US3509997A - Laminar flow sluice concentrator - Google Patents

Laminar flow sluice concentrator Download PDF

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Publication number
US3509997A
US3509997A US778446A US3509997DA US3509997A US 3509997 A US3509997 A US 3509997A US 778446 A US778446 A US 778446A US 3509997D A US3509997D A US 3509997DA US 3509997 A US3509997 A US 3509997A
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United States
Prior art keywords
slurry
flow
concentrator
sluice
section
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Expired - Lifetime
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US778446A
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English (en)
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William B Tomlinson
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Carpco Res & Eng Inc
Carpco Research & Eng Inc
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Carpco Res & Eng Inc
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    • A—HUMAN NECESSITIES
    • A21—BAKING; EDIBLE DOUGHS
    • A21C—MACHINES OR EQUIPMENT FOR MAKING OR PROCESSING DOUGHS; HANDLING BAKED ARTICLES MADE FROM DOUGH
    • A21C11/00—Other machines for forming the dough into its final shape before cooking or baking
    • A21C11/16—Extruding machines
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION 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
    • B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/02—Washing granular, powdered or lumpy materials; Wet separating using shaken, pulsated or stirred beds as the principal means of separation
    • B03B5/26—Washing granular, powdered or lumpy materials; Wet separating using shaken, pulsated or stirred beds as the principal means of separation in sluices

Definitions

  • the sluice section includes a first portion defining means for initiating a laminar flow of the slurry and converging the flow, to thereby increase the depth and velocity of the slurry and efficiently stratify the materials into a plurality of strata; a second portion defining means for maintaining the laminar flow of the slurry and diverging the flow, to thereby decrease the depth and velocity of the slurry and evenly spread the strata; and a discharge means for removing a fraction of the stratified material from the concentrator.
  • This invention relates to sluice concentrators, and more particularly to a sluice concentrator that is specifically adapted to separate a desired particulate material from a mixture of particulate materials in which other mterials are present having specific gravities similar to that of the desired material and in which the desired material is present in very small quantities.
  • a well-known phenomenon occurs when a liquid in which particulate materials of different specific gravities are suspended, i.e., a slurry of such materials, is permitted to flow in a relatively tranquil state through a conduit.
  • the particulate materials stratify into a plurality of strata according to their relative specific gravities; the material of greatest specific gravity being on the bottom and the material of least specific gravity being on the top, with the materials of intermediate specific gravities being arranged therebetween.
  • This phenomenon has been used advantageously for separating minerals of different specific gravities.
  • a tapered sluice concentrator is provided, through which a substantialy laminar flow of a slurry of the minerals to be separated is directed.
  • the mineral particles arrange themselves, under the influence of gravity, into strata according to their specific gravities.
  • an increase in the depth and velocity of the slurry tends to accelerate the rate of Stratification.
  • the sluice concentrator of the invention provides a solution to the aforementioned difficulty associated with conventional tapered sluice concentrators, and is particularly adapted for separating finely divided minerals of similar specific gravities.
  • the concentrator of the invention includes a sluice section that is adapted to receive a slurry of the materials to be separated.
  • the sluice section includes; a first portion which defines means for initiating a laminar flow of the slurry and converging said flow, to thereby increase the depth and velocity of the slurry and stratify the materials into a plurality of strata according to their specific gravities; a second portion contiguous with said first portion which defines means for maintaining the laminar flow of the slurry and diverging said flow, to thereby decrease the depth and velocity of the slurry and evenly spread the strata; and a discharge means disposed adjacent the second portion for removing a fraction of the stratified materials from the concentrator.
  • the concentrator also includes a feed means associated with the sluice section for feeding an even flow of the slurry to the first portion of the sluice section.
  • the concentrator further includes at least one additional sluice section which is contiguous with the above-mentioned first section and which is adapted to receive the slurry after it has passed through the first section.
  • the additional sluice section is structurally similar to the first section; including a first portion which defines means for maintaining the laminar flow of the slurry and reconverging said flow, to thereby again increase the depth and velocity of the slurry and restratify the materials into a plurality of strata according to their specific gravities after the above-mentioned first fraction is removed therefrom; a second portion contiguous with said first portion which defines means for maintaining the laminar flow of the slurry and rediverging said flow, to thereby again decrease the depth and velocity of the slurry and again evenly spread the strata; and an additional discharge means disposed adjacent the second portion of the additional sluice section for removing an additional fraction of the stratified materials from the concentrator.
  • FIG. 1 is a plan view of the concentrator of the invention
  • FIG. 2 is an elev-ational view, partially in section, of the concentrator shown in FIG. 1;
  • FIG. 3 is a vertical sectional view of the concentrator shown in FIG. 1;
  • FIG. 4 is a sectional view taken along line 44 of FIG. 3;
  • FIG. 5 is an enlarged vertical sectional view of a portion of the concentrator shown in FIG. 1.
  • FIGS. 1 and 2 A preferred embodiment of the concentrator of the invention is shown in FIGS. 1 and 2, as designated by reference numeral 10.
  • Concentrator includes a conduit 16 defining a first sluice section 12, a second sluice section 14 and a third sluice section 15; the feed end of second section 14 being contiguous with the discharge end of first section 12 and the feed end of third section 15 being contiguous with the discharge end of second section 14.
  • Conduit 16 comprises a pair of opposed, converging, continuous sidewalls 18 and a continuous bottom wall 20, and is supported by a plurality of legs 22.
  • Concentrator 10 also includes a feed means 24 for introducing the slurry into first sluice section 12.
  • the feed means is descibed in detail below.
  • a flow guide 26 is connected to the inside surface of each sidewall 18 along the section of conduit 16 defining first sluice section 12.
  • the flow guides preferably are connected to the sidewalls by adjustable means which permit the position of the guides to be regulated longitudinally of conduit 16.
  • Adjust means conveniently comprise slots 17 formed in sidewalls 18 within which are accommodated threaded studs 19 afifixed to flow guides 26. The studs are locked in position by nuts 25.
  • each of flow guides 26 is defined by an inwardly curved segment 28 and an outwardly curved segment 30.
  • Each inwardly curved segment is contiguous with the associated outwardly curved segment and forms therewithv a continuous unbroken convex curve.
  • First portion 32 defines means for initiating a laminar flow of the slurry introduced therein and converging such flow. Convergence of the flow causes the depth and velocity of the slurry to increase. In the presence of the laminar flow, these conditions induce the particulate materials in the slurry to stratify, under the influence of gravity, into a plurality of strata according to their relative specific gravities.
  • Second portion 34 defines means for maintaining the laminar flow of the slurry'and diverging such flow. Divergence of the flow causes the depth and velocity of the slurry to decrease. In the presence of the laminar flow, these conditions induce the strata of particulate materials to spread laterally of the flow across the surface of bottom wall 20.
  • First sluice section 12 also includes a discharge means 36 disposed adjacent second portion 34 for removing a fraction of the stratified particulate materials from the concentrator.
  • the discharge means comprises a plate 38 which is removably insertable into a recess 40 (FIG. 5) in bottom wall 20, and which preferably is located near the junctures of outwardly curved segments 30 and the inside surfaces of sidewalls 18.
  • Plate 38 may be made of a plastic material, such as polyvinyl chloride, or any other suitable material, and has a transverse slot 42 therein which overlies a transverse slot 44 in bottom wall 20.
  • a fraction of the stratified particulate materials passes through slots 42 and 44 as the slurry flows thereover, and may be separately collected below conduit 16. Since plate 38 is removable, other similar plates having slots of diiferent shapes and dimensions can be substituted for plate 38 as required for reasons discussed in detail below.
  • Second sluice section 14 commences at discharge means 36.
  • a flow guide 39 is connected to the inside surface of each sidewall 18 along the portion of conduit 16 defining sluice section 14. If desired, flow guides 39 may be connected to sidewalls 18 by adjustable means which permit the position of the flow guides to be regulated longitudinally of conduit 16, as described above in connection with flow guides 26.
  • Flow guides 39 are structurally similar to flow guides 26 and form with bottom wall 20 a first portion 41 and a second portion 43.
  • First portion 41 similarly to first portion 32, defines means for maintaining the laminar flow of the slurry introduced into the feed end of section 14 from the discharge end of section 12 and reconverging such flow. Reconvergence of the flow causes the depth and velocity of the slurry to again increase, thereby inducing the particulate materials in the slurry to restratify after the first faction has been removed therefrom.
  • Second portion 43 similarly to second portion 34, defines means for maintaining the laminar flow of the slurry and rediverging such flow. Redivergence of the flow causes the depth and velocity of the slurry to again decrease, thereby inducing the particulate materials in the slurry to again spread laterally across the surface of bottom wall 20.
  • Second sluice section 14 also includes a discharge means 46, which is structurally similar to discharge means 36, for removing a second fraction of the stratified particulate materials from the concentrator.
  • Discharge means 46 preferably is located near the lower junctures 45 of flow guides 39 and the inside surfaces of sidewalls 18.
  • Third sluice section 15 commences at discharge means 46, and includes a pair of flow guides 47, which are structurally similar to flow guides 26 and 39, and a discharge means 48 which is structurally similar to discharge means 36 and 46. A third fraction of the stratified particulate materials is removed from the concentrator by discharge means 48.
  • Conduit 16 extends downwardly a short distance beyond third sluice section 15, which terminates at discharge means 48, to discharge end 23.
  • the fraction of the particulate materials not removed by discharge means 36, 46 and 48 flows out of conduit 16 at discharge end 23.
  • the inside surfaces of sidewalls 18, bottom wall 20, and flow guides 26, 39 and 47 are made so smooth as is economicaly feasible, such as by coating such surfaces with a durable plastic material, thereby reducing boundary layer turbulence along the surfaces of the conduit contacted by the slurry.
  • Feed. means 24 includes a receptacle 50 which is positioned above feed end 21 and which comprises a plurality of sidewalls 52, 54, 56 and 58, and a bottom wall 60.
  • Receptacle 50 has an open top through which a continuous supply of the slurry of particulate materials to be separated is introduced therein.
  • the receptacle has at least one port, and preferably a plurality of ports 62, opening therefrom above bottom Wall 60. As shown in FIG. 4, ports 62 preferably comprise a plurality of horizontally spaced circular openings in sidewall 56; the latter being disposed transversely of conduit 16.
  • Feed means 24 also includes a baflle 63 disposed transversely of conduit. 16 and interposed between receptacle 50 and first portion 32 of first sluice section 12.'Bafl le 63 has a rectangular cutout therein which is positioned adjacent bottom wall 20 and defines therewith a relatively narrow transverse opening 65, through which the slurry flows from feed end 21 into first portion 32. Any turbulence generated by the passage of the slurry from receptacle 50 into feed end 21 is suppressed by the passage of the slurry through opening 65. Baflle 63 thus insures that a relatively tranquil flow of the slurry will pass into first portion 32.
  • Concentrator is specifically adapted to separate finely divided minerals of diflferent specific gravities. And in particular, the concentrator has proven extremely efficient for separating a desired heavy mineral from mixtures in which other minerals are present having specific gravities similar to that of the desired mineral and in which the desired mineral is present in very small quantities.
  • An example of such a desired heavy mineral is monazite, an ore of cerium and thorium. Monazite has a specific gravity of 5.0, and frequently is found in mixtures containing ilmenite, specific gravity 4.7; zircon, specific gravity 4.68; garnet, specific gravity 4.3; rutile, specific gravity 4.25; staurolite, specific gravity 3.75; kyanite, specific gravity 3.66 and other minerals of lesser specific gravities.
  • a continuous supply of a slurry of a mixture of the minerals to be separated is introduced into receptacle 50 and a head of the slurry established therein (FIG. 3). From receptacle 50 the slurry fiows through ports 62 into feed end 21 and through bafile opening 65 into first portion 32 of first sluice section 12.
  • first portion 32 laminar flow condition is achieved almost immediately.
  • the flow is then converged smoothly as it passes through the zone defined by portion 32 so that the depth and velocity of the slurry are gradually increased.
  • the mineral particles are elficiently stratified according to their different specific gravities with the desired heavy mineral, such as monazite, comprising the lower-most strata.
  • the slurry then passes into the second portion 34 of first sluice section 12 where the laminar flow condition of the slurry is maintained and the flow diverged smoothly as the flow passes through the zone defined by portion 34.
  • the depth and velocity of the slurry is decreased so that the strata of mineral particles are slowed down and spread evenly across the width of bottom wall 20.
  • the initial convergence of the flow promotes the recovery of a high grade concentrates fraction and the subsequent divergence of the flow promotes a high recovery rate of such fraction.
  • plate 38 may be removed from recess 40 and replaced by a similar plate having a slot therein of a different shape and dimensions than slot 42.
  • the plates of discharge means 46 and 48 may be replaced by other plates having slots of different shapes and dimensions therein.
  • the wider the slot in a particular plate the greater will be the amount of mineral particles removed from the concentrator by the discharge means in which such plate is employed. This permits the grade and recovery rate of the separated fractions to be accurately controlled.
  • Concentrator 10 comprises an eflicient and relatively inexpensive means for separating particulate materials of different specific gravities, and in particular for separating a desired heavy mineral from a mixture of finely divided mineral particles in which other minerals having specific gravities similar to that of the desired mineral are present.
  • a concentrator for separating particulate materials of different specific gravities comprising:
  • conduit having an upper feed end and a lower discharge end
  • a feed means associated with said conduit for feeding an even flow of a slurry of the materials to be separated into said feed end, said feed means including turbulence suppression means for promoting a tranquil flow of the slurry from said feed end;
  • At least one sluice section defined by said conduit and adapted to receive the slurry from said feed end
  • said sluice section including a first portion defining means for initiating and maintaining a laminar flow of the slurry therethrough and converging said flow, thereby increasing the depth and velocity of the slurry and stratifying the materials into a plurality of strata according to the different specific gravities thereof, a second portion contiguous with said first portion, said second portion defining means for maintaining the laminar flow of the slurry therethrough and diverging said flow, thereby decreasing the depth and velocity of the slurry and evenly spreading said strata, and a discharge means disposed adjacent said second portion for removing a fraction of the stratified materials from the concentrator.
  • a second sluice section defined by said conduit and contiguous with said first-mentioned section, said second sluice section being adapted to receive the slurry after it has passed through said first section and including a first portion defining means for maintaining the laminar flow of the slurry therethrough and reconverging said flow, thereby again increasing the depth and velocity of the slurry and restratifying the materials into a plurality of strata according to the different specific gravities thereof after said firstmentioned fraction is removed therefrom, a second portion defining means for maintaining the laminar fiow of the slurry therethrough and rediverging said flow, thereby again decreasing the depth and velocity of the slurry and again evenly spreading said strata, and a second discharge means disposed adjacent said second portion of said second section for removing a second fraction of the stratified materials from the concentrator.
  • a third sluice section defined by said conduit and contiguous with said second section, said third sluice section being adapted to receive the slurry after it has passed through said second section and including a first portion defining means for maintaining the laminar flow of the slurry therethrough and reconverging said fiow, thereby again increasing the depth and velocity of the slurry and restratifying the materials into a plurality of strata according to the different specific gravities thereof after said second fraction is removed therefrom, a second portion defining means for maintaining the laminar flow of the slurry and rediverging said flow, thereby again decreasing the depth and velocity of the slurry therethrough and again evenly spreading said strata, and a third discharge means disposed adjacent said second portion of said third section for removing a third 8 fraction of the stratified materials from the concentrator.
  • a concentrator for separating particulate materials of different specific gravities as recited in claim 7, wherein said first and second portions of each of said first, second and third sluice sections are formed by said conduit and a pair of opposed continuous flow guides.
  • a concentrator for separating particulate materials of different specific gravities as recited in claim 8, wherein said flow guides are curved inwardly along said first portion'of each of said first, second and third sections and are curved outwardly along said second portion of each of said sections.
  • a concentrator for separating particulate materials of different specific gravities as recited in claim 1, wherein said feed means includes a receptacle for receiving a continuous supply of the slurry, said receptacle having at least one port opening therefrom above the bottom thereof, said port being positioned above said feed end so that a head of the slurry will be established within the receptacle and the slurry will be discharged therefrom through said port in an even flow into the feed end.
  • a process for separating particulate materials of different gravities comprising the successive steps of:

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
US778446A 1968-11-25 1968-11-25 Laminar flow sluice concentrator Expired - Lifetime US3509997A (en)

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US77844668A 1968-11-25 1968-11-25

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US (1) US3509997A (enrdf_load_stackoverflow)
DE (1) DE1952003A1 (enrdf_load_stackoverflow)
FR (1) FR2024112A1 (enrdf_load_stackoverflow)
GB (1) GB1225211A (enrdf_load_stackoverflow)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3731811A (en) * 1969-07-02 1973-05-08 Bahco Ab Apparatus for adjusting the concentration of a circulating liquid suspension to a determined, constant value
US3909398A (en) * 1973-10-16 1975-09-30 Meat Separator Corp Bone dropout pan
US4222857A (en) * 1977-12-15 1980-09-16 Mccarthy James R Apparatus for separating selected particulate materials from a mixture of solids and liquids

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2034662C1 (ru) * 1994-04-29 1995-05-10 Борис Петрович Садковский Способ обогащения полезных ископаемых и устройство для его осуществления

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US189928A (en) * 1877-04-24 Improvement in ore sluices and concentrators
US1704185A (en) * 1927-02-24 1929-03-05 France Antone Plant for washing coal and other minerals
US1771081A (en) * 1927-03-04 1930-07-22 France Antoine Plant for washing coal and other minerals
US2171674A (en) * 1937-02-12 1939-09-05 Walter W Johnson Classifier

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US189928A (en) * 1877-04-24 Improvement in ore sluices and concentrators
US1704185A (en) * 1927-02-24 1929-03-05 France Antone Plant for washing coal and other minerals
US1771081A (en) * 1927-03-04 1930-07-22 France Antoine Plant for washing coal and other minerals
US2171674A (en) * 1937-02-12 1939-09-05 Walter W Johnson Classifier

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3731811A (en) * 1969-07-02 1973-05-08 Bahco Ab Apparatus for adjusting the concentration of a circulating liquid suspension to a determined, constant value
US3909398A (en) * 1973-10-16 1975-09-30 Meat Separator Corp Bone dropout pan
US4222857A (en) * 1977-12-15 1980-09-16 Mccarthy James R Apparatus for separating selected particulate materials from a mixture of solids and liquids

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GB1225211A (enrdf_load_stackoverflow) 1971-03-17
FR2024112A1 (enrdf_load_stackoverflow) 1970-08-28
DE1952003A1 (de) 1970-05-27

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