Grinding mills
11465154 · 2022-10-11
Assignee
Inventors
- Alex HEATH (Melville, AU)
- Jeffrey Victor BELKE (Mt Pleasant, AU)
- Edward Allan JAMIESON (Bayswater, AU)
Cpc classification
International classification
Abstract
A stirring device for stirring a particulate material and a grinding media in a grinding mill includes one or more protective elements that extend outwardly from a body to deflect the particulate material and the grinding media from the body to minimize contact of the mixture of the particulate material and the grinding media against the body and to promote contact between the particulate material and the grinding media.
Claims
1. A method of grinding a particulate mineral ore material, the method comprising: stirring a mixture of said particulate mineral ore material and a grinding media by a stirring device having a body, said particulate mineral ore material having a density of at least 2,000 kg/m3, and deflecting the mixture of said particulate mineral ore material and said grinding media from the body of said stirring device by a plurality of protective elements extending outwardly from said body and being spaced apart around said body, wherein the body comprises a rotating annular grinding disc, and wherein the plurality of protective elements are elongated in a plane orthogonal to an axis of rotation of the rotating annular grinding disc and arranged at an angle to a direction of rotation of the rotating annular grinding disc to deflect the mixture of the particulate mineral ore material particles and grinding media and to promote contact between the particulate mineral ore material particles and grinding media, wherein the plurality of protective elements extend outwardly from the annular grinding disc in an axial direction of the annular grinding disc and radially outward of an outer circumferential edge of the annular grinding disc.
2. A stirring device for stirring a mixture of a particulate material and a grinding media in a grinding mill, the stirring device comprising: a rotating annular grinding disc body, a plurality of protective elements that extend outwardly from said disc body and are spaced apart around said disc body to deflect the mixture of said particulate material and said grinding media from said disc body, wherein said particulate material are mineral ore particles having a density of at least 2,000 kg/m.sup.3, and wherein the plurality of protective elements are elongated in a plane orthogonal to an axis of rotation of the disc body and arranged at an angle to a direction of rotation of said disc body to deflect the mixture of the particulate mineral ore material particles and grinding media to minimize contact of the mixture of particulate mineral ore material particles and grinding media against the disc body and to promote contact between the particulate mineral ore material particles and grinding media, wherein the plurality of protective elements extend outwardly from the disc body in an axial direction of the disc body and radially outward of an outer circumferential edge of the disc body.
3. The stirring device of claim 2, wherein said plurality of protective elements extend at an angle to a surface of said disc body.
4. The stirring device of claim 2, wherein said disc body comprises opposed surfaces and said plurality of protective elements extend from at least one of said opposed surfaces, wherein the plurality of protective elements includes a first protective element and an adjacent, second protective element, the first and second protective elements defining a circumferential gap therebetween, and wherein at least one of the opposed surfaces spans the gap and interconnects the first and second protective elements.
5. The stirring device of claim 2, wherein said plurality of protective elements each comprise at least one of a projection, an elongated body, a block-shaped element, a flange, a tooth, a planar element, a vane, a blade, a fin, a plate, a bar, a post, a rod, a channel-shaped element, a V-shaped element, a U-shaped element, a depression, a recess, a ramp-like element and a wedge-shaped element.
6. The stirring device of claim 5, wherein said plurality of protective elements comprise said block-shaped element, wherein said block-shaped element is operatively coupled to said disc body so that opposed sides of said block-shaped element extend outwardly from said opposed surfaces of said disc body and/or wherein said block-shaped element comprises an outer end that extends radially outwardly from the outer circumferential edge of said disc body.
7. Use of the stirring device of claim 2 in a stirring device assembly.
8. A stirring device assembly for a grinding mill body, comprising a plurality of stirring devices of claim 2 mounted to a drive shaft for rotating said stirring devices.
9. Use of the stirring device assembly of claim 8 as a mill impeller in a grinding mill.
10. A mill body comprising a stirring device assembly, the stirring device assembly comprising a plurality of the stirring device of claim 2 mounted to a drive shaft for rotating said plurality of stirring devices.
11. A grinding mill comprising said mill body of claim 10.
12. The grinding mill of claim 11, wherein said grinding mill is a fine grinding mill having a power consumption of 10 to 70 kWhr/t.
13. The stirring device of claim 2, wherein the plurality of protective elements includes a first protective element and an adjacent, second protective element, the first and second protective elements defining a circumferential gap therebetween, the outer circumferential edge spanning the gap and interconnecting the first and second protective elements.
14. A method of grinding a particulate material in a grinding mill of the type having a mill body and a drive shaft for rotating a plurality of annular grinding discs within said mill body, said method comprising: introducing grinding media into said mill body; introducing said particulate material through an inlet, wherein said particulate material are mineral ore particles having a density of at least 2,000 kg/m.sup.3; and operating said drive shaft to rotate said annular grinding discs within said mill body, said annular grinding discs being mounted coaxially along said drive shaft; wherein said rotation of said annular grinding discs induces a rotating flow of a mixture of said particulate material and said grinding media within said mill body to grind said particulate material against said grinding media to produce smaller sized mineral particles, wherein a plurality of protective elements deflect said particulate material and said grinding media away from bodies of said annular grinding discs, wherein said plurality of protective elements are spaced apart around said body of said annular grinding disc, and wherein the plurality of protective elements are elongated in a plane orthogonal to an axis of rotation of the annular grinding disc and arranged at an angle to a direction of rotation of said annular grinding disc to deflect the mixture of the particulate mineral ore material particles and grinding media to minimise contact of the mixture of particulate mineral ore material particles and grinding media against the body of the annular grinding disc, wherein the plurality of protective elements extend outwardly from the body of the annular grinding disc in an axial direction of the body of the annular grinding disc and radially outward of an outer circumferential edge of the body of the annular grinding disc.
15. A grinding element for a grinding mill, comprising: an annular grinding disc mountable coaxially on a rotating drive shaft within a grinding mill, said annular grinding disc having opposed radial surfaces and an outermost circumferential edge, wherein the outermost circumferential edge interconnects the opposed radial surfaces, a plurality of protective elements provided along the opposed radial surfaces and along the outermost circumferential edge, wherein the protective elements protrude from said opposed radial surfaces and from said outermost circumferential edge and are spaced apart from each other in a circumferential direction along said opposed radial surfaces and along said outermost circumferential edge, and wherein the protective elements are elongated in a radial plane and arranged at an angle to a direction of rotation of said annular grinding disc to deflect a mixture of particulate mineral ore material to be grinded and grinding media from the opposed radial surfaces and from the outermost circumferential edge, to thereby minimize contact of the mixture of particulate mineral ore material to be grinded and grinding media against the opposed radial surfaces and against the outermost circumferential edge and to promote contact between the particulate mineral ore material to be grinded and grinding media, the particulate mineral ore material having a density of at least 2,000 kg/m.
16. The grinding element of claim 15, wherein each of the plurality of protective elements includes: a first portion extending radially along and protruding upwardly from an upper-facing radial surface of the opposed radial surfaces; a second portion extending radially along and protruding downwardly from a lower-facing radial surface of the opposed radial surfaces such that the first and second portions protrude from the annular grinding disc in opposite directions; and a third portion protruding radially outward from the outermost circumferential edge such that the third portion is positioned radially outward of the first and second portions.
17. The grinding element of claim 16, wherein the third portion is directly connected to each of the first and second portions.
18. The grinding element of claim 16, wherein a gap is defined between the third portion of a first protective element of the plurality of protective elements and the third portion of a second protective element of the plurality of protective elements that is adjacent the first protective element.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Preferred embodiments of the invention will now be described, by way of example only, with reference to the accompanying drawings in which:
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PREFERRED EMBODIMENTS OF THE INVENTION
(17) The present invention will now be described with reference to the following examples which should be considered in all respects as illustrative and non-restrictive. In the Figures, corresponding features within the same embodiment or common to different embodiments have been given the same reference numerals. Referring to
(18) In this embodiment, the mill body 2 is arranged vertically in the grinding mill 1 and has a bottom inlet 7 and a top outlet 8. It will be appreciated that in other embodiments, the mill body 2 is arranged to be inclined or at an angle in the grinding mill 1. In some embodiments, the mill body 2 is arranged to lie horizontally in the grinding mill 1. Likewise, in other embodiments, the inlet 7a and outlet 8 can be placed at locations of the mill body 2 other than the bottom and top, respectively.
(19) A charge of feed slurry comprising mineral ore particles is fed into the mill body 2 through the bottom inlet 7. Grinding media M is also added into the mill body 2 initially through the outlet 8 before the feed slurry is added and grinding mill 1 is in operation. Once the grinding mill 1 is in operation, the initial charge of grinding media M tends to wear out due to the grinding process. Accordingly, grinding media M is also progressively added with the feed slurry through the inlet 7 as the grinding mill 1 operates. The grinding media M typically comprises ceramic or steel beads that range from 1 mm to 5 mm in diameter. The size of the grinding media M may vary in other embodiments, depending on requirements. For example, the diameter of the grinding media can be 30 or 50 times the diameter of the slurry particles, which can be measured by reference to F80 or F100, which is discussed in more detail below. The mill body 2 is rotated by the drive mechanism 4 about the axis 6 to rotate or stir the feed slurry and grinding media together, causing the feed slurry particles to be crushed or ground against between the grinding media. The ground product is then discharged through the top outlet 8.
(20) Referring to
(21) An internal side wall 13 of the mill body 2 has a plurality of planar annular shelves 14 extending into the internal cavity 15 between the stirring devices 12 to sub-divide the mill body 2 so that the feed slurry flows upwardly from the bottom inlet 7 through openings 16 and eventually is discharged from the top outlet 8 after grinding. The shelves 14 tend to subdivide the internal cavity 15 into individual chambers 17. In this embodiment, the grinding mill 1 is a fine grinding mill, and is called a high intensity grinding mill, in which the rotating action of the stirring devices 12 results in intense grinding of the slurry particles by the grinding media M occurring in the cavity 15 adjacent the stirring devices. Fine grinding mills have a relatively high power consumption in order to achieve fine grinding, in the range from 10 kWhr/t to 70 kWhr/t (kilowatt hours per tonne). In this embodiment, the fine grinding mill has a power consumption of 30 kWhr/t.
(22) Referring to
(23) A plurality of protective elements 25 adjacent to the outer edge 23 extends outwardly from the disc body 20 to deflect the slurry particles and grinding media M. This effectively minimises or reduces the shear around the disc body 20 by minimising contact of the mixture of slurry particles and grinding media M against the disc body 20 and promoting contact between the slurry particles and grinding media. A mounting ring 28 is connected via arms 29 (typically known as spokes) to the disc body 20 for mounting each grinding disc 12 to the drive shaft 11 of the stirring device assembly 11. The protective elements 25 in this embodiment take the form of blocks or block-like elements that are integrally formed with the disc body 20 and arranged so that opposed sides 31, 32 and one end 33 of the blocks project outwardly from the planar surfaces 21, 22 and outer edge 23, respectively. Each block 25 thus extends both substantially orthogonally relative to the opposed planar surfaces 21, 22 via its opposed sides 31, 32 and radially outwardly from the outer edge 23 via its end 33. Alternatively, the protective elements 25 are in the form of U-shaped blocks mounted to the disc body 20 so that opposed sides 31, 32 and one end 33 of each block 25 extends or projects outwardly from the planar surfaces 21, 22 and outer edge 23 of the disc body, respectively.
(24) In operation, the drive mechanism 4 rotates the drive shaft 11 of the stirring device assembly 10, rotating the grinding discs 12 that in turn rotate the feed slurry and grinding media within the internal cavity 15 of the mill body 2. This rotation causes the feed slurry particles to be ground against and between the harder grinding media, thus releasing valuable mineral particles and reducing them in size for further downstream processing after being discharged through the outlet 8. The feed slurry particles may also be ground against the mill impeller 10. This grinding action occurs over a period of time and thus can be viewed as attrition of the slurry particles. In addition, the blocks 25 act to create a zone (relative to the motion of the grinding disc 12) around the outer circumferential edges 23 and the opposed surfaces 21, 22 of the disc body 20, promoting contact between the feed slurry particles and the grinding media M. In effect, a rotating pocket of material comprising the feed slurry and grinding media M is formed and “captured” in the zone that can be transported by the blocks 25. At the same time, the zone created by the blocks 25 minimises the amount of shear or slippage at the surfaces 21, 22 of the grinding discs 12, thus reducing the amount of wear on the grinding discs 12. That is, the protective elements 25 tend to move the slurry and the grinding media M away from the grinding discs 12. This means that there is less chance of shear or slippage being concentrated at the grinding discs 12. In addition, there is a lower probability of impacts occurring between the grinding media M and the grinding discs 12, and any impacts that do occur are not substantial but only minor in nature. Hence, the grinding discs 12 do not suffer excessive wear during operation of the mill body 2 in the grinding mill 1.
(25) It is known by those skilled in the art that concentrated mineral ore slurries frequently act as non-Newtonian (shear thinning) fluids with a yield stress. This means that such slurries tend to act as a solid body and do not act as a fluid until sufficient force is applied (exceeding the yield stress), after which the viscosity drops dramatically. As a consequence, in a conventional grinding mill of the type that uses a series of stirring elements like grinding discs, the highest shear force is applied by the rotational torque at the lowest radius from the rotational centre due to the geometry of the rotating discs and drive shaft. This results in the non-Newtonian slurry material yielding and becoming fluid immediately adjacent to the drive shaft and grinding discs, with the rest of the slurry material remaining stationary, or close to stationary. This results in the shear or “slip” being concentrated right at the surface of the grinding discs, accelerating the amount of wear to the grinding discs. Accelerated wear of the grinding discs makes their operational life very short, thus requiring more frequent replacement than desired. The frequent replacement of the grinding discs also increases the amount of downtime, reducing the efficiency of the grinding mill, as well as increasing maintenance costs.
(26) From this description of conventional fine grinding mills using stirring elements, the technical advantages and benefits of the invention become apparent by way of contrast. In the embodiment of the invention, the zone around the outer edge 23 and the planar surfaces 21, 22 created by the blocks 25 alleviates or overcomes the above drawbacks and deficiencies that occur in conventional grinding mills. That is, the zone minimises or reduces the amount of wear on the grinding discs 12 by minimising the differential speed between the grinding media M and the grinding discs 12 (i.e. the amount of shear), prolonging their operational life. Consequently, there is less frequent replacement of the grinding discs 12, thus reducing maintenance costs and increasing grinding mill capacity due to there being less downtime for maintenance. By improving the amount or frequency of contact between the feed slurry particles and the grinding media M, the zone improves the efficiency of grinding in the grinding mill 1. Furthermore, the zone increases the amount of the feed slurry that acts as a fluid.
(27) It will be appreciated that the protective elements 25 can take any number of forms in order to create the zone around each grinding disc 12. The protective elements 25 can be any form of projection that extends from the surfaces of the grinding disc 12, such as the upper planar surface 21, the lower planar surface 22, its outer edge 23 or any combination thereof. The protective element 25 can thus be planar, curved or adopt any polyhedral shape that protrudes for generating the zone. Some examples of possible shapes for the protective element 25 are illustrated in
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(31) Three different embodiments of the protective elements are illustrated in
(32) While the protective elements illustrated in
(33) Furthermore, while the protective elements 25, 40, 55, 74, 80 extend substantially orthogonally from the planar surfaces 21, 22, these protective elements can extend at an angle to the planar surfaces 21, 22 in similar fashion to the embodiment shown in
(34) Yet further configurations for the stirring devices 12 are illustrated in
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(39) It is contemplated in a further aspect that the invention can be implemented in relation to the mill body 2 rather than the mill impeller 10. In this aspect, the invention takes an opposite configuration for the mill body 2 by providing the protective elements 25 on the shelves 14 on the inner sidewalls 13 instead of on the grinding discs 12 so as to deflect the slurry particles and grinding media M from the shelves 14 and inner sidewalls 13. This enables a zone to be created around the shelves 14 and inner sidewalls 13, minimising wear on these components of the mill body 2. In this alternative configuration, as best shown in
(40) In yet another embodiment, the protective elements 25 are provided on the drive shaft 11 of the mill impeller to further enhance the zone created around the grinding discs 12. The protective elements 25 in this embodiment are axially aligned with the longitudinal axis 6 of the drive shaft 11 and may be located on annular shelves or discs similar to the mounting ring 28 and/or directly on the drive shaft.
(41) While the embodiments have been described with reference to a vertically arranged mill body, the invention may also be used in other mill types, such as grinding mills having a horizontally arranged or an angled mill body. Furthermore, the invention has also been developed for use with high intensity grinding mills that are grinding fine particulates, but is also equally applicable to other grinding mills of the type that use stationary mill shells with rotating stirring elements.
(42) It will also be appreciated that the invention is readily applicable to various types of particulate material having a variety of particle sizes and particle size distributions. Particle size is usually measured at the feed and at the discharge outlet. Hence, the particle size of the slurry at the feed inlet is typically measured as F80, meaning that 80% of the feed particles pass through a nominated screen mesh size. For example, a F80=100 μm means that 80% of all particles present will pass through a 100 μm screen aperture. An alternative measurement is F100, meaning that 100% of the feed particles pass through a nominated screen mesh size. Similarly, it will be understood by one skilled in the art that P80 means that 80% of the particles pass through a nominated screen mesh size. For example, a P80=600 μm means that 80% of all particles present will pass through a 600 μm screen aperture. The present invention has been primarily developed to process particle sizes in the range of F80=30 μm to F80=4000 μm, especially in the range of F80=80 μm to F80=200 μm for the incoming particulate material and particles sizes in the range of P80=0.1 μm to P80=1000 μm, especially in the range of P80=1 μm to P80=50 μm for the ground product. Hence, the present invention permits the grinding mill 1 to process a wide range of particle sizes for mineral particles having a wider particle size distribution in the above stated F80 and P80 ranges to produce very fine particle sizes down to P80=1 μm. Thus, the invention is readily applicable to many different types of particulate materials and is not limited to particular mineral ore types, but can include iron, quartz, copper, nickel, zinc, lead, gold, silver and platinum. Other particulate materials that can be processed using the invention include concrete, cement, recyclable materials (such as glass, ceramics, electronics and metals), food, paint pigment, abrasives and pharmaceutical substances. In these other applications, the invention is used to reduce the size of the particulate material using a grinding process.
(43) It will further be appreciated that any of the features in the preferred embodiments of the invention can be combined together and are not necessarily applied in isolation from each other. For example, different types of protective elements can be used on the same mill impeller, such as shown in
(44) By providing protective elements on the stirring devices, shaft assembly or shelves of the mill body to create a zone, the invention reduces the amount of wear and thus prolongs the operational life of the components of the grinding mill, reducing maintenance time, costs and improving efficiency of the grinding mill. The zone generated by the protective elements also promotes slurry particle contact with the grinding media, also improving grinding efficiency. Thus, the grinding mill is able to operate more efficiently, consuming components such as grinding discs as at lower rate while grinding at faster rates. Moreover, the invention when implemented in a mill impeller can be readily retrofitted in existing fine grinding mills. In all these respects, the invention represents a practical and commercially significant improvement over the prior art.
(45) Although the invention has been described with reference to specific examples, it will be appreciated by those skilled in the art that the invention may be embodied in many other forms.