US468066A - Separator - Google Patents

Separator Download PDF

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US468066A
US468066A US468066DA US468066A US 468066 A US468066 A US 468066A US 468066D A US468066D A US 468066DA US 468066 A US468066 A US 468066A
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Prior art keywords
particles
stops
barriers
separation
seeds
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07B—SEPARATING 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
    • B07B13/00—Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices
    • B07B13/10—Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices using momentum effects
    • B07B13/11—Grading 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

Definitions

  • FAIRFAX 1I IVIIEELAN, OF SANTA BARBARA, CALIFORNIA.
  • My invention relates to the art of separation, and especially with relation to the separation of foreign particles from grains, seeds, che.
  • the general object of my invention is to separate the smoother from the rougher particles of any material which is composed of particles of dierent degrees of smoothness, and its special object is to separate the dirt and other foreign particles from grains, and particularly from leguminous seeds.
  • My invention consists in feeding material composed of particles of different degrees of smoothness upon a rotating surface on which said particles are subjected Vto centrifugal action, which produces a separation of those particles having a less coefficient or friction with the surface from those particles having a greater coefficient or friction therewith.
  • My invention also consists, in connection with the above, of guiding the material to such a point on the surface Where the centrifugal force can act to effect the separation of the smoother from the rougher particles, then relieving the particles to permit their separation, and then catching the separated particles at different points on the surface and maintaining their' separation.
  • My invention also consists in the novel sepa- Y rating-table hereinafter fully described, and
  • Figure l is a perspective view of my separater, the supporting devices for the barriers D and stops E and F being omitted.
  • Fig. 2 is a plan of the table, the supports for the barriers and stops being shown in dotted lines.
  • A is a frame or stand, in which is mounted a shaft B, adapted to be rotated by suitable means, as by a belt extending to the pulley Z9.
  • This shaft carries a tablev C, which rotates with the shaft.
  • a circular feed-chamber c In the center of the table is made a circular feed-chamber c for the material.
  • the barriers D Over or upon the surface of the table and around the circumference of the feedchamber and tangential thereto are the barriers D, which consist of any suitable stops. These are separated from each other, so that the spaces between their inner ends communicate with the central feed-chamber.
  • E are the first stops of the outer series. These are fixed over or upon the table and are substantially parallel with the barriers D. They extend from the circumference of the table inwardly and terminate short of the planes of the ends of the barriers, thus leaving a space e between their adjacent ends. These stops E are not in line with the barriers, but are set a little behind them, as shown.
  • the second stops of the outer series are the second stops of the outer series. They extend parallel with and back of the stops E. They reach from the outer circumference of the table to a point beyond the inner end of the stops E and lie behind and overlap the spaces e.
  • the surface of the table may be of any suitable character-smooth or of arougher nature. Tire-cloth will serve the purpose.
  • G is a hopper to feed the'material.
  • Vith grains and seeds especially leguminous seeds, all sorts of substances are mixed, principally particles of dirt, but small twigs, sticks, the., and mutilated and imperfect grains and seeds are also present.
  • the perfect grains and seeds are much smoother than the mutilated ones and are far smoother than the particles of dirt, sticks, twigs, &c.
  • Centrifugal force, acting upon particles of different degrees of smoothness resting upon a surface will overcome the frictional coefficient of and act upon the smoother particles to a greater extent than upon the rougher particles.
  • the material to be separated is fed from the hopper G into the central feed-chamber c of the table C.
  • the table is given a rotary motion and the material is fed out from the central chamber equally all round upon and against the barriers D.
  • the centrifugal force acting upon the smoother grains and seeds, causes them to glide or slip outwardly sufficiently to bridge or span the spaces e, so that they land after traveling through an eccentric curve upon the first stops E; but the rougher particles-dirt, mutilated seeds and grains, sticks, twigs, tc-having a greater frictional coefficient with the surface of table C, do not so readily slip or glide, and failing to span or-bridge the spaces c they fall through said spaces and are caught by the second stops F.
  • the capacity of the device is greatly increased by the continuous feed from the circumference of the feed-chamber c.
  • a separator consisting of a rotating table, draft-barriers for guiding the material outwardly, and outer stops separated from each other and from the draft-barriers to catch the separated particles aft-er leaving said barriers,lsubstantially as herein described.
  • a separator consisting of a rotating table, the draft-barriers for guiding the material outwardly, the rst stops E, separated from the draft-barriers by spaces, and the second stops F behind stops E and overlapping the spaces, substantially as herein described.
  • a separator consisting of the rotating table having the central feed-chamber, the barriers D, tangential to the circumference of said chamber, the first stops E, having spaces between their inner ends and the outer ends of the'barriers, and the secondl stops F behind the stops E, overlapping said spaces,

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  • Pretreatment Of Seeds And Plants (AREA)

Description

(No Model.)
F. H. WHEELAN.
Patented Feb. 2, 1892.
SEPARATOR.
In Yulllmlu Amp.; 4]] wmf ullllll UNTTFD STATES PATENT OFFICE.
FAIRFAX 1I. IVIIEELAN, OF SANTA BARBARA, CALIFORNIA.
SEPARATOR.
SPECIFICATION forming part of Letters Patent No. 468,066, dated February 2, 1892.
Application filed March 5, 1891. Serial No. 383,889. (No model.)
To all whom, it may concern.-
Be it known that I, FAIRFAX n. WHEELAN,
a citizen of the United States, residing at Santa Barbara, Santa Barbara county, State of California, haveinvented an Improvement in Separators; and 'I hereby declare the following to be a full, clear, and exact description of the same.
My invention relates to the art of separation, and especially with relation to the separation of foreign particles from grains, seeds, che.
The general object of my invention is to separate the smoother from the rougher particles of any material which is composed of particles of dierent degrees of smoothness, and its special object is to separate the dirt and other foreign particles from grains, and particularly from leguminous seeds.
My invention consists in feeding material composed of particles of different degrees of smoothness upon a rotating surface on which said particles are subjected Vto centrifugal action, which produces a separation of those particles having a less coefficient or friction with the surface from those particles having a greater coefficient or friction therewith.
My invention also consists, in connection with the above, of guiding the material to such a point on the surface Where the centrifugal force can act to effect the separation of the smoother from the rougher particles, then relieving the particles to permit their separation, and then catching the separated particles at different points on the surface and maintaining their' separation.
My invention also consists in the novel sepa- Y rating-table hereinafter fully described, and
specifically pointed out in the claims.
Referring to the accompanying drawings for a more complete explanation of my invention, Figure lis a perspective view of my separater, the supporting devices for the barriers D and stops E and F being omitted. Fig. 2 is a plan of the table, the supports for the barriers and stops being shown in dotted lines.
A is a frame or stand, in which is mounted a shaft B, adapted to be rotated by suitable means, as by a belt extending to the pulley Z9. This shaft carries a tablev C, which rotates with the shaft. In the center of the table is made a circular feed-chamber c for the material. Over or upon the surface of the table and around the circumference of the feedchamber and tangential thereto are the barriers D, which consist of any suitable stops. These are separated from each other, so that the spaces between their inner ends communicate with the central feed-chamber.
E are the first stops of the outer series. These are fixed over or upon the table and are substantially parallel with the barriers D. They extend from the circumference of the table inwardly and terminate short of the planes of the ends of the barriers, thus leaving a space e between their adjacent ends. These stops E are not in line with the barriers, but are set a little behind them, as shown.
F are the second stops of the outer series. They extend parallel with and back of the stops E. They reach from the outer circumference of the table to a point beyond the inner end of the stops E and lie behind and overlap the spaces e. The surface of the table may be of any suitable character-smooth or of arougher nature. Tire-cloth will serve the purpose.
G is a hopper to feed the'material.
The separation which I effect is founded upon the diiferent degrees of smoothness between the different particles of the material to be separated. It is obvious that a particle having a rough surface has a greater coefficient of friction with the surface on which it rests than a particle having a smoother surface, and this is the more so if the surface on which the particles rest be of a somewhat rough character.
Vith grains and seeds, especially leguminous seeds, all sorts of substances are mixed, principally particles of dirt, but small twigs, sticks, the., and mutilated and imperfect grains and seeds are also present. As a matter of fact, the perfect grains and seeds are much smoother than the mutilated ones and are far smoother than the particles of dirt, sticks, twigs, &c. Centrifugal force, acting upon particles of different degrees of smoothness resting upon a surface will overcome the frictional coefficient of and act upon the smoother particles to a greater extent than upon the rougher particles. Therefore if grains and seeds mixed with foreign parti- IOO cles having a rougher surface than themselves be fed upon a rotating table the centrifugal force, acting upon the different particles, will affect them differently, according to their frictional coeiiicients, and will separate those having a less from vthose having a greater frictional coefficient. Therefore the smooth grains and seeds will be thrown on or from the surface to a different extent from the foreign particlesl and will be separated from them. This is the main separation, and. the dierent particles may be received at different points and kept separated; but While this method of separation would subserve a useful purpose, another step should be added to the method to provide for the highest efficiency and operativeness of the separating process and the means by which it is accomplished. This added step is the controlling of the particles upon the table in such a manner as to induce separation at the best points and to maintain this separation when once made. These are the purposes of the barriers and stops, and the operation of the device described will be now readily understood.
The material to be separated is fed from the hopper G into the central feed-chamber c of the table C. The table is given a rotary motion and the material is fed out from the central chamber equally all round upon and against the barriers D. Now, from the position of these barriers, and recognizing what is known as draft in the action of material upon a rotating surface, (such as a millstone provided with what is termed furrows and land,) it will readily be understood that thematerial will travel outwardly against the barriers D, and as it travels outwardly it is approaching the planes of circles of greater diameter in the surface of the table. When it reaches the outer ends of the barriers,it is then in a position to be acted upon favorably by the centrifugal force due to the rotation of the table. At this point the centrifugal force, acting upon the smoother grains and seeds, causes them to glide or slip outwardly sufficiently to bridge or span the spaces e, so that they land after traveling through an eccentric curve upon the first stops E; but the rougher particles-dirt, mutilated seeds and grains, sticks, twigs, tc-having a greater frictional coefficient with the surface of table C, do not so readily slip or glide, and failing to span or-bridge the spaces c they fall through said spaces and are caught by the second stops F. There is thus a separation, the smoother particles being caught by the stops E and the rougher particles by the stops F, and by means of draft they are carried out to the outer end of the stopsl and are dropped separately over the edge of the table, where suitable means may be employed for receiving them and keeping them separate.
The capacity of the device is greatly increased by the continuous feed from the circumference of the feed-chamber c.
Having thus described my invention, whatl claim as new, and desire to secure by Letters Patent, is- V 1. A separator consisting of a rotating table, draft-barriers for guiding the material outwardly, and outer stops separated from each other and from the draft-barriers to catch the separated particles aft-er leaving said barriers,lsubstantially as herein described.
2. A separator consisting of a rotating table, the draft-barriers for guiding the material outwardly, the rst stops E, separated from the draft-barriers by spaces, and the second stops F behind stops E and overlapping the spaces, substantially as herein described.
3; A separator consisting of the rotating table having the central feed-chamber, the barriers D, tangential to the circumference of said chamber, the first stops E, having spaces between their inner ends and the outer ends of the'barriers, and the secondl stops F behind the stops E, overlapping said spaces,
substantially as herein described.
In witness whereof I have hereunto set my hand.
FAIRFAX II. VIIEELAN.
Witnesses:
S. H. N oURsE, J. A. BAYLEss.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3485360A (en) * 1967-08-11 1969-12-23 Atomic Energy Commission Particle separator
US3672500A (en) * 1969-08-25 1972-06-27 Atomic Energy Authority Uk Apparatus for grading particles according to their sphericity
WO2018018155A1 (en) * 2016-07-29 2018-02-01 9754741 Canada Ltd. Method and apparatus for singulating particles in a stream

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3485360A (en) * 1967-08-11 1969-12-23 Atomic Energy Commission Particle separator
US3672500A (en) * 1969-08-25 1972-06-27 Atomic Energy Authority Uk Apparatus for grading particles according to their sphericity
WO2018018155A1 (en) * 2016-07-29 2018-02-01 9754741 Canada Ltd. Method and apparatus for singulating particles in a stream
EP3490730A4 (en) * 2016-07-29 2020-03-18 9754741 Canada Ltd. METHOD AND APPARATUS FOR INDIVIDUALIZING PARTICLES IN A STREAM
RU2757185C2 (en) * 2016-07-29 2021-10-11 9754741 Кэнэда Лтд. Method and unit for separating particles in a flow
US11185892B2 (en) 2016-07-29 2021-11-30 9754741 Canada Ltd. Method and apparatus for singulating particles in a stream
CN115428625A (en) * 2016-07-29 2022-12-06 9754741加拿大有限公司 Method and apparatus for separating particles in a stream

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