US1705351A - Method and apparatus for the classification of materials by elutriation - Google Patents

Method and apparatus for the classification of materials by elutriation Download PDF

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US1705351A
US1705351A US207977A US20797727A US1705351A US 1705351 A US1705351 A US 1705351A US 207977 A US207977 A US 207977A US 20797727 A US20797727 A US 20797727A US 1705351 A US1705351 A US 1705351A
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tank
water
particles
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valve
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/62Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type
    • B03B5/623Upward current classifiers

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  • This invention has reference to a method and apparatus for the classification by elutriation of materials of-various kinds as for instance those that, have to be powdered before classification and also those thatare naturally of a soft nature, as for example fullers earth, china cla and the like that do not need to be powdere It relates particularly to amethod and apparatus whereby oversize particles can be separated from fine particles in amixture thereof with water coming from another classifier in which powdered material has been subjected to a preliminary classification by elutriation and it may be desired to return the said oversize particles to a wet grinding mill to be reground.
  • Apparatus suitable for purposes such as mentioned comprises according to the invention, a tank having an inlet at the top for the mixture of water with the material to be treated, a bowl, conical or like shaped lower end having a contracted outlet at the bottom for oversize particles, a valve for closing the said outlet, a horizontal partition arranged at an intermediate portion of its height and formed with a number of inverted conical passages, a clean water supply pipe terminating below the partition and means adapted to open and control the valve in an automatic manner and permit oversize particles to be discharged from the tank to a grinding mill, or other receptacle or place, to suit requirement, the valve operating means being dependent for action upon the accumulation'of a predetermined depth of coarse particles in the lower portion ofthe tank.
  • Fig. 1 shows partly in side elevation and partly in vertical section, one construction of apparatus embodying the invention.
  • Fig, 2 shows in plan, a part of such apparatus.
  • Fig. 3 shows in vertical section one construction of meansthat may be used for automatically opening and controlling the outlet valve of such apparatus.
  • Fig. 4 shows partly in elevation and partly in vertical section and Fig. 5 in plan, with parts removed, modified means for automatically opening and controlling the said outlet valve.
  • the apparatus shown in Figs. 1 and 2 comprise a tank at having at the top an inlet connected to a pipe 0 for supplying the mixture of water with oversize and fine particlesof solid material to be classified, and a bowl or like shaped lower end d that forms a collecting chamber having a contracted outlet 03 for partially dewatered coarse particles of solid material, a valve 6 for closing the said outlet, a horizontal artition f arranged at an intermediate portion of the height of the tank" and formed with a number of inverted conical passages g, a clean water supply pipe h terminating below the partition and means adapted to open and control the valve in an automatic manner and permit oversize particles to be discharged from the chamber 03 to the feed box of a grinding mill, a por-' tion of which is shown at z, the valve operating means being dependent for action upon the accumulation of coarseparticles in the lower portion of the tank a.
  • the inletat the upper part of the tank consists of a centrally .arranged. vertical tube is through which the mixture of water (hereinafter called for distinction carrier water) and oversize and fine particles supplied by the pipe 0, it may be from a hopper 0 ⁇ into which it. is fed from a chute c with water, is projected downward intothe tank a.
  • carrier water mixture of water
  • An outer vertical tube on carrying at its lower end a truncated conical shell n surrounds the central tube lcso as to form therewith an annular passage 0, serving as a vent for bubbles of air in the carrier water, and between the said conical shell n and the wall of the tank a is a second truncated conical shell 1* forming, with the inner shell n, an inwardly and upwardly inclined.
  • annular passage 8 and with'the tank, an annular pocket t of substantially inverted conical shape in section and having an annular outlet opening t at the bottom.
  • the top of the tank a is provided with a water bverflow trough u connected'to an overflow pipe o.
  • the arrangement is such that the mixture of ence of their own weight. and the increased and 1' and thence into the upper part of the tank through which it rises to the top thereof where it overflows into the trough u and the overflow pipe '2) so that it can be led away to any desired place, it may be a settling tank in which the fine particles settle. Particles of intermediate size will fall, under the influence of gravity,'through the water 'rising'to the top of the tank a and collect in the outer annular pocket 25 and fall through the annular opening i into the lower part of the tank above the partition f and there mingle with the oversize particles separating out in this portion of the tank.
  • teetering water a small sup 1y of clean water, hereinafter called teetering water, isfed into the said collecting chamber d, below the partition, through a fresh Water supply pipe h and rises through the several conical passages in parallel at a velocity adjusted to allow relatively coarse particles only to descend.
  • the oversize particles collected in the chamber (1 are discharged through the outlet (Z in a partially dewatered condition and into, it may be, the feedbox c3 of a grinding mill, or other receptacleor place under the control of the aforesaid valve 0 which, as hereinbefore stated, is more or less opened or closed in an automatic manner depending upon the height of the coarse particles collected the chamber cl.
  • valve 6 conveniently in the form of a hinged shoe as shown, normally closes the outlet d under the action of a Weight w and is moved into a more or less open position by a tension device, for instance a rod 3 connected to a lever arm a which is arrangedto be raised or lowered by mechanism, dependent for action upon the depth of the coarse particles in the collecting chamber (Z.
  • a tension device for instance a rod 3 connected to a lever arm a which is arrangedto be raised or lowered by mechanism, dependent for action upon the depth of the coarse particles in the collecting chamber (Z.
  • This mechanism may, according to oneconstruction and as shown in Fig. 3, comprise a gear box I mounted upon the top of the dewatering tank, a pair of semi-circularcams 2 and 3 having upwardly inclined faces, arranged to be rotated at a very slow speed, as by bevel gear 4 from a shaft 5 driven from any convenient source, and a vertical centrally arranged rotary spindle 6 (hereinafter called the floating spindle) which acts against the lever a and is provided with. a pair of lateral arms 7 and 8 carrying rollers 9 and 10 which bear on the respective faces of the cams.
  • the degree of slope of the cam faces is not constant but increases from bottom to top.
  • the floating spindle 6 is provided with a second pair of co-axial arms 11 which engage inoppositely arranged vertical slots 12 in an enlarged end 13* of a vertical spindle 13 that extends centrally through the dewatering tank a and partition 7 (Fig.1) therein into the collecting chamber (Z and is there connected by a pair of arms 14 to two quadrant shaped blades 15 arranged within the collecting chamber 03 where they become more or less embedded in the coarse particles A collected therein.
  • the arrangement is such that the floating spindle'6 is constantly subjected to two opposing stresses, namely, a
  • the arrangement is such that, at starting, when there are. no oversize particles in the collecting chamber d, thevalve e is held in its closed position by the weight w and the cams 2 and 3, rollers 9 and 10, floating spindle 6, vertical spindle 13 and blades 15, 1'0- tate slowly as a whole.
  • the rollers 9 and 10 When oversize particles have collected in the chamber d and offer a certain degree of resistance to motion of the blades 15, the rollers 9 and 10 are caused to move a short distance up the faces of the cams 2and 3 and thereby open the valve e to a small extent which allows coarse particles to escape, and if coarse particles are deposited in the charnber 12 at the same rate as coarse particles are being discharged'through theoffer less resistance to the motion of the blades, and the said rollers will descend the faces of the cams and permit the valve to move and reduce therate of discharge of particles.
  • the said rollers will fall sufliciently to enable the valve to close the discharge outlet and the valve will not be again opened until a suflicient mass thereof has formed to offer sufficient resistance to motion of the blades as to cause the rollers to travel up the faces of the cams and thereby again open the valve to a greater or less extent to enable the discharge of particles to again take place.
  • the discharge of coarse particles from the tank is caused to take place continuously or intermittently, in anautomatic manner, according to the rate of deposit of coarse particles in the lower portion ofthe tank.
  • Figs. 4 and 5 show a modified and preferred arrangement for automatically controlling the outlet valve.
  • This arrangement is shown applied to the dewatering arrangement shown in Fig. 1, in this example, the cams 2 and 3 are fixed to a worm wheel 16 driven by a worm 17' on a driving shaft 5 and journalled upon the upper end of a central support 1 carried by the bottom plate 1 of the gear box 1.
  • .T-his gear box is adapted to be fixed to the top of the tank a as in the arrangement shown in Fig. 1.
  • the pair of rollers 9 and 10 are carried by a horizontal shaft 18 to the central portion of which is fixed a vertical spindle 19 extending freely into a hole 20 in the shaft 13 'to the lower end of wheels 24 mounted to turn on the transverse shaft 18.
  • z is a lever pivoted at one end at 2 and connected at its other endthrough a rod to the weighted end of an outlet valve, like the lever z inFigs. 1 and 2.
  • An intermediate portion of the said lever has jointed thereto at 2 an abutment device 25 that bears through a ball bearing 26, upon the central portion of the horizontal shaft 18.
  • the vertical'shaft 13 is driven from the rotating cams 2 and 3 through the rollers 9 and 10, shaft 18, grooved the rollers 9 and 10 bearing thereon and lift the latter and the shaft 18, which, through the abutment device 25 lifts the lever a about 1ts plvot 2 and opens the discharge valve to a greater or less degree, as in the arrangement shown in Figs. 1 and 2.
  • the pipe it used for supplying teetering water to the collectlng chamber cl below the teetering partition f (Fig. 1) is arranged'to surround the shaft 13 and extends, like such shaft, through the said partition into the collecting chamber at (Fig. 1). It receives its supply of water from a chamber 27 formed in the central support 1 and connected to a supply pipe 28.
  • a liquid tight packing 29 is arranged between the support 1 and shaft 13 at the top of the chamber 27.
  • the details of construction can be modified in various ways.
  • What I claim is z- 1.
  • a method of classifying material by elutriation consisting in projecting a mixture of the said material with water into a body of Water that is flowing upwardly at a less velocity than the downwardly projected mixture, whereby the heavier' lea particles of material in the mixture will be projected to the bottom of the body of water while lighter particles in the mixture will and allowing the heavier and cleaned'particles to fall through the'washing water.
  • a method of classifying material by elutriation consisting in projecting a mixture of the said material with water into a body of water that is flowing upwardlyat a less velocity than the downwardly projected mixture, whereby the-heav ier particles of material in the mixture will be projected to the bottom of the body of water while'lighter particles in the mixture will be carried upward .by the rising water, dividing the heavier particles into separate accumulations thereof, washing said accumulations of heavier particles by clean water caused to flow upward through them so as to remove lighter particles attached to the heavier particles and carry such lighter particles upward into the rising body of water, allowing the heavier and cleaned particles to fall through the washing water, running off the rising Water with lighter particles and automatically removing the heavier and cleaned particles from the washing water.
  • Apparatus for the classification of material by elutriation comprising a tank having an outlet at the top, a valve controlled outlet at the bottom, a horizontal partition arranged at an intermediate portion of the height of said tank and having a plurality of inverted truncated conical passages therethrough,' a verticahconduit arranged in the upper central portion of said tank and above said partition, the space between the lower end of said conduit and partition being unobstructed, means for causing a mixture of the material to be classified and water to be projeeted downward through said conduit and means for supplying clean washing water to said tank below said partition.
  • Apparatus for the classification of material by elutriation comprising a tank having an outlet at the top, a valve controlled outlet at the bottom, a horizontal partition arranged at an intermediate portion of the height of said tank and having a plurality of inverted truncated conical passages therethrough, a vertical conduit arranged in the upper central portion of said tank and above said partition, the space between the lower end of said conduit and partition being unobstructed, a receptacle for a mixture of the material to be classified, and water, connected to and arranged at a height above said conduit sufficient to cause the mixture to be projected downward through said conduit into the portion of the tank above said partition, and means for delivering a stream of clean washing water to said tank below said partition.
  • Apparatus for the classification of material by elutriation comprising a tank having upper and lower outlets, a loaded valve adapted normally to close the lower. outlet, a horizontal partition arranged at an intermediate portion of the height of said tank between said outlets, and having a plurality of inverted conical passages therein, a vertical conduit arranged in the upper central portion of said tank and above said partition, the space between the lower end of said conduit and partition being unobstructed, means for causing a mixture of the material to be classified, with water, to be delivered in a downward direction under pressure through said condult, means for supplying clean washing.
  • valve opening means being dependent for action on accumulation of coarse material in the lower portion of said tank.
  • Apparatus for the classification of material by elutriation comprising a tank, having an upper outlet overflow, a horizontal partition arranged at an intermediate portion of the height of said tank and having a plurality of inverted truncated openings therethrough, a vertical conduit arranged in the upper central portion of said tank and above said par tition, means for delivering a mixture of material to be classified, and water, under pressure, in a downward direction through said conduit into the tank towards said partition,
  • Apparatus for the classification of material by elutriation comprising a tank havmg an upper outlet overflow, a horizontal partition arranged at an intermediate portion of the height of said tank and having a plurality of inverted truncated openings therethrough, a vertical conduit arranged in the upper central portion of said tank and above said partition, means for delivering a mixture of materialto be classified, and water, under pressure, in .a downward direction through said conduit into the tank towards said partition, means for delivering clean washing Water into said tank below said partition and a second truncated conical shell arranged between the first mentioned shell and the wall of the tank and forming with the said first mentioned shell an annular passage communicating with the overflow outlet for water carrying fine particles of powdered material, and with the wall of the tank, an inverted conical pocket having an annular outlet at the bottom through which particles of'intermediate size can fall into the portion of the tank above said partition.

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Description

March 1929- L. ANDREWS ,705,351 METHOD AND APPARATUS FOR THE CLASSIFICATION OF MATERIALS BY ELUTRIATION v Filed July 23, 1927 2 Sheets-Sheet 1 Patented Mar. 12, 1929.
UNITED STA TES' LEONARD ANDREWS, OF WESTMINSTER, ENGLANDL mnrnon AND APPARATUS FOR THE CLASSIFICATION or MATERIALS BY- A ELUTRIATION.
Application filed July 23, 1927, Serial No. 207,977, and in Great Britain July 30, 1926.
This invention has reference to a method and apparatus for the classification by elutriation of materials of-various kinds as for instance those that, have to be powdered before classification and also those thatare naturally of a soft nature, as for example fullers earth, china cla and the like that do not need to be powdere It relates particularly to amethod and apparatus whereby oversize particles can be separated from fine particles in amixture thereof with water coming from another classifier in which powdered material has been subjected to a preliminary classification by elutriation and it may be desired to return the said oversize particles to a wet grinding mill to be reground. In the latter case,'it is important as afiecting the fliciency of grinding, that all fine particles remaining in the water, should be removed from the oversize particles and that the water escaping with the oversize particles should be reduced it may be to about one third of the weight of the particles being discharged.
Apparatus suitable for purposes such as mentioned, comprises according to the invention, a tank having an inlet at the top for the mixture of water with the material to be treated, a bowl, conical or like shaped lower end having a contracted outlet at the bottom for oversize particles, a valve for closing the said outlet, a horizontal partition arranged at an intermediate portion of its height and formed with a number of inverted conical passages, a clean water supply pipe terminating below the partition and means adapted to open and control the valve in an automatic manner and permit oversize particles to be discharged from the tank to a grinding mill, or other receptacle or place, to suit requirement, the valve operating means being dependent for action upon the accumulation'of a predetermined depth of coarse particles in the lower portion ofthe tank.
In the accompanying illustrative drawings, Fig. 1 shows partly in side elevation and partly in vertical section, one construction of apparatus embodying the invention. Fig, 2 shows in plan, a part of such apparatus. Fig. 3 shows in vertical section one construction of meansthat may be used for automatically opening and controlling the outlet valve of such apparatus. Fig. 4 shows partly in elevation and partly in vertical section and Fig. 5 in plan, with parts removed, modified means for automatically opening and controlling the said outlet valve.
The apparatus shown in Figs. 1 and 2 comprise a tank at having at the top an inlet connected to a pipe 0 for supplying the mixture of water with oversize and fine particlesof solid material to be classified, and a bowl or like shaped lower end d that forms a collecting chamber having a contracted outlet 03 for partially dewatered coarse particles of solid material, a valve 6 for closing the said outlet, a horizontal artition f arranged at an intermediate portion of the height of the tank" and formed with a number of inverted conical passages g, a clean water supply pipe h terminating below the partition and means adapted to open and control the valve in an automatic manner and permit oversize particles to be discharged from the chamber 03 to the feed box of a grinding mill, a por-' tion of which is shown at z, the valve operating means being dependent for action upon the accumulation of coarseparticles in the lower portion of the tank a. In the example nowbeing described, the inletat the upper part of the tank consists of a centrally .arranged. vertical tube is through which the mixture of water (hereinafter called for distinction carrier water) and oversize and fine particles supplied by the pipe 0, it may be from a hopper 0} into which it. is fed from a chute c with water, is projected downward intothe tank a. An outer vertical tube on carrying at its lower end a truncated conical shell n surrounds the central tube lcso as to form therewith an annular passage 0, serving as a vent for bubbles of air in the carrier water, and between the said conical shell n and the wall of the tank a is a second truncated conical shell 1* forming, with the inner shell n, an inwardly and upwardly inclined.
annular passage 8, and with'the tank, an annular pocket t of substantially inverted conical shape in section and having an annular outlet opening t at the bottom. The top of the tank a is provided with a water bverflow trough u connected'to an overflow pipe o.
. The arrangement is such that the mixture of ence of their own weight. and the increased and 1' and thence into the upper part of the tank through which it rises to the top thereof where it overflows into the trough u and the overflow pipe '2) so that it can be led away to any desired place, it may be a settling tank in which the fine particles settle. Particles of intermediate size will fall, under the influence of gravity,'through the water 'rising'to the top of the tank a and collect in the outer annular pocket 25 and fall through the annular opening i into the lower part of the tank above the partition f and there mingle with the oversize particles separating out in this portion of the tank.
The oversize particles fall on to the partition 7, which forms a teetering bed, and through the conical passages g therein in which they will gravitate into the collectingchamber d. To prevent any fine material passing through the conical passages g in the partition, to the collecting chamber d, a small sup 1y of clean water, hereinafter called teetering water, isfed into the said collecting chamber d, below the partition, through a fresh Water supply pipe h and rises through the several conical passages in parallel at a velocity adjusted to allow relatively coarse particles only to descend.
So long as theconical passages g are all free of solid matter, the clear teetering water flows with equal velocity upward through all ofthem but as soon asthe material has collected more in some passages than in others, the increased density in the charged passages restricts the flow of teetering water therethrough to such an extent as to allow the cparse particles to discharge until these pas-Q sagg'es become free ones, thus allowing other passages to discharge in their turn.
The oversize particles collected in the chamber (1 are discharged through the outlet (Z in a partially dewatered condition and into, it may be, the feedbox c3 of a grinding mill, or other receptacleor place under the control of the aforesaid valve 0 which, as hereinbefore stated, is more or less opened or closed in an automatic manner depending upon the height of the coarse particles collected the chamber cl. According to one arrangement for this purpose the valve 6, conveniently in the form of a hinged shoe as shown, normally closes the outlet d under the action of a Weight w and is moved into a more or less open position by a tension device, for instance a rod 3 connected to a lever arm a which is arrangedto be raised or lowered by mechanism, dependent for action upon the depth of the coarse particles in the collecting chamber (Z.
This mechanism may, according to oneconstruction and as shown in Fig. 3, comprise a gear box I mounted upon the top of the dewatering tank, a pair of semi-circularcams 2 and 3 having upwardly inclined faces, arranged to be rotated at a very slow speed, as by bevel gear 4 from a shaft 5 driven from any convenient source, and a vertical centrally arranged rotary spindle 6 (hereinafter called the floating spindle) which acts against the lever a and is provided with. a pair of lateral arms 7 and 8 carrying rollers 9 and 10 which bear on the respective faces of the cams. The degree of slope of the cam faces is not constant but increases from bottom to top. The floating spindle 6 is provided with a second pair of co-axial arms 11 which engage inoppositely arranged vertical slots 12 in an enlarged end 13* of a vertical spindle 13 that extends centrally through the dewatering tank a and partition 7 (Fig.1) therein into the collecting chamber (Z and is there connected by a pair of arms 14 to two quadrant shaped blades 15 arranged within the collecting chamber 03 where they become more or less embedded in the coarse particles A collected therein. The arrangement is such that the floating spindle'6 is constantly subjected to two opposing stresses, namely, a
downward pressure caused by the lever arm 2, due to the weight as acting to close the valve 6 and acting to cause the rollers 9 and 10 to run down the faces of the cams 2 and 3 and thus permit the valve to be closed, and to a retarding torque, due to motion of the blades 15 inthe mass of coarse particles A, and which tends to cause the rollers to roll up the faces of the said cams and thereby raise the floating spindle 6 and lever z and open the valve e to a greater or less extent.
The arrangement is such that, at starting, when there are. no oversize particles in the collecting chamber d, thevalve e is held in its closed position by the weight w and the cams 2 and 3, rollers 9 and 10, floating spindle 6, vertical spindle 13 and blades 15, 1'0- tate slowly as a whole. When oversize particles have collected in the chamber d and offer a certain degree of resistance to motion of the blades 15, the rollers 9 and 10 are caused to move a short distance up the faces of the cams 2and 3 and thereby open the valve e to a small extent which allows coarse particles to escape, and if coarse particles are deposited in the charnber 12 at the same rate as coarse particles are being discharged'through theoffer less resistance to the motion of the blades, and the said rollers will descend the faces of the cams and permit the valve to move and reduce therate of discharge of particles. If the rate of deposit of coarse particles falls to such an extent that the mass thereof offers little or no resistance to movement of the blades, the said rollers will fall sufliciently to enable the valve to close the discharge outlet and the valve will not be again opened until a suflicient mass thereof has formed to offer sufficient resistance to motion of the blades as to cause the rollers to travel up the faces of the cams and thereby again open the valve to a greater or less extent to enable the discharge of particles to again take place. Thus, the discharge of coarse particles from the tank is caused to take place continuously or intermittently, in anautomatic manner, according to the rate of deposit of coarse particles in the lower portion ofthe tank.
. Figs. 4 and 5 show a modified and preferred arrangement for automatically controlling the outlet valve. This arrangement is shown applied to the dewatering arrangement shown in Fig. 1, in this example, the cams 2 and 3 are fixed to a worm wheel 16 driven by a worm 17' on a driving shaft 5 and journalled upon the upper end of a central support 1 carried by the bottom plate 1 of the gear box 1. .T-his gear box is adapted to be fixed to the top of the tank a as in the arrangement shown in Fig. 1. The pair of rollers 9 and 10 are carried by a horizontal shaft 18 to the central portion of which is fixed a vertical spindle 19 extending freely into a hole 20 in the shaft 13 'to the lower end of wheels 24 mounted to turn on the transverse shaft 18. z is a lever pivoted at one end at 2 and connected at its other endthrough a rod to the weighted end of an outlet valve, like the lever z inFigs. 1 and 2. An intermediate portion of the said lever has jointed thereto at 2 an abutment device 25 that bears through a ball bearing 26, upon the central portion of the horizontal shaft 18. In this modified arrangement the vertical'shaft 13 is driven from the rotating cams 2 and 3 through the rollers 9 and 10, shaft 18, grooved the rollers 9 and 10 bearing thereon and lift the latter and the shaft 18, which, through the abutment device 25 lifts the lever a about 1ts plvot 2 and opens the discharge valve to a greater or less degree, as in the arrangement shown in Figs. 1 and 2.
In the example shown in Fig. 4, the pipe it used for supplying teetering water to the collectlng chamber cl below the teetering partition f (Fig. 1) is arranged'to surround the shaft 13 and extends, like such shaft, through the said partition into the collecting chamber at (Fig. 1). It receives its supply of water from a chamber 27 formed in the central support 1 and connected to a supply pipe 28.
A liquid tight packing 29 is arranged between the support 1 and shaft 13 at the top of the chamber 27. The details of construction can be modified in various ways.
What I claim is z- 1. A method of classifying material by elutriation, said method consisting in projecting a mixture of the said material with water into a body of Water that is flowing upwardly at a less velocity than the downwardly projected mixture, whereby the heavier' lea particles of material in the mixture will be projected to the bottom of the body of water while lighter particles in the mixture will and allowing the heavier and cleaned'particles to fall through the'washing water.
. 2. A method of classifying material by elutriation, said method consisting in projecting a mixture of the said material with water into a body of water that is flowing upwardlyat a less velocity than the downwardly projected mixture, whereby the-heav ier particles of material in the mixture will be projected to the bottom of the body of water while'lighter particles in the mixture will be carried upward .by the rising water, dividing the heavier particles into separate accumulations thereof, washing said accumulations of heavier particles by clean water caused to flow upward through them so as to remove lighter particles attached to the heavier particles and carry such lighter particles upward into the rising body of water, allowing the heavier and cleaned particles to fall through the washing water, running off the rising Water with lighter particles and automatically removing the heavier and cleaned particles from the washing water.
3. Apparatus for the classification of material by elutriation, comprising a tank having an outlet at the top, a valve controlled outlet at the bottom, a horizontal partition arranged at an intermediate portion of the height of said tank and having a plurality of inverted truncated conical passages therethrough,' a verticahconduit arranged in the upper central portion of said tank and above said partition, the space between the lower end of said conduit and partition being unobstructed, means for causing a mixture of the material to be classified and water to be projeeted downward through said conduit and means for supplying clean washing water to said tank below said partition.
4. Apparatus for the classification of material by elutriation, comprising a tank having an outlet at the top, a valve controlled outlet at the bottom, a horizontal partition arranged at an intermediate portion of the height of said tank and having a plurality of inverted truncated conical passages therethrough, a vertical conduit arranged in the upper central portion of said tank and above said partition, the space between the lower end of said conduit and partition being unobstructed, a receptacle for a mixture of the material to be classified, and water, connected to and arranged at a height above said conduit sufficient to cause the mixture to be projected downward through said conduit into the portion of the tank above said partition, and means for delivering a stream of clean washing water to said tank below said partition.
5. Apparatus for the classification of material by elutriation, comprising a tank having upper and lower outlets, a loaded valve adapted normally to close the lower. outlet, a horizontal partition arranged at an intermediate portion of the height of said tank between said outlets, and having a plurality of inverted conical passages therein, a vertical conduit arranged in the upper central portion of said tank and above said partition, the space between the lower end of said conduit and partition being unobstructed, means for causing a mixture of the material to be classified, with water, to be delivered in a downward direction under pressure through said condult, means for supplying clean washing.
water to said tank below said partition and rotary means adapted to open said valve automatically against the action of the closing load thereon, said valve opening means being dependent for action on accumulation of coarse material in the lower portion of said tank.
6. Apparatus for the classification of material by elutriation, comprising a tank, having an upper outlet overflow, a horizontal partition arranged at an intermediate portion of the height of said tank and having a plurality of inverted truncated openings therethrough, a vertical conduit arranged in the upper central portion of said tank and above said par tition, means for delivering a mixture of material to be classified, and water, under pressure, in a downward direction through said conduit into the tank towards said partition,
means for delivering clean washing Water intosaid tank below said partition, and a tube surrounding said conduit and carrying at its lower end a truncated conical shell, said tube with shell forming with said conduit, an annular air vent terminating above the overflow outlet, and with the wall of the tank, an annular outlet passage communicating with the overflow outlet for water carrying fine particles of powdered material.
7. Apparatus for the classification of material by elutriation, comprising a tank havmg an upper outlet overflow, a horizontal partition arranged at an intermediate portion of the height of said tank and having a plurality of inverted truncated openings therethrough, a vertical conduit arranged in the upper central portion of said tank and above said partition, means for delivering a mixture of materialto be classified, and water, under pressure, in .a downward direction through said conduit into the tank towards said partition, means for delivering clean washing Water into said tank below said partition and a second truncated conical shell arranged between the first mentioned shell and the wall of the tank and forming with the said first mentioned shell an annular passage communicating with the overflow outlet for water carrying fine particles of powdered material, and with the wall of the tank, an inverted conical pocket having an annular outlet at the bottom through which particles of'intermediate size can fall into the portion of the tank above said partition.
Signed at London,'England, this 14th day of July, 1927.
LEONARD ANDREWS.
US207977A 1926-07-30 1927-07-23 Method and apparatus for the classification of materials by elutriation Expired - Lifetime US1705351A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2418821A (en) * 1944-12-18 1947-04-15 Coghill William Hawes Plural stage hydraulic classifier
US2560809A (en) * 1946-07-10 1951-07-17 Reserve Mining Co Method and apparatus for separating materials
US2610737A (en) * 1947-11-11 1952-09-16 Eder Theodor Process of and apparatus for strictly limited separation of mixtures by the speed of fall in liquid media
US3012671A (en) * 1959-08-31 1961-12-12 Int Minerals & Chem Corp Flotation apparatus
US4038178A (en) * 1974-11-19 1977-07-26 Risto Tapani Hukki Apparatus for controlling discharge of classified sand from a hydraulic classifier
US4807761A (en) * 1983-09-22 1989-02-28 C-H Development & Sales, Inc. Hydraulic separating method and apparatus
US4822482A (en) * 1986-01-21 1989-04-18 C-H Development And Sales, Inc. Hydraulic separating apparatus and method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2418821A (en) * 1944-12-18 1947-04-15 Coghill William Hawes Plural stage hydraulic classifier
US2560809A (en) * 1946-07-10 1951-07-17 Reserve Mining Co Method and apparatus for separating materials
US2610737A (en) * 1947-11-11 1952-09-16 Eder Theodor Process of and apparatus for strictly limited separation of mixtures by the speed of fall in liquid media
US3012671A (en) * 1959-08-31 1961-12-12 Int Minerals & Chem Corp Flotation apparatus
US4038178A (en) * 1974-11-19 1977-07-26 Risto Tapani Hukki Apparatus for controlling discharge of classified sand from a hydraulic classifier
US4807761A (en) * 1983-09-22 1989-02-28 C-H Development & Sales, Inc. Hydraulic separating method and apparatus
US4822482A (en) * 1986-01-21 1989-04-18 C-H Development And Sales, Inc. Hydraulic separating apparatus and method

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