US1366766A - Pneumatic flotation cell and method - Google Patents
Pneumatic flotation cell and method Download PDFInfo
- Publication number
- US1366766A US1366766A US23993A US2399315A US1366766A US 1366766 A US1366766 A US 1366766A US 23993 A US23993 A US 23993A US 2399315 A US2399315 A US 2399315A US 1366766 A US1366766 A US 1366766A
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- US
- United States
- Prior art keywords
- tank
- partitions
- flotation cell
- pulp
- pneumatic flotation
- 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
- 238000000034 method Methods 0.000 title description 8
- 238000005188 flotation Methods 0.000 title description 6
- 238000005192 partition Methods 0.000 description 26
- 239000012530 fluid Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 239000006260 foam Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910000497 Amalgam Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000005267 amalgamation Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000013528 metallic particle Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/24—Pneumatic
- B03D1/26—Air lift machines
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/02—Froth-flotation processes
- B03D1/028—Control and monitoring of flotation processes; computer models therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1412—Flotation machines with baffles, e.g. at the wall for redirecting settling solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1493—Flotation machines with means for establishing a specified flow pattern
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/24—Pneumatic
- B03D1/245—Injecting gas through perforated or porous area
Definitions
- My invention relates to a method of and an apparatus for concentrating metallic ores by separating the metallic particles from the barren or rocky constituents thereof, and the invention consists of the method and the parts and the constructions, arrangements and combinations of parts which I will hereinafter describe and claim.
- FIG. l is a longitudinal sectional view of a flotation cell embodying my invention.
- Fi 2 is a cross sectional view on the line X- of 1.
- Fig. 3 is a longitudinal sectional view of a ortion of a flotation cell of modified form.
- buoyant processes which is distinguished from the usual amalgamation processes in which the ore forms an amalgam, in that in the buoyant process a certain percentage of oil, or of two dissimilar oils or an oil and acid, or an oil and an alkali, or some other suitable substance, is mixed with finely ground ore pulp and the mixture is then subjected to aeration for the purpose of producin a froth composed of bubbles of air and .01 to which the mineral particles attach, said froth having the appearance of an aggregation or mass of soap bubbles, which when collected and the froth discharged or broken down by natural settlement or by the addition of cold water, or other means, displaces the mineral particles that have been caught.
- A represents a tank of suitable material and which is herein shown as of substantially rectangular form and comprising a bottom, a, front and rear ends, a, an and sides a the bottom in the present instance being shown substantially level and there being supported a suit able distance thereabove, a false bottom, B, of some suitable porous or pervious material, whlch should have the function of permitting the passage through it of a gaseous medium, but not the water or pulp.
- the space between the permanent and false bottom of the tank constitutes an air chamber.
- This chamber may run continuously from one end of the tank to the other, and it may be subdivided by means of partitions, b, and into this chamber or chambers air or other gaseous fluid may be delivered under pressure through a supply pipe, 0, and valve-controlled branches, at.
- the tank is also provided with a series of more or less closely related permanent partitions, D, which are fixedly secured between the sides of the tank so as to form a series of compartments one succeeding the other from the front to the rear end of the machine, said partitions having their lower ends terminating a short distance above the false bottom, B, as shown in Fig. 1.
- Each of the partitions, D is provided with a gate, f, which is slidably mounted on the lower portion of the partition and is provided with a stem, 9, which extends upwardly through a hand-wheel, h, at the upper portion of the tank, whereby the gate may be adjusted relatively to the partitions to regulate the height of the passage between the bottom of the gate and the false bottom through which passage the pulp is permitted to flow from the head end to the tail end of the tank.
- a which forms a weir, the height of which determines and also serves to maintain the liquid level within the tank, said weir or opening being overlapped by a plate, 70, which forms between itself and the end wall of the tank, a passage, Z, throu h which the tailings pass to the weir, and into a suitable receiver, m.
- the tank is also provided with a concentrates launder, 1, extending along one or both sides of the upper portion of the tank and into which launder the froth generated in the tank during the admission of'the gaseous fluid into the pulp overflows in the manner well known in this art.
- the overflow edge in the present instance is slightly inclined toward the tail end of the tank, but obviously this edge could be level, instead of set down a trifle at each of the partitions as shown, without in any manner departing from the spirit of my invention.
- the bottom of the tank, A is shown as provided with a. series of cells, B, of substantially funnel-shape and into each of which one of the valve-controlled branch pipes, 03', conducts the air or gaseous medium to the cell so that it may be delivered through the porous bottom and into the fluid contents of the tank, for aerating said contents and cansing the generation of a foam or froth, which rises through the liquid contents and accumulates on the surface thereof and gradually accumulates until it passes over the overflow edge of the tank and into the launder, before mentioned.
- Fig. 3 will prove of convenience in operation in case some of the sections of the porous material, if made of sections, are damaged by accident or otherwise, and have to be removed. In this case the damaged section could be cut out and the tank still continue to run with but little sacrifice in efficiency.
- the pulp with its addition of a froth producing agent is fed into the head end of the machine and flows toward the tail end and gradually rises in the several compartments between the fixed partitions until the proper level of the fluid is reached and which level is determined by the position of the weir at the tail end of the machine.
- the gates may be so adjusted relatively to the porous false bottom of the tank as to create an eddy, or movement of the pulp, at the gate suflicient to keep the sands in the pulp in suspension.
- the heavy sands or tailings are caused to travel along the false bottom and beneath the successive gates and to be finally delivered through the weir at the tail end of the machine, While the foam or froth generated in the tank rises through the spaces between the partitions and accumulates on the surface of the liquid contents and gradually builds up thereon and overflows the top edge of the tank and into the launder before mentioned.
- a tank having a bottom forming a permeable bed through which a gaseous medium is delivered for the purpose of aerating the liquid contents of the tank, means for delivering the gaseous medium through the bed, said tank having a series of spaced partitions whose lower edges terminate above said permeable bed, said partitions being movable toward and from said bed and adapted to constrict the openings beneath the partitions and create eddies in proximity to the partitions whereby sands agitated into suspension by passing under one partition will be caught in the eddy created by the next succeeding partition.
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- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biotechnology (AREA)
- General Engineering & Computer Science (AREA)
- Paper (AREA)
Description
J. M. CALLOW.
PNEUMATIC FLOTATION CELL AND METHOD.
APPLICATION FILED APR. 26, 1915.
1,366,766. Patented Jan. 25, 1921.
woemtoo Quorum UNITED STATES PATENT OFFICE.
JOHN M. CALLOW, OF SALT LAKE CITY, UTAH, ASSIGNOR, BY MESNE ASSIGNMENTS,
TO PNEUMATIC PROCESS FLOTATION COMPANY, OF NEW YORK, N. Y., A CORPORA- TION OF DELAWARE.
PNEUMATIC FLOTATION CELL AND METHOD.
Specification of Letters Patent.
Patented Jan. 25, 1921.
Application filed April 26, 1915. Serial No. 23,993.
To all whom it may concern:
Be it known that I, JOHN M. CALLow, a subject of the King of Great Britain, residing at Salt Lake Cit in the county of Salt Lake and State of tah, have invented certain new and useful Improvements in Pneumatic Flotation Cells and Methods, of which the following is a specification.
My invention relates to a method of and an apparatus for concentrating metallic ores by separating the metallic particles from the barren or rocky constituents thereof, and the invention consists of the method and the parts and the constructions, arrangements and combinations of parts which I will hereinafter describe and claim.
In he accompanying drawing forming part 0 this specification and in which similar letters of reference indicate like parts in the several views Figure l is a longitudinal sectional view of a flotation cell embodying my invention.
Fi 2 is a cross sectional view on the line X- of 1.
Fig. 3 is a longitudinal sectional view of a ortion of a flotation cell of modified form.
he present invention is distinctly related to the art commonly known as buoyant processes and which is distinguished from the usual amalgamation processes in which the ore forms an amalgam, in that in the buoyant process a certain percentage of oil, or of two dissimilar oils or an oil and acid, or an oil and an alkali, or some other suitable substance, is mixed with finely ground ore pulp and the mixture is then subjected to aeration for the purpose of producin a froth composed of bubbles of air and .01 to which the mineral particles attach, said froth having the appearance of an aggregation or mass of soap bubbles, which when collected and the froth discharged or broken down by natural settlement or by the addition of cold water, or other means, displaces the mineral particles that have been caught.
In the accompanying drawings embodying my aforesaid invention, A, represents a tank of suitable material and which is herein shown as of substantially rectangular form and comprising a bottom, a, front and rear ends, a, an and sides a the bottom in the present instance being shown substantially level and there being supported a suit able distance thereabove, a false bottom, B, of some suitable porous or pervious material, whlch should have the function of permitting the passage through it of a gaseous medium, but not the water or pulp.
The space between the permanent and false bottom of the tank constitutes an air chamber. This chamber may run continuously from one end of the tank to the other, and it may be subdivided by means of partitions, b, and into this chamber or chambers air or other gaseous fluid may be delivered under pressure through a supply pipe, 0, and valve-controlled branches, at.
The tank is also provided with a series of more or less closely related permanent partitions, D, which are fixedly secured between the sides of the tank so as to form a series of compartments one succeeding the other from the front to the rear end of the machine, said partitions having their lower ends terminating a short distance above the false bottom, B, as shown in Fig. 1.
Each of the partitions, D, is provided with a gate, f, which is slidably mounted on the lower portion of the partition and is provided with a stem, 9, which extends upwardly through a hand-wheel, h, at the upper portion of the tank, whereby the gate may be adjusted relatively to the partitions to regulate the height of the passage between the bottom of the gate and the false bottom through which passage the pulp is permitted to flow from the head end to the tail end of the tank.
At the head end of the tank there is also an inclined partition, i, the lower end of which terminates above the false bot-tom,
constructed with an outlet opening, a, which forms a weir, the height of which determines and also serves to maintain the liquid level within the tank, said weir or opening being overlapped by a plate, 70, which forms between itself and the end wall of the tank, a passage, Z, throu h which the tailings pass to the weir, and into a suitable receiver, m.
The tank is also provided with a concentrates launder, 1, extending along one or both sides of the upper portion of the tank and into which launder the froth generated in the tank during the admission of'the gaseous fluid into the pulp overflows in the manner well known in this art. The overflow edge in the present instance is slightly inclined toward the tail end of the tank, but obviously this edge could be level, instead of set down a trifle at each of the partitions as shown, without in any manner departing from the spirit of my invention.
In the construction shown in Fig. 3, the bottom of the tank, A, is shown as provided with a. series of cells, B, of substantially funnel-shape and into each of which one of the valve-controlled branch pipes, 03', conducts the air or gaseous medium to the cell so that it may be delivered through the porous bottom and into the fluid contents of the tank, for aerating said contents and cansing the generation of a foam or froth, which rises through the liquid contents and accumulates on the surface thereof and gradually accumulates until it passes over the overflow edge of the tank and into the launder, before mentioned.
The construction of Fig. 3 will prove of convenience in operation in case some of the sections of the porous material, if made of sections, are damaged by accident or otherwise, and have to be removed. In this case the damaged section could be cut out and the tank still continue to run with but little sacrifice in efficiency.
The general operation of the device will be understood by those skilled in the art, it being sufficient to say that the pulp with its addition of a froth producing agent is fed into the head end of the machine and flows toward the tail end and gradually rises in the several compartments between the fixed partitions until the proper level of the fluid is reached and which level is determined by the position of the weir at the tail end of the machine. By providing each of the station partitions, D, with an adjustable gate and employing substantially a large number of partitions, the gates may be so adjusted relatively to the porous false bottom of the tank as to create an eddy, or movement of the pulp, at the gate suflicient to keep the sands in the pulp in suspension. This is the essential object in using a large number of partitions and in disposing these partitions only a short distance apart, because the sands which have been agitated in suspension by the first constricted openingformed beneath the gate of the first partition, will be caught in the eddy created by the next succeeding opening, which operation extends throughout the length of the machine.
Thus, the heavy sands or tailings are caused to travel along the false bottom and beneath the successive gates and to be finally delivered through the weir at the tail end of the machine, While the foam or froth generated in the tank rises through the spaces between the partitions and accumulates on the surface of the liquid contents and gradually builds up thereon and overflows the top edge of the tank and into the launder before mentioned.
From what has been heretofore said it will be apparent that I preventthe blanketing of a permeable septum which forms the bottom of a bubble flotation ore concentrator, by subdividing the pulp body longitudinally of the separator, into a series of bodies having closely restricted communication substantially only in the plane of the permeable bottom, and create in each body in proximity to each point of communication, an eddy or eddies adapted to scour the surface of said bottom and transport material having a tendency to settle on said bottom through the separator.
Having thus described my invention what I claim as new and desire to secure by Letters Patent is 2- 1. The process of preventing the blanketing of a permeable septum forming the bottom of a bubble flotation ore separator consisting in subdividing the pulp body longitudinally of the separator into a series of bodies having closely restricted communication only in the plane immediately above the permeable bottom, and creating in each body in proximity to the points of communication, eddies adapted to scour the surface of said bottom and transport material having a tendency to settle on said bottom through the separator.
2. In apparatus of the character described, a tank having a bottom forming a permeable bed through which a gaseous medium is delivered for the purpose of aerating the liquid contents of the tank, means for delivering the gaseous medium through the bed, said tank having a series of spaced partitions whose lower edges terminate above said permeable bed, said partitions being movable toward and from said bed and adapted to constrict the openings beneath the partitions and create eddies in proximity to the partitions whereby sands agitated into suspension by passing under one partition will be caught in the eddy created by the next succeeding partition.
3. In apparatus of the character described, the combination of a tank having a bottom forming a permeable bed for supplying a aseous medium into the fluid contents of t e tank, means for delivering the gaseous medium through the bed, and vertical partitions in the tank adjustable toward and from said bottom and adapted to constrict the passages beneath the partitions and to form eddies in the flowing pulp in the vicinity of the partitions whereby sands agitated into suspension by passing under one partition will be caught in an eddy cre- 10 ated by the next succeeding partition.
In testimony whereof I aifix my signature.
JOHN M. CALLOW.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US23993A US1366766A (en) | 1915-04-26 | 1915-04-26 | Pneumatic flotation cell and method |
SE51519D SE51519C1 (en) | 1915-04-26 | 1920-02-16 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US23993A US1366766A (en) | 1915-04-26 | 1915-04-26 | Pneumatic flotation cell and method |
Publications (1)
Publication Number | Publication Date |
---|---|
US1366766A true US1366766A (en) | 1921-01-25 |
Family
ID=21818285
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US23993A Expired - Lifetime US1366766A (en) | 1915-04-26 | 1915-04-26 | Pneumatic flotation cell and method |
Country Status (2)
Country | Link |
---|---|
US (1) | US1366766A (en) |
SE (1) | SE51519C1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2905322A (en) * | 1956-09-27 | 1959-09-22 | Harry B Cannon | Method and apparatus for separating and concentrating reagentized granular mixtures |
US20060021916A1 (en) * | 2004-07-06 | 2006-02-02 | Voith Paper Patent Gmbh | Method for the flotation of contaminants from an aqueous fibrous suspension |
-
1915
- 1915-04-26 US US23993A patent/US1366766A/en not_active Expired - Lifetime
-
1920
- 1920-02-16 SE SE51519D patent/SE51519C1/xx unknown
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2905322A (en) * | 1956-09-27 | 1959-09-22 | Harry B Cannon | Method and apparatus for separating and concentrating reagentized granular mixtures |
US20060021916A1 (en) * | 2004-07-06 | 2006-02-02 | Voith Paper Patent Gmbh | Method for the flotation of contaminants from an aqueous fibrous suspension |
Also Published As
Publication number | Publication date |
---|---|
SE51519C1 (en) | 1922-04-26 |
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