US852558A - Centrifugal concentrator. - Google Patents

Centrifugal concentrator. Download PDF

Info

Publication number
US852558A
US852558A US22428804A US1904224288A US852558A US 852558 A US852558 A US 852558A US 22428804 A US22428804 A US 22428804A US 1904224288 A US1904224288 A US 1904224288A US 852558 A US852558 A US 852558A
Authority
US
United States
Prior art keywords
conduit
openings
compartments
air
sieve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US22428804A
Inventor
Charles T Heisel
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US22428804A priority Critical patent/US852558A/en
Application granted granted Critical
Publication of US852558A publication Critical patent/US852558A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • B07B9/00Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets

Definitions

  • My invention relates to improvements in concentrators, and the object of my invention is to provide an apparatus wherein va-- rious kinds cf finely pulverized materials of different gravity can be separated or concentrated in a dry state or'condition by the use of air, or in a moist state or condition by the use of water or other fluid, and also for classifying finely pulverized material of the same gravity, by separating them as to their different grades of fineness or coarseness, by feed- 2 5 ing the finely pulverized material into the apparatus no faster than will allow the propelling medium to keep the material in constant suspension from start to finish.
  • FIG. 1 represents a plan view of said concentrator.
  • FIG. 2 is a partial vertical sectional view thereof, and
  • Fig. 3 is a vertical sectional view on line X X. v
  • Substantial y this apparatus consists of a helical or evolute shaped conduit, which 4 preferably built up in sections, a feeding device and means effecting an air draft or fluid current through said conduit, side compart- .ments for receiving and discharging the concentrates, and means for regulating a side draft or current through said compartments,
  • the volume of air, or other medium which 5 travels in'a helical path along and through said conduit serves as a ropelling medium for moving the pulverize material upon be-.
  • the conduit through which the material. is drawn may comprisemore or less sections or windings, de ending upon the nature of the material to e separated or concentrated, in each of the windingsso much of a separation of the light from the heavy is effected, finally the lightest is drawn off through the last winding as tailings or Waste material.
  • This improved concentrator is adapted for concentrating different kinds of materials, but ismore particularly intended for concentrating gold bearing ore and placer dirt which 71: is subsequently treated in a combined se arator and amalgamator for which I ma e separate application for Letters Patent.
  • the helical or evolute conduit is preferably built up in sections to facili- 7 5 tate transportation thereof into or in mountainous countries or regions, and making repairs, etc.
  • Flanged and bolted connections are preferred for the sections, which are preferably built up of sheet metal; the terminals thereof are bound 'in flanged fittings which are bolted face to face (preferably .in vertical direction).
  • a conduit of any desirable length can thus be readily. built up and also taken apart from: or at any point thereof.
  • side pockets or side compartments are attached to any number of the circular sections which communicate with them by way of openings '0, .a cover or slide Dis provided for each of said openings for the purpose of regulating the extent of said 0 enings, said slides can conveniently be reac ed'for adjustment upon removal of the hand hole plate a.
  • a removable hand hole plate a is provided 10 5 upon the circular part of some of the sections for observation and other purposes.
  • the intake A is practically a; horizontal extension of the first section of the conduit, at A 5 air or afluid is drawn in, suction being 1 1o said branch K is placed a sieve Land above said sieve is posited a'ho per Mwith a bottom agitator N.
  • the sai agitator N may be drawn more or less close unto the hop er M for the purpose of governing the uantityto be fed; while the sieve is provided to distribute such quantities in a uniformly divided state into the conduit. Motion may be imparted to the sieve and agitator in any suitable manner.
  • a yokeb As shown there is attached to the sieve a yokeb with an u wardly extending pin a, and journale'd 1n bearing (1 of the ho per stands 0 is a crank or cam shaft P, whic im arts a reciprocating motion to the sieve and vibratory motion to the loosely suspended agitator.
  • the reci rocating motion of the sieve is caused by t e crank or cam pin e striking one or the other side of the yoke, while the vibratory motion of the agitator is effected owing to' the engagement of pin a into an obliquely extending groove,-which isformed by arallel dependin lugs T of the bottom oft e agitator.
  • the vi ratory motion of the a itator delivers the material to the spout h from where it drops onto the sieve and subsequently into the conduit. -The moment the pulverized material reaches the conduit, motion is imparted thereto by the draft or current effected within said conduit.
  • thelatter is whirled with more or less rapidity along the outer circularly winding walls of the conduit inducing or developing centrifugal force.
  • Centrifugal force throws the material outwardly, thus the heavier particles are always nearest the outer walls and escape first in assing or reaching the openings C to be col ected in the compartments B from where it discharges automatically from out of the channels H H by. way of the counterbalanced bottoms or gates H H, which in consequence of the suction are held closed until the weight of the accumulation overcomes the suction, when they automatically discharge and are immediately closed again by virtue ofsaid suction and counterbalances.
  • Other suitable means however may results.
  • the conduit with side openin s can be extended to such a length that fina ly the entire contents of the conduit will pass out into the side pockets or the tailings may be discharged into the open air or some dumpin pit.
  • the concentration of material within each .of the pockets can thus be regulated in a very simple, sensitive and automatic manner.
  • This side draft or current can be regulated so delicately, that every stage from very little to nearly all of the material treated may be allowed to pass through the openings C, as this side draft or current acts as a screen or resistance through .which the heavier particles will pass in consequence of the centrifugal force they have acquired in whirling around and through the helical or evolute shaped conduit.
  • the cross sectionsof the conduit are shown to be of rectangular form, there may be de artures made from such form, for in regar to shape, the outer wall a only is of importance, and the con tour of said wall should be straightor ap-' proximately flat as shown.
  • the entire conduit may be SlPPOItGd upon asuitabl'e foundation or stan ards (not shown).
  • a concentrator the combination of a helical conduit, a feeder therefor, suitable means forming compartments at the side of the conduit having openings leading from the outer air into the conduit, means to vary the size of conduit openings, means to regulate the size of the outer air openings, means near the terminal of the conduit to induce an air current therethrough, and also through the side compartments into the conduit through the outer air openings and the conduit openings for the purpose of regulating thedischarge of the material into said side compartments, as shown and set forth.
  • a concentrator for pulverized ore comprising a helical conduit, a suitable feeding from the outer air into the conduit, means to.
  • a concentrator i'or pulverized mate rial the combination of a helical conduit, a power agitated i'eed hopper and sieve at one end thereof, means at'the opposite end to induce an air current therethrough, suitable means l'orming compartments at the side of the conduit having suction closed balanced gates at the bottom thereof, and having openings leading from the outer air into the conduit, means to vary the size of the conduit openings, means to regulate the outer air openings whereby a graduated classification ol' the material is ell'ected 1n and along said compartments as and for the purpose set I l'orth.
  • compartments therewith of means at or near the end of the. conduit for inducing an air draft therethrough and means to vary the size of the openings in said compartments leading from the outer air and into the said conduit for regulating the discharge of the heavier material into said compartments.
  • a concentrator for pulverized materials the combination with a helieally winding conduit ol' suitable means forming 0on1- partments along one side of said conduit, said compartimmts having controllable openings leading from the outer air and controllable openings leading into. the conduit and means inducing an air draft through said eon duit and the said compartments for the purpose as set forth.

Description

:55); 552,555. PATE-NTED MAY 7, 1907.
0. T. HEISEL. GENTRIPUGAL GONGBNTRATOR.
APPLICATION FILED 8EPT.13.1904.
INIVENTOR UNITED STATES PATENT OFFICE.
CHARLES T. nEIsEL, F CLEVELAND, oruo. c
Specification of Letters Patent.
Patented May 7, 1907.
Application fi1edSeptomber13,i904- swarm). 224.288.
To all whom it may concern:
Beit known that I, CHAltLES T. HEISEL, a
citizen of the United States, residing in the city of Cleveland, county of Cuyahoga, and 5 State of Ohio, have invented certain new and useful Improvements in Centrifugal Concentrators, of which the following is a specifica I of extracting gold from its ore under Serial Number 224,287, on September 13, 1904.
My invention relates to improvements in concentrators, and the object of my invention is to provide an apparatus wherein va-- rious kinds cf finely pulverized materials of different gravity can be separated or concentrated in a dry state or'condition by the use of air, or in a moist state or condition by the use of water or other fluid, and also for classifying finely pulverized material of the same gravity, by separating them as to their different grades of fineness or coarseness, by feed- 2 5 ing the finely pulverized material into the apparatus no faster than will allow the propelling medium to keep the material in constant suspension from start to finish. I attain this ob ect in an apparatus constructed and aro ranged substantially as shown in the accompanying drawing in which Figure 1 represents a plan view of said concentrator. Fig. 2 is a partial vertical sectional view thereof, and Fig. 3 is a vertical sectional view on line X X. v
Like letters of'reference denote like parts in the drawin and specification.
Substantial y this apparatus consists of a helical or evolute shaped conduit, which 4 preferably built up in sections, a feeding device and means effecting an air draft or fluid current through said conduit, side compart- .ments for receiving and discharging the concentrates, and means for regulating a side draft or current through said compartments,
to act as a screen or aresistance which overcomes the centrifugal force of the lighter material. Y
The volume of air, or other medium which 5 travels in'a helical path along and through said conduit serves as a ropelling medium for moving the pulverize material upon be-.
ing fed into said conduit. Depending upon the force of the air or other draft, more or less centrifugal force be imparted to the material undergoing concentration, (respectively separation.) according to their specific gravity.-
The conduit through which the material. is drawn may comprisemore or less sections or windings, de ending upon the nature of the material to e separated or concentrated, in each of the windingsso much of a separation of the light from the heavy is effected, finally the lightest is drawn off through the last winding as tailings or Waste material.
This improved concentrator is adapted for concentrating different kinds of materials, but ismore particularly intended for concentrating gold bearing ore and placer dirt which 71: is subsequently treated in a combined se arator and amalgamator for which I ma e separate application for Letters Patent.
" As above stated, the helical or evolute conduitis preferably built up in sections to facili- 7 5 tate transportation thereof into or in mountainous countries or regions, and making repairs, etc.
As shown two sections A A complete just one winding and any number of-such windings may be assembled into one conduit.
Flanged and bolted connections are preferred for the sections, which are preferably built up of sheet metal; the terminals thereof are bound 'in flanged fittings which are bolted face to face (preferably .in vertical direction). With material thus prepared, a conduit of any desirable length can thus be readily. built up and also taken apart from: or at any point thereof. Along the conduit side pockets or side compartments are attached to any number of the circular sections which communicate with them by way of openings '0, .a cover or slide Dis provided for each of said openings for the purpose of regulating the extent of said 0 enings, said slides can conveniently be reac ed'for adjustment upon removal of the hand hole plate a.
Near the bottom and'preferably in the outer wall of said side compartments areioo openings E which are likewise under control ofa cover or slide F, explanation concerning the purpose of said openings will be hereafter made. a
A removable hand hole plate a is provided 10 5 upon the circular part of some of the sections for observation and other purposes.
The intake A is practically a; horizontal extension of the first section of the conduit, at A 5 air or afluid is drawn in, suction being 1 1o said branch K is placed a sieve Land above said sieve is posited a'ho per Mwith a bottom agitator N. The sai agitator N may be drawn more or less close unto the hop er M for the purpose of governing the uantityto be fed; while the sieve is provided to distribute such quantities in a uniformly divided state into the conduit. Motion may be imparted to the sieve and agitator in any suitable manner. As shown there is attached to the sieve a yokeb with an u wardly extending pin a, and journale'd 1n bearing (1 of the ho per stands 0 is a crank or cam shaft P, whic im arts a reciprocating motion to the sieve and vibratory motion to the loosely suspended agitator. The reci rocating motion of the sieve is caused by t e crank or cam pin e striking one or the other side of the yoke, while the vibratory motion of the agitator is effected owing to' the engagement of pin a into an obliquely extending groove,-which isformed by arallel dependin lugs T of the bottom oft e agitator. The vi ratory motion of the a itator delivers the material to the spout h from where it drops onto the sieve and subsequently into the conduit. -The moment the pulverized material reaches the conduit, motion is imparted thereto by the draft or current effected within said conduit.
Depending upon the force of the draft or current or the nature of the material, thelatter is whirled with more or less rapidity along the outer circularly winding walls of the conduit inducing or developing centrifugal force. Centrifugal force throws the material outwardly, thus the heavier particles are always nearest the outer walls and escape first in assing or reaching the openings C to be col ected in the compartments B from where it discharges automatically from out of the channels H H by. way of the counterbalanced bottoms or gates H H, which in consequence of the suction are held closed until the weight of the accumulation overcomes the suction, when they automatically discharge and are immediately closed again by virtue ofsaid suction and counterbalances. Other suitable means however may results.
Naturally through that opening which is nearest the intake, the heaviest material will escape, while through the succeeding openings, lighter materials will pass out. Ob-
be employed to accomplish such viously the conduit with side openin s can be extended to such a length that fina ly the entire contents of the conduit will pass out into the side pockets or the tailings may be discharged into the open air or some dumpin pit.
y way of the openings E side drafts or currents can be effected; in this way the dis-' charge. of theconcentrate can be regulated and separately so within each and every one of these side pockets or compartments. If, for instance, air enters the pocket nearest the intake, then onlythe very heaviest material will enter said pocket, orin other words, the
collection therein is diminished and such are the conditions with each and every one of the side pockets, the concentration of material within each .of the pockets can thus be regulated in a very simple, sensitive and automatic manner. This side draft or current can be regulated so delicately, that every stage from very little to nearly all of the material treated may be allowed to pass through the openings C, as this side draft or current acts as a screen or resistance through .which the heavier particles will pass in consequence of the centrifugal force they have acquired in whirling around and through the helical or evolute shaped conduit.
While in the drawings the cross sectionsof the conduit are shown to be of rectangular form, there may be de artures made from such form, for in regar to shape, the outer wall a only is of importance, and the con tour of said wall should be straightor ap-' proximately flat as shown. The entire conduit may be SlPPOItGd upon asuitabl'e foundation or stan ards (not shown).
What I claim and desire to secure by LettersPatent is:
1. In a concentrator the combination of a helical conduit, a feeder therefor, suitable means forming compartments at the side of the conduit having openings leading from the outer air into the conduit, means to vary the size of conduit openings, means to regulate the size of the outer air openings, means near the terminal of the conduit to induce an air current therethrough, and also through the side compartments into the conduit through the outer air openings and the conduit openings for the purpose of regulating thedischarge of the material into said side compartments, as shown and set forth.
2. A concentrator for pulverized ore, comprising a helical conduit, a suitable feeding from the outer air into the conduit, means to.
vary the sizeofthe conduit-openings, means to regulate the outerair openings, and suction-clo'sed balanced gates at the bottom of the compartments whereby the concentrate is automatically discharged, all constructed and arranged substantially as and for the purpose set forth.
3. lit a concentrator i'or pulverized mate rials the combination of a helical conduit, a power agitated i'eed hopper and sieve at one end thereof, means at'the opposite end to induce an air current therethrough, suitable means l'orming compartments at the side of the conduit having suction closed balanced gates at the bottom thereof, and having openings leading from the outer air into the conduit, means to vary the size of the conduit openings, means to regulate the outer air openings whereby a graduated classification ol' the material is ell'ected 1n and along said compartments as and for the purpose set I l'orth.
compartments therewith of means at or near the end of the. conduit for inducing an air draft therethrough and means to vary the size of the openings in said compartments leading from the outer air and into the said conduit for regulating the discharge of the heavier material into said compartments.
5. In a concentrator for pulverized materials the combination with a helieally winding conduit ol' suitable means forming 0on1- partments along one side of said conduit, said compartimmts having controllable openings leading from the outer air and controllable openings leading into. the conduit and means inducing an air draft through said eon duit and the said compartments for the purpose as set forth.
CHARLES 'l. HEISEL.
l/Vitnesses:
GEO. D. IIILE, B. l. EIBLER/
US22428804A 1904-09-13 1904-09-13 Centrifugal concentrator. Expired - Lifetime US852558A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US22428804A US852558A (en) 1904-09-13 1904-09-13 Centrifugal concentrator.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US22428804A US852558A (en) 1904-09-13 1904-09-13 Centrifugal concentrator.

Publications (1)

Publication Number Publication Date
US852558A true US852558A (en) 1907-05-07

Family

ID=2921016

Family Applications (1)

Application Number Title Priority Date Filing Date
US22428804A Expired - Lifetime US852558A (en) 1904-09-13 1904-09-13 Centrifugal concentrator.

Country Status (1)

Country Link
US (1) US852558A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2643769A (en) * 1949-01-10 1953-06-30 Buehler Ag Geb Method and apparatus for separating solids from gases
US2713977A (en) * 1950-12-29 1955-07-26 H H And H Mfg Co Milling apparatus for grains and other materials

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2643769A (en) * 1949-01-10 1953-06-30 Buehler Ag Geb Method and apparatus for separating solids from gases
US2713977A (en) * 1950-12-29 1955-07-26 H H And H Mfg Co Milling apparatus for grains and other materials

Similar Documents

Publication Publication Date Title
EP0006867A1 (en) Apparatus and process for ordinary and submarine mineral beneficiation
US762866A (en) Ore-separator.
US2854136A (en) Method and apparatus for separating solid materials of different specific gravities
US852558A (en) Centrifugal concentrator.
US1285061A (en) Flotation apparatus.
US2144418A (en) Method and apparatus for sorting or classifying solids
US1250553A (en) Apparatus for sorting heterogeneous materials.
US696870A (en) Machine for cleaning and assorting raisins.
US143219A (en) Improvement in separators for coal, ores
US1787759A (en) Ore separator
US696604A (en) Ore-concentrator.
US888156A (en) Dry concentrator.
US603319A (en) Cisco
US982583A (en) Hydraulic classifier for ores.
US3042203A (en) Air-flow material separator
US244114A (en) Louis de soulages
US152810A (en) Improvement in jiggers for separating ores
US555920A (en) Andrew b
US676969A (en) Ore-concentrator.
US654290A (en) Ore-concentrator.
US775944A (en) Ore-concentrator.
US517799A (en) Ore separator and classifier
US1058828A (en) Ore-classifier.
US602250A (en) Jacques angel
US650800A (en) Apparatus for separating metals from their ores, &c.