US2783887A - Cyclone separator - Google Patents
Cyclone separator Download PDFInfo
- Publication number
- US2783887A US2783887A US2783887DA US2783887A US 2783887 A US2783887 A US 2783887A US 2783887D A US2783887D A US 2783887DA US 2783887 A US2783887 A US 2783887A
- Authority
- US
- United States
- Prior art keywords
- vortex
- bowl
- particles
- fluid
- cyclone
- 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
Links
- 239000002245 particle Substances 0.000 description 22
- 239000012530 fluid Substances 0.000 description 12
- 238000002347 injection Methods 0.000 description 6
- 239000007924 injection Substances 0.000 description 6
- 239000012141 concentrate Substances 0.000 description 4
- 230000035515 penetration Effects 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 241000239290 Araneae Species 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000002500 effect on skin Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2405—Feed mechanisms for settling tanks
- B01D21/2411—Feed mechanisms for settling tanks having a tangential inlet
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/26—Separation of sediment aided by centrifugal force or centripetal force
- B01D21/267—Separation of sediment aided by centrifugal force or centripetal force by using a cyclone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/02—Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
- B04C5/04—Tangential inlets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/08—Vortex chamber constructions
- B04C5/081—Shapes or dimensions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/08—Vortex chamber constructions
- B04C5/103—Bodies or members, e.g. bulkheads, guides, in the vortex chamber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
- B04C5/13—Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow
Definitions
- This invention relates to improvements in methods of and apparatus for concentrating ores and the like by centrifugally separating particles of various densities and more particularly to so-called cyclone separators and separation methods.
- the air or liquid entrained particles to be separated are fed into the cyclone tangentially and in any case, the fluid, either gaseous or liquid, entraining such particles, serves as the medium for forming a vortex within the cyclone structure.
- a vortex is set up within a cyclone separator by means of a suitable fluid and the particles of various densities to be separated are injected into the separator in such manner that each individual particle must penetrate through the fluid surface or wall of the fluid vortex therein, it being manifest that the skin effect of the fluid vortex wall is penetrated to a varying depth according to the kinetic energy of a particle striking such surface and the area-density relationship of such particle.
- Figure l is a sectional view of one form of a cyclone class of separator according to the invention, illustrating means for injecting the particles of various densities to be separated into the surface of a vortex formed therein by a vortex forming fluid;
- Figure 2 is a sectional view of a modified form of particle injector feeder.
- FIG. 1 shows a preferred form of cyclone separator according to the invention, comprised of a bowl part 11 having an axially located concentrate opening 12 communicating with a nozzle 13 and a tailings discharge opening 14 of larger diameter, preferably arranged within a relatively large launder 15 of cylindrical construction, rising to a substantial height but having a tailings discharge spout 16 located therein.
- this construction may be formed in an integral casting.
- An inlet nozzle 17 extends tangentially into the bowl at the point of its maximum inner diameter as at 18 whereby a suitable fluid such as water or air may be injected as a vortex forming medium into the bowl at suflicient pressure to create a fast circulating body of fluid 19 of annular shape between the walls 20 of the bowl and the upwardly diverging surface of the vortex 22.
- a suitable fluid such as water or air
- the depth of penetration of the vortex skin 21 by a particle will be determined by the velocity of the individual particle and its mass. A new factor also arises in that the penetration of the particle will also be controlled by the area-density relationship of the particle.
- Very light small particles will effect a negligible penetration of the skin 21 and will be carried by the upward motion of the latter through the tailings outlet to the tailings discharge spout 16. Particles of smaller effective area per unit mass will eifect a deeper penetration as will those of greater kinetic energy.
- the fluid vortex forming media is adjusted in its pressure of injection into the bowl until the heavier particles of ore pulp teed just penetrate the wall of the vortex; the particles having the greater specific gravity are smaller than other mineral particles and penetrate more rapidly, being carried to the wall of the concentrate bowl and down to the concentrate discharge opening. Larger particles of lesser specific gravity will not penetrate so effectively and are carried to tailings discharge.
- the bottom plate 25 of the feed injector pipe 23 is replaced by a flat disc rotated about the axis of the concentrator, this form being designated in Figure 2 wherein the flat disc 25 is supported by the rod 26 carried by open spider guides 27 in the tube 28.
- the rod 26 may be rotated by any suitable drive means such as the motor illustrated.
- the disc 25 along with the drive and rod 26, is raised or lowered until a desired rate of feed is arrived at, in conjunction with the best speed of rotation of the disc.
- the launder 15 is in the form of a vertical open-ended surge pipe which may be of very great height to effect a more uniform vortex in the separator bowl 11.
- the arrows illustrated on the drawing, indicate the direction of flow of the fluid vortex medium within the bowl.
- my injection system for cyclone type of separators enables a greater control through a large number of factors effecting separation and permits an independent control over feed rate of the material being introduced for separation as compared with the rate of injection of the fluid medium forming the vortex.
- the feed injection device being located axially of the vortex may be raised or lowered therewithin to obtain maximum eificiency of injection and separation, along with the control of feed rate and the control of the vortex itself, by independent means.
- acyclone separator having a separating bowl with an axially located concentrate opening of relatively small orilice' diameter and a co-axial opposed tailings opening of relatively large diameter but of a lesser diameter than said bowl, the combination therewith of: a surge pipe co-axially formed on said bowl and projecting beyond the tailings opening thereof; a tailings outlet on said surge pipe; a vortex forming medium inlet located tangentially on said bowl; and a feed injector device disposed coaxially in said bowl, including means for distributing feed therefrom outwardly toward the surface of a vortex formed within said bowl by the vortex forming medium.
- the feed injector device is in the form of a tube disposed co-axially within said separator and projecting through the tailings opening thereof; and wherein the feed distributing means is in the form of a fitting defining in conjunction with said tube substantially, a circumferential slot.
Landscapes
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Geometry (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Cyclones (AREA)
Description
- WWi a, in! I 20 HIM G. G. CHISHOLM CYCLONE SEPARATOR Filed Oct. 22, 1952 4 1 'G/lBf/ff 5, 5/71/5170! /& lay/7 s.
United States PatentOfl ice 2,783,887 Patented Mar. 5, 1,195?
CYCLONE SEPARAEGR Gilbert G. Chisholm, sybeiscrosse lliican, Ontario, Can- ,ada assignor of fifty-one percent to Raymond -Basil Earl Robinson Application October 22, 1952, Serial No. 316,264
2 Claims. (Cl. 209-211) This invention relates to improvements in methods of and apparatus for concentrating ores and the like by centrifugally separating particles of various densities and more particularly to so-called cyclone separators and separation methods.
In conventional cyclone separators used in the concentration of an ore pulp or in dust collection techniques, the air or liquid entrained particles to be separated are fed into the cyclone tangentially and in any case, the fluid, either gaseous or liquid, entraining such particles, serves as the medium for forming a vortex within the cyclone structure.
According to the present invention, a vortex is set up within a cyclone separator by means of a suitable fluid and the particles of various densities to be separated are injected into the separator in such manner that each individual particle must penetrate through the fluid surface or wall of the fluid vortex therein, it being manifest that the skin effect of the fluid vortex wall is penetrated to a varying depth according to the kinetic energy of a particle striking such surface and the area-density relationship of such particle. persons that the method and apparatus for separating materials according to the present invention will give more closely consistent results Where the particle size distribution of a given sample to be separated is small; that is, the particles are all of substantially the same size.
The invention will be appreciated in more detail by reference to the following specification taken in conjunction with the accompanying drawings.
In the drawings:
Figure l is a sectional view of one form of a cyclone class of separator according to the invention, illustrating means for injecting the particles of various densities to be separated into the surface of a vortex formed therein by a vortex forming fluid; and
Figure 2 is a sectional view of a modified form of particle injector feeder.
In the drawings, shows a preferred form of cyclone separator according to the invention, comprised of a bowl part 11 having an axially located concentrate opening 12 communicating with a nozzle 13 and a tailings discharge opening 14 of larger diameter, preferably arranged within a relatively large launder 15 of cylindrical construction, rising to a substantial height but having a tailings discharge spout 16 located therein. As indicated, this construction may be formed in an integral casting.
An inlet nozzle 17 extends tangentially into the bowl at the point of its maximum inner diameter as at 18 whereby a suitable fluid such as water or air may be injected as a vortex forming medium into the bowl at suflicient pressure to create a fast circulating body of fluid 19 of annular shape between the walls 20 of the bowl and the upwardly diverging surface of the vortex 22.
It will be apparent to skilled Elbe-observed that in the type of vortex formed,
rising-fromthe-centroid opening 12 to and beyond the tailings opening 1 4 with some -'reeirculation within'the aaccordi ngly; as iparticles of various densities are prolocated pipe 24 having an end fitting 25 defining in conjunction with the pipe, a circumferential slot 26, the particles proceed from such slot at a velocity determined by the injection pressure and rotation of the injector, if desired, to strike the skin 21 of the vortex 22 and penetrate such skin to enter the body of fluid 19.
The depth of penetration of the vortex skin 21 by a particle will be determined by the velocity of the individual particle and its mass. A new factor also arises in that the penetration of the particle will also be controlled by the area-density relationship of the particle.
Very light small particles will effect a negligible penetration of the skin 21 and will be carried by the upward motion of the latter through the tailings outlet to the tailings discharge spout 16. Particles of smaller effective area per unit mass will eifect a deeper penetration as will those of greater kinetic energy.
In operation, the fluid vortex forming media is adjusted in its pressure of injection into the bowl until the heavier particles of ore pulp teed just penetrate the wall of the vortex; the particles having the greater specific gravity are smaller than other mineral particles and penetrate more rapidly, being carried to the wall of the concentrate bowl and down to the concentrate discharge opening. Larger particles of lesser specific gravity will not penetrate so effectively and are carried to tailings discharge.
If it is desired to feed dry ore, the bottom plate 25 of the feed injector pipe 23 is replaced by a flat disc rotated about the axis of the concentrator, this form being designated in Figure 2 wherein the flat disc 25 is supported by the rod 26 carried by open spider guides 27 in the tube 28. The rod 26 may be rotated by any suitable drive means such as the motor illustrated. The disc 25 along with the drive and rod 26, is raised or lowered until a desired rate of feed is arrived at, in conjunction with the best speed of rotation of the disc.
As will be apparent from an examination of Figure 1, the launder 15 is in the form of a vertical open-ended surge pipe which may be of very great height to effect a more uniform vortex in the separator bowl 11. The arrows illustrated on the drawing, indicate the direction of flow of the fluid vortex medium within the bowl.
From the foregoing, it will be apparent that my injection system for cyclone type of separators enables a greater control through a large number of factors effecting separation and permits an independent control over feed rate of the material being introduced for separation as compared with the rate of injection of the fluid medium forming the vortex. Moreover, the feed injection device being located axially of the vortex may be raised or lowered therewithin to obtain maximum eificiency of injection and separation, along with the control of feed rate and the control of the vortex itself, by independent means.
It is intended that the present disclosure should not be construed in any limiting sense other than that indicated by the scope of the following claims.
What I claim as my invention is:
1. In acyclone separator having a separating bowl with an axially located concentrate opening of relatively small orilice' diameter and a co-axial opposed tailings opening of relatively large diameter but of a lesser diameter than said bowl, the combination therewith of: a surge pipe co-axially formed on said bowl and projecting beyond the tailings opening thereof; a tailings outlet on said surge pipe; a vortex forming medium inlet located tangentially on said bowl; and a feed injector device disposed coaxially in said bowl, including means for distributing feed therefrom outwardly toward the surface of a vortex formed within said bowl by the vortex forming medium.
2. In a cyclone separator, the combination claimed in claim 1 wherein the feed injector device is in the form of a tube disposed co-axially within said separator and projecting through the tailings opening thereof; and wherein the feed distributing means is in the form of a fitting defining in conjunction with said tube substantially, a circumferential slot.
References Cited in the file of this patent UNITED STATES PATENTS
Publications (1)
Publication Number | Publication Date |
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US2783887A true US2783887A (en) | 1957-03-05 |
Family
ID=3446367
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US2783887D Expired - Lifetime US2783887A (en) | Cyclone separator |
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US (1) | US2783887A (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2856072A (en) * | 1955-05-04 | 1958-10-14 | Kronstad Haavard | Centrifugal separators |
US2900080A (en) * | 1956-02-17 | 1959-08-18 | Gen Electric | Drain means for clothes washer |
US2958420A (en) * | 1957-05-27 | 1960-11-01 | Phillips Petroleum Co | Hydrocyclone and process |
US2963154A (en) * | 1958-01-29 | 1960-12-06 | Vane Zdenek | Centrifugal separation apparatus |
US2965232A (en) * | 1959-05-04 | 1960-12-20 | Vane Zdenek | Centrifugal screen separation apparatus |
US2976994A (en) * | 1958-02-06 | 1961-03-28 | Oreclone Concentrating Corp | Mineral concentrating and separating apparatus |
US3023903A (en) * | 1958-12-03 | 1962-03-06 | Nortons Tividale Ltd | Heavy media process and apparatus |
US3389793A (en) * | 1967-04-12 | 1968-06-25 | Stamicarbon | Cyclone washer with water only |
US3396844A (en) * | 1964-05-20 | 1968-08-13 | Ajem Lab Inc | Vortical separator |
US5078549A (en) * | 1989-07-19 | 1992-01-07 | J. M. Voith Gmbh | Hydrocyclone |
US20120097280A1 (en) * | 2009-05-08 | 2012-04-26 | Watreco Ip Ab | Vortex generator with vortex chamber |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US530445A (en) * | 1894-12-04 | Purifier and aerator | ||
US851599A (en) * | 1906-03-27 | 1907-04-23 | James Francis Latimer | Apparatus for separating minerals. |
US1012151A (en) * | 1910-07-22 | 1911-12-19 | William Polglase | Hydraulic system of ore separation. |
US1319208A (en) * | 1919-10-21 | Apparatus for separating or concentrating ores | ||
US1825157A (en) * | 1926-12-03 | 1931-09-29 | Anthracite Separator Co | Method and apparatus for hydraulically separating materials |
US2538870A (en) * | 1947-09-08 | 1951-01-23 | Atlantie Refining Company | Dewaxing hydrocarbon oil with vortex separator |
DE804430C (en) * | 1948-04-14 | 1951-04-23 | Stamicarbon | Method and device for classifying mixtures of particles |
US2655263A (en) * | 1950-10-12 | 1953-10-13 | Ferros Metals Res Company Ltd | Ore pulp concentrator |
-
0
- US US2783887D patent/US2783887A/en not_active Expired - Lifetime
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US530445A (en) * | 1894-12-04 | Purifier and aerator | ||
US1319208A (en) * | 1919-10-21 | Apparatus for separating or concentrating ores | ||
US851599A (en) * | 1906-03-27 | 1907-04-23 | James Francis Latimer | Apparatus for separating minerals. |
US1012151A (en) * | 1910-07-22 | 1911-12-19 | William Polglase | Hydraulic system of ore separation. |
US1825157A (en) * | 1926-12-03 | 1931-09-29 | Anthracite Separator Co | Method and apparatus for hydraulically separating materials |
US2538870A (en) * | 1947-09-08 | 1951-01-23 | Atlantie Refining Company | Dewaxing hydrocarbon oil with vortex separator |
DE804430C (en) * | 1948-04-14 | 1951-04-23 | Stamicarbon | Method and device for classifying mixtures of particles |
US2655263A (en) * | 1950-10-12 | 1953-10-13 | Ferros Metals Res Company Ltd | Ore pulp concentrator |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2856072A (en) * | 1955-05-04 | 1958-10-14 | Kronstad Haavard | Centrifugal separators |
US2900080A (en) * | 1956-02-17 | 1959-08-18 | Gen Electric | Drain means for clothes washer |
US2958420A (en) * | 1957-05-27 | 1960-11-01 | Phillips Petroleum Co | Hydrocyclone and process |
US2963154A (en) * | 1958-01-29 | 1960-12-06 | Vane Zdenek | Centrifugal separation apparatus |
US2976994A (en) * | 1958-02-06 | 1961-03-28 | Oreclone Concentrating Corp | Mineral concentrating and separating apparatus |
US3023903A (en) * | 1958-12-03 | 1962-03-06 | Nortons Tividale Ltd | Heavy media process and apparatus |
US2965232A (en) * | 1959-05-04 | 1960-12-20 | Vane Zdenek | Centrifugal screen separation apparatus |
US3396844A (en) * | 1964-05-20 | 1968-08-13 | Ajem Lab Inc | Vortical separator |
US3389793A (en) * | 1967-04-12 | 1968-06-25 | Stamicarbon | Cyclone washer with water only |
US5078549A (en) * | 1989-07-19 | 1992-01-07 | J. M. Voith Gmbh | Hydrocyclone |
US20120097280A1 (en) * | 2009-05-08 | 2012-04-26 | Watreco Ip Ab | Vortex generator with vortex chamber |
US9243653B2 (en) * | 2009-05-08 | 2016-01-26 | Watreco Ip Ab | Vortex generator with vortex chamber |
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