Google Patents

Recovery of minerals Download PDF

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Publication number
US3700103A
US3700103A US842528A US3700103DA US3700103A US 3700103 A US3700103 A US 3700103A US 842528 A US842528 A US 842528A US 3700103D A US3700103D A US 3700103DA US 3700103 A US3700103 A US 3700103A
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Prior art keywords
impeller
cell
standpipe
spaced
shaft
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US842528A
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Walter C Giebel
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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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/14Flotation machines
    • B03D1/16Flotation machines with impellers; Subaeration machines
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/86Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis co-operating with deflectors or baffles fixed to the receptacle
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/55Baffles; Flow breakers
    • 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/14Flotation machines
    • B03D1/1443Feed or discharge mechanisms for flotation tanks
    • B03D1/1456Feed mechanisms for the slurry
    • 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/14Flotation machines
    • B03D1/1493Flotation machines with means for establishing a specified flow pattern

Definitions

  • ABSTRACT Apparatus for treating ore pulp in a treatment cell attendant to recovery of minerals therefrom having a rotatable shaft with an attached impeller and a radially projecting annular disc, the disc including a plurality of projections attached thereto and a cylindrical collar disposed above the disc and joined thereto, thus forming a rotating standpipe so that the path of flow of ore pulp through the eye of the impeller is well defined.
  • a stabilizer ring is joined to the cell adjacent the impeller so that a shear zone is developed in the ore pulp, the stabilizer ring being configurated to maximize turbulence in the shear zone and minimize surging and boiling of the ore pulp at the surface thereof.
  • An insert is adapted to nest within a rectangular cell so that the rectangular cell operatively receives the stabilizer ring.
  • the present invention provides novel impeller structure comprising improved fluid flow control through the impeller structure.
  • a stabilizer ring is disposed adjacent the impeller structure, the stabilizer ring being uniquely configurated so as to form a shear zone adjacent the impeller wherein substantial turbulence and intimate contact with mineral-treatment compound mixture is accommodated.
  • the unique configuration of the stabilizer ring and the relationship between the stabilizer ring and the impeller structure prevents excessive boiling at the surface of the ore pulp.
  • ore pulp means a solution and/or suspension of mineral bearing ore prior to the extraction of all valuable minerals therefrom.
  • Another important object of the present invention is to provide novel stabilizer ring structure which avoids excessive boiling of the ore pulp at the surface thereof.
  • One still further object of the present invention is to provide a novel cell adaptor to allow the improved stabilizer ring to be used with rectangular cells.
  • Another and no less important object of the present invention is the provision for an improved rotating standpipe combination including a cylindrical collar which defines a preferred path for flow of ore pulp into the impeller and which improves the mixing of ore pulp with air air bubbles and treatment compound.
  • a further and important object of the present invention is to provide additional novel structure in a stabelizer, or agitator ring, in combination with the novel impeller with rotating standpipe, wherein the said stabelizer comprises a plurality of radially placed blades which are concave, or curved, wherein the concavity, or curvature of the said blades is in the vertical plane of the said blade, and the said curvature extends from the bottom edge of the blade to the top edge of the blade.
  • FIG. 1 is an exploded perspective view of one presently preferred embodiment of the impeller structure and cylindrical collar of the invention
  • FIG. 2 is a top plan view of a stabilizer ring embodiment utilized in a circular treatment cell
  • FIG. 3 is a transverse cross section taken along lines 33 of FIG. 2;
  • FIG. 4 is a top plan view of a square treatment cell with a cell adapter and attached stabilizer ring nested therein;
  • FIG. 5 is a transverse cross section taken along lines 55 of FIG. 4;
  • FIG. 6 is a fragmentaryplan view of the stabilizer ring embodiment of FIG. 4;
  • FIG. 7 is cross section taken along lines 77 of FIG.
  • FIGS. 8 and 9 are fragmentary cross sectional illustrations of alternative embodiments of the stabilizer ring of the invention.
  • FIG. 10 illustrates in cross section another stabilizer ring embodiment disposed within a treatment cell, the impeller structure-of FIG. 1 being illustrated in normal position adjacent the stabilizer ring;
  • FIG. 11 is a elevational view shown partly in cross section illustrating the configuration of the blades of the stabilizer ring illustrated in the embodiment of FIG. 10;
  • FIG. 12 illustrates in cross section another presently preferred stabilizer ring blade embodiment
  • FIG. l3 is a top plan view of a cylindrical treatment cell with stabilizer ring in place and also illustrating another embodiment of the cylindrical rotating standpipe and impeller structure of the invention
  • FIG. 14 is a transverse cross section taken along lines 14-14 of FIG. 13;
  • FIG. 15 is a top plan view shown partially broken away to reveal the internal configuration of scoop structure comprising part of the improved cylindrical standpipe and impeller structure which may be used with the embodiment of FIGS. 13 and 14; and
  • FIGS. 16 and 17 are fragmentary cross sections taken along lines 16-l6 and l7l7 of FIG. 15 respectively.
  • the component parts of theimpeller structure generally designated 30 is illustrated in exploded perspective in FIG. 1.
  • the structure 30 comprises a central shaft 32 which may be a solid or tubular shaft as desired, and is normally telescopically disposed first through a cylindrical sleeve 34 having a plurality of impeller blades 37 radially projecting outwardly therefrom.
  • Each of the impeller blades 37 has an inverted triangular configuration so that as the impeller blades are rotated with the sleeve 34, ore pulp (not shown) in contact therewith will be thrust generally downwardly.
  • the shaft 32 is non-rotatably joined to the sleeve 34 such as with a spline joint or key or the like.
  • the shaft 32 is also telescopically disposed through aperture 36 comprising part of a cylindrical collar or standpipe generally designated 38.
  • the collar 38 comprises an annular outer wall 40.
  • the cylindrical collar 38 is interiorly hollow and is connected to a central hub 42 with spokes 41 radially projecting inwardly from the outer wall 40.
  • the spokes 41 are preferably identical in number as and aligned with the impeller blades 37.
  • the hub 42 defines aperture 36, aperture 36 being centrally disposed completely through the hub 42.
  • Hub 42 is interiorly provided with a key in order to be nonrotatably joined to the shaft 32. Alternatively, hub 42 may be otherwise permanently non-rotatably secured to the shaft 32.
  • the outer wall 40 and the spokes 41 cooperate to define a plurality of passageways 44 which open above and below the cylindrical standpipe 38.
  • the passageways 44 have an important purpose which will be hereinafter more fully described.
  • the lower end 46 of the standpipe 38 is provided with a peripheral flange 48 which projects outwardly from the standpipe 38.
  • the flange 48 is provided with spaced apertures 50 through which bolts 52 are normally disposed.
  • Bolts 52 are adapted to be similarly disposed through corresponding apertures 54 disposed at spaced locations in an annular disc 56.
  • Annular disc 56 has a substantially smooth planar upper surface 58 and similarly, a substantially smooth lower planar surface 60.
  • Disc 56 has an enlarged circular aperture 62 disposed central of the disc and having a dimension which is essentially the same as the inside dimension of the cylindrical standpipe 38.
  • the cylindrical standpipe 38 may be disposed upon the upper surface 58 of the disc 56 and secured I thereto by bolts 52 and made secure thereon by threading nuts 64 on the respective threaded ends 66 of bolts 52.
  • the disc 56 may be non-rotatably joined to shaft 32 by hub 34 and blades 37, making them integral with disc 56 so that spokes 41 and hub 42 of the standpipe 38 are unnecessary.
  • a plurality of downwardly depending fingers 68 is disposed adjacent the outer periphery of disc 56.
  • Each finger comprises a cylindrical abrasive resistant rubber tube having a central throughbore 70.
  • An elongated bolt 72 is adapted to be disposed through the bore 70 and also through apertures 74 spaced adjacent the periphery of discf56. Nuts 76, threadedly secure bolts 72 and fingers 68 to the disc 56.
  • the attachment feature of the fingers 68 to the disc 56 is particularly important since prior to the instant invention, impeller fingers comprised a permanent part of the impeller structure. Frequently, the fingers would become broken or otherwise unusable and it was necessary for the entire impeller structure to be either discarded or substantially repaired.
  • the above described embodiment accommodates placement and replacement of impeller fingers in a rapid and efficient manner without disturbing the remainder of the impeller structure.
  • the underside 60 of the disc 56 is also provided with radially downwardly projecting vanes 78. Vanes 78 are permanently secured to the disc 56 and radially traverse the lateral dimension of the disc from the apertures 62 to the peripheral edge thereof. If desired, the vanes 78 may also be removably attached to the disc 56.
  • the above-described impeller structure 30 accommodates downward channeling of ore pulp (not shown) through the passageways 44 in the standpipe 38 and through the impeller blades 37 which thrust the ore pulp downwardly.
  • ore pulp not shown
  • the impeller structure 30 accommodates downward channeling of ore pulp (not shown) through the passageways 44 in the standpipe 38 and through the impeller blades 37 which thrust the ore pulp downwardly.
  • fingers 68 and vanes 78 in addition, agitate and condition the ore pulp.
  • FIGS. 2 and 3 illustrate a cylindrical treatment cell or vat generally designated 80.
  • the treatment cell 80 may be used for any one of the mineral dressing procedures, the cell 80 will be discussed in connection with a froth flotation procedure for convenience of illustration.
  • the cell 80 as best illustrated in FIG. 3, has a downwardly tapered bottom 82 and rounded corners 84 so that the bottom 82 has a configuration somewhat similar to a vortex.
  • the cell 80 is generally circular in plan view, which circular configuration is critical for the reasons which hereinafter follow. 7
  • An annular stabilizer ring or agitator ring 86 is disposed inside of the cell 80 and spaced somewhat above the corners 84 so as to be contiguous with the internal peripheral surface 88 of the cell 80.
  • the stabilizer ring 86 is preferably formed of rubber or other resilient material and comprises spaced teeth or wedgelike segments 90 which comprise baffles and project toward the interior of the cell 80.
  • Each segment 90 has side faces 92 which are acutely angularly related both with respect to opposed side faces of adjacent segments and with respect to each other.
  • the stabilizer ring 86 comprises an annular bore 94 disposed through each segment 90 so that a circular passageway exists throughout the annular length of the stabilizer ring, the passageway being broken only by the faces 92 of the segments 90.
  • a vertically disposed port 96 (FIG. 3) communicates the lowermost portion of the aperture 94 with the bottom of the cell 80 so that air bubbles or mineral pulp trapped within the bore 94 can be expelled therethrough.
  • an upper port 98 communicates the outside peripheral edge of the bore 94 with the upper portion of the cell 80 so that air bubbles and ore pulp being agitated within the cell 80 can be communicated through the port 98 to flush trapped minerals and ore pulp out through the port 96.
  • FIGS. 2 and 3 also illustrate a conventional power driven solid or tubular shaft 100 which is suspended from a remote elevated location (not shown) and is non-rotatably secured to impeller structure 102 which may be structure 30 (FIG. 1) or, if desired, may be conventional as illustrated in FIGS. 2 and 3.
  • the impeller structure 102 has impeller blades 104 which radially project outwardly therefrom.
  • the impeller blades 104 have sufficient length so as to pass substantially close to but not at any time touch the segments 90. As best illustrated in FIG. 3, the vertical position of the impeller blades 104 is preferred to be essentially central of the stabilizer ring 86.
  • the impellers 104 are rotated by a power source (not shown) to cause the ore pulp beneath the stabilizer ring 86 to revolve in one circular direction. Ore pulp and mineral laden air bubbles above the stabilizer ring 86 revolve in the cell 80 (in direction opposite to impeller rotation) due to the effect of the stabilizer ring 86.
  • the invented apparatus creates two distinct shear zones within the body of the ore pulp, one between the rotating impeller and the stationary stabelizer, and one in the pulp body where the reversal of pulp flow direction takes place; this is a new and beneficial method of agitation and aeration in a mineral dressing device.
  • the shear zones cause substantially increased contact between minerals in the ore pulp and the air bubbles so that that frothing is more efficent in causing minerals to adhere to the frothing bubbles.
  • the stabilizer ring 86 substantially reduces surging and boiling of the pulp into the froth column which builds upon the surface of the ore pulp near the top of the cell 80.
  • the tendency of the minerals adhering to and carried by the froth column at the top of the cell 80 to fall back into the mineral pulp is substantially reduced and the well-known problem of weeping of the floated minerals back into the mineral pulp is minimized.
  • the mineral bearing froth is collected from the surface of cell 80 and the minerals are recovered therefrom in a conventional manner.
  • FIGS. 4-7 7 It has been found that the new and advantageous results provided as described above are not accomplished or achieved where the cell 80 is square in configuration. It is also well known that most conventional treatment cells are square in horizontal cross section. Therefore, in order to achieve the same useful result in conventional square cells, the adapter embodiment of FIGS. 4 and 5 is provided.
  • FIGS. 4 and 5 illustrate a conventional treatment cell 110 which is square in horizontal cross section. As best illustrated in FIG. 5, the cell has a substantially flat bottom 112 and'is open at the top 114.
  • a treatment cell adapter generally designated 116 which has a circular horizontal cross section, is nested within the cell 110 so as to contact tangentially the side portions of the cell 110 as at 118.
  • the adapter 116 has a conical bottom 120 which tapers inwardly toward a vortex 122.
  • the bottom corners 124 are rounded and a plurality of radial spaced apertures 126 are disposed in the bottom 120 so as to open adjacent each corner 128 of the square cell 110.
  • the upper edge 130 of the cell adapter 116 is disposed somewhat beneath the upper edge 114 of the cell 110.
  • ore pulp and treatment solution and air bubbles can easily pour from the cell into the adapter particularly at the location adjacent each corner 128.
  • the adapter 1 16 is interiorally provided with a stabilizer ring 132, the ring 132 being substantially similar to the stabilizer ring 86 illustrated in FIGS. 2 and 3 except ring 132 comprises an additional upper port 134 which aids the aperture 98 in preventing accumulation of ore pulp and reagent material within the passageway 94 (see FIGS. 6 and 7).
  • the embodiment of FIGS. 4 and 5 illustrates the stabilizer ring as used in conjunction with impeller structure 30 previously discussed above with respect to FIG. 1.
  • the stabilizer ring generally designated and illustrated in FIG. 8 may be substituted for the stabilizer rings 132 or 86 illustrated in FIGS. 5 and 3, respectively.
  • the stabilizer ring 140 is annular in plan view and is essentially square in transverse cross section as illustrated in FIG. 8.
  • the stabilizer ring 140 comprises a plurality of essentially wedge-shaped segments 142 and an essentially square bore 144 exists through each of the segments in order to form an annular passageway.
  • the passageway is provided with a bottom port 146 and two top ports 148 and 149 which cooperate with the port 146 to flush the passageway 144 of ore pulp or treatment reagents or the like.
  • the stabilizer ring embodiment in FIG. 9 generally designated 150.
  • Stabilizer ring 150 differs from stabilizer ring 140 in that the upper surface 152 has a substantial downward slope or taper. This downward taper is particularly advantageous in preventing accumulation of ore pulp and treatment material upon the upper surface 152.
  • the interior passageway or channel 154 has an upper surface which tapers downwardly toward the center of the stabilizer ring. Otherwise, stabilizer ring 150 is substantially similar to stabilizer ring 140 and like parts are designated with like numerals throughout.
  • FIG. 10 illustrates a treatment cell 158 which is circular in horizontal cross section and which has a flat bottom 160.
  • Impeller structure 30 which is substantially identical to the impeller structure 30 illustrated in FIG. 1, is disposed within the treatment cell 158 essentially central thereof.
  • annular metal ring 162 Adjacent the bottom of the treatment cell 158 is mounted an annular metal ring 162 (best shown in FIG. 1 l
  • the metal ring 162 is rigidly mounted upon the interior surface of the cell 158 somewhat above the bottom and is provided with a plurality of spaced rigid baffles or stabilizer blades 164.
  • Each blade 164 is provided with an L-shaped bracket 166 which has an aperture (not shown) adapted to be aligned with a bore hole (not shown) in the annular ring 162 so that a bolt 168 may be threadedly disposed therein to secure the stabilizer blades 164 in position around the annular ring;
  • each of the stabilizer blades 164 is arcuately shaped so that the concave surface 170 of the stabilizer blade 164 faces a direction opposite the direction of rotation of the impeller structure 30. It has been found that this particular configuration improves the contact between ore pulp and air bubbles and other treatment material while simultaneously preventing excessive boiling and surging at the surface of the treatment cell 158. i
  • the stabilizer blade 172 may be substituted for the blade 164 above described.
  • Stabilizer blade 172 comprises an'inner metal core 174'which is disposed within resilient material l76such as rubber. having a biconcave configuration.
  • the impeller structure 30 may be rotated in either direction to accomplish the same advantageous result above described.
  • FIGS. 13 and 14 illustrate a treatment cell 180 which comprises a cylindrical upper section 182 which is open at the top and terminates adjacent the bottom in an outwardly projecting annular flange 184.
  • Section 182 may have spaced ports 220 which communicate the interior of cell 180 with a source of ore pulp.
  • the bottom section 186 of the cell 180 is'open at the top so as to communicate directly with the upper section 182 and is provided with an upper peripheral flange 188 adapted to mate with flange 184 and to be secured thereto such as with bolts 190.
  • a seal or sealantv may be interposed between the flanges 184 and 188 in order that the joint may be made water-tight.
  • Bottom section 186 has rounded comers 192 and tapers annularly downwardly to a vortex 194. If
  • annular stabilizer ring such as stabilizer ring 86 above described.
  • a rotatable shaft 204 is disposed central of the cell 180 and suspended therein from a position above the cell (not shown).
  • a lower end 206 of the shaft 204 is non-rotatably secured to an annular collar 208 having a plurality of radially-extending impeller blades 210 integral therewith.
  • an annular collar 208 having a plurality of radially-extending impeller blades 210 integral therewith.
  • a second collar 212 Intermediate the length of the shaft 204 is a second collar 212 (see FIG. 14).
  • Collar 212 has radially projecting spokes 214 which are normally essentially parallel to the projecting impeller blades 210.
  • An elongated, diametrally enlarged tubular rotating standpipe 216 is preferably joined to the impeller blades 210 at the juncture therewith and is also joined to spokes 214 such as by keying or the like.
  • the standpipe 216 has sufficient axial dimension so that the upper edge of the standpipe 216 is near the top of cell 180.
  • Standpipe 216 is provided with spaced apertures 218 which are disposed beneath the level of spokes 214 to communicate the interior 221 of the standpipe 216 with the interior of cell 180.
  • Standpipe 216 is open at the top and the bottom so that a passageway exists from the top of the standpipe 216 through the spokes 214 and to impeller blades 210 to the bottom of the cell.
  • treatment or conditioning compounds are 238, removing the scoop from aperture 218 and replacfed into the cell and ore pulp may be communicated therein either through the ports 200 or through feed conduit 222 or both.
  • the ore pulp carried by the conduit 222 is channeled directly into the collar or standpipe 216 between the spokes 214 so as to be channeled into the impeller blades 210.
  • a unique flow pattern results, which is identical in effect, as to the creation of two distinct shear zones, such as were described andunder embodiments of FIGS.
  • the collar or standpipe 216 may be modified as illustrated in FIGS. 15 17 to improve the efficiency thereof.
  • the upper sleeve 212 is provided with spokes 224 which have a T-configuration in cross section.
  • the horizontal upper portion of 226 of the T (FIG. 16) is integral with an upper collar insert 228.
  • the insert 228 is cylindrical in configuration and has substantially the same inside and outside diametral dimensions as the collar or standpipe 216.
  • the vertical portion 230 of the T- shaped spoke 224 has a smaller longitudinal dimension than the upper portion 226 and is disposed beneath the lower edge 232 of the insert 228.
  • the insert 228 when the insert 228 is placedupon the standpipe 204 the vertical portion 230 of the spokes 224 will be disposed within and abut the collar or standpipe 216 so that collar or standpipe 216 will remain centered about the shaft 204. Also, the insert 228 will be coaxial and essentially coextensive the with collar or standpipe 216.
  • apertures 218 in collar or standpipe 216 may be provided with scoops 236.
  • Each scoop 236 is preferably formed of deformable rubber or the like and is provided with a peripheral slot 238 (FIG. 17) which allows the scoop 236 to be secured in the aperture 218.
  • scoops 236 can be orientedin either direction selectively so that even if the direction of rotation of the standpipe 216 is reversed, the direction of orientation of the scoop 236 may be disposed 180 from that illustrated by manually collapsing the scoop in the vicinity of peripheral slot ing the scoop in the reverse orientation.
  • a mineral treating cell comprising a circular vat into which a mineral bearing pulp suspension and a treatment substance are disposed, the improvement comprising:
  • an impeller non-rotatably carried upon a centrally disposed rotatable shaft, the impeller comprising a plurality of blades having a configuration so that when the impeller is rotated in the mineral suspension, the suspension will be thrown downwardly toward the bottom of the vat;
  • an agitator ring mounted upon the interior periphery of the vat adjacent the location of the impeller, the agitator ring comprising resiliently deformable essentially wedge-shaped segments the ends of which are spaced from the impeller blades so that as the impeller rotates within the mineral suspension, shear zones are developed by the agitator ring thereby generating maximum contact of treatment substance and minerals without excessive boiling of the suspension within the vat at the pulp surface, 7
  • a cell as defined in claim 1 wherein said central shaft upon which the impellers are mounted comprises a cylindrical standpipe concentrically disposed around and spaced from the central shaft, at least the lower end of the standpipe being disposed within the treatment substance and pulp suspension adjacent the impellers; and means disposed at the upper end of the standpipe for delivering the fresh pulp suspension to the upper end of the standpipe so that pulp suspension is communicated directly therethrough to the rotating impeller blades for shearing of large air bubbles into substance and ul sus ension.
  • a cell as efiiied 51 claim 6 wherein the standpipe is concentrically spaced from the central shaft for rotation therewith and further comprising scoop means mounted upon .the standpipe adjacent each spaced I aperture so that the opening of the scoop means is in the direction of rotation of the standpipe to recirculate the pulp suspension through the standpipe to the impeller blades.
  • a mineral recovery apparatus comprising in combination a treatment cell adapted to receive a mineral suspension and a treatment substance
  • a rotatable impeller shaft centrally disposed within and spaced from the side and bottom of the cell;
  • an impeller non-rotatably mounted upon the shaft and comprising a plurality of radially projecting blades, each having an inverted triangular'cross section for downwardly throwing the mineral suspension;
  • annular disc having at least one aperture for passing the mineral suspension therethrough and being attached to and generally below the cylindrical standpipe for rotation therewith, the disc carrying on the underside thereof a plurality of downwardly projecting fingers disposed in spaced locations around the periphery of the disc.
  • An apparatus as defined in claim 9 further comprising radially spaced, downwardly projecting paddle bladesrigidly secured to the underside of the disc adjacent the fingers and directed radially outward from the axis of the impeller shaft and the rotating standpipe.
  • a mineral treating cell comprising a vat into which mineral bearing pulp suspension and a treatment substance are disposed, the improvement comprising:
  • the disc member comprising (a) impeller blades spaced radially outward from the axis of the shaft, (b) at least one aperture adjacent the shaft, (0) a plurality of spaced depending fingers disposed adjacent the periphery thereof and (d) a standpipe non-rotatably mounted upon the disc member and spaced from the shaft for defining a flow path through the aperture.

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Abstract

Apparatus for treating ore pulp in a treatment cell attendant to recovery of minerals therefrom, the apparatus having a rotatable shaft with an attached impeller and a radially projecting annular disc, the disc including a plurality of projections attached thereto and a cylindrical collar disposed above the disc and joined thereto, thus forming a rotating standpipe so that the path of flow of ore pulp through the eye of the impeller is well defined. A stabilizer ring is joined to the cell adjacent the impeller so that a shear zone is developed in the ore pulp, the stabilizer ring being configurated to maximize turbulence in the shear zone and minimize surging and boiling of the ore pulp at the surface thereof. An insert is adapted to nest within a rectangular cell so that the rectangular cell operatively receives the stabilizer ring.

Description

[ 1 Oct. 24, 1972 [54] RECOVERY OF MINERALS [72] Inventor: Walter C. Giebel, General Delivery,
Sheridan, Mont.
22 Filed: July 17,1969
21 Appl. No.: 842,528
[52] US. Cl ..209/169, 261/93 [51} Int. Cl. ..B03d 1/14 [58] Field of Search ..209/169, 170; 261/87, 93
[56] References Cited UNITED STATES PATENTS 1,935,190 11/1933 Munro ..261/93 2,875,897 3/1959 Booth ..209/169 2,944,802 7/1960 Daman ..261/93 X 2,966,266 12/1960 Coke ..261/93 X 2,973,095 2/1961 Anderson et a1. ..209/169 v 3,070,229 12/ 1962 Benozzo ..209/170 X 3,098,818 7/1963 Daman et a1. ..209/169 3,327,851 6/1967 Anderson ..209/169 3,378,141 4/1968 Warman ..209/169 3,437,203 4/1969 Nakamura ..209/169 3,491,880 1/1970 Reck ..261/93 FOREIGN PATENTS OR APPLICATIONS 358,715 4/1938 Italy ..209/169 Primary Examiner-Tim R. Miles Attorney-Lynn G. Foster [57] ABSTRACT Apparatus for treating ore pulp in a treatment cell attendant to recovery of minerals therefrom, the apparatus having a rotatable shaft with an attached impeller and a radially projecting annular disc, the disc including a plurality of projections attached thereto and a cylindrical collar disposed above the disc and joined thereto, thus forming a rotating standpipe so that the path of flow of ore pulp through the eye of the impeller is well defined. A stabilizer ring is joined to the cell adjacent the impeller so that a shear zone is developed in the ore pulp, the stabilizer ring being configurated to maximize turbulence in the shear zone and minimize surging and boiling of the ore pulp at the surface thereof. An insert is adapted to nest within a rectangular cell so that the rectangular cell operatively receives the stabilizer ring.
12 Claims, 17 Drawing Figures IIO PATENTEU MIT 24 I972 SHEET 1 BF 6 air INVENTOR. WALTER C. GIEBEL FIG. I
ATTORNEY PATENTEU BT 24 I 3,700.1 O3
sum 2 OF 6 96 I02 Q\ I04 90 9o 96 y 84 INVENTOR.
\ WALTER c. GIEBEL a2 BY FIG. 3
ATTORNEY PATENTEU 24 3,700,103
SHEET 4 [IF 6 INVENTOR.
' WALTER c. en; M fl ATTORNEY PATENTEUUBT 24 m2 3.700.103
' SHEET 5 0F 6 2m 20s 206 202 r\\ I92 I I 194 I96 200 FIG. l4
INVENTOR. WALTER C. GIEBEL BY Z 2 ATTORNEY PATENTEDUBT 24 I972 SHEET 6 BF 6 FIG. l5
INVENTOK WALTER C. GIEBEL FIG. I7
FIG. l6
BY f
ATTORNEY RECOVERY OF MINERALS FIELD OF THE INVENTION pounds in the cell while simultaneously avoiding excessive boiling at the surface of the pulp.
DESCRIPTION OF THE PRIOR ART The recovery of minerals by froth flotation and related mineral treatment is well known. Generally, the well-known procedure includes circulating an ore pulp suspension or solution through a treatment cell and agitating the pulp to mix minerals within the pulp with frothing or other treatment compounds pursuant to recovery of the minerals.
It is also known to provide a series of rigid stator blades to break up air bubbles introduced into the ore pulp and expose minerals for attachment to the frothforming bubbles. For example, see. U. S. Pat. Nos. 2,767,964 and 2,973,095. Nevertheless, it has been found that impeller-stator combinations presently used create undesirable boiling of ore pulp at the surface of the treatment cell. The boiling and surging of the ore pulp cause minerals carried by froth bubbles upon the ore pulp surface to fall back into the ore pulp thereby substantially decreasing the effectiveness of Y mineral recovery and increasing the time and cost for recovery.
BRIEF SUMMARY AND OBJECTS OF THE INVENTION It is a primary object of the present invention to provide improved turbulence and improved contact of ore pulp with air bubbles and treatment compounds within the treatment cell-without causing a correspondingly high boiling of the pulp into the froth column. formed by the mineral laden bubbles upon the surface of the said ore pulp.
The present invention provides novel impeller structure comprising improved fluid flow control through the impeller structure. A stabilizer ring is disposed adjacent the impeller structure, the stabilizer ring being uniquely configurated so as to form a shear zone adjacent the impeller wherein substantial turbulence and intimate contact with mineral-treatment compound mixture is accommodated. The unique configuration of the stabilizer ring and the relationship between the stabilizer ring and the impeller structure prevents excessive boiling at the surface of the ore pulp. In this specification, ore pulp means a solution and/or suspension of mineral bearing ore prior to the extraction of all valuable minerals therefrom.
It is, therefore, another important object of the present invention to provide novel impeller structure accommodating improved contact between minerals in the ore pulp with air bubbles and treatment compound.
Another important object of the present invention is to provide novel stabilizer ring structure which avoids excessive boiling of the ore pulp at the surface thereof.
One still further object of the present invention is to provide a novel cell adaptor to allow the improved stabilizer ring to be used with rectangular cells.
Another and no less important object of the present invention is the provision for an improved rotating standpipe combination including a cylindrical collar which defines a preferred path for flow of ore pulp into the impeller and which improves the mixing of ore pulp with air air bubbles and treatment compound.
A further and important object of the present invention is to provide additional novel structure in a stabelizer, or agitator ring, in combination with the novel impeller with rotating standpipe, wherein the said stabelizer comprises a plurality of radially placed blades which are concave, or curved, wherein the concavity, or curvature of the said blades is in the vertical plane of the said blade, and the said curvature extends from the bottom edge of the blade to the top edge of the blade.
These and other objects and features of the present invention will become more fully apparent from the following description and appended claims taken in conjunction with the accompanying drawings wherein:
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an exploded perspective view of one presently preferred embodiment of the impeller structure and cylindrical collar of the invention;
FIG. 2 is a top plan view of a stabilizer ring embodiment utilized in a circular treatment cell;
FIG. 3 is a transverse cross section taken along lines 33 of FIG. 2;
FIG. 4 is a top plan view of a square treatment cell with a cell adapter and attached stabilizer ring nested therein;
FIG. 5 is a transverse cross section taken along lines 55 of FIG. 4;
FIG. 6 is a fragmentaryplan view of the stabilizer ring embodiment of FIG. 4;
FIG. 7 is cross section taken along lines 77 of FIG.
FIGS. 8 and 9 are fragmentary cross sectional illustrations of alternative embodiments of the stabilizer ring of the invention;
FIG. 10 illustrates in cross section another stabilizer ring embodiment disposed within a treatment cell, the impeller structure-of FIG. 1 being illustrated in normal position adjacent the stabilizer ring;
FIG. 11 is a elevational view shown partly in cross section illustrating the configuration of the blades of the stabilizer ring illustrated in the embodiment of FIG. 10;
FIG. 12 illustrates in cross section another presently preferred stabilizer ring blade embodiment;
FIG. l3 is a top plan view of a cylindrical treatment cell with stabilizer ring in place and also illustrating another embodiment of the cylindrical rotating standpipe and impeller structure of the invention;
FIG. 14 is a transverse cross section taken along lines 14-14 of FIG. 13;
FIG. 15 is a top plan view shown partially broken away to reveal the internal configuration of scoop structure comprising part of the improved cylindrical standpipe and impeller structure which may be used with the embodiment of FIGS. 13 and 14; and
FIGS. 16 and 17 are fragmentary cross sections taken along lines 16-l6 and l7l7 of FIG. 15 respectively.
DESCRIPTION OF PREFERRED EMBODIMENTS The Embodiment of FIG. 1
The component parts of theimpeller structure generally designated 30 is illustrated in exploded perspective in FIG. 1. The structure 30 comprises a central shaft 32 which may be a solid or tubular shaft as desired, and is normally telescopically disposed first through a cylindrical sleeve 34 having a plurality of impeller blades 37 radially projecting outwardly therefrom. Each of the impeller blades 37 has an inverted triangular configuration so that as the impeller blades are rotated with the sleeve 34, ore pulp (not shown) in contact therewith will be thrust generally downwardly. The shaft 32 is non-rotatably joined to the sleeve 34 such as with a spline joint or key or the like.
The shaft 32 is also telescopically disposed through aperture 36 comprising part of a cylindrical collar or standpipe generally designated 38. The collar 38 comprises an annular outer wall 40. The cylindrical collar 38 is interiorly hollow and is connected to a central hub 42 with spokes 41 radially projecting inwardly from the outer wall 40. The spokes 41 are preferably identical in number as and aligned with the impeller blades 37. The hub 42 defines aperture 36, aperture 36 being centrally disposed completely through the hub 42. Hub 42 is interiorly provided with a key in order to be nonrotatably joined to the shaft 32. Alternatively, hub 42 may be otherwise permanently non-rotatably secured to the shaft 32.
The outer wall 40 and the spokes 41 cooperate to define a plurality of passageways 44 which open above and below the cylindrical standpipe 38. The passageways 44 have an important purpose which will be hereinafter more fully described. The lower end 46 of the standpipe 38 is provided with a peripheral flange 48 which projects outwardly from the standpipe 38. The flange 48 is provided with spaced apertures 50 through which bolts 52 are normally disposed.
Bolts 52 are adapted to be similarly disposed through corresponding apertures 54 disposed at spaced locations in an annular disc 56. Annular disc 56 has a substantially smooth planar upper surface 58 and similarly, a substantially smooth lower planar surface 60. Disc 56 has an enlarged circular aperture 62 disposed central of the disc and having a dimension which is essentially the same as the inside dimension of the cylindrical standpipe 38. The cylindrical standpipe 38 may be disposed upon the upper surface 58 of the disc 56 and secured I thereto by bolts 52 and made secure thereon by threading nuts 64 on the respective threaded ends 66 of bolts 52. Clearly, if desired, the disc 56 may be non-rotatably joined to shaft 32 by hub 34 and blades 37, making them integral with disc 56 so that spokes 41 and hub 42 of the standpipe 38 are unnecessary.
A plurality of downwardly depending fingers 68 is disposed adjacent the outer periphery of disc 56. Each finger comprises a cylindrical abrasive resistant rubber tube having a central throughbore 70. An elongated bolt 72 is adapted to be disposed through the bore 70 and also through apertures 74 spaced adjacent the periphery of discf56. Nuts 76, threadedly secure bolts 72 and fingers 68 to the disc 56.
The attachment feature of the fingers 68 to the disc 56 is particularly important since prior to the instant invention, impeller fingers comprised a permanent part of the impeller structure. Frequently, the fingers would become broken or otherwise unusable and it was necessary for the entire impeller structure to be either discarded or substantially repaired. The above described embodiment accommodates placement and replacement of impeller fingers in a rapid and efficient manner without disturbing the remainder of the impeller structure.
The underside 60 of the disc 56 is also provided with radially downwardly projecting vanes 78. Vanes 78 are permanently secured to the disc 56 and radially traverse the lateral dimension of the disc from the apertures 62 to the peripheral edge thereof. If desired, the vanes 78 may also be removably attached to the disc 56.
The above-described impeller structure 30 accommodates downward channeling of ore pulp (not shown) through the passageways 44 in the standpipe 38 and through the impeller blades 37 which thrust the ore pulp downwardly. Depending fingers 68 and vanes 78, in addition, agitate and condition the ore pulp.
The Embodiment of FIGS. 2 and 3 FIGS. 2 and 3 illustrate a cylindrical treatment cell or vat generally designated 80. Although the treatment cell 80 may be used for any one of the mineral dressing procedures, the cell 80 will be discussed in connection with a froth flotation procedure for convenience of illustration. The cell 80, as best illustrated in FIG. 3, has a downwardly tapered bottom 82 and rounded corners 84 so that the bottom 82 has a configuration somewhat similar to a vortex. As can be appreciated from FIG. 2, the cell 80 is generally circular in plan view, which circular configuration is critical for the reasons which hereinafter follow. 7
An annular stabilizer ring or agitator ring 86 is disposed inside of the cell 80 and spaced somewhat above the corners 84 so as to be contiguous with the internal peripheral surface 88 of the cell 80. The stabilizer ring 86 is preferably formed of rubber or other resilient material and comprises spaced teeth or wedgelike segments 90 which comprise baffles and project toward the interior of the cell 80. Each segment 90 has side faces 92 which are acutely angularly related both with respect to opposed side faces of adjacent segments and with respect to each other.
The stabilizer ring 86 comprises an annular bore 94 disposed through each segment 90 so that a circular passageway exists throughout the annular length of the stabilizer ring, the passageway being broken only by the faces 92 of the segments 90. A vertically disposed port 96 (FIG. 3) communicates the lowermost portion of the aperture 94 with the bottom of the cell 80 so that air bubbles or mineral pulp trapped within the bore 94 can be expelled therethrough. Also, an upper port 98 communicates the outside peripheral edge of the bore 94 with the upper portion of the cell 80 so that air bubbles and ore pulp being agitated within the cell 80 can be communicated through the port 98 to flush trapped minerals and ore pulp out through the port 96.
FIGS. 2 and 3 also illustrate a conventional power driven solid or tubular shaft 100 which is suspended from a remote elevated location (not shown) and is non-rotatably secured to impeller structure 102 which may be structure 30 (FIG. 1) or, if desired, may be conventional as illustrated in FIGS. 2 and 3. The impeller structure 102 has impeller blades 104 which radially project outwardly therefrom. The impeller blades 104 have sufficient length so as to pass substantially close to but not at any time touch the segments 90. As best illustrated in FIG. 3, the vertical position of the impeller blades 104 is preferred to be essentially central of the stabilizer ring 86.
I have discovered that the above combination of elements creates a novel and advantageous shear zone when ore pulp and frothing or other treatment material are disposed in the cell 80. In operation, the impellers 104 are rotated by a power source (not shown) to cause the ore pulp beneath the stabilizer ring 86 to revolve in one circular direction. Ore pulp and mineral laden air bubbles above the stabilizer ring 86 revolve in the cell 80 (in direction opposite to impeller rotation) due to the effect of the stabilizer ring 86. Thus, the invented apparatus creates two distinct shear zones within the body of the ore pulp, one between the rotating impeller and the stationary stabelizer, and one in the pulp body where the reversal of pulp flow direction takes place; this is a new and beneficial method of agitation and aeration in a mineral dressing device. The shear zones cause substantially increased contact between minerals in the ore pulp and the air bubbles so that that frothing is more efficent in causing minerals to adhere to the frothing bubbles.
Moreover, the stabilizer ring 86 substantially reduces surging and boiling of the pulp into the froth column which builds upon the surface of the ore pulp near the top of the cell 80. Thus, the tendency of the minerals adhering to and carried by the froth column at the top of the cell 80 to fall back into the mineral pulp is substantially reduced and the well-known problem of weeping of the floated minerals back into the mineral pulp is minimized. The mineral bearing froth is collected from the surface of cell 80 and the minerals are recovered therefrom in a conventional manner.
The Embodiments of FIGS. 4-7 7 It has been found that the new and advantageous results provided as described above are not accomplished or achieved where the cell 80 is square in configuration. It is also well known that most conventional treatment cells are square in horizontal cross section. Therefore, in order to achieve the same useful result in conventional square cells, the adapter embodiment of FIGS. 4 and 5 is provided.
FIGS. 4 and 5 illustrate a conventional treatment cell 110 which is square in horizontal cross section. As best illustrated in FIG. 5, the cell has a substantially flat bottom 112 and'is open at the top 114. A treatment cell adapter generally designated 116, which has a circular horizontal cross section, is nested within the cell 110 so as to contact tangentially the side portions of the cell 110 as at 118. The adapter 116 has a conical bottom 120 which tapers inwardly toward a vortex 122. The bottom corners 124 are rounded and a plurality of radial spaced apertures 126 are disposed in the bottom 120 so as to open adjacent each corner 128 of the square cell 110.
It is presently preferred that the upper edge 130 of the cell adapter 116 is disposed somewhat beneath the upper edge 114 of the cell 110. Thus, ore pulp and treatment solution and air bubbles can easily pour from the cell into the adapter particularly at the location adjacent each corner 128.
The adapter 1 16 is interiorally provided with a stabilizer ring 132, the ring 132 being substantially similar to the stabilizer ring 86 illustrated in FIGS. 2 and 3 except ring 132 comprises an additional upper port 134 which aids the aperture 98 in preventing accumulation of ore pulp and reagent material within the passageway 94 (see FIGS. 6 and 7). The embodiment of FIGS. 4 and 5 illustrates the stabilizer ring as used in conjunction with impeller structure 30 previously discussed above with respect to FIG. 1.
The Embodiments of FIGS. 8 and 9 If desired, the stabilizer ring generally designated and illustrated in FIG. 8 may be substituted for the stabilizer rings 132 or 86 illustrated in FIGS. 5 and 3, respectively. The stabilizer ring 140 is annular in plan view and is essentially square in transverse cross section as illustrated in FIG. 8. The stabilizer ring 140 comprises a plurality of essentially wedge-shaped segments 142 and an essentially square bore 144 exists through each of the segments in order to form an annular passageway. The passageway is provided with a bottom port 146 and two top ports 148 and 149 which cooperate with the port 146 to flush the passageway 144 of ore pulp or treatment reagents or the like.
Alternatively, the stabilizer ring embodiment in FIG. 9 generally designated 150. could be used in place of the stabilizer rings 132 and 86, respectively illustrated in FIGS. Sand 3. Stabilizer ring 150 differs from stabilizer ring 140 in that the upper surface 152 has a substantial downward slope or taper. This downward taper is particularly advantageous in preventing accumulation of ore pulp and treatment material upon the upper surface 152. Also, the interior passageway or channel 154 has an upper surface which tapers downwardly toward the center of the stabilizer ring. Otherwise, stabilizer ring 150 is substantially similar to stabilizer ring 140 and like parts are designated with like numerals throughout.
The Embodiment of FIGS. 10-12 FIG. 10 illustrates a treatment cell 158 which is circular in horizontal cross section and which has a flat bottom 160. Impeller structure 30 which is substantially identical to the impeller structure 30 illustrated in FIG. 1, is disposed within the treatment cell 158 essentially central thereof.
Adjacent the bottom of the treatment cell 158 is mounted an annular metal ring 162 (best shown in FIG. 1 l The metal ring 162 is rigidly mounted upon the interior surface of the cell 158 somewhat above the bottom and is provided with a plurality of spaced rigid baffles or stabilizer blades 164. Each blade 164 is provided with an L-shaped bracket 166 which has an aperture (not shown) adapted to be aligned with a bore hole (not shown) in the annular ring 162 so that a bolt 168 may be threadedly disposed therein to secure the stabilizer blades 164 in position around the annular ring;
It is particularly important that each of the stabilizer blades 164 is arcuately shaped so that the concave surface 170 of the stabilizer blade 164 faces a direction opposite the direction of rotation of the impeller structure 30. It has been found that this particular configuration improves the contact between ore pulp and air bubbles and other treatment material while simultaneously preventing excessive boiling and surging at the surface of the treatment cell 158. i
If desired, the stabilizer blade 172 may be substituted for the blade 164 above described. Stabilizer blade 172 comprises an'inner metal core 174'which is disposed within resilient material l76such as rubber. having a biconcave configuration. When the stabilizer blade embodiment of FIG. 12 is rigidly joined to theannular ring 162, the impeller structure 30 may be rotated in either direction to accomplish the same advantageous result above described.
The Embodiment of FIGS. 13-17 FIGS. 13 and 14 illustrate a treatment cell 180 which comprises a cylindrical upper section 182 which is open at the top and terminates adjacent the bottom in an outwardly projecting annular flange 184. Section 182 may have spaced ports 220 which communicate the interior of cell 180 with a source of ore pulp.
As best illustrated in FIG. 14, the bottom section 186 of the cell 180 is'open at the top so as to communicate directly with the upper section 182 and is provided with an upper peripheral flange 188 adapted to mate with flange 184 and to be secured thereto such as with bolts 190. If desired, a seal or sealantv may be interposed between the flanges 184 and 188 in order that the joint may be made water-tight.
Bottom section 186 has rounded comers 192 and tapers annularly downwardly to a vortex 194. If
with a suitable annular stabilizer ring such as stabilizer ring 86 above described.
A rotatable shaft 204 is disposed central of the cell 180 and suspended therein from a position above the cell (not shown). A lower end 206 of the shaft 204 is non-rotatably secured to an annular collar 208 having a plurality of radially-extending impeller blades 210 integral therewith. Intermediate the length of the shaft 204 is a second collar 212 (see FIG. 14). Collar 212 has radially projecting spokes 214 which are normally essentially parallel to the projecting impeller blades 210.
An elongated, diametrally enlarged tubular rotating standpipe 216 .is preferably joined to the impeller blades 210 at the juncture therewith and is also joined to spokes 214 such as by keying or the like. The standpipe 216 has sufficient axial dimension so that the upper edge of the standpipe 216 is near the top of cell 180. Standpipe 216 is provided with spaced apertures 218 which are disposed beneath the level of spokes 214 to communicate the interior 221 of the standpipe 216 with the interior of cell 180. Standpipe 216 is open at the top and the bottom so that a passageway exists from the top of the standpipe 216 through the spokes 214 and to impeller blades 210 to the bottom of the cell The embodiment of FIGS. 13 and 14 is particularly useful for agitators, aerators and conditioners other than flotation apparatus. In the operation of the embodiment, treatment or conditioning compounds are 238, removing the scoop from aperture 218 and replacfed into the cell and ore pulp may be communicated therein either through the ports 200 or through feed conduit 222 or both. The ore pulp carried by the conduit 222 is channeled directly into the collar or standpipe 216 between the spokes 214 so as to be channeled into the impeller blades 210. A unique flow pattern results, which is identical in effect, as to the creation of two distinct shear zones, such as were described andunder embodiments of FIGS. 47, wherein the ore pulp passing through the collar or standpipe 216 is exposed to the treatment compounds in the shear zones developed by the agitator ring 86 and thereafter forced upwardly along the sides of the cell 180. Ore pulp entering through the ports 220 will be caused to flow through the ports 218 to flow downwardly through the collar or standpipe 216 and into the impeller blades 210. Thus, essentially all of the ore pulp entering into the cell 180 will be brought into intimate contact with the treatment and conditioning compounds.
If desired, the collar or standpipe 216 may be modified as illustrated in FIGS. 15 17 to improve the efficiency thereof. In the embodiment of FIGS. 15-17, the upper sleeve 212 is provided with spokes 224 which have a T-configuration in cross section. The horizontal upper portion of 226 of the T (FIG. 16) is integral with an upper collar insert 228. The insert 228 is cylindrical in configuration and has substantially the same inside and outside diametral dimensions as the collar or standpipe 216. The vertical portion 230 of the T- shaped spoke 224 has a smaller longitudinal dimension than the upper portion 226 and is disposed beneath the lower edge 232 of the insert 228. Thus, when the insert 228 is placedupon the standpipe 204 the vertical portion 230 of the spokes 224 will be disposed within and abut the collar or standpipe 216 so that collar or standpipe 216 will remain centered about the shaft 204. Also, the insert 228 will be coaxial and essentially coextensive the with collar or standpipe 216.
Also, if desired, apertures 218 in collar or standpipe 216 (FIG. 14) may be provided with scoops 236. Each scoop 236 is preferably formed of deformable rubber or the like and is provided with a peripheral slot 238 (FIG. 17) which allows the scoop 236 to be secured in the aperture 218.
.material and convey the pulp to the interior of standpipe 216 during rotation thereof. 7
It should be appreciated that scoops 236 can be orientedin either direction selectively so that even if the direction of rotation of the standpipe 216 is reversed, the direction of orientation of the scoop 236 may be disposed 180 from that illustrated by manually collapsing the scoop in the vicinity of peripheral slot ing the scoop in the reverse orientation.
From the foregoing it is apparent that new and improved structure for treating ore pulp pursuant to the recovery of minerals therefrom has been provided by substantially increasing the effectiveness of aeration, agitation, conditioning and related treatment without 9 excessive surging and boiling adjacent the top of the treatment cell.
The invention may be embodied in other specific forms without departing from thespirit or essential characteristics thereof. The present embodiments are, therefore, to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore to be embraced therein.
What is claimed and desired to be secured by United States Letters Patent is:
l. A mineral treating cell comprising a circular vat into whicha mineral bearing pulp suspension and a treatment substance are disposed, the improvement comprising:
an impeller non-rotatably carried upon a centrally disposed rotatable shaft, the impeller comprising a plurality of blades having a configuration so that when the impeller is rotated in the mineral suspension, the suspension will be thrown downwardly toward the bottom of the vat; and
an agitator ring mounted upon the interior periphery of the vat adjacent the location of the impeller, the agitator ring comprising resiliently deformable essentially wedge-shaped segments the ends of which are spaced from the impeller blades so that as the impeller rotates within the mineral suspension, shear zones are developed by the agitator ring thereby generating maximum contact of treatment substance and minerals without excessive boiling of the suspension within the vat at the pulp surface, 7
2. A cell as defined in claim 1 wherein said agitator ring is hollow, each segment having apertures communicating the hollow thereof with the exterior .to
minimize clogging the hollow with sediment.
3. A cell as defined in claim 2 wherein said segments are semi-circular in cross section.
4. A cell as defined in claim 2 wherein said segments are square in cross section.
5. A cell as defined in claim 2 wherein said segments have an upper surface comprising an inclined ramp surface with the highest point disposed adjacent the vat and the lowest point disposed adjacent the impeller path.
6. A cell as defined in claim 1 wherein said central shaft upon which the impellers are mounted comprises a cylindrical standpipe concentrically disposed around and spaced from the central shaft, at least the lower end of the standpipe being disposed within the treatment substance and pulp suspension adjacent the impellers; and means disposed at the upper end of the standpipe for delivering the fresh pulp suspension to the upper end of the standpipe so that pulp suspension is communicated directly therethrough to the rotating impeller blades for shearing of large air bubbles into substance and ul sus ension.
8. A cell as efiiied 51 claim 6 wherein the standpipe is concentrically spaced from the central shaft for rotation therewith and further comprising scoop means mounted upon .the standpipe adjacent each spaced I aperture so that the opening of the scoop means is in the direction of rotation of the standpipe to recirculate the pulp suspension through the standpipe to the impeller blades.
9. A mineral recovery apparatus comprising in combination a treatment cell adapted to receive a mineral suspension and a treatment substance;
a rotatable impeller shaft centrally disposed within and spaced from the side and bottom of the cell;
a hollow cylindrical collar concentrically spaced from the impeller shaft and non-rotatably associated therewith; i
an impeller non-rotatably mounted upon the shaft and comprising a plurality of radially projecting blades, each having an inverted triangular'cross section for downwardly throwing the mineral suspension; and
an annular disc having at least one aperture for passing the mineral suspension therethrough and being attached to and generally below the cylindrical standpipe for rotation therewith, the disc carrying on the underside thereof a plurality of downwardly projecting fingers disposed in spaced locations around the periphery of the disc.
10. An apparatus as defined in claim 9 wherein said fingers are mounted upon the disc by structure accommodating selective removal of the fingers and replacement thereof by similar fingers in the event of structural damage.
11. An apparatus as defined in claim 9 further comprising radially spaced, downwardly projecting paddle bladesrigidly secured to the underside of the disc adjacent the fingers and directed radially outward from the axis of the impeller shaft and the rotating standpipe. 12. A mineral treating cell comprising a vat into which mineral bearing pulp suspension and a treatment substance are disposed, the improvement comprising:
a rotatable shaft and a disc member non-rotatably mounted upon the shaft, the disc member comprising (a) impeller blades spaced radially outward from the axis of the shaft, (b) at least one aperture adjacent the shaft, (0) a plurality of spaced depending fingers disposed adjacent the periphery thereof and (d) a standpipe non-rotatably mounted upon the disc member and spaced from the shaft for defining a flow path through the aperture.

Claims (12)

1. A mineral treating cell comprising a circular vat into which a mineral bearing pulp suspension and a treatment substance are disposed, the improvement comprising: an impeller non-rotatably carried upon a centrally disposed rotatable shaft, the impeller comprising a plurality of blades having a configuration so that when the impeller is rotated in the mineral suspension, the suspension will be thrown downwardly toward the bottom of the vat; and an agitator ring mounted upon the interior periphery of the vat adjacent the location of the impeller, the agitator ring comprising resiliently deformable essentially wedge-shaped segments the ends of which are spaced from the impeller blades so that as the impeller rotates within the mineral suspension, shear zones are developed by the agitator ring thereby generating maximum contact of treatment substance and minerals without excessive boiling of the suspension within the vat at the pulp surface.
2. A cell as defined in claim 1 wherein said agitator ring is hollow, each segment having apertures communicating the hollow thereof with the exterior to minimize clogging the hollow with sediment.
3. A cell as defined in claim 2 wherein said segments are semi-circular in cross section.
4. A cell as defined in claim 2 wherein said segments are square in cross section.
5. A cell as defined in claim 2 wherein said segments have an upper surface comprising an inclined ramp surface with the highest point disposed adjacent the vat and the lowest point disposed adjacent the impeller path.
6. A cell as defined in claim 1 wherein said central shaft upon which the impellers are mounted comprises a cylindrical standpipe concentrically disposed around and spaced from the central shaft, at least the lower end of the standpipe being disposed within the treatment substance and pulp suspension adjacent the impellers; and means disposed at the upper end of the standpipe for delivering the fresh pulp suspension to the upper end of the standpipe so that pulp suspension is communicated directly therethrough to the rotating impeller blades for shearing of large air bubbles into small ones, and dispersion into and throughout openings in the agitator ring.
7. A cell as defined in claim 6 wherein the cylindrical standpipe is provided with spaced apertures at an axial location adjacent the surface level of the treatment substance and pulp suspension.
8. A cell as defined in claim 6 wherein the standpipe is concentrically spaced from the central shaft for rotation therewith and further comprising scoop means mounted upon the standpipe adjacent each spaced aperture so that the opening of the scoop means is in the direction of rotation of the standpipe to recirculate the pulp suspension through the standpipe to the impeller blades.
9. A mineral recovery apparatus comprising in combination a treatment cell adapted to receive a mineral suspension and a treatment substance; a rotatable impeller shaft centrally disposed within and spaced from the side and bottom of the cell; a hollow cylindrical collar concentrically spaced from the impeller shaft and non-rotatably associated therewith; an impeller non-rotatably mounted upon the shaft and cOmprising a plurality of radially projecting blades, each having an inverted triangular cross section for downwardly throwing the mineral suspension; and an annular disc having at least one aperture for passing the mineral suspension therethrough and being attached to and generally below the cylindrical standpipe for rotation therewith, the disc carrying on the underside thereof a plurality of downwardly projecting fingers disposed in spaced locations around the periphery of the disc.
10. An apparatus as defined in claim 9 wherein said fingers are mounted upon the disc by structure accommodating selective removal of the fingers and replacement thereof by similar fingers in the event of structural damage.
11. An apparatus as defined in claim 9 further comprising radially spaced, downwardly projecting paddle blades rigidly secured to the underside of the disc adjacent the fingers and directed radially outward from the axis of the impeller shaft and the rotating standpipe.
12. A mineral treating cell comprising a vat into which mineral bearing pulp suspension and a treatment substance are disposed, the improvement comprising: a rotatable shaft and a disc member non-rotatably mounted upon the shaft, the disc member comprising (a) impeller blades spaced radially outward from the axis of the shaft, (b) at least one aperture adjacent the shaft, (c) a plurality of spaced depending fingers disposed adjacent the periphery thereof and (d) a standpipe non-rotatably mounted upon the disc member and spaced from the shaft for defining a flow path through the aperture.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2839758C2 (en) * 1978-09-13 1982-05-06 Fried. Krupp Gmbh, 4300 Essen Agitator for a flotation system
US4454078A (en) * 1980-11-10 1984-06-12 General Signal Corporation Mixing systems having agitators for mixing gas with liquid
US5591327A (en) * 1993-12-09 1997-01-07 Walters; Jeremy P. A. Flotation equipment
US6832690B2 (en) * 2003-01-02 2004-12-21 Outokumpu Oyj Guiding device for a flotation machine

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1935190A (en) * 1931-07-30 1933-11-14 Nat Aniline & Chem Co Inc Process and apparatus for mixing gases with liquids
US2875897A (en) * 1953-06-22 1959-03-03 Booth Lionel Earl Flotation machine
US2944802A (en) * 1955-02-16 1960-07-12 Denver Equip Co Froth flotation and aeration apparatus
US2966266A (en) * 1957-12-11 1960-12-27 Hugh W Coke Mineral flotation apparatus and method
US2973095A (en) * 1957-07-09 1961-02-28 Galigher Company Impeller-stator combination for aeration machines
US3070229A (en) * 1958-07-21 1962-12-25 Loro & Parisini Spa Apparatus for the froth-flotation of minerals
US3098818A (en) * 1961-04-05 1963-07-23 Denver Equip Co Concentration apparatus and method
US3327851A (en) * 1965-01-25 1967-06-27 Galigher Company Flotation machine and stator therefor
US3378141A (en) * 1963-03-28 1968-04-16 Res & Dev Pty Ltd Froth flotation apparatus
US3437203A (en) * 1963-02-20 1969-04-08 Koichi Nakamura Flotation apparatus
US3491880A (en) * 1967-12-07 1970-01-27 Arthur G Mckee Co Flotation apparatus and process

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1935190A (en) * 1931-07-30 1933-11-14 Nat Aniline & Chem Co Inc Process and apparatus for mixing gases with liquids
US2875897A (en) * 1953-06-22 1959-03-03 Booth Lionel Earl Flotation machine
US2944802A (en) * 1955-02-16 1960-07-12 Denver Equip Co Froth flotation and aeration apparatus
US2973095A (en) * 1957-07-09 1961-02-28 Galigher Company Impeller-stator combination for aeration machines
US2966266A (en) * 1957-12-11 1960-12-27 Hugh W Coke Mineral flotation apparatus and method
US3070229A (en) * 1958-07-21 1962-12-25 Loro & Parisini Spa Apparatus for the froth-flotation of minerals
US3098818A (en) * 1961-04-05 1963-07-23 Denver Equip Co Concentration apparatus and method
US3437203A (en) * 1963-02-20 1969-04-08 Koichi Nakamura Flotation apparatus
US3378141A (en) * 1963-03-28 1968-04-16 Res & Dev Pty Ltd Froth flotation apparatus
US3327851A (en) * 1965-01-25 1967-06-27 Galigher Company Flotation machine and stator therefor
US3491880A (en) * 1967-12-07 1970-01-27 Arthur G Mckee Co Flotation apparatus and process

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2839758C2 (en) * 1978-09-13 1982-05-06 Fried. Krupp Gmbh, 4300 Essen Agitator for a flotation system
US4454078A (en) * 1980-11-10 1984-06-12 General Signal Corporation Mixing systems having agitators for mixing gas with liquid
US5591327A (en) * 1993-12-09 1997-01-07 Walters; Jeremy P. A. Flotation equipment
US6832690B2 (en) * 2003-01-02 2004-12-21 Outokumpu Oyj Guiding device for a flotation machine

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