Method and system for releasing mineral from synthetic bubbles and beads
11135597 · 2021-10-05
Assignee
Inventors
- Paul J. ROTHMAN (Windsor, CT, US)
- Mark R. FERNALD (Enfield, CT, US)
- Francis K. DIDDEN (Wallingford, CT, US)
- Christian V. O'Keefe (Durham, CT, US)
- Douglas H. Adamson (Masfield Center, CT, US)
Cpc classification
B03C1/01
PERFORMING OPERATIONS; TRANSPORTING
Y02W30/52
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B04C1/00
PERFORMING OPERATIONS; TRANSPORTING
B03C5/00
PERFORMING OPERATIONS; TRANSPORTING
B01D37/02
PERFORMING OPERATIONS; TRANSPORTING
Y10T428/2982
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B07B1/00
PERFORMING OPERATIONS; TRANSPORTING
B01D39/00
PERFORMING OPERATIONS; TRANSPORTING
International classification
B04C1/00
PERFORMING OPERATIONS; TRANSPORTING
B01D39/00
PERFORMING OPERATIONS; TRANSPORTING
B01D37/02
PERFORMING OPERATIONS; TRANSPORTING
B03C1/01
PERFORMING OPERATIONS; TRANSPORTING
B03C5/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A synthetic bead for use in mineral separation is described. The synthetic bead has a surface made of a synthetic material such as polymer and the synthetic material is functionalized with molecules having a functional group for attaching mineral particles to the surface in a separation process. The synthetic beads can be placed in flotation cell containing a mixture of water, valuable material and unwanted material or in a pipeline where the mixture is transported from one location to another. The enriched synthetic beads carrying the mineral particles are separated from the unwanted materials in the mixture. The mineral particles are then released from the synthetic beads by means of low pH treatment, ultrasonic agitation, thermal or electromagnetic treatment.
Claims
1. An apparatus comprising: a plurality of synthetic beads carrying mineral particles, each of the synthetic beads made of a synthetic material having a surface and a plurality of molecules attached to the surface, the molecules comprising a functional group having a chemical bond for attracting one or more of the mineral particles to the molecules so as to cause the mineral particles to attach to synthetic beads, the surface comprising a coating for providing the plurality of molecules, the coating being made of a coating material different from the synthetic material, the coating material comprising a hydrophobic chemical selected from the group consisting of polysiloxanates, poly(dimethylsiloxane) and fluoroalkysilane; and a releasing apparatus configured to interrupt the chemical bond of the functional group so as to remove the mineral particles from the synthetic beads.
2. The apparatus according to claim 1, wherein the synthetic beads carrying the mineral particles are received in a mixture having a first temperature, wherein said release apparatus is configured to cause the synthetic beads carrying the mineral particles to contact with a medium having a second temperature higher than the first temperature.
3. The apparatus according to claim 1, wherein the synthetic beads carrying the mineral particles are caused to contact with a liquid, and wherein said release apparatus is configured to apply a sonic agitation to the liquid so as to cause the mineral particles to separate from the synthetic beads.
4. The apparatus according to claim 1, wherein the synthetic beads carrying the mineral particles are received along with a mixture having a first pH value, wherein said release apparatus is configured to cause the synthetic beads carrying the mineral particles to contact with a medium having a second pH value different from the first pH value.
5. The apparatus according to claim 1, wherein the synthetic beads carrying the mineral particles are caused to contact with a liquid, and wherein said release apparatus is configured to apply microwaves to the liquid so as to cause the mineral particles to separate from the synthetic beads.
6. The apparatus according to claim 1, wherein said release apparatus is configured to mechanically cause the synthetic beads to move against each other.
7. The apparatus according to claim 3, wherein said release apparatus is an ultrasonic source configured to provide the sonic agitation to the liquid.
8. The apparatus according to claim 7, wherein the ultrasonic source is configured to produce ultrasound in the range of 10 Hz to 10 MHz for the sonic agitation.
9. The apparatus according to claim 4 wherein the second pH value ranges from 0 to 7.
10. The apparatus according to claim 1, wherein said release apparatus is configured to stir the synthetic beads so as to interrupt the chemical bond.
11. The apparatus according to claim 1, wherein at least a part of the synthetic beads carrying the mineral particles is made of a magnetic material, and wherein said release apparatus is configured to magnetically stir the synthetic beads.
12. The apparatus according to claim 1, wherein the synthetic beads carrying the mineral particles are received along with a mixture, wherein said release apparatus is configured to perform two or more interruption techniques, including: 1) to lower pH value of the mixture, 2) to apply an ultrasound to the mixture; 3) to increase the temperature of the mixture and 4) to mechanically stir the mixture.
13. The apparatus according to claim 12, wherein said release apparatus is configured to perform the two or more interruption techniques on the mixture concurrently or sequentially.
14. The apparatus according to claim 1, wherein the synthetic beads carrying the mineral particles received in a mixture having a pH value; and the releasing apparatus comprises a controller arranged to release an acidic material for lowering the pH value of the mixture, wherein the acidic material has a pH value of 0 to 6.
15. The apparatus according to claim 1, wherein the synthetic beads carrying the mineral particles received in a liquid and each of the synthetic beads has a surface structure; and the releasing apparatus comprises a sonic source arranged to apply ultrasonic waves so as to affect the surface structure.
16. The apparatus according to claim 1, wherein the synthetic material comprises polymer or polymer-based materials.
17. The apparatus according to claim 16, wherein the polymer is selected from the group consisting of polyamides (nylon), polyesters, polyurethanes, phenol-formaldehyde, urea-formaldehyde, melamine-formaldehyde, polyacetal, polyethylene, polyisobutylene, polyacrylonitrile, poly(vinyl chloride), polystyrene, poly(methyl methacrylates), poly(vinyl acetate), poly(vinylidene chloride), polyisoprene, polybutadiene, polyacrylates, poly(carbonate) and phenolic resin.
18. The apparatus according to claim 1, wherein the synthetic material comprises silica or silica-based materials, or glass or glass-based materials.
19. The apparatus according to claim 1, wherein each of the synthetic beads comprises a body made of the synthetic material for providing the surface.
20. The apparatus according to claim 1, wherein each of the synthetic beads comprises a shell made of the synthetic material for providing the surface.
Description
BRIEF DESCRIPTION OF THE DRAWING
(1) Referring now to the drawing, which are not necessarily drawn to scale, the foregoing and other features and advantages of the present invention will be more fully understood from the following detailed description of illustrative embodiments, taken in conjunction with the accompanying drawing in which like elements are numbered alike:
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DETAILED DESCRIPTION OF THE INVENTION
FIG. 1
(29) By way of example,
(30) The flotation cell or column 12 may be configured with a top part or piping 22, e.g., having a valve 22a, to receive the pulp slurry or mixture 14 and also with a bottom part or piping 24 to receive the synthetic bubbles or beads 70. In operation, the buoyancy of the synthetic bubbles or beads 70 causes them to float upwardly from the bottom to the top of the flotation cell or column 12 through the pulp slurry or mixture 14 in the flotation cell or column 12 so as to collide with the water, valuable material and unwanted material in the pulp slurry or mixture 14. The functionalization of the synthetic bubbles or beads 70 causes them to attach to the valuable material in the pulp slurry or mixture 14. As used herein, the term “functionalization” means that the properties of the material making up the synthetic bubbles or beads 70 are either selected (based upon material selection) or modified during manufacture and fabrication, to be “attracted” to the valuable material, so that a bond is formed between the synthetic bubbles or beads 70 and the valuable material, so that the valuable material is lifted through the cell or column 12 due to the buoyancy of the synthetic bubbles or beads 70. For example, the surface of synthetic bubbles or beads has functional groups for collecting the valuable material. Alternatively, the synthetic bubbles or beads are functionalized to be hydrophobic for attracting wetted mineral particles—those mineral particles having collector molecules attached thereto. As a result of the collision between the synthetic bubbles or beads 70 and the water, valuable material and unwanted material in the pulp slurry or mixture 14, and the attachment of the synthetic bubbles or beads 70 and the valuable material in the pulp slurry or mixture 14, the enriched polymer or polymer-based bubbles 18 having the valuable material attached thereto will float to the top of the flotation cell 12 and form part of the froth formed at the top of the flotation cell 12. The flotation cell 12 may include a top part or piping 20 configured to provide the enriched polymer or polymer-based bubbles 18 having the valuable material attached thereto, which may be further processed consistent with that set forth herein. In effect, the enriched polymer or polymer-based bubbles 18 may be taken off the top of the flotation cell 12 or may be drained off by the top part or piping 20.
(31) The flotation cell or column 12 may be configured to contain an attachment rich environment, including where the attachment rich environment has a high pH, so as to encourage the flotation recovery process therein. The flotation recovery process may include the recovery of ore particles in mining, including copper. The scope of the invention is not intended to be limited to any particular type or kind of flotation recovery process either now known or later developed in the future. The scope of the invention is also not intended to be limited to any particular type or kind of mineral of interest that may form part of the flotation recovery process either now known or later developed in the future.
(32) According to some embodiments of the present invention, the synthetic bubbles or beads 70 may be configured with a surface area flux by controlling some combination of the size of the polymer or polymer-based bubbles and/or the injection rate that the pulp slurry or mixture 14 is received in the flotation cell or column 12. The synthetic bubbles or beads 70 may also be configured with a low density so as to behave like air bubbles. The synthetic bubbles or beads 70 may also be configured with a controlled size distribution of medium that may be customized to maximize recovery of different feed matrixes to flotation as valuable material quality changes, including as ore quality changes.
(33) According to some embodiments of the present invention, the flotation cell or column 12 may be configured to receive the synthetic bubbles or beads 70 together with air, where the air is used to create a desired froth layer in the mixture in the flotation cell or column 12 in order to achieve a desired grade of valuable material. The synthetic bubbles or beads 70 may be configured to lift the valuable material to the surface of the mixture in the flotation cell or column.
The Thickener 28
(34) The apparatus 10 may also include piping 26 having a valve 26a for providing tailings to a thickener 28 configured to receive the tailings from the flotation cell or column 12. The thickener 28 includes piping 30 having a valve 30a to provide thickened tailings. The thickener 28 also includes suitable piping 32 for providing reclaimed water back to the flotation cell or column 12 for reuse in the process. Thickeners like element 28 are known in the art, and the scope of the invention is not intended to be limited to any particular type or kind either now known or later developed in the future.
The Bead Recovery Process or Processor 50
(35) According to some embodiments of the present invention, the apparatus 10 may further comprises a bead recovery process or processor generally indicated as 50 configured to receive the enriched polymer or polymer-based bubbles 18 and provide reclaimed polymer or polymer-based bubbles 52 without the valuable material attached thereon so as to enable the reuse of the polymer or polymer-based bubbles 52 in a closed loop process. By way of example, the bead recovery process or processor 50 may take the form of a washing station whereby the valuable mineral is mechanically, chemically, or electro-statically removed from the polymer or polymer-based bubbles 18.
(36) The bead recovery process or processor 50 may include a releasing apparatus in the form of a second flotation cell or column 54 having piping 56 with a valve 56a configured to receive the enriched polymer bubbles or beads 18; and substantially release the valuable material from the polymer bubbles or beads 18, and also having a top part or piping 57 configured to provide the reclaimed polymer bubbles or beads 52, substantially without the valuable material attached thereon The second flotation cell or column 54 may be configured to contain a release rich environment, including where the release rich environment has a low pH, or including where the release rich environment results from ultrasonic waves pulsed into the second flotation cell or column 54.
(37) The bead recovery process or processor 50 may also include piping 58 having a valve 56a for providing concentrated minerals to a thickener 60 configured to receive the concentrated minerals from the flotation cell or column 54. The thickener 60 includes piping 62 having a valve 62a to provide thickened concentrate. The thickener 60 also includes suitable piping 64 for providing reclaimed water back to the second flotation cell or column 54 for reuse in the process. Thickeners like element 60 are known in the art, and the scope of the invention is not intended to be limited to any particular type or kind either now known or later developed in the future.
(38) Embodiments are also envisioned in which the enriched synthetic beads or bubbles are placed in a chemical solution so the valuable material is dissolved off, or are sent to a smelter where the valuable material is burned off, including where the synthetic beads or bubbles are reused afterwards.
Dosage Control
(39) According to some embodiments of the present invention, the synthetic beads or bubbles 70 may be functionalized to control the chemistry of the process being performed in the cell or column, e.g. to release a chemical to control the chemistry of the flotation separation process.
(40) In particular, the flotation cell or column 12 in
(41) The scope of the invention is intended to include other types or kinds of functionalization of the synthetic beads or bubbles in order to provide other types or kinds of control of the chemistry of the process being performed in the cell or column, including either functionalizations and controls both now known and later developed in the future. For example, the synthetic beads or bubbles may be functionalized to control the pH of the mixture that forms part of the flotation separation process being performed in the flotation cell or column.
FIG. 2: The Collision Technique
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(43) In operation, the collision technique causes vortices and collisions using enough energy to increase the probability of touching of the polymer or polymer-based materials 206 and the valuable material in the mixture 202, but not too much energy to destroy bonds that form between the polymer or polymer-based materials 206 and the valuable material in the mixture 202. Pumps, not shown, may be used to provide the mixture 202 and the synthetic bubbles or beads 206 are the appropriate pressure in order to implement the collision technique.
(44) By way of example, the first device 210 and the second device 212 may take the form of shower-head like devices having a perforated nozzle with a multiplicity of holes for spraying the mixture and the synthetic bubbles or beads towards one another. Shower-head like devices are known in the art, and the scope of the invention is not intended to be limited to any particular type or kind thereof either now known or later developed in the future. Moreover, based on that disclosed in the instant patent application, a person skilled in the art without undue experimentation would be able to determine the number and size of the holes for spraying the mixture 202 and the synthetic bubbles or beads 206 towards one another, as well as the appropriate pumping pressure in order to provide enough energy to increase the probability of touching of the polymer or polymer-based materials 206 and the valuable material in the mixture 202, but not too much energy to destroy bonds that form between the polymer or polymer-based materials 206 and the valuable material in the mixture 202.
(45) As a result of the collision between the synthetic bubbles or beads 206 and the mixture, enriched synthetic bubbles or beads having the valuable material attached thereto will float to the top and form part of the froth in the flotation cell 201. The flotation cell 201 may include a top part or piping 214 configured to provide enriched synthetic bubbles or beads 216, e.g., enriched polymer bubbles as shown, having the valuable material attached thereto, which may be further processed consistent with that set forth herein.
(46) The alternative apparatus 200 may be used in place of the flotation columns or cells, and inserted into the apparatus or system shown in
FIGS. 3A-5D: The Synthetic Bubbles or Beads
(47) The bubbles or beads used in mineral separation are referred herein as synthetic bubbles or beads. At least the surface of the synthetic bubbles or beads has a layer of polymer functionalized to attract or attach to the value material or mineral particles in the mixture. The term “polymer bubbles or beads”, and the term “synthetic bubbles or beads” are used interchangeably. The term “polymer” in this specification means a large molecule made of many units of the same or similar structure linked together. The unit can be a monomer or an oligomer which forms the basis of, for example, polyamides (nylon), polyesters, polyurethanes, phenol-formaldehyde, urea-formaldehyde, melamine-formaldehyde, polyacetal, polyethylene, polyisobutylene, polyacrylonitrile, poly(vinyl chloride), polystyrene, poly(methyl methacrylates), poly(vinyl acetate), poly(vinylidene chloride), polyisoprene, polybutadiene, polyacrylates, poly(carbonate), phenolic resin, polydimethylsiloxane and other organic or inorganic polymers. The list is not necessarily exhaustive. Thus, the synthetic material can be hard or rigid like plastic or soft and flexible like an elastomer. While the physical properties of the synthetic beads can vary, the surface of the synthetic beads is chemically functionalized to provide a plurality of functional groups to attract or attach to mineral particles. (By way of example, the term “functional group” may be understood to be a group of atoms responsible for the characteristic reactions of a particular compound, including those define the structure of a family of compounds and determine its properties.)
(48) For aiding a person of ordinary skill in the art in understanding various embodiments of the present invention,
(49) In some embodiments of the present invention, a synthetic bead has a solid-phase body made of a synthetic material, such as polymer. The polymer can be rigid or elastomeric. An elastomeric polymer can be polyisoprene or polybutadiene, for example. The synthetic bead 70 has a bead body 80 having a surface comprising a plurality of molecules with one or more functional groups for attracting mineral particles to the surface. A polymer having a functional group to collect mineral particles is referred to as a functionalized polymer. In one embodiment, the entire interior part 82 of the synthetic bead 80 is made of the same functionalized material, as shown in
(50) According to a different embodiment of the present invention, the synthetic bead 70 can be a porous block or take the form of a sponge or foam with multiple segregated gas filled chambers. The combination of air and the synthetic beads or bubbles 70 can be added to traditional naturally aspirated flotation cell.
(51) It should be understood that the term “bead” does not limit the shape of the synthetic bead of the present invention to be spherical, as shown in
(52) It should also be understood that the surface of a synthetic bead, according to the present invention, is not limited to an overall smooth surface as shown in
(53) It should also be noted that the synthetic beads of the present invention can be realized by a different way to achieve the same goal. Namely, it is possible to use a different means to attract the mineral particles to the surface of the synthetic beads. For example, the surface of the polymer beads, shells can be functionalized with a hydrophobic chemical molecule or compound. Alternatively, the surface of beads made of glass, ceramic and metal can be coated with hydrophobic chemical molecules or compounds. Using the coating of glass beads as an example, polysiloxanates can be used to functionalize the glass beads in order to make the synthetic beads. In the pulp slurry, xanthate and hydroxamate collectors can also be added therein for collecting the mineral particles and making the mineral particles hydrophobic. When the synthetic beads are used to collect the mineral particles in the pulp slurry having a pH value around 8-9, it is possible to release the mineral particles on the enriched synthetic beads from the surface of the synthetic beads in an acidic solution, such as a sulfuric acid solution. It is also possible to release the mineral particles carrying with the enriched synthetic beads by sonic agitation, such as ultrasonic waves.
(54) The multiplicity of hollow objects, bodies, elements or structures may include hollow cylinders or spheres, as well as capillary tubes, or some combination thereof. The scope of the invention is not intended to be limited to the type, kind or geometric shape of the hollow object, body, element or structure or the uniformity of the mixture of the same. Each hollow object, body, element or structure may be configured with a dimension so as not to absorb liquid, including water, including where the dimension is in a range of about 20-30 microns. Each hollow object, body, element or structure may be made of glass or a glass-like material, as well as some other suitable material either now known or later developed in the future.
(55) By way of example, the multiplicity of hollow objects, bodies, elements or structures that are received in the mixture may include a number in a range of multiple thousands of bubbles or beads per cubic foot of mixture, although the scope of the invention is not intended to be limited per se to the specific number of bubbles. For instance, a mixture of about three thousand cubic feet may include multiple millions of bubbles or beads, e.g., having a size of about 1 millimeter, in three thousand cubic feet of the mixture.
(56) The multiplicity of hollow objects, bodies, elements or structures may be configured with chemicals applied to prevent migration of liquid into respective cavities, unfilled spaces or holes before the wet concrete mixture cures, including where the chemicals are hydrophobic chemicals.
(57) The one or more bubbles may take the form of a small quantity of gas, including air, that is trapped or maintained in the cavities, unfilled spaces, or holes of the multiplicity of hollow objects, bodies, elements or structures.
(58) The scope of the invention is intended to include the synthetic bubbles or beads shown herein being made from a polymer or polymer-based material, or a silica or silica-based, or a glass or glass-based material.
FIGS. 6-11: Releasing Mechanism
(59) Various embodiments of the present invention are envisioned as examples to show that the valuable minerals can be mechanically, chemically, thermally, optically or electromagnetically removed or released from the enriched synthetic beads or bubbles.
(60) By way of example, the bead recovery process or processor 50 as shown in
Thermally Releasing Valuable Material
(61) The synthetic beads or bubbles 70, as shown in
Sonically Releasing Valuable Material
(62) When ultrasonic waves are applied in a solution or mixture containing the enriched polymer bubbles or beads, at least two possible effects could take place in interrupting the attachment of the valuable material to the surface of the polymer bubbles or beads. The sound waves could cause the attached mineral particles to move rapidly against the surface of the polymer bubbles or beads, thereby shaking the mineral particles loose from the surface. The sound waves could also cause a shape change to the synthetic bubbles, affecting the physical structures on the surface of the synthetic bubbles. It is known that ultrasound is a cyclic sound pressure with a frequency greater than the upper limit of human hearing. Thus, in general, ultrasound goes from just above 20 kilohertz (KHz) all the way up to about 300 KHz. In ultrasonic cleaners, low frequency ultrasonic cleaners have a tendency to remove larger particle sizes more effectively than higher operational frequencies. However, higher operational frequencies tend to produce a more penetrating scrubbing action and to remove particles of a smaller size more effectively. In mineral releasing applications involving mineral particles finer than 100 μm to 1 mm or larger, according to some embodiments of the present invention, the ultrasonic wave frequencies range from 10 Hz to 10 MHz. By way of example, the bead recovery process or processor 50 as shown in
Chemically Releasing Valuable Material
(63) In physisorption, the valuable minerals are reversibly associated with the synthetic bubbles or beads, attaching due to electrostatic attraction or van der Waals bonding. The physisorbed mineral particles can be desorbed or released from the surface of the synthetic bubbles or beads if the pH value of the solution changes. Furthermore, the surface chemistry of the most minerals is affected by the pH. Some minerals develop a positive surface charge under acidic conditions and a negative charge under alkaline conditions. The effect of pH changes is generally dependent on the collector and the mineral collected. For example, chalcopyrite becomes desorbed at a higher pH value than galena, and galena becomes desorbed at a higher pH value than pyrite. If the valuable mineral is collected at a pH of 8 to 11, it is possible to weaken the bonding between the valuable mineral and the surface of the polymer bubbles or beads by lower the pH to 7 and lower. However, an acidic solution having a pH value of 5 or lower would be more effective in releasing the valuable mineral from the enriched polymer bubbles or beads. According to one embodiment of the present invention, the bead recovery process or processor 50 as shown in
(64) In general, the pH value is chosen to facilitate the strongest attachment, and a different pH value is chosen to facilitate release. Thus, according to some embodiments of the present invention, one pH value is chosen for mineral attachment, and a different pH value is chosen for mineral releasing. The different pH could be higher or lower, depending on the specific mineral and collector.
Electromagnetically Releasing Valuable Material
(65) More than one way can be used to interrupt the bonding between the mineral particles and the synthetic bubbles or beads electromagnetically. For example, it is possible to use microwaves to heat up the enriched synthetic bubbles or beads and the water in the flotation column. It is also possible use a laser beam to weaken the bonds between the functional groups and the polymer surface itself. Thus, it is possible to provide a microwave source or a laser light source where the enriched synthetic bubbles or beads are processed. By way of example, the bead recovery process or processor 50 as shown in
Mechanically Releasing Valuable Material
(66) When the enriched synthetic bubbles or beads are densely packed such that they are in a close proximity to each other, the rubbing action among adjacent synthetic bubbles or beads may cause the mineral particles attached to the enriched synthetic bubbles or beads to be detached. By way of example, the bead recovery process or processor 50 as shown in
Other Types or Kinds of Release Techniques
(67) A heater like element 150 (
(68) The scope of the invention is also intended to include other types or kinds of releasing apparatus consistent with the spirit of the present invention either now known or later developed in the future.
Multi-Stage Removal of Valuable Material
(69) More than one of the methods for releasing the valuable material from the enriched synthetic bubbles or beads can be used in the same bead recovery process or processor at the same time. For example, while the enriched synthetic bubbles or beads 18 are subjected to ultrasonic agitation (see
FIG. 12: Horizontal Pipeline
(70) According to some embodiments of the present invention, the separation process can be carried out in a horizontal pipeline as shown in
(71) It should be understood that the sized-based bead or bubble, weight-based bead or bubble, magnetic-based bead or bubble as described in conjunction with
(72) A mineral particle 171 in the slurry, after combined with one or more collector molecules 73, becomes a wetted mineral particle 172. The collector molecule 73 has a functional group 78 attached to the mineral particle 171 and a hydrophobic end or molecular segment 76. The hydrophobic end or molecular segment 76 is attracted to the hydrophobic molecules 179 on the polymer surface 174.
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(75) According to some embodiments of the present invention, only a portion of the surface of the synthetic bead is functionalized to be hydrophobic. This has the benefits as follows:
(76) 1. Keeps too many beads from clumping together—or limits the clumping of beads,
(77) 2. Once a mineral is attached, the weight of the mineral is likely to force the bead to rotate, allowing the bead to be located under the bead as it rises through the flotation cell; a. Better cleaning as it may let the gangue to pass through b. Protects the attached mineral particle or particles from being knocked off, and c. Provides clearer rise to the top collection zone in the flotation cell.
(78) According to some embodiments of the present invention, only a portion of the surface of the synthetic bead is functionalized with collectors. This also has the benefits of
(79) 1. Once a mineral is attached, the weight of the mineral is likely to force the bead to rotate, allowing the bead to be located under the bead as it rises through the flotation cell; a. Better cleaning as it may let the gangue to pass through b. Protects the attached mineral particle or particles from being knocked off, and c. Provides clearer rise to the top collection zone in the flotation cell.
(80) According to some embodiments of the present invention, one part of the synthetic bead is functionalized with collectors while another part of same synthetic bead is functionalized to be hydrophobic as shown in
(81) This “hybrid” synthetic bead can collect mineral particles that are wet and not wet.
Applications
(82) The scope of the invention is described in relation to mineral separation, including the separation of copper from ore. It should be understood that the synthetic beads according to the present invention, whether functionalized to have a collector or functionalized to be hydrophobic, are also configured for use in oilsands separation—to separate bitumen from sand and water in the recovery of bitumen in an oilsands mining operation. Likewise, the functionalized filters and membranes, according to some embodiments of the present invention, are also configured for oilsands separation.
(83) According to some embodiments of the present invention, the surface of a synthetic bead can be functionalized to have a collector molecule. The collector has a functional group with an ion capable of forming a chemical bond with a mineral particle. A mineral particle associated with one or more collector molecules is referred to as a wetted mineral particle. According to some embodiments of the present invention, the synthetic bead can be functionalized to be hydrophobic in order to collect one or more wetted mineral particles.
(84) The scope of the invention is intended to include other types or kinds of applications either now known or later developed in the future, e.g., including a flotation circuit, leaching, smelting, a gravity circuit, a magnetic circuit, or water pollution control.
The Scope of the Invention
(85) It should be further appreciated that any of the features, characteristics, alternatives or modifications described regarding a particular embodiment herein may also be applied, used, or incorporated with any other embodiment described herein. In addition, it is contemplated that, while the embodiments described herein are useful for homogeneous flows, the embodiments described herein can also be used for dispersive flows having dispersive properties (e.g., stratified flow). Although the invention has been described and illustrated with respect to exemplary embodiments thereof, the foregoing and various other additions and omissions may be made therein and thereto without departing from the spirit and scope of the present invention.