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US2778498A - Separation of materials - Google Patents

Separation of materials Download PDF

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Publication number
US2778498A
US2778498A US518225A US51822555A US2778498A US 2778498 A US2778498 A US 2778498A US 518225 A US518225 A US 518225A US 51822555 A US51822555 A US 51822555A US 2778498 A US2778498 A US 2778498A
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United States
Prior art keywords
plane
particles
receptacle
broken
separation
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Expired - Lifetime
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US518225A
Inventor
Vincent George Clarkson
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Imperial Chemical Industries Ltd
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Imperial Chemical Industries Ltd
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Publication date
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Publication of US2778498A publication Critical patent/US2778498A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B13/00Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices
    • B07B13/10Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices using momentum effects
    • B07B13/11Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices using momentum effects involving travel of particles over surfaces which separate by centrifugal force or by relative friction between particles and such surfaces, e.g. helical sorters
    • B07B13/113Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices using momentum effects involving travel of particles over surfaces which separate by centrifugal force or by relative friction between particles and such surfaces, e.g. helical sorters shaking tables

Definitions

  • the present invention relates to the separation of materials and particularly to the separation of whole spheroidal solid particles from mixtures with broken and/or irregular shaped particles of similar material.
  • a process for the separation of whole spheroidal solid particles from mixtures with broken and/or irregular shaped particles which comprises feeding the mixture on to an inclined plane at an upper part thereof with a velocity having a component across the plane and maintaining the plane in transverse vibration, whereby the whole spheroidal particles are caused to roll downwardly across the plane with sufficient momentum to carry them across a gap at the lower edge of the plane into a collecting receptacle and the broken and/ or irregular shaped particles are caused to slide down the plane and to drop through said gap into another collecting receptacle.
  • the mixture of whole spheroidal solid par ticles with broken and/or irregular shaped particles is fed to the vibrating inclined plane at or near the top thereof in such a manner that the particles have a velocity component across the plane so that the whole spheroidal solid particles are caused to roll in downwardly curved paths across the plane while the broken and/or irregular shaped particles, due to their greater frictional resistance and inability to roll, slide more directly, under the influence of the vibrations of the plane, to the lower edge of the plane.
  • the present invention also includes the provision of apparatus for carrying out the separation, said apparatus comprising in combination an inclined plane, means for continuously vibrating the plane, a receptacle at the lower edge of the plane arranged in spaced relation thereto to define a gap between said edge of the plane and the receptacle and a further receptacle below the gap so 2,778,498 Patented Jan. 22, 1957 7 one or both inclined edges of the plane, together with means for feeding the mixture of solid particles on to the plane with a velocity having a component across the plane.
  • the apparatus may be constructed of any suitable material, for example sheet steel or aluminum or even wood.
  • At least the upper portion of theside of the receptacle which defines the gap at the lower edge of the inclined plane is adjustable both horizontally and vertically so that the height of its upper edge relative to the lower edge of the inclined plane and its distance therefrom may be arranged to allow unobstructed flow of the whole spheroidal particles from the plane into the receptacle while preventing broken and/or irregular shaped particles from falling into it.
  • the vertical adjustment is preferably arranged to allow of the upper edge of said side of the receptacle to incline downwards towards the inclined edge or edges of the plane remote from the point at which the mixture is fed on to the plane.
  • the numeral 1 denotes an inclined plane defined by an upper edge 2, a lower edge 3 and and inclined edges 4 and 5.
  • An electro-magnetic vibrator, denoted by numeral 6, is attached to the underside of the plane at about its mid-point.
  • receptacle 7 is arranged in spaced relation to the lower edge 3 of the inclined plane 1 to define the gap 11, in which is arranged, the receptacle 12 (shown in elevation in Figure 1) having an outlet at 13. It will be understood that the back Wall 9 of the receptacle 7 forms in part a common division wall between the receptacles 7 and 12.
  • a further receptacle 14 is provided at the inclined edge 5 of the plane, said receptacle 14 being ar ranged with an outlet at 15 which is common to it and to receptacle 7.
  • the ancillary parts of the apparatus comprise a feed hopper 18, a vibrating tray feeder 19, and an inclined chute 20 which is conveniently of semi-circular section.
  • the feed hopper 18 is provided with a coarse mesh grid 21 for removing undesired large particles from the mixture charged to the hopper and with an outlet pipe 22 having a screwed sleeve 23 for controlling, by vertical adjustment thereof, the rate of flow of the mixture to the vibrating tray feeder 19.
  • the numeral 16 denotes a suitable container for receiving the spheroidal particles which are discharged from the outlet 15 of the receptacles 7 and 14.
  • the numeral 1'7 likewise denotes a container for receiving the separated broken and/ or irregular shaped particles which are discharged from the receptacle 12 through the outlet 13.
  • alumina-silica catalyst beads of substantially spherical shape ranging in nominal size from to 1/ diameter and containing about 25% of brs scn bead t m n o the roken fr men s lar er than many Whole beads, may be successfully treated by the process and apparatus of the present invention to recover more than 75% of the total with at least 94% whole beads by using an inclined plane of sheet aluminum 4 feet wide by 2 feet long, said plane being inclined at an angle of 7 to the horizontal and secured at the upper and lower 4 foot edges and vibrated at a frequency of 10 cycles per second with an amplitude of 0.005 inch by means of an electro-rnagnetie vibrator located on the underside of the plane at about the middle point; the feed of particles at a steady rate of 13 pounds per hour being passed on to the plane, at an upper point of one inclined edge, in a direction across the plane from a chute inclined at an angle of 30 to the horizontal.
  • Apparatus for separating Whole spheroidal solid particles from mixtures with broken particles which comprises in combination an inclined plane, means for cont nu usly r rat as the Plane a re ptacle at the owe edge of the plane arranged in spaced relation thereto to define a gap between said edge of the plane and the receptacle and a further receptacle below the gap so defined together with means for feeding the mixture of solid particles on to the plane with avelocity having a component across the plane.
  • Apparatus as claimed in claim 1 in which a further receptacle is provided adjacent at least one inclined edge oftheplane.

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  • Jigging Conveyors (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Combined Means For Separation Of Solids (AREA)

Description

Jan. 22, 1957 G. C. VINCENT SEPARATION OF MATERIALS Filed June 2'7, 1955 Inventor GEORGE CLARKSON VINCENT A ttorneys United States PatentO 2,778,498 SEPARATION OF MATERIALS George Clarkson Vincent, Norton-on-Tees, England,- signor to Imperial Chemical Industries Limited, London, England, a corporation of Great Britain Application June 21, 1955, Serial No. 518,225 Claims priority, application Great Britain July 2, 1954 2 Claims. (Cl. 209-118) The present invention relates to the separation of materials and particularly to the separation of whole spheroidal solid particles from mixtures with broken and/or irregular shaped particles of similar material.
According to the present invention there is provided a process for the separation of whole spheroidal solid particles from mixtures with broken and/or irregular shaped particles which comprises feeding the mixture on to an inclined plane at an upper part thereof with a velocity having a component across the plane and maintaining the plane in transverse vibration, whereby the whole spheroidal particles are caused to roll downwardly across the plane with sufficient momentum to carry them across a gap at the lower edge of the plane into a collecting receptacle and the broken and/ or irregular shaped particles are caused to slide down the plane and to drop through said gap into another collecting receptacle.
Preferably the mixture of whole spheroidal solid par ticles with broken and/or irregular shaped particles is fed to the vibrating inclined plane at or near the top thereof in such a manner that the particles have a velocity component across the plane so that the whole spheroidal solid particles are caused to roll in downwardly curved paths across the plane while the broken and/or irregular shaped particles, due to their greater frictional resistance and inability to roll, slide more directly, under the influence of the vibrations of the plane, to the lower edge of the plane.
It will be understood that some of the whole spheroidal particles will fortuitously be less impeded than others while the mixture is being fed on to the plane and in consequence will trace out less downwardly curved paths. Since, however the broken and/or irregular shaped particles slide more directly to the lower edge of the plane, it is convenient to arrange the plane of a width which is sufficient to accommodate the spread of the broken and/or irregular shaped particles and of the major portion of the whole spheroidal particles and to provide receptacles at one or both inclined edges of the plane, depending on the position at which the mixture is fed thereto, in order to collect the minor portion of the whole spheroidal particles which trace out the least downwardly curved paths and will pass off the plane at 1 either of its inclined edges.
It will also be understood that the actual dimensions and inclination of the plane will depend upon several factors, for example the size range of the particles in the mixture to be separated, the manner of feeding and the point at which the mixture is fed on to the plane and the frequency and amplitude of the vibration of the lane. p The present invention also includes the provision of apparatus for carrying out the separation, said apparatus comprising in combination an inclined plane, means for continuously vibrating the plane, a receptacle at the lower edge of the plane arranged in spaced relation thereto to define a gap between said edge of the plane and the receptacle and a further receptacle below the gap so 2,778,498 Patented Jan. 22, 1957 7 one or both inclined edges of the plane, together with means for feeding the mixture of solid particles on to the plane with a velocity having a component across the plane. The apparatus may be constructed of any suitable material, for example sheet steel or aluminum or even wood.
In the construction of the apparatus it is desirable for at least the upper portion of theside of the receptacle which defines the gap at the lower edge of the inclined plane to be adjustable both horizontally and vertically so that the height of its upper edge relative to the lower edge of the inclined plane and its distance therefrom may be arranged to allow unobstructed flow of the whole spheroidal particles from the plane into the receptacle while preventing broken and/or irregular shaped particles from falling into it. The vertical adjustment is preferably arranged to allow of the upper edge of said side of the receptacle to incline downwards towards the inclined edge or edges of the plane remote from the point at which the mixture is fed on to the plane.
One form of the apparatus according to the present invention is illustrated in the two figures of the accompanying schematic drawing in which Figure 1 is an elevation and Figure 2 is a plan view.
Referring to the drawing, the numeral 1 denotes an inclined plane defined by an upper edge 2, a lower edge 3 and and inclined edges 4 and 5. An electro-magnetic vibrator, denoted by numeral 6, is attached to the underside of the plane at about its mid-point.
Referring particularly to Figure 2 of the drawing, the
receptacle 7 is arranged in spaced relation to the lower edge 3 of the inclined plane 1 to define the gap 11, in which is arranged, the receptacle 12 (shown in elevation in Figure 1) having an outlet at 13. It will be understood that the back Wall 9 of the receptacle 7 forms in part a common division wall between the receptacles 7 and 12. A further receptacle 14 is provided at the inclined edge 5 of the plane, said receptacle 14 being ar ranged with an outlet at 15 which is common to it and to receptacle 7. I
The ancillary parts of the apparatus comprise a feed hopper 18, a vibrating tray feeder 19, and an inclined chute 20 which is conveniently of semi-circular section. The feed hopper 18 is provided with a coarse mesh grid 21 for removing undesired large particles from the mixture charged to the hopper and with an outlet pipe 22 having a screwed sleeve 23 for controlling, by vertical adjustment thereof, the rate of flow of the mixture to the vibrating tray feeder 19.
The numeral 16 denotes a suitable container for receiving the spheroidal particles which are discharged from the outlet 15 of the receptacles 7 and 14. The numeral 1'7 likewise denotes a container for receiving the separated broken and/ or irregular shaped particles which are discharged from the receptacle 12 through the outlet 13.
When the plant is in operation the whole spheroidal particles trace out paths such as those indicated in Figure 2 of the drawing by the letters (a), (b), (c), (d) while the broken and/ or irregular shaped particles traces out paths such as those indicated by the letters (e), (f),
It has been found that alumina-silica catalyst beads of substantially spherical shape ranging in nominal size from to 1/ diameter and containing about 25% of brs scn bead t m n o the roken fr men s lar er than many Whole beads, may be successfully treated by the process and apparatus of the present invention to recover more than 75% of the total with at least 94% whole beads by using an inclined plane of sheet aluminum 4 feet wide by 2 feet long, said plane being inclined at an angle of 7 to the horizontal and secured at the upper and lower 4 foot edges and vibrated at a frequency of 10 cycles per second with an amplitude of 0.005 inch by means of an electro-rnagnetie vibrator located on the underside of the plane at about the middle point; the feed of particles at a steady rate of 13 pounds per hour being passed on to the plane, at an upper point of one inclined edge, in a direction across the plane from a chute inclined at an angle of 30 to the horizontal.
I claim:
1. Apparatus for separating Whole spheroidal solid particles from mixtures with broken particles which comprises in combination an inclined plane, means for cont nu usly r rat as the Plane a re ptacle at the owe edge of the plane arranged in spaced relation thereto to define a gap between said edge of the plane and the receptacle and a further receptacle below the gap so defined together with means for feeding the mixture of solid particles on to the plane with avelocity having a component across the plane.
2. Apparatus" as claimed in claim 1 in which a further receptacle is provided adjacent at least one inclined edge oftheplane.
i ereq es S im! in t e fil s patent "UNITE-VD S'rATEs'rATENTS"
US518225A 1954-07-02 1955-06-27 Separation of materials Expired - Lifetime US2778498A (en)

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2891646A (en) * 1954-06-07 1959-06-23 Q Tee Inc Hopper for delivering round articles
US3945915A (en) * 1973-02-09 1976-03-23 Fmc Corporation Method of and apparatus for assorting particles according to the physical characteristics thereof
WO1989002320A1 (en) * 1987-09-17 1989-03-23 Cyprus Industrial Minerals Company Method and apparatus for friction sorting of particulate materials
FR2635475A1 (en) * 1987-09-17 1990-02-23 Cyprus Ind Minerals Corp Method and apparatus for sorting particulate materials by friction
US4986424A (en) * 1985-10-23 1991-01-22 Europeenne De Retraitement Process and apparatus for separating materials of different shapes or sizes
US5080235A (en) * 1990-09-27 1992-01-14 Cyprus Mines Corporation Small particle separator
US5082552A (en) * 1986-03-10 1992-01-21 Cri International, Inc. Hydrotreating with catalyst particles using length and density grading
AU622671B2 (en) * 1989-03-31 1992-04-16 Cyprus Industrial Minerals Company Method and apparatus for friction sorting of particulate materials
US5427253A (en) * 1994-06-20 1995-06-27 Koehler; Thomas V. Taconite pellet separator

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1141852A (en) * 1913-07-21 1915-06-01 Henry M Sutton Process of and apparatus for sizing or classifying comminuted materials.
US1283284A (en) * 1918-10-29 Clarence Q Fayne Method of and apparatus for the grading or sizing of materials of all kinds.
US1426957A (en) * 1919-10-13 1922-08-22 American Milling Co Apparatus for separating seeds
US2658616A (en) * 1950-04-14 1953-11-10 Olin Ind Inc Process for classifying iron shot

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1283284A (en) * 1918-10-29 Clarence Q Fayne Method of and apparatus for the grading or sizing of materials of all kinds.
US1141852A (en) * 1913-07-21 1915-06-01 Henry M Sutton Process of and apparatus for sizing or classifying comminuted materials.
US1426957A (en) * 1919-10-13 1922-08-22 American Milling Co Apparatus for separating seeds
US2658616A (en) * 1950-04-14 1953-11-10 Olin Ind Inc Process for classifying iron shot

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2891646A (en) * 1954-06-07 1959-06-23 Q Tee Inc Hopper for delivering round articles
US3945915A (en) * 1973-02-09 1976-03-23 Fmc Corporation Method of and apparatus for assorting particles according to the physical characteristics thereof
US4986424A (en) * 1985-10-23 1991-01-22 Europeenne De Retraitement Process and apparatus for separating materials of different shapes or sizes
US5082552A (en) * 1986-03-10 1992-01-21 Cri International, Inc. Hydrotreating with catalyst particles using length and density grading
WO1989002320A1 (en) * 1987-09-17 1989-03-23 Cyprus Industrial Minerals Company Method and apparatus for friction sorting of particulate materials
GR880100622A (en) * 1987-09-17 1989-06-22 Cyprus Ind Minerals Corp Method and apparatus for feiction sorting of particulate materials
FR2635475A1 (en) * 1987-09-17 1990-02-23 Cyprus Ind Minerals Corp Method and apparatus for sorting particulate materials by friction
US5069346A (en) * 1987-09-17 1991-12-03 Cyprus Mines Corporation Method and apparatus for friction sorting of particulate materials
AU622671B2 (en) * 1989-03-31 1992-04-16 Cyprus Industrial Minerals Company Method and apparatus for friction sorting of particulate materials
US5080235A (en) * 1990-09-27 1992-01-14 Cyprus Mines Corporation Small particle separator
US5427253A (en) * 1994-06-20 1995-06-27 Koehler; Thomas V. Taconite pellet separator

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