US1509915A - Concentrator - Google Patents
Concentrator Download PDFInfo
- Publication number
- US1509915A US1509915A US599926A US59992622A US1509915A US 1509915 A US1509915 A US 1509915A US 599926 A US599926 A US 599926A US 59992622 A US59992622 A US 59992622A US 1509915 A US1509915 A US 1509915A
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- US
- United States
- Prior art keywords
- fluid
- container
- tube
- apertures
- materials
- 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
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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
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force
Definitions
- This invention relates to concentrators, and more particularly to that ty e of concentrators in which separation o materials is effected by delivering a fluid bearing the l5 materials to be separated into a chamber,
- One important feature of the present invention resides in means by .which a whirl promoting force may be exerted upon the material bearing fluid at various ⁇ ints lengthwise of the separating chamllnthe presence construction, the arrangement is such that the heavier particles are 4o thrown outwardly by' centrifugal force against the wall of the separating chamber,
- Fig. 1 is a vertical sectional view through a concentrator constructed in accordance with the present invention.
- Fig. 2 is an enlar ed sectional view taken on the line 2 2 of ig. 1;
- Fig. 3 is a side elevation of a slightly different concentrator construction.
- a container 10 is provided in the form of a drum which is maintained in a standing position by an suitable means (not shown), and within the container or drum 10 is mounted a tube 11 extending longitudinally thereof and which preferably protrudes beyond each end of the drum 10.
- the upper end oflthe drum is .closed by a head 12 and the lower end of the drum is closed by an inclined end wall 13.
- the material laden fluid may be directed into the drum l() at the upper end thereof by a pipe 14, and this pipe preferably discharges tangentially into the drum 10 to impart aewhirling motion to the fluid as it enters the drum, and the head 12 referably has a downwardly extending s irai? construction as shown to impart a dbwuward motion to the fluid that causes it to whirl spirally downward within the annular space 15 between the drum and tube.
- the inner tube 11 has apertures 16 formed through the wall thereof at s aoed points about the tube and lengthwise t ereof, and these apertures permit fluid to pass into the tube from the annular chamber 15.
- the material bearin fluid delivered to the drum 10 be maintained in a whirling condition so that the heavier particles carried by the fluid will be thrown outwardly b centrifugal force while the lighter particles will remain suspended within the fluid, and to this end, in the present case, provision is made for delivering jets of fluid through apertures 17 within the wall of the drum 10 and against the fluid within the chamber l5.
- this is accomplished by providing a jacket 18 about the drum l0, and duid which is free from the materials to be treated is delivered under pressure into the chamber formed by the jacket. From this chamber the fluid passes inwardly into the chamber 15 through the apertures 17, and these yapertures preferably are constructed as shown in Fig. 2 so that the fluid forced inwardly through these apertures enters the chamber in substanwhirling condition, and the heavier materials that are thrown outwardly by centrifugal force strike against the wall of the drum 10 and slide downwardly into the lower end of the drum, which preferably emptiesinto a closed bin 20.
- the fluid r which ⁇ is forced through the apertures 17 should be delivered to the jacket 18 at a higher pressure than the pressure at which the material bearing fluid is delivered to 'n the container, in order to force the fluid inwardly through the apertures against the pressure of the fluid within the container,
- coneshaped aprons 21 are provided which embrace the tube 11 and extend downwardly over the' apertures 16 to form protected chambers about these apertures.
- the lower end of the tube 13 preferably is connected to a closed bin 22 and the materials that settle within the tube 11 pa downward into this bin.
- the bins 20 vand 22 are closed to prevent the fluid from escaping through the lower ends of .the drum and tube respectively, and when it is desired to empty the bins 20 and 22 the upper valves 23 and 24 may be closed while the lower valves 25 and 26 are opened.
- a short cylinder 27 may be placed about the tube 11 at the upper end of the drum lOvto increase the diameter of this tube at the point where the pipe 14 delivers fluid intoI the space between the drum 10 and cylinder 27 with a whirling movement.
- the lighter materials which are not se arated out by the whirling motion f e uid, and which do not settle within the tube 11 will passjofl' with the fluid through the upper end of this tube, and if desired a fa'n or pump may be connected to the upper end of this tube to projnote the flow of the fluid upwardly therethrough, and this flow may be controlled by theyalve 28.
- the amount of fluid delivered by the pipes 14 and 19 may be controlled by the valves 29 and 30 respectively.
- the apertures 17 may be formed at a slight inclination as shown in Fig. 1 so that they will direct their jets of fluid downwardly in the general direction in which the fluid within the chamber 15 whirls downward.
- the concentrator of the present invention is well adapted to treat materials that are suspended in either a liquid or gas, and the construction shown in Fig. 1 is provided with sliding gates or valves that are satisfactory to control the flow of air, while in Fig. 3 valves are shown ofl a t pe that are commonly used to control the ow of liquids. In other respects the construction shown in Fig. 3 is substantially the same as that shown in Fig. ⁇ 1.
- a concentrator comprising, in combination, a container supported in a standing position, a tube mounted lcentrally within said container and having apertures therein along its length for the passage of fluid from the container into the tube, means for delivering a fluid bearing the materials to be treated into the upper portion of the container with a downward whirlin movement about the tube to throw the eavier materials outward by centrifugal force away from the tube, and means for directing jets of a fluid inwardly through the walls of the container in substantially a tangential direction further to romote whirling movement of the material aring fluid moving downwardly within the container.
- a concentrator comprising, in combination, a container supported in a standing position, a tube mounted centrally within said container and having apertures therein along its length for the paage of fluid from the container into the tube, means for delivering a fluid bearing the materials to be treated into the upper portion of the container with a downward whirling movement about the tube to throw the heavier materials outward by centrifugal force away from the tube, means for directin jets of a fluid inwardly through the wal s of the container in substantially a tangential direction furtherto romote whirling movement ofv the material bearing fluid moving downwardly within the container, and means for deflecting the whirling fluid away from said apertures.
- a concentrator comprising, in combination, a container supported 1n a standing position, a tube mounted centrally within said container and having apertures therein along its length for the passage of fluid from the rcontainer into the tube, means for delivering a fluid bearing the materials to be treated into the upper portion of the container with a downward whirling movement about the tube to throw the heavier materials outward by centrifugal force away from the tube, a' jacket surrounding the container and having means for delivering a fluid into the space between the container and jacket with a whirling movement, and the container having apertures in its walls to direct the fluid within the jacket into the container in a. direction further to promote whirling movement of the material bearing fluid within the container.
- a concentrator comprising, in combination, a container supported in a standing position, a tube mounted centrally within said container and having apertures therein along its length.. for the passage of fluid from the container into the tube, means for deliverin al fluid bearing the materials to be treate into the upper portion of the container with a downward whirling movement about the tube tothrow the heavier materials outward by centrifugal force away from the tube, a jacket surrounding the container and having means for forcing a fluid into the space between the container and jacket, the container having ⁇ apertures in its walls to direct fluid from the jacket into the container in substantially a tangential movement further to promote whirling movement of the material bearing fluid within the container, and aprons adjacent the apertures within the tube to deflect the whirling fluid from the apertures.
- a concentrator comprising, in combination, a container supported in a standing position, a tube mounted centrally within the container and adapted to receive the fluid delivered to thecontainer and to conduct the fluid therefrom, means for delivering fluid bearing the materials to be treated into the container with a downward whirling movement about the tube to throw the heavier materials outwardly by centrifugal force against the wall of the container, and means for directing jets of fluid tangentially inwardly through the wall of the container at a pressure in excess of the pressure at which the material bearing fluid is delivered to the container further to promote whirling movement of the fluid moving downwardly within the container.
- a concentrator comprising, in combination, a container supported in a standing position and having narrow elongated slots formed in its walls around the container andat distributed points lengthwise thereof, a tube mounted centrally within the container and-A having apertures therein along its length for the passage of fluid from the container into the tube, means for delivering a fluid bearing the materials to be treated into the upper portion of the container with a downward whirling movement about the tube to throw the heavier materials outwardly by centrifugal force away from the tube, and means-for forcing a fluid through said narrow slots to produce jets directed substantially tangentially against the material bearing fluid within the container fur.
- ther lto promote a whirling movement of the fluid moving downward therein.
- a concentrator comprising, in combination, a tubular container having slots formed in its ⁇ walls at' oints throughout a substantial portion of its length, a tube mounted centrally within the container and having apertures therein along its length for the passage of fluid from the container into the tube, means for delivering a fluid bearing thematerials to be treated into the upper portion of the container with a downwardly whirling movement about the tube to throw the heavier materials outwardly by centrifugal force away from the tube, cone-shaped aprons extending downwardly over said apertures to deflect the whirling fluid from the apertures, and means for forcing fluid inwardly through said slots in substantially a tangential direction further to promote whirling movement of the material bearing fluid moving downwardly in the container
Description
Sept. 30 1924. Y 1,509,915
A. H. sTEBBlNs /Nl/ENTOR.'
ATTORNEY sept. 3o', 1924, Y
A. H. STEBBINS CONCENTRATOR Filed Nov. 9, 1922 2 Sheets-Sheet 2 /NVENTOR ATTORNEY @MV1/,mma I @my Patented Sept. 30, 1924.
ALBERT E. STEBBINS, OF LOS ANGELES, CALIFORNIA.
CON CENTRATOB.
Application filed November 9, 1922. Serial No. 599,926.
To all whom it may concern.
Be it known that I, ALBERT H. STEBBINS, a citizen of the United States, residing at Los Angeles, in the count of Los Angeles and State of California, ave invented an Improvement in Concentrators, of which the following description, in connection with the accompanying drawings, is a specification, like characters on the drawings repre- Ml senting like parts.
This invention relates to concentrators, and more particularly to that ty e of concentrators in which separation o materials is effected by delivering a fluid bearing the l5 materials to be separated into a chamber,
and imparting a whirling movement to the fluid so that the heavier particles therein will be thrown outwardly by centrifugal force away from the lighter particles.
Various fluids either gaseous or liquid may be used as the material bearing medium, but in most cases it will be desirable to use either air or water, depending upon the specific gravity, size and other properties of the materials to be treated.
In concentrators of this type it is important that the material bearing fluid be kept in active motion until the desired separation of the materials is effected, for if the 3@ motion of the fluid is reduced the light:
and heavy materials will settle together,
One important feature of the present invention, therefore, resides in means by .which a whirl promoting force may be exerted upon the material bearing fluid at various `ints lengthwise of the separating chamllnthe presence construction, the arrangement is such that the heavier particles are 4o thrown outwardly by' centrifugal force against the wall of the separating chamber,
and the fluid bearing the lighter materials moves inwardly and enters apertures in the wall of a tube mounted centrally within 4a the separating chamber.
It is important that the movement of the material bearin fluid be arrested adjacent the apertures o the central tube, and another feature of the invention resides in 5o means for arresting the movement of the fluid adjacent these apertures.
Other fea-tures'of the invention and novel combination of parts in addition to the above will be hereinafter described in connection with the accompanying drawings which illustrate one good practical form thereof. i
In the drawings:
Fig. 1 is a vertical sectional view through a concentrator constructed in accordance with the present invention.
Fig. 2 is an enlar ed sectional view taken on the line 2 2 of ig. 1; and
Fig. 3 is a side elevation of a slightly different concentrator construction.
In the embodiment of the invention shown in the drawings, a container 10 is provided in the form of a drum which is maintained in a standing position by an suitable means (not shown), and within the container or drum 10 is mounted a tube 11 extending longitudinally thereof and which preferably protrudes beyond each end of the drum 10. The upper end oflthe drum is .closed by a head 12 and the lower end of the drum is closed by an inclined end wall 13.
The material laden fluid may be directed into the drum l() at the upper end thereof by a pipe 14, and this pipe preferably discharges tangentially into the drum 10 to impart aewhirling motion to the fluid as it enters the drum, and the head 12 referably has a downwardly extending s irai? construction as shown to impart a dbwuward motion to the fluid that causes it to whirl spirally downward within the annular space 15 between the drum and tube. The inner tube 11 has apertures 16 formed through the wall thereof at s aoed points about the tube and lengthwise t ereof, and these apertures permit fluid to pass into the tube from the annular chamber 15.
It is desirablekk that the material bearin fluid delivered to the drum 10 be maintained in a whirling condition so that the heavier particles carried by the fluid will be thrown outwardly b centrifugal force while the lighter particles will remain suspended within the fluid, and to this end, in the present case, provision is made for delivering jets of fluid through apertures 17 within the wall of the drum 10 and against the fluid within the chamber l5.
In the construction shown this is accomplished by providing a jacket 18 about the drum l0, and duid which is free from the materials to be treated is delivered under pressure into the chamber formed by the jacket. From this chamber the fluid passes inwardly into the chamber 15 through the apertures 17, and these yapertures preferably are constructed as shown in Fig. 2 so that the fluid forced inwardly through these apertures enters the chamber in substanwhirling condition, and the heavier materials that are thrown outwardly by centrifugal force strike against the wall of the drum 10 and slide downwardly into the lower end of the drum, which preferably emptiesinto a closed bin 20. The fluid r which `is forced through the apertures 17 should be delivered to the jacket 18 at a higher pressure than the pressure at which the material bearing fluid is delivered to 'n the container, in order to force the fluid inwardly through the apertures against the pressure of the fluid within the container,
and since different pipes 14 and 19 are provided for delivering fluid tothe upper part of the container and jacket respectively the relative pressures may be varied as desired.
The fluid from which the heavier par- Iticles have been removed centrifugal force will be crowded inward y toward the tube` 11 to enter the apertures 16, and it is desirable to provide means for arresting the `whirling movement of the fluid adjacent these apertures. In the present case, coneshaped aprons 21 are provided which embrace the tube 11 and extend downwardly over the' apertures 16 to form protected chambers about these apertures.
The lower end of the tube 13 preferably is connected to a closed bin 22 and the materials that settle within the tube 11 pa downward into this bin. The bins 20 vand 22 are closed to prevent the fluid from escaping through the lower ends of .the drum and tube respectively, and when it is desired to empty the bins 20 and 22 the upper valves 23 and 24 may be closed while the lower valves 25 and 26 are opened.
A short cylinder 27 may be placed about the tube 11 at the upper end of the drum lOvto increase the diameter of this tube at the point where the pipe 14 delivers fluid intoI the space between the drum 10 and cylinder 27 with a whirling movement.
The lighter materials which are not se arated out by the whirling motion f e uid, and which do not settle within the tube 11 will passjofl' with the fluid through the upper end of this tube, and if desired a fa'n or pump may be connected to the upper end of this tube to projnote the flow of the fluid upwardly therethrough, and this flow may be controlled by theyalve 28. The amount of fluid delivered by the pipes 14 and 19 may be controlled by the valves 29 and 30 respectively.
In some cases it may be desirable to form the apertures 17 at a slight inclination as shown in Fig. 1 so that they will direct their jets of fluid downwardly in the general direction in which the fluid within the chamber 15 whirls downward.
As stated, the concentrator of the present invention is well adapted to treat materials that are suspended in either a liquid or gas, and the construction shown in Fig. 1 is provided with sliding gates or valves that are satisfactory to control the flow of air, while in Fig. 3 valves are shown ofl a t pe that are commonly used to control the ow of liquids. In other respects the construction shown in Fig. 3 is substantially the same as that shown in Fig.` 1.
What is claimed is:
1. A concentrator comprising, in combination, a container supported in a standing position, a tube mounted lcentrally within said container and having apertures therein along its length for the passage of fluid from the container into the tube, means for delivering a fluid bearing the materials to be treated into the upper portion of the container with a downward whirlin movement about the tube to throw the eavier materials outward by centrifugal force away from the tube, and means for directing jets of a fluid inwardly through the walls of the container in substantially a tangential direction further to romote whirling movement of the material aring fluid moving downwardly within the container.
2. A concentrator comprising, in combination, a container supported in a standing position, a tube mounted centrally within said container and having apertures therein along its length for the paage of fluid from the container into the tube, means for delivering a fluid bearing the materials to be treated into the upper portion of the container with a downward whirling movement about the tube to throw the heavier materials outward by centrifugal force away from the tube, means for directin jets of a fluid inwardly through the wal s of the container in substantially a tangential direction furtherto romote whirling movement ofv the material bearing fluid moving downwardly within the container, and means for deflecting the whirling fluid away from said apertures.
3. A concentrator comprising, in combination, a container supported 1n a standing position, a tube mounted centrally within said container and having apertures therein along its length for the passage of fluid from the rcontainer into the tube, means for delivering a fluid bearing the materials to be treated into the upper portion of the container with a downward whirling movement about the tube to throw the heavier materials outward by centrifugal force away from the tube, a' jacket surrounding the container and having means for delivering a fluid into the space between the container and jacket with a whirling movement, and the container having apertures in its walls to direct the fluid within the jacket into the container in a. direction further to promote whirling movement of the material bearing fluid within the container. y
4. A concentrator comprising, in combination, a container supported in a standing position, a tube mounted centrally within said container and having apertures therein along its length.. for the passage of fluid from the container into the tube, means for deliverin al fluid bearing the materials to be treate into the upper portion of the container with a downward whirling movement about the tube tothrow the heavier materials outward by centrifugal force away from the tube, a jacket surrounding the container and having means for forcing a fluid into the space between the container and jacket, the container having `apertures in its walls to direct fluid from the jacket into the container in substantially a tangential movement further to promote whirling movement of the material bearing fluid within the container, and aprons adjacent the apertures within the tube to deflect the whirling fluid from the apertures.
5. A concentrator comprising, in combination, a container supported in a standing position, a tube mounted centrally within the container and adapted to receive the fluid delivered to thecontainer and to conduct the fluid therefrom, means for delivering fluid bearing the materials to be treated into the container with a downward whirling movement about the tube to throw the heavier materials outwardly by centrifugal force against the wall of the container, and means for directing jets of fluid tangentially inwardly through the wall of the container at a pressure in excess of the pressure at which the material bearing fluid is delivered to the container further to promote whirling movement of the fluid moving downwardly within the container. y
6. A concentrator comprising, in combination, a container supported in a standing position and having narrow elongated slots formed in its walls around the container andat distributed points lengthwise thereof, a tube mounted centrally within the container and-A having apertures therein along its length for the passage of fluid from the container into the tube, means for delivering a fluid bearing the materials to be treated into the upper portion of the container with a downward whirling movement about the tube to throw the heavier materials outwardly by centrifugal force away from the tube, and means-for forcing a fluid through said narrow slots to produce jets directed substantially tangentially against the material bearing fluid within the container fur. l
ther lto promote a whirling movement of the fluid moving downward therein.
7. A concentrator comprising, in combination, a tubular container having slots formed in its` walls at' oints throughout a substantial portion of its length, a tube mounted centrally within the container and having apertures therein along its length for the passage of fluid from the container into the tube, means for delivering a fluid bearing thematerials to be treated into the upper portion of the container with a downwardly whirling movement about the tube to throw the heavier materials outwardly by centrifugal force away from the tube, cone-shaped aprons extending downwardly over said apertures to deflect the whirling fluid from the apertures, and means for forcing fluid inwardly through said slots in substantially a tangential direction further to promote whirling movement of the material bearing fluid moving downwardly in the container In testimony whereof, I have lsigned my name to this specification.
ALBERT H. STEBBINS.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US599926A US1509915A (en) | 1922-11-09 | 1922-11-09 | Concentrator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US599926A US1509915A (en) | 1922-11-09 | 1922-11-09 | Concentrator |
Publications (1)
Publication Number | Publication Date |
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US1509915A true US1509915A (en) | 1924-09-30 |
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ID=24401683
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US599926A Expired - Lifetime US1509915A (en) | 1922-11-09 | 1922-11-09 | Concentrator |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2460938A (en) * | 1944-08-05 | 1949-02-08 | Johns Manville | Method and apparatus for cleaning asbestos |
US2612266A (en) * | 1945-10-11 | 1952-09-30 | Colgate Palmolive Peet Co | Cooling of sprayed products |
US3305940A (en) * | 1963-10-14 | 1967-02-28 | Isler Walter | Heat exchange between granular material and gas |
US3731393A (en) * | 1970-06-13 | 1973-05-08 | Morinaga Milk Industry Co Ltd | Method of and apparatus for fluidizing particulate substance |
US3901794A (en) * | 1972-07-21 | 1975-08-26 | Polysius Ag | Circulatory air sifter |
US4299563A (en) * | 1980-06-02 | 1981-11-10 | National Gypsum Company | Cyclone processor and separator |
US6530484B1 (en) * | 1999-11-18 | 2003-03-11 | Multotec Process Equipment (Proprietary) Ltd. | Dense medium cyclone separator |
US9884325B2 (en) * | 2015-08-21 | 2018-02-06 | Andritz Ag | Hydrocyclone with fine material depletion in the cyclone underflow |
-
1922
- 1922-11-09 US US599926A patent/US1509915A/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2460938A (en) * | 1944-08-05 | 1949-02-08 | Johns Manville | Method and apparatus for cleaning asbestos |
US2612266A (en) * | 1945-10-11 | 1952-09-30 | Colgate Palmolive Peet Co | Cooling of sprayed products |
US3305940A (en) * | 1963-10-14 | 1967-02-28 | Isler Walter | Heat exchange between granular material and gas |
US3731393A (en) * | 1970-06-13 | 1973-05-08 | Morinaga Milk Industry Co Ltd | Method of and apparatus for fluidizing particulate substance |
US3901794A (en) * | 1972-07-21 | 1975-08-26 | Polysius Ag | Circulatory air sifter |
US4299563A (en) * | 1980-06-02 | 1981-11-10 | National Gypsum Company | Cyclone processor and separator |
US6530484B1 (en) * | 1999-11-18 | 2003-03-11 | Multotec Process Equipment (Proprietary) Ltd. | Dense medium cyclone separator |
US9884325B2 (en) * | 2015-08-21 | 2018-02-06 | Andritz Ag | Hydrocyclone with fine material depletion in the cyclone underflow |
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