US2369401A - Froth skimming and crowding device for flotation machines - Google Patents
Froth skimming and crowding device for flotation machines Download PDFInfo
- Publication number
- US2369401A US2369401A US504550A US50455043A US2369401A US 2369401 A US2369401 A US 2369401A US 504550 A US504550 A US 504550A US 50455043 A US50455043 A US 50455043A US 2369401 A US2369401 A US 2369401A
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- Prior art keywords
- froth
- skimming
- machine
- machines
- flotation
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Classifications
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- 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
- B03D1/16—Flotation machines with impellers; Subaeration 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
- B03D1/1443—Feed or discharge mechanisms for flotation tanks
- B03D1/1462—Discharge mechanisms for the froth
-
- 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
Definitions
- Froth flotation machines present a considerable problem in froth overflow, particularly when highly miner'alized froths, are produced, or where it is attempted to float relatively coarse particles.
- skimming devices operating close to the froth overflow lip also do not skim efficiently the froth located more nearly in the center of the machine and as the central vortex is the point where there is maximum agitation it is also the point where bubbles are most readily broken and the necessity of rapid removal is at a maximum.
- An ven more serious disadvantage of the conven ional types of froth skimmers lies in the fact that they are driven at a constant predetermined speed. As a result, if the skimming speed is adjusted for certain conditions of froth, changes in these conditions will find the skimming device operating at a speed which is not the optimum.
- a froth flotation machine should release its froth over a relatively narrow area of surface immediately adjacent to froth overflow lips and the skimming device should remove the tion machines of the circular or more generally non-elongated type.
- a freely rotatable cone is centrally mounted in. the cell with its apex extending downinto the central 'vortex, the tip of the cone being cut off to permit the drive shaft for the agitating means to pass through in the case of machines driven from the top which is. the more common type.
- the conical surface of the device of the present invention extends to a pointfairly near the over-- flow lip so that the surfaceof liquid in the cell is in the form of a narrow annulus. Fins are attached to the conical device so that the rotary 'motion of the pulp in the cell due to the rotary "agitating means tends to turn the device which is provided with skimming blades at its periphery. In operation, therefore, the device spins at a speed which is governed by the operation of the cell, the froth is crowded into a narrow annulus and is immediately skimmed into the launder.
- The, device of the present invention performs two functions simultaneously, namely the crowding of the'froth into a narrow surface of disengagement and immediately skimming of the froth whichv rises to the surface. At the same time the device does not require additional power or rather the power requirements are negligible and ditions. If the agitating means is speeded up resulting in a more rapid vortex the skimmer and froth crowding device of the present invention spins faster. The same is true where there is a very violent froth disengagement which increases the volume of rising material and hence the speed with which the pulp swirls in the cell. Over a wide range, therefore, optimum skimming rate can be maintained-by a suitable desig of the driving fins and skimming blades of the present invention.
- the device is simple, extremely cheap to manufacture, and requires practically no maintenance. It also does not add to the complication'of flotation machine drives.
- the operation of the device of the present invention is most simple in a circular flotation ma- Chine where the round overflow lip is concentric with the rotating agitating means, and it is precisely this type of machine which is most diflicult to skim satisfactorily by the conventional skimming devices involving rotating paddles.
- the invention is not limited to a. machine which is exactly circular. On the contrary it is pos ible to use the device for a square machine or even in a rectangular machine, provided it is not too elongated. Thu in a square machine or a rectangular machine in which the pairs of sides do not diifer greatly in length a somewhat longer skimmer blade will operate satisfactorily.
- the device of the present invention is not well suited for very long narrow machines.
- the overflow lip may extend only on two sides.
- the length of the skimmer blades is chosen so that they will skim froth satisfactorily over the two sides.
- non-elongated will be used to describe circular machines, square machines, and machines of substantially rectangular shape in which the difference in length of the pairs of sides is not great. It should be understood that this term is intended to have no other meaning.
- the shaft is iournaled in a stationary hollow shaft 8 through which air is introduced through the valved inlet in the customary manner.
- this stationary shaft there is mounted the frusto conical device 9 of the present invention, which is provided with a flange l6 forming a housing for a bearing "ion a collar l5 fastened to the shaft 8.
- the conical device is attached to the bearing by the flat spokes II and is provided stator causes the pulp in the cell to swirl form ing a vortex.
- the swirling of the pulp spins the skimming device by means or the fins l3 and I4.
- Froth is crowded by the conical surface so that it reaches the surface of the cell in a narrow an- I nulus between the outer periphery of the crowding and skimming device and the froth overflow lip.
- the skimming blades I! remove the froth promptly from this narrow zone before any considerable loss of'mineral'particles can take place.
- the device of the present invention is'applicable to round froth flotation machines ofvarious 'types used with various ores and reagents. It
- the device of the present invention will adjust itself to change in operating conditions, it is desirable to design and dimension the device for best results with a particular type of froth flotation operation- However, over a wide range no material changes in design are. necessary and, therefore, devices of the presentinvention may be used interchangeably in a number of operations.
- the conical portion of the device of the present invention is shown as hollow. This is the most satisfactory mechanical design in most cases. However, it is not essential and a solid cone may beused in some cases but its extra weight usually renders it undesirable.
- a. non-elongated mechanical froth flotation machine provided with a rotary agitating 40 means driven by a verticleshaft rising above the machine
- the improvement which comprises i an inverted conical body rotatably mounted concentric with said shaft and leaving a narrow space between its'periphery and the froth overflow lips of the machine, flns attached to the conical body and extendingout radially into the pulp to cause the conical body to rotate .with swirling of the pulp in the machine, and skiinming blades attached to the periphery of the conical body positioned to skim froth over the overflow lips into the froth launder of the machine.
- skimmingfdevlce' is not mechanical but-is merely thing which increases the rotation of this vortex 2.
- a round froth flotation machine of the mechanical type provided with a central rotary centric with said shaft and leaving an-annular space between its periphery and the froth overflow lip' of the machine, fins attached to the conical body and extending out radially to cause it to rotate with swirling of the pulp in the machine, and skimming blades attached-to the periphery of the conical body positioned to skim froth over the overflow lip into the froth launder of the machine.
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Description
Feb. 13, 1945.
FROTH SKIMMING N. MORASH 2,369,401
AND CROWDING DEVICE FOR FLOTATION MACHINES Filecl 001;. l, 1943' 2 Sheets-Sheet l L? INVENTOR Nap/m4 MOPHJH ATTORNEY Feb. 13, 1945. N. MORASH 2,369,401
FROTH SKIMMING AND CROWDING DEVICE FOR FLOTATION MACHINES Filed 001;. '1, 1943 2 Sheets-Sheet 2 l N V E N TO R Mommwfl/mw .9,
ATTORNEY Patented Feb. 13, 1945 FROTH SKIMMING AND CROW'DING DEVICE FOR FLOTATION MACHINES Norman Morash, Stamford, Conn., assignor to American Cyanamid Company, New York, N. Y., a corporation of Maine Application October 1, 1943, Serial No. 504,550 2 Claims. (01. 209-169) This invention relates to an improvement in mechanical froth flotation machines.
Froth flotation machines present a considerable problem in froth overflow, particularly when highly miner'alized froths, are produced, or where it is attempted to float relatively coarse particles.
The ability of the bubbles of the froth to sustain heavy weights of minerals is limited becausethe bubbles tend to break or drop their mineral load unless they are promptly removed from the machine. For this reason various froth skimming devices have been used. In rectangular machines it is common to have mechanically driven paddles along the two froth overflow lips whichslowly turn and skim off the froth. It has also been proposed a few years ago to apply mechanically driven rotary ski-mmers to froth flotation machines of the round type. Both of these devices are of considerable help in the rapid removal of mineralized froth. However, they are open to a number of'disadvantages. For one thing, they require a separate mechanical drive and in the case of rectangular machines usually two drives with resulting additional power consumption and complication. skimming devices operating close to the froth overflow lip also do not skim efficiently the froth located more nearly in the center of the machine and as the central vortex is the point where there is maximum agitation it is also the point where bubbles are most readily broken and the necessity of rapid removal is at a maximum. An ven more serious disadvantage of the conven ional types of froth skimmers lies in the fact that they are driven at a constant predetermined speed. As a result, if the skimming speed is adjusted for certain conditions of froth, changes in these conditions will find the skimming device operating at a speed which is not the optimum.
Ideally a froth flotation machine should release its froth over a relatively narrow area of surface immediately adjacent to froth overflow lips and the skimming device should remove the tion machines of the circular or more generally non-elongated type. a
According to the present invention a freely rotatable cone is centrally mounted in. the cell with its apex extending downinto the central 'vortex, the tip of the cone being cut off to permit the drive shaft for the agitating means to pass through in the case of machines driven from the top which is. the more common type. The conical surface of the device of the present invention extends to a pointfairly near the over-- flow lip so that the surfaceof liquid in the cell is in the form of a narrow annulus. Fins are attached to the conical device so that the rotary 'motion of the pulp in the cell due to the rotary "agitating means tends to turn the device which is provided with skimming blades at its periphery. In operation, therefore, the device spins at a speed which is governed by the operation of the cell, the froth is crowded into a narrow annulus and is immediately skimmed into the launder.
The, device of the present invention performs two functions simultaneously, namely the crowding of the'froth into a narrow surface of disengagement and immediately skimming of the froth whichv rises to the surface. At the same time the device does not require additional power or rather the power requirements are negligible and ditions. If the agitating means is speeded up resulting in a more rapid vortex the skimmer and froth crowding device of the present invention spins faster. The same is true where there is a very violent froth disengagement which increases the volume of rising material and hence the speed with which the pulp swirls in the cell. Over a wide range, therefore, optimum skimming rate can be maintained-by a suitable desig of the driving fins and skimming blades of the present invention.
It is an, advantage of the present invention that the device is simple, extremely cheap to manufacture, and requires practically no maintenance. It also does not add to the complication'of flotation machine drives.
The operation of the device of the present invention is most simple in a circular flotation ma- Chine where the round overflow lip is concentric with the rotating agitating means, and it is precisely this type of machine which is most diflicult to skim satisfactorily by the conventional skimming devices involving rotating paddles. However, the invention is not limited to a. machine which is exactly circular. On the contrary it is pos ible to use the device for a square machine or even in a rectangular machine, provided it is not too elongated. Thu in a square machine or a rectangular machine in which the pairs of sides do not diifer greatly in length a somewhat longer skimmer blade will operate satisfactorily. The device of the present invention is not well suited for very long narrow machines. In the case of rectangular machines the overflow lip may extend only on two sides. In such cases the length of the skimmer blades is chosen so that they will skim froth satisfactorily over the two sides. In the claims the term non-elongated" will be used to describe circular machines, square machines, and machines of substantially rectangular shape in which the difference in length of the pairs of sides is not great. It should be understood that this term is intended to have no other meaning.
- The invention will be described in greater detail in connection with a circular froth flotation machine of the Fagergren type, but it is an advantage of the present invention that it is not limited to this machine but is useable in any mechanical circular machine in which rotary the skimming The rotor is driven by the shaft 6 by means of v the pulley 1 from a source of power not shown.
The shaft is iournaled in a stationary hollow shaft 8 through which air is introduced through the valved inlet in the customary manner. On
I this stationary shaft there is mounted the frusto conical device 9 of the present invention, which is provided with a flange l6 forming a housing for a bearing "ion a collar l5 fastened to the shaft 8. The conical device is attached to the bearing by the flat spokes II and is provided stator causes the pulp in the cell to swirl form ing a vortex. The swirling of the pulp spins the skimming device by means or the fins l3 and I4. Froth is crowded by the conical surface so that it reaches the surface of the cell in a narrow an- I nulus between the outer periphery of the crowding and skimming device and the froth overflow lip. The skimming blades I! remove the froth promptly from this narrow zone before any considerable loss of'mineral'particles can take place. i
It should beznoted that "since the driveof the dependent on the vortex in the flotation cell anywill speed up the rotation of the skimming and crowding device. As the speed of'the agitator is increased so will'the speed of the vortex and more rapid skimming will result which is needed in order to take care of the larger amount of froth. Similarly where the frothing is very heavy the spinning in the cell will increase and correspondingly more-rapid skimming will take place. Within wide ranges, therefore, the device of the present invention will automatically adjust itself to changes in operating conditions of the cell requiring, therefore, a minimum of adjustment during operation.
The device of the present invention is'applicable to round froth flotation machines ofvarious 'types used with various ores and reagents. It
is particularly important in operations where skimming is a serious problem, for example certain non-metallic operations such as phosphate flotation, the clarification of lubricating coolants by froth flotation means, and the like. the device of the present invention will adjust itself to change in operating conditions, it is desirable to design and dimension the device for best results with a particular type of froth flotation operation- However, over a wide range no material changes in design are. necessary and, therefore, devices of the presentinvention may be used interchangeably in a number of operations.
The conical portion of the device of the present invention is shown as hollow. This is the most satisfactory mechanical design in most cases. However, it is not essential and a solid cone may beused in some cases but its extra weight usually renders it undesirable.
I claim: 1. In a. non-elongated mechanical froth flotation machine provided with a rotary agitating 40 means driven by a verticleshaft rising above the machine, the improvement which comprises i an inverted conical body rotatably mounted concentric with said shaft and leaving a narrow space between its'periphery and the froth overflow lips of the machine, flns attached to the conical body and extendingout radially into the pulp to cause the conical body to rotate .with swirling of the pulp in the machine, and skiinming blades attached to the periphery of the conical body positioned to skim froth over the overflow lips into the froth launder of the machine.
skimmingfdevlce'is not mechanical but-is merely thing which increases the rotation of this vortex 2. In a round froth flotation machine of the mechanical type provided with a central rotary centric with said shaft and leaving an-annular space between its periphery and the froth overflow lip' of the machine, fins attached to the conical body and extending out radially to cause it to rotate with swirling of the pulp in the machine, and skimming blades attached-to the periphery of the conical body positioned to skim froth over the overflow lip into the froth launder of the machine.
. [NORMAN MORASH.
While
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US504550A US2369401A (en) | 1943-10-01 | 1943-10-01 | Froth skimming and crowding device for flotation machines |
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US504550A US2369401A (en) | 1943-10-01 | 1943-10-01 | Froth skimming and crowding device for flotation machines |
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US2369401A true US2369401A (en) | 1945-02-13 |
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US504550A Expired - Lifetime US2369401A (en) | 1943-10-01 | 1943-10-01 | Froth skimming and crowding device for flotation machines |
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Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2880869A (en) * | 1953-07-27 | 1959-04-07 | Harry L Mcneill | Ore concentration method and apparatus |
US5039400A (en) * | 1987-10-07 | 1991-08-13 | Outokumpu Oy | Flotation machine |
US5234112A (en) * | 1991-10-02 | 1993-08-10 | Servicios Corporativos Frisco S.A. De C.V. | Flotation reactor with external bubble generator |
US5251764A (en) * | 1991-03-27 | 1993-10-12 | Outomec Oy | Flotation machine |
WO1993020945A1 (en) * | 1992-04-16 | 1993-10-28 | Atomaer Pty Ltd | Froth wash and froth removal system |
US5266240A (en) * | 1991-03-20 | 1993-11-30 | Servicios Corporativos Frisco, S.A. De C.V. | Flotation reactor with external bubble generator |
US5341938A (en) * | 1991-03-20 | 1994-08-30 | Servicios Corporativos Frisco, S.A. De C.V. | Method of separating materials in a flotation reactor |
US5611917A (en) * | 1995-11-02 | 1997-03-18 | Baker Hughes Incorporated | Flotation cell crowder device |
US20040099575A1 (en) * | 2002-11-27 | 2004-05-27 | Khan Latif A. | Method and apparatus for froth flotation |
WO2010142844A1 (en) | 2009-06-09 | 2010-12-16 | Outotec Oyj | A froth flotation method and an apparatus for extracting a valuable substance from a slurry |
WO2019008214A1 (en) | 2017-07-04 | 2019-01-10 | Outotec (Finland) Oy | A froth flotation arrangement and a froth flotation method |
-
1943
- 1943-10-01 US US504550A patent/US2369401A/en not_active Expired - Lifetime
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2880869A (en) * | 1953-07-27 | 1959-04-07 | Harry L Mcneill | Ore concentration method and apparatus |
US5039400A (en) * | 1987-10-07 | 1991-08-13 | Outokumpu Oy | Flotation machine |
US5266240A (en) * | 1991-03-20 | 1993-11-30 | Servicios Corporativos Frisco, S.A. De C.V. | Flotation reactor with external bubble generator |
US5341938A (en) * | 1991-03-20 | 1994-08-30 | Servicios Corporativos Frisco, S.A. De C.V. | Method of separating materials in a flotation reactor |
US5251764A (en) * | 1991-03-27 | 1993-10-12 | Outomec Oy | Flotation machine |
ES2065217A2 (en) * | 1991-03-27 | 1995-02-01 | Outomec Oy | Flotation machine |
US5234112A (en) * | 1991-10-02 | 1993-08-10 | Servicios Corporativos Frisco S.A. De C.V. | Flotation reactor with external bubble generator |
WO1993020945A1 (en) * | 1992-04-16 | 1993-10-28 | Atomaer Pty Ltd | Froth wash and froth removal system |
US5611917A (en) * | 1995-11-02 | 1997-03-18 | Baker Hughes Incorporated | Flotation cell crowder device |
US20040099575A1 (en) * | 2002-11-27 | 2004-05-27 | Khan Latif A. | Method and apparatus for froth flotation |
US6793079B2 (en) | 2002-11-27 | 2004-09-21 | University Of Illinois | Method and apparatus for froth flotation |
US20050051465A1 (en) * | 2002-11-27 | 2005-03-10 | Khan Latif A. | Method for froth flotation |
US7328806B2 (en) | 2002-11-27 | 2008-02-12 | University Of Illinois | Apparatus for froth cleaning |
WO2010142844A1 (en) | 2009-06-09 | 2010-12-16 | Outotec Oyj | A froth flotation method and an apparatus for extracting a valuable substance from a slurry |
WO2019008214A1 (en) | 2017-07-04 | 2019-01-10 | Outotec (Finland) Oy | A froth flotation arrangement and a froth flotation method |
EP3648894A4 (en) * | 2017-07-04 | 2021-02-17 | Outotec (Finland) Oy | A froth flotation arrangement and a froth flotation method |
US11033909B2 (en) | 2017-07-04 | 2021-06-15 | Outotec (Finland) Oy | Froth flotation arrangement and a froth flotation method |
EP4115982A1 (en) * | 2017-07-04 | 2023-01-11 | Metso Outotec Finland Oy | A froth flotation arrangement and a froth flotation method |
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